BS en 12285-1-2003 (2006) [PDF]
BRITISH STANDARD BS EN 12285-1:2003 Incorporating Corrigendum No. 1 Workshop fabricated steel tanks — Part 1: Horizont
46 1 1MB
Papiere empfehlen
![BS en 12285-1-2003 (2006) [PDF]](https://vdoc.tips/img/200x200/bs-en-12285-1-2003-2006.jpg)
- Author / Uploaded
- dahzah
Datei wird geladen, bitte warten...
Zitiervorschau
BRITISH STANDARD
BS EN 12285-1:2003 Incorporating Corrigendum No. 1
Workshop fabricated steel tanks — Part 1: Horizontal cylindrical single skin and double skin tanks for the underground storage of flammable and non-flammable water polluting liquids
The European Standard EN 12285-1:2003 has the status of a British Standard
ICS 13.300; 23.020.10
12&23 8,5) C3: pH value ≤ 7 C4: pH value 3 to 6 C5: Mass of formic acid ≤ 2 % C6: Mass of sulphur trioxide > 25 % C7: pH value of the water 5 to 9 D:
Mass of chloride < 0,5 %; pH value 5 at minimum
E:
Free from mixtures; except necessary stabilizers
E1: Free from iron salts E2: Free from arsen-V-connections F:
Free from fluoride
F1: Mass of fluoride < 0,5 % and mass of chloride < 350 ppm G: Free from ammonium salts I:
Only with inhibitors against corrosion, e. g. amines or ammonia
L:
Not free from water
L1: Mass of water > 0,05 %; no copper, tin or lead as part of the metal alloy S:
Free from sulphur
B.4.3.2
Conditions related to working conditions
Code H, H1,
Temperature of the liquid under working conditions, in particular when heating, filling and evacuating
H2,H3: the tank, should not exceed 30°C. H4: Temperature of the liquid under working conditions, in particular when heating, filling and evacuating the tank, should not exceed 40°C. H5: Temperature of the liquid under working conditions, in particular when heating, filling and evacuating the tank, should not exceed 65°C. H6: Temperature of the liquid under working conditions, in particular when heating, filling and evacuating the tank, should not exceed 100°C. H7: Tanks should be installed in a manner to take into account heating, caused by climatic changes. The temperature at the tank wall should not exceed 25°C. 27
EN 12285-1:2003 (E)
H8: Temperature of the liquid under working conditions, in particular when heating, filling and evacuating the tank, should not exceed 200°C. K1: Inner tank wall completely free from rust K2: Material free from copper K3: When changing the liquid the tanks should be passivated by an oxal solution before filling. M: The tanks should be installed in such a manner that the temperature of the liquid does not exceed 30°C. N:
Nitrogen or another suitable inert gas should be introduced into the tanks in order to create a permanent overpressure.
T:
At the time of filling it is essential that the tank is technically free from water and should be tightly sealed to avoid moisture increase. Where moisture may gain entry condition N is applicable.
T1: It is essential that the tank under working condition is properly vented. The vent should have an air drying system to avoid moisture entering the tank. U:
Only solution liquids (alcalic solutions) and their defined mixtures of which (or of its components) the acceptance with the tank material is proved or certified according to 3.
U1: The solution is permitted for warm hydrous solutions of ammonium nitrate in concentration of more than 80 % and 93 % at maximum assuming that a)
the pH value of the liquid measured in a 10 % hydrous solution is between 5 and 7 and
b)
the solutions do not include more than 0,2 % flammable liquids and chloreous compounds of chlorine with a chloreous content of more than 0,2 %.
The tanks are provided with a shut-off-device, which is designed in such a way that no overpressure will exist in the tank and which protects the tank against leakage and the increase of foreign liquids. The shut-off-device of the tank should be designed in such a way that the storaged ammonium nitrate will not effect its operation. B.4.4 act. aq. b.p. conc. ctg. f.p. liq. n.i.l. p(50) soln. subst. u.o.n. °C + 0 UN-Nr.
28
Explanation of the abbreviations in the positive-liquid-list Active Aqueous Start of boiling (boiling point) Concentration Containing Flash point Liquid Only solvents mentioned in the positive-liquid-list Vapour pressure at 50°C Solution Substance Unless otherwise named in the positive-liquid-list Degrees centigrade Liquid is allowed Liquid is not allowed Liquid has not been evaluated Number for the marking of the medium according to a medium list prepared by the United Nations
Acetal, with a f.p. below -18°C
Acetaldehyde
Acetaldol
Acetic acid, aq. soln. ctg. 50 to 80% of pure acid
Acetic acid, aq. soln. ctg. over 25% to below 50% of pure acid
Acetic acid, aq. soln. ctg. more than 80% of pure acid
Acetic acid, technical grade, purity 99,7% min.
Acetic anhydride
Acetoin, monomeric, 85% aq. soln.
Acetone
Acetone cyanohydrin, stabilized
Acetone oil, with a f.p. of -18 to below 0°C
Acetone oil, with a f.p. of 0 to below 21°C
2
3
4
5
6
7
8
9
10
11
12
13
14
1091
1091
1541
1090
2621
1715
2789
2789
2790
2790
2839
1089
1088
1088
2
1
Acetal, with a f.p. of -18 to below 21°C
UNNo.
Liquid
1
No.
75
75
115
A III AI AI
B
A II
B
AI
AI
5
class
0,89
0,89
0,93
0,8
1,02
1,09
1,06
1,11
0,79
0,83
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
------
------
------
------
------
------
++++++
---+++
++++++
++++++
C3
C
M1
AC
EN
AC
AC
8
conditions
A B C D E F 7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
6
kg/l
Danger Density
0,02
0,84
56
0,04
140
0,08
118
2,8
0,16
0,16
4
mbar
at 50°C
Vapour pressure
182
21
102
102
3
°C
Boiling point
Table B.2 — Positive-liquid-list
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
++++++
9
A B C D E F
Group of tank
Group of tank
C3
M1
BH4
BH4
BH4
BH4
N
10
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
++++++
11
29
C3
B
B
B
B
N
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
conditions A B C D E F
Qualifying
1.4306, 1.4541
Material No.
EN 12285-1:2003 (E)
Acrolein, stabilized
Acrylamide, aq. soln.
Acrylonitrile, stabilized
Acrylic acid, stabilized
Adhesives, in flammable solvent, n.i.l., liq., with a
18
19
20
21
22
30
24
23
Acetylacetone
17
f.p. of 21 to 55°C and a b.p. over 50°C
Adhesives, in flammable solvents, n.i.l., liq., with a
f.p. of 0 to below 21°C and a b.p. over 50°C
Adhesives, in flammable solvent, n.i.l., liq., with a
f.p. of-18 to below 0°C and a b.p. over 35°C
Acetophenone
16
1133
1133
1133
2218
1093
2074
1092
2310
1648
2
1
Acetonitrile
UNNo.
Liquid
15
No.
EN 12285-1:2003 (E)
0,03
141
0,4
77
0,92
A II
AI
AI
A II
AI
AI
A II
A III
0,07
B
5
0,37
4
mbar
53
140
202
80
3
°C
1,06
0,81
0,87
0,98
1,03
0,79
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
0 0 0 0 0 0
--+--+
------
-----+
------
++++++
++++++
7
U
U
U
M
MN
C
8
++++++
++++++
++++++
--+--+
--+--+
0 0 +0 0 +
-----+
---+++
++++++
++++++
9
U
U
U
M
M
H3
MN
AN
B
10
++++++
++++++
++++++
--+--+
--+--+
0 0 +0 0 +
-----+
---+++
++++++
++++++
11
U
U
U
M
M
H3
M
AN
B
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
31
30
29
28
27
26
25
No.
Alcoholic beverages, with a f.p. of 21 to 55°C
with a f.p. below -18°C and a b.p. over 35°C
Adhesives, in flammable solvents, n.i.l., viscous,
with a f.p. of 0 to below 21°C and a b.p. over 50°C
Adhesives, in flammable solvents, n.i.l., viscous,
with a f.p. of -18 to below 0°C and a b.p. over 35°C
Adhesives, in flammable solvents, n.i.l., viscous,
f.p. below -18°C and a b.p. over 35°C
Adhesives, in flammable solvents, n.i.l., liq., with a
f.p. over 61 to 100°C and a b.p. over 100°C
Adhesives, in flammable solvents, n.i.l., liq., with a
f.p. of 55 up to 61°C and a b.p. over 100°C
3065
1133
1133
1133
1133
1133
2
1
Adhesives, in flammable solvents, n.i.l., liq., with a
UNNo.
Liquid
78
0,31
4
mbar
3
°C
AI
AI
AI
AI
A III
A III
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
BC
U
U
U
U
U
U
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
B
U
U
U
U
U
U
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
conditions A B C D E F conditions A B C D E F
A B C D E F
Group of tank
B
U
U
U
U
U
U
12
31
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Group of tank Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
32
38
37
36
35
34
to 61°C and a b.p. of 200°C min.
Alcohols, toxic, u.o.n., liq., with a f.p. over 55°C up
to 61°C and a b.p. over 35 to below 200°C or more
Alcohols, toxic, u.o.n., liq., with a f.p. over 55°C up
and a b.p. of 200°C min.
Alcohols, toxic, u.o.n., liq., with a f.p. of 21 to 55°C
and a b.p. over 35 to below 200°C
Alcohols, toxic, u.o.n., liq., with a f.p. of 21 to 55°C
over 61°C and a b.p. of 200°C min.
Alcohols, injurious to health, u.o.n., liq., with a f.p.
over 61°C, and a b.p. over 35 to below 200°C
Alcohols, injurious to health, u.o.n., liq. with a f.p.
33
2929
2929
2929
2929
2810
2810
3065
2
1
Alcoholic beverages, with a f.p. over 55°C up to 61°C
UNNo.
Liquid
32
No.
EN 12285-1:2003 (E)
35
1,75
0,31
4
mbar
78
3
°C
A III
A III
A II
A II
A III
A III
5
1
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
7
BC
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
B2
B2
B
10
++++++
++++++
++++++
++++++
++++++
++++++
11
conditions A B C D E F conditions A B C D E F
A B C D E F
Group of tank
B2
B2
B2
B2
B2
B2
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Group of tank Qualifying
1.4306, 1.4541
Material No.
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
44
43
42
41
40
39
No.
b.p. of 200°C min.
Alcohols, toxic, u.o.n., with a f.p. over 61°C and a
a b.p. over 35 to below 200°C
Alcohols, toxic, u.o.n., liq., with a f.p. over 61°C and
-18°C and a b.p. over 35°C
Alcohols, toxic, u.o.n., with a f.p. below
-18°C and a b.p. of 35°C max.
Alcohols, toxic, u.o.n., with a f.p. below
-18°C to below 21°C and a b.p. over 35°C
Alcohols, toxic, u.o.n., with a f.p. of
of -18 to below 21°C and a b.p. of 35°C max.
2810
2810
1986
1986
1986
1986
2
1
Alcohols, toxic, u.o.n., with a f.p.
UNNo.
Liquid
4
mbar
3
°C
A III
A III
AI
AI
AI
AI
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
++++++
++++++
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
B2
B2
10
++++++
++++++
++++++
++++++
++++++
++++++
11
conditions A B C D E F conditions A B C D E F
A B C D E F
Group of tank
B2
B2
B2
B2
B2
B2
12
33
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Group of tank Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
34
51
50
49
48
47
46
45
No.
2
1
over 55°C up to 61°C and a b.p. over 100°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
21 to 55°C and a b.p. over 50°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p. of
-18 to below 21°C and a b.p. over 50°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p. of
-18 to below 21°C and a b.p. over 35°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p. of
to below 21°C and a b.p. over 35°C
Alcohols, injurious to health, u.o.n., with a f.p. of -18
-18 to below 21°C and a b.p. of 35°C max.
Alcohols, not toxic or corrosive, u.o.n., with a f.p. of
to below 21°C and a b.p. of 35°C max.
1987
1987
1987
1987
1987
1987
1987
UNNo.
Liquid
Alcohols, injurious to health, u.o.n., with a f.p. of -18
EN 12285-1:2003 (E)
4
mbar
3
°C
A III
A II
AI
AI
AI
AI
AI
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
B2
B2
B2
10
conditions
A B C D E F conditions A B C D E F 7
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
B2
B2
B2
B2
B2
B2
B2
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
58
57
56
55
54
53
52
No.
over 100°C,
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
below -18°C and a b.p. over 50°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
below -18°C and a b.p. over 35°C
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
-18°C and a b.p. over 35°C
Alcohols, injurious to health, u.o.n., with a f.p. below
below -18°C and a b.p. of 35°C max.
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
-18°C and a b.p. of 35°C max.
Alcohols, injurious to health, u.o.n., with a f.p. below
over 61°C up to 100°C and a b.p. over 100°C
1987
1987
1987
1987
1987
2
1
Alcohols, not toxic or corrosive, u.o.n., with a f.p.
UNNo.
Liquid
4
mbar
3
°C
AI
AI
AI
AI
AI
A III
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
B2
B2
B2
10
conditions
A B C D E F conditions A B C D E F 7
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
35
B2
B2
B2
B2
B2
B2
B2
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
36
64
63
62
61
60
59
No.
2
1
-18°C and a b.p. over 35°C
u.o.n., with a f.p. below
Alcohols, highly toxic on swallowing or skin contact,
over 35°C
u.o.n., with a f.p. of -18 to below 21°C and a b.p
Alcohols, highly toxic on swallowing or skin contact,
over 55 up to 61°C and a b.p. of 200°C min.
Alcohols, injurious to health, u.o.n., liq., with a f.p.
over 55 up to 61°C and a b.p. below 200°C
Alcohols, injurious to health, u.o.n., liq., with a f.p.
of 21 to 55°C and a b.p. of 200°C
Alcohols, injurious to health, u.o.n., liq., with a f.p.
of 21 to 55°C and a b.p. of 50 to 200°C
1986
1986
1987
1987
1987
1987
UNNo.
Liquid
Alcohols, injurious to health, u.o.n., liq., with a f.p.
EN 12285-1:2003 (E)
4
mbar
3
°C
AI
AI
A III
A III
A II
A II
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
++++++
++++++
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
B2
B2
10
++++++
++++++
++++++
++++++
++++++
++++++
11
B2
B2
B2
B2
B2
B2
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
65
70
69
68
67
66
No.
55°C and a b.p. of 200°C min.
Alcohols, highly toxic, u.o.n., liq., with a f.p. of 21 to
to 55°C and a b.p. over 35°C to below 200°C
Alcohols, highly toxic, u.o.n., liq., with a f.p. of 21
f.p. below 21°C and a b.p. over 35°C
Alcohols, highly toxic on inhalation, u.o.n., with a
f.p. below 21°C and a b.p. of 35°C max.
Alcohols, highly toxic on inhalation, u.o.n., with a
of 35°C max.
u.o.n., with a f.p. of -18 to below 21°C and a b.p.
Alcohols, highly toxic on swallowing or skin contact,
-18°C and a b.p. of 35°C max.
u.o.n., with a f.p. below
2929
2929
2929
2929
1986
1986
2
1
Alcohols, highly toxic on swallowing or skin contact,
UNNo.
Liquid
3
°C
4
mbar
AI
AI
AI
A II
A II
AI
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
++++++
++++++
++++++
++++++
++++++
++++++
9 B2
B2
B2
B2
B2
B2
10
++++++
++++++
++++++
++++++
++++++
++++++
11 B2
B2
B2
B2
B2
B2
12
37
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
38
77
76
75
74
73
72
71
No.
2
1
with a f.p. of 21 to 55°C and a b.p. over 35°C
Aldrin preparation, liq., ctg. 7 to 75% act. subst.,
with a f.p. of -18 to below 21°C and a b.p. over 35°C
Aldrin preparation, liq., ctg. 7 to 75% act. subst.,
with a f.p. of -18 to below 21°C and a b.p. of 35°C max.
Aldrin preparation, liq., ctg. 7 to 75% act. subst.,
61°C and a b.p. of 200°C min.
Alcohols, highly toxic, u.o.n., liq., with a f.p. over
61°C and a b.p. over 35°C to below 200°C
Alcohols, highly toxic, u.o.n., liq., with a f.p. over
55°C up to 61°C and a b.p. of 200°C min.
Alcohols, highly toxic, u.o.n., liq., with a f.p. over
up to 61°C and a b.p. over 35°C to below 200°C
2995
2762
2762
2810
2810
2929
2929
UNNo.
Liquid
Alcohols, highly toxic, u.o.n., liq., with a f.p. over 55
EN 12285-1:2003 (E)
4
mbar
3
°C
A II
AI
AI
A III
A III
A III
A III
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
------
------
------
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
------
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
9
B2
B2
B2
B2
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
ACU
ACU
ACU
B2
B2
B2
B2
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
2
1
Allyl acetate
Allyl isothiocyanate, stabilized
84
subst., with a f.p. over 61°C and a b.p. over 35°C
Aldrin preparation, liq., ctg. over 75 up to 100% act.
35°C
subst., with a f.p. of 21 to 61°C and a b.p. over
Aldrin preparation, liq., ctg. over 75 up to 100% act.
35°C max.
subst., with a f.p. of -18 to 21°C and a b.p. over
Aldrin preparation, liq., ctg. over 75 up to 100% act.
b.p. of 35°C max.
subst., with a f.p. over -18 to below 21°C and a
Aldrin preparation, liq., ctg. over 75 up to 100% act.
with a f.p. over 61°C and a b.p. over 35°C
1545
2333
2996
2995
2762
2762
2996
UNNo.
Liquid
Aldrin preparation, liq., ctg. 7 to 75% act. subst.,
83
82
81
80
79
78
No.
151
103
0,03
0,18
4
mbar
3
°C
A II
AI
A III
A II
AI
AI
A III
5
1,02
0,93
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
0 0 +0 0 +
------
------
------
------
------
7
A
ECH3
8
++++++
0 0 -0 0 +
------
------
0 0 0 0 0 0
0 0 0 0 0 0
------
9
BC
H3N
10
++++++
0 0 -0 0 +
++++++
++++++
++++++
++++++
++++++
11
BC
39
H3N
ACU
ACU
ACU
ACU
ACU
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
2-amino-m-xylene, liq.
4-amino-m-xylene, liq.
5-amino-m-xylene, liq.
3-amino-o-xylene, liq.
Aminonitrobenzenes, isomer mixture, liq.
2-(2-aminoethoxy)ethanol
3-(2-aminoethylamino)propylamine
N-(2-aminoethyl)ethanolamine
N,N'-bis(2-aminoethyl)ethylenediamine
N-aminoethylpiperazine
1-aminonaphthalene, liq.
2-aminonaphthalene, liq.
87
88
89
90
91
92
93
94
95
96
97
98
40
Amino-p-xylene, liq.
86
1650
2077
2815
2259
1760
2735
3055
1661
1711
1711
1711
1711
1711
1545
2
1
Allyl mustard oil, stabilized
UNNo.
Liquid
85
No.
EN 12285-1:2003 (E)
1,06 0,94 1,04
306
299
220
260
244
200
232
1,13 1,06
0,99
0,98
0,02 A III
A III
A III
A III
A III
A III
1,02
6
A II
5
kg/l
0,03
4
mbar
151
3
°C
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
AH6
A
8
++++++
++++++
++++++
++++++
+++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
B
B
B
B
BH6
BC
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
D
D
D
D
BH6
BC
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
2-aminopropane
N,N'-bis(3-aminopropyl)ethylenediamine
Ammonia solutions, 10 to 35%, density: 0,88 to
102
103
104
Ammonium polysulfide solns.
Ammonium sulfide soln. with a f.p. of 21 to 61°C
Ammonium sulfide, solns. with a f.p. over 61°C
Amyl alcohol, with a f.p. of -18 to below 21°C
Amyl alcohol, with a f.p. of 21 to below 55°C
107
108
109
110
up to 93%
Ammonium nitrate, aq. soln., hot, conc. over 80%
106
105
4'-aminophenetole
101
0,957 at 15°C, in water
3'-aminophenetole
100
1201
1201
2683
2683
2818
2426
2672
2735
1221
2311
2311
2311
2
1
2'-aminophenetole
UNNo.
Liquid
99
No.
100
0,11
0,11
100
200
32
2,1
A II
A II
B
1,07
250
0,82
0,82
1,03
1,03
0,96
0,69
1,05
A III
233
6
kg/l
5
mbar
4
3
°C
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
ABC
ABC
C2
C2
C2
BG
8
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
9
B
B
C2
C2
C2
B
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
B
B
C2
C2
U1
D
12
41
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
Anisole
Aviation turbine fuel ASTM D 1695 Jet A
Aviation turbine fuel ASTM D 1695 Jet A1
Aviation turbine fuel ASTM D 1695 Jet B, with a f.p.
114
115
116
117
42
121
Aviation turbine fuel JP-4, with a f.p. of
120
Aviation turbine fuel JP-4, with a f.p. of 0 to below 21°C
-18 to below 0°C
Aviation turbine fuel JP-1
of 0 to below 21°C
Aviation turbine fuel ASTM D 1695 Jet B, with a f.p.
119
118
o-anisidine
113
of -18 to below 0°C
m-anisidine
112
1863 1863
0,03
AI
AI
A II
AI
AI
A II
A II
A II
1
1,09
A III
1,1
6 1,02
5
kg/l
4
mbar
155
225
251
184
3
°C
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
1223
1863
1863
1223
1223
2222
2431
2810
1547
2
1
Aniline
UNNo.
Liquid
111
No.
EN 12285-1:2003 (E)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
------
++++++
7
I
I
I
I
I
I
I
K3
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
2
1
Azacycloheptane
Benzaldehyde
Benzene
129
130
to 100°C
Aviation turbine fuel JP-7, with a f.p. over 61°C up
61°C
Aviation turbine fuel JP-7, with a f.p. over 55 up to
21°C
Aviation turbine fuel JP-6, with a f.p. of 0 to below
-18 to below 0°C
Aviation turbine fuel JP-6, with a f.p. of
100°C
Aviation turbine fuel JP-5, with a f.p. over 61 up to
61°C
1114
2493
1223
1863
1863
1223
UNNo.
Liquid
Aviation turbine fuel JP-5, with a f.p. over 55 up to
128
127
126
125
124
123
122
No.
80
178
139
= 150
AI
A III
0,37
B
A III
A III
AI
AI
A III
A III
5
0,05
4
mbar
3
°C
0,88
1,05
0,88
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
7
ACS
AC
I
I
I
I
I
I
8
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
AB
B
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
AB
D
12
43
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
Benzyl chloride, stabilized
Benzyldimethylamine
Benzylidene chloride
Bicyclo[2.2.1]hepta-2,5-diene, stabilized,
134
135
136
137
44
Bitumen, in petroleum distillates, liq., with
140
over 50°C
a f.p. of -18 to below 21°C and a b.p.
Bis(trimethylsilyl)amine
with a f.p. below -18°C
Bicyclo[2.2.1]hepta-2,5-diene, stabilized,
139
138
Benzylamine, with a f.p. over 61°C
133
with a f.p. of -18 to below 21°C
Benzothiol
132
1999
1993
2251
2251
1886
2619
1738
1719
2337
2224
2
1
Benzonitrile
UNNo.
Liquid
131
No.
EN 12285-1:2003 (E)
A II A III A III A II A III
0,08
0,29
AI
AI
AI
AI
A III
0,29
5
4
mbar
126
89
89
205
185
179
185
169
191
3
°C
0,78
0,91
0,91
1,26
0,9
1,1
0,99
1,08
1,01
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
---+++
++++++
0 0 0 0 0 0
++++++
------
++++++
7
CET
BG
A
8
++++++
---+++
++++++
++++++
0 0 0 0 0 0
++++++
0 0 0 0 0 0
++++++
++++++
++++++
9
T
B
B
10
++++++
---+++
++++++
++++++
0 0 0 0 0 0
++++++
--+--+
++++++
++++++
++++++
11
T
D
M
D
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
145
144
143
142
141
No.
a f.p. over 100°C
Bitumen, in petroleum distillates, liq., with
over 50°C
with a f.p. of -18 up to 21°C and a b.p.
Bitumen, in petroleum distillates, viscous,
over 150°C
a f.p. over 61°C up to 100°C and a b.p.
Bitumen, in petroleum distillates, liq., with
150°C
a f.p. over 55 up to 61°C and a b.p. over
Bitumen, in petroleum distillates, liq., with
100°C
a f.p. of 21 to 55°C and a b.p. over
1999
1999
1999
2
1
Bitumen, in petroleum distillates, liq., with
UNNo.
Liquid
4
mbar
3
°C
AI
A III
A III
A II
5
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
7
8
++++++
++++++
++++++
++++++
++++++
9
10
++++++
++++++
++++++
++++++
++++++
11
12
45
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
2-bromo-2-methylpropane
1-bromo-3-chloropropane
1-bromo-3-methylbutane
Bromobenzene
152
153
154
155
46
1-bromo-2-methylpropane
0°C
Brake fluid, hydraulic, with a f.p. below
up to 100°C
Brake fluid, hydraulic, with a f.p. over 61
151
150
149
Brake fluid, hydraulic, with a f.p. over 55
148
up to 61°C
Brake fluid, hydraulic, with a f.p. of 21 to 55°C
below 21°C
2514
2341
2688
2342
2342
2
1
Brake fluid, hydraulic, with a f.p. of 0 to
UNNo.
Liquid
147
146
No.
EN 12285-1:2003 (E)
156
121
142
74
92
100
100
100
100
100
3
°C
0,03
0,09
0,05
0,47
0,28
A II
A II
A III
AI
AI
AI
A III
A III
A II
AI
5
4
mbar
1,5
1,26
1,6
1,22
1,27
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
AC
AC
AC
AC
8
------
------
------
------
++++++
++++++
++++++
++++++
++++++
9
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A
AC
AC
AC
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Bromoethane
2-bromopentane
1-bromopropane, with a f.p. of -18 to
159
160
161
3-bromopropene
Butanedione
Butanethiol, isomer mixture, with a f.p. of
164
165
166
-18 to below 21°C
2-bromopropane
55°C
1-bromopropane, with a f.p. of 21 to
163
162
2-bromobutane
158
below 21°C
1-bromobutane, with a f.p. of 21°C min.
157
2347
2346
1099
2344
1993
1993
2343
1891
2339
1126
1126
2
1
1-bromobutane, with a f.p. below 21°
UNNo.
Liquid
156
No.
0,35
0,51
0,74
0,51
0,51
0,11
1,48
0,23
0,18
0,18
4
mbar
88
70
60
71
71
116
38
91
101
101
3
°C
AI
AI
AI
AI
A II
AI
AI
AI
AI
A II
AI
5
0,99
1,43
1,32
1,35
1,35
1,22
1,46
1,26
1,28
1,28
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
------
------
------
+ + + + +.+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
AC
AC
AC
AC
AC
AC
AC
AC
8
++++++
++++++
------
------
------
------
------
------
------
------
------
9
10
++++++
++++++
-----+
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
11
47
EHN
AC
AC
AC
AC
AC
A
A
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
1-butanol
2-butanol, with a f.p. below 21°C
2-butanol, with a f.p. of 21°C min.
tert-butanol
2-butanone
2-buten-1-ol
2-butenal, stabilized
2-butoxyethanol, with a f.p. of 61°C
170
171
172
173
174
175
176
177
48
178
2-butanethiol
169
2-butoxyethanol, with a f.p. over 61°C
max.
1-butanethiol
below -18°C
2369
2369
1143
2614
1193
1120
1120
1120
1120
2347
2347
2347
2
1
Butanethiol, isomer mixture, with a f.p.
UNNo.
Liquid
168
167
No.
EN 12285-1:2003 (E)
171
171
102
115
80
83
100
100
118
85
0,17
0,11
0,38
0,25
0,12
0,12
0,06
0,31
0,2
98
4
mbar
3
°C
AI
A II
AI
AI
A II
A II
A II
AI
AI
AI
5
0,9
0,9
0,85
0,86
0,81
0,79
0,81
0,81
0,81
0,83
0,85
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
---+++
++++++
---+++
++++++
++++++
++++++
++++++
------
------
------
7
AN
EC
N
BC
BC
BC
BC
8
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
+++++
9
N
B
B
B
B
10
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
N
B
B
B
B
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Butoxyl
n-butyl acetate
sec-butyl acetate
tert-butyl acetate
n-butyl acrylate, stabilized
sec-butyl alcohol
Di-n-butylamine
Di-sec-butylamine
n-butylamine
N,N-Di-n-butylaminoethanol
N-n-butylaniline
n-butylbenzene
sec-butylbenzene
tert-butylbenzene
179
180
181
182
183
184
185
186
187
188
189
190
191
192
No.
2
1
2709
2709
2738
2873
1125
2734
2248
1120
2348
1123
1123
1123
2708
UNNo.
Liquid
169
173
183
241
222
78
134
159
100
148
98
112
127
166
3
°C
0,02
0,02
A II
A II
0,87
0,86
0,86
A III
0,93
0.74
0,75
0,77
0,81
0,9
0,87
0,87
0,88
0,96
6
0,86
B
A II
A II
A II
A II
AI
AI
A II
A III
5
kg/l
0,32
0,06
0,03
0,12
0,04
0,18
0,11
0,07
0,03
4
mbar
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
7
EC
EC
EC
BG
G
G
BC
CM
AC
AC
AC
AC
8
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
9
A5BN
B
B
B
B
C1M
C1
C1
C1
C1
10
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
11
49
A5DN
D
D
B
M
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
EN 12285-1:2003 (E)
tert-butyl chloride
Di-n-butyl ether
n-butyl formate
n-butylglycol acetate
n-butyl isocyanate
tert-butyl isocyanate
n-butyl methacrylate, stabilized
198
199
200
201
202
203
204
50
sec-butyl chloride
below -18°C
Butyl chloride, isomer mixture, with a f.p.
197
196
Butyl chloride, isomer mixture, with a f.p.
195
of -18 to below 21°C
n-butyl butyrate
194
2227
2484
2485
1128
1149
1127
1127
1127
1127
1993
2342
2
1
tert-butyl bromide
UNNo.
Liquid
193
No.
EN 12285-1:2003 (E)
163
84
115
184
107
140
51
68
0,02
0,3
A II
AI
AI
A III
0,1
AI
A II
AI
AI
AI
AI
A II
AI
5
0,14
0,04
0,99
0,57
0,02
0,47
4
mbar
166
74
3
°C
0,9
0,85
0,89
0,94
0,9
0,77
0,85
0,88
0,87
1,22
6
kg/l
Boiling Vapour Danger Density point pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
AC
AC
A
AC
AC
AC
AC
AC
AC
8
--+--+
---+++
---+++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
------
9
M
BCT
BCT
AC1
10
--+--+
---+++
---+++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
11
M
BCT
BCT
AC
12
conditions
Qualifying
A B C D E F conditions A B C D E F conditions A B C D E F
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
Qualifying
1.4306, 1.4541
Group of tank
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
tert-butyl methyl ketone
Butylphenol, liq.
Butylphenol, melted
2-sec-butylphenol
2-tert-butylphenol
n-butyl propionate
Butyltoluenes, with a f.p. of 61°C max.
Butyltoluenes, with a f.p. over 61°C
4-tert-butyltoluene
n-butyl vinyl ether, stabilized
Butyraldehyde
n-butyric acid
Butyric anhydride
206
207
208
209
210
211
212
213
214
215
216
217
218
2739
2820
1129
2352
2667
2667
2667
1914
2228
2228
2228
2228
1224
2350
2
1
n-butyl methyl ether
UNNo.
Liquid
205
No.
198
164
76
94
193
190
190
146
222
226
200
200
106
70
3
°C
Boiling point
A III
0,98
A III
0,82 0,96
AI
0,78
0,85
0,85
0,85
0,08
0,44
AI
A III
0,22
A III
0,88
0,98
A II
0,98
0,03
0,92
0,81
0,74
6
1,03
AI
AI
5
kg/l
0,11
0,55
4
mbar
Vapour Danger Density pressure class at 50°C
Table B.2 (continued)
0 0 0 0 0 0
------
------
-----+
++++++
++++++
++++++
++++++
------
------
------
------
------
++++++
ACMN
AC
AC
AC
AC
A
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
0 0 0 0 0 0
------
---+++
-----+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Group of tank
CN
ACMN
AC1
E
E
EH6
E
++++++
++++++
---+++
-----+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A B C D E F
conditions
10
Group of tank
N
51
ACMN
BH8
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
1.4306, 1.4541
Material No.
EN 12285-1:2003 (E)
Carbon disulfide
Carbon tetrachloride
1-chloro-3-bromopropane
1-chloro-2,2-dimethylpropane
1-chloro-2,3-epoxypropane
2-chloro-4-methylaniline
3-chloro-2-methylaniline
3-chloro-4-methylaniline, liq.
4-chloro-2-methylaniline, liq.
5-chloro-2-methylaniline, liq.
222
223
224
225
226
227
228
229
230
231
52
Camphor oil
221
of 65% max.
Calcium chlorate, aq. solns. with a conc.
220
2239
2239
2239
2239
2239
2023
1107
2688
1846
1131
1130
2429
2411
2
1
Butyronitrile
UNNo.
Liquid
219
No.
EN 12285-1:2003 (E)
237
240
241
241
223
116
84
142
77
46
1,14 1,17
1,19
A III
1,16 1,19
A III
1,18
0,87
1,6
1,6
1,27
0,86
0,8
6
kg/l
A II
AI
A III
AI
A II
AI
5
0,09
0,4
0,05
0,42
1,15
100
0,09
4
mbar
Vapour Danger Density pressure class at 50°C
118
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
--+--+
-----+
0 0 0 0 0 0
++++++
++++++
E
E
E
E
E
AC
ACH2
AC
ACH
EHN
BC
C
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
++++++
++++++
++++++
++++++
------
------
------
------
-----+
++++++
++++++
++++++
9
A B C D E F
Group of tank
E
E
E
E
E
HN
BC
++++++
++++++
++++++
++++++
++++++
++++++
------
++++++
++++++
-----+
++++++
++++++
++++++
11
A B C D E F
conditions
10
Group of tank
E
E
E
E
E
AC
AC
HN
BC
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
1.4306, 1.4541
Material No.
6-chloro-3-methylaniline, liq.
2-chloro-3-methylbutane
1-chloro-2-methylbutane
2-chloro-2-methylbutane
1-chloro-3-methylbutane
3-chloro-4-methylphenyl isocyanate, liq.
1-chloro-2-methylpropane
2-chloro-2-methylpropane
1-chloro-2-nitrobenzene, liq.
1-chloro-3-nitrobenzene, liq.
2-chloro-6-nitrobenzene, liq.
4-chloro-2-nitrotoluene, liq.
4-chloro-3-nitrotoluene, liq.
233
234
235
236
237
238
239
240
241
242
243
244
245
2810
2810
2810
1578
1578
1127
1127
2206
1107
1107
1107
1107
2239
2239
2
1
6-chloro-2-methylaniline
UNNo.
Liquid
232
No.
260
240
238
236
246
51
68
226
99
1,35 1,27 1,26 1,37
0,85
0,88
1,21
0,87
0,87
0,86
1,35
AI
AI
AI
AI
AI
AI
1
0,56
0,22
0,4
86
0,36
1,19
6 1,19
5
kg/l
4
mbar
Vapour Danger Density pressure class at 50°C
93
228
220
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
--+--+
--+--+
--+--+
--+--+
++++++
++++++
AC
AC
AC
AC
AC
AC
AC
CET
ACH2
ACH2
ACH2
ACH2
E
E
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++-+++
------
------
------
------
++++++
++++++
9
A B C D E F
Group of tank
CEH5T
E
E
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++-+++
------
------
------
------
+++++
++++++
11
A B C D E F
conditions
10
Group of tank
53
CEH5T
E
E
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
1.4306, 1.4541
Material No.
EN 12285-1:2003 (E)
3-chloro-4-nitrotoluene, liq.
3-chloro-1-propene
2-chloroaniline, liq.
3-chloroaniline, liq.
Chloroanilines, isomer mixture, liq.
Chlorobenzene
Chlorobutane, isomer mixture, with a f.p.
249
250
251
252
253
254
255
54
257
256
2-chloro-4-nitrotoluene, liq.
248
1-chlorobutane
below -18°C
Chlorobutane, isomer mixture, with a f.p.
of -18 to below 21°C
1-chloro-4-nitrobenzene, liq.
247
1127
1127
1127
1134
2019
2019
2019
1100
2810
2810
1578
2810
2
1
5-chloro-2-nitrotoluene, liq.
UNNo.
Liquid
246
No.
EN 12285-1:2003 (E)
79
0,4
0,07
132
AI
AI
AI
A II
0,89
1,11
1,22
231
209
1,21
0,95
1,27
AI
1,27
1,21
1,3
6 1,32
5
kg/l
4
mbar
Vapour Danger Density pressure class at 50°C
44
200
260
242
260
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
------
------
------
------
++++++
++++++
++++++
++++++
AC
AC
AC
AC
AC
AC
AC
AC
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
++++++
++++++
++++++
------
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
9
A B C D E F
Group of tank
E
E
E
10
conditions
Qualifying
1.4306, 1.4541
Material No.
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
++++++
++++++
++++++
-----+
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
11
A B C D E F
Group of tank
E
E
E
EHN
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
alpha-chlorohydrin
Chloroform, stabilized with alcohols or
260
261
1-chloropentane
2-chloropentane
3-chloropentane
3-chlorophenyl isocyanate
266
267
268
f.p. over 55°C up to 61°C
1-chlorooctane, technical grade, with a
265
264
1-chlorooctane, technical grade, with a
263
f.p. of 21 to 55°C
1-chlorooctane, pure
262
olefins
2-chloroethanol
259
2810
1107
1107
1107
1993
1993
1888
2689
1135
1127
2
1
2-chlorobutane
UNNo.
Liquid
258
No.
204
98
97
108
175
175
182
62
213
128
68
3
°C
Boiling point
0,22
0,23
0,15
0,02
0,02
0,02
0,71
AI
AI
AI
A III
A II
A III
1,27
0,87
0,87
0,89
0,88
0,88
0,87
1,5
1,32
0,88
6
1,21
AI
5
kg/l
0,05
0,57
4
mbar
Vapour Danger Density pressure class at 50°C
Table B.2 (continued)
---+++
--+--+
--+--+
--+--+
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
CT
ACH2
ACH2
ACH2
AC
AC
AC
A2CM
AC
AC
AC
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
---+++
------
- - -- - -
------
++++++
++++++
++++++
------
++++++
++++++
0 0 0 0 0 0
9
A B C D E F
Group of tank
CT
AC
AC
AC
AC
AC
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Qualifying
---+++
------
------
------
++++++
++++++
++++++
--+--+
++++++
++++++
0 0 0 0 0 0
11
55
CT
AC
AC
AC
AEM
AC
AC
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2689 1100 2238 2238 2238 2234 2234 2234 1136
272 3-chloropropane-1,2-diol
273 3-chloropropene
274 2-chlorotoluene
275 3-chlorotoluene
276 4-chlorotoluene
277 2-chlorotrifluoromethylbenzene
278 3-chlorotrifluoromethylbenzene
279 4-chlorotrifluoromethylbenzene
280 Coal tar distillate, with a f.p. of -18 to
56
2356
271 2-chloropropane
below 0°C and a b.p. over 35°C
1278
270 1-chloropropane
2
1 1991
UNNo.
Liquid
269 Chloroprene, stabilized
No.
EN 12285-1:2003 (E)
0,05
0,04
0,05
0,03
0,03
0,03
1,21
1,61
1,16
0,75
4
mbar
AI
A II
A III
A II
A II
A II
AI
AI
AI
AI
5
1,35
1,37
1,45
1,06
1,07
0,95
1,32
0,87
0,9
0,96
6
kg/l
Vapour Danger Density pressure class at 50°C
139
153
137
162
162
158
44
213
35
47
59
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
0 0 0 0 0 0
AB
A
A
A
AC
AC
AC
AC
AC
AC
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
------
------
------
------
------
------
------
++++++
------
------
-----+
9
A B C D E F
Group of tank
B
AC
ACMN
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Qualifying
++++++
------
------
------
------
------
------
-----+
++++++
++++++
------
-----+
11
B
EHN
AC
C
ACMN
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
to 61°C and a b.p. over 100°C
287 Coal tar naphtha, with a f.p. over 55 up
55°C and a b.p. over 60°C
286 Coal tar naphtha, with a f.p. of 21 to
below 21°C and a b.p. over 50°C
2553
2553
0,41
285 Coal tar naphtha, with a f.p. of -18 to
2553
1136
1136
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
284 Coal tar distillate, with a f.p. over 61 up to 100°C and a b.p. over 100°C
to 61°C and a b.p. over 100°C
283 Coal tar distillate, with a f.p. over 55 up
55°C and a b.p. over 50°C
282 Coal tar distillate, with a f.p. of 21 to
below 21°C and a b.p. over 50°C
1136
UNNo.
Liquid
281 Coal tar distillate, with a f.p. of 0 to
No.
A III
A II
AI
A III
A III
A II
AI
5
class
0,9
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
AB
AB
AB
AB
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Group of tank
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
57
B
B
B
B
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2922
293 Cresols, aqueous alkaline soln.s with a
1760
297 Cyanamide, aq. soln. with a conc. of 50% max.
58
1918
2022
296 Cumene
xylenols etc.
295 Cresylic acid, liq., mixture of cresols,
of not more than 1,5 kg/l
294 Cresols, aq. alkaline soln.s, with a density
2922
A III
2076
292 p-cresol, liq.
density of not more than 1,3 kg/l
A III
2076
291 o-cresol, liq.
0,04
152
= 100
202
191
A III
2076
290 m-cresol, liq.
202
A III
2076
289 Cresol, isomer mixture, liq.
A II
A III
A III
5
mbar
°C
0,86
1,02
1,05
1,03
6
kg/l
Danger Density class
288 Coal tar naphtha, with a f.p. over 61 up to 100°C and a b.p. over 100°C
2
1
Vapour pressure at 50°C
Boiling point
4
UNNo.
Liquid
Table B.2 (continued)
3
No.
EN 12285-1:2003 (E)
--+--+
++++++
------
------
------
------
------
------
------
0 0 0 0 0 0
C4M
A
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
--+--+
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Group of tank
C4M
B
B
BH5
BH5
BH5
BH5
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
C4M
BH6
B
B
BH6
BH6
BH6
BH6
12
A B C D E F conditions
conditions
10
Group of tank
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
1.4306, 1.4541
Material No.
2
1
1935
300 Inorganic cyanides, aq. solns., with a
1145 3054 1915 2256
303 Cyclohexane
304 Cyclohexanethiol
305 Cyclohexanone
306 Cyclohexene, with a f.p. of -18 to below
stabilized
307 Cyclohexene, with a f.p. below -18°C,
2256
2242
302 Cycloheptene
21°C, stabilized
2241
301 Cycloheptane
conc. of 30% max.
2404
299 Cyanoethane
max.
1935
UNNo.
Liquid
298 Cyanide, aq. solns., with a conc. of 30%
No.
83
83
156
158
81
112
0,34
0,34
0,03
0,03
AI
AI
A II
A II
AI
AI
0,39
AI
B
5
0,82
0,82
0,95
0,98
0,78
0,83
0,81
0,79
6
kg/l
Danger Density class
0,11
119
0,21
97
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
---+++
---+++
++++++
------
++++++
++++++
++++++
------
0 0 0 0 0 0
------
7
N
N
AC
A
A
8
---+++
---+++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
--+--+
9
N
N
H1
H1
10
conditions
conditions
A B C D E F
A B C D E F
Qualifying Group of tank Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
---+++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
--+--+
11
59
N
H1
H1
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2734
2488 2520 2520 2358 1146 2244 2245 2246
311 N-cyclohexylethylamine
312 Cyclohexyl isocyanate
313 1,3-cyclooctadiene, stabilized
314 cis,cis-1,5-cyclooctadiene, stabilized
315 Cyclooctatetraene, stabilized
316 Cyclopentane
317 Cyclopentanol
318 Cyclopentanone
319 Cyclopentene
60
2357
310 Cyclohexylamine, with a f.p. of 21°C min.
to below 21°C
2357
309 Cyclohexylamine, with a f.p. of from -18
2
1 2243
UNNo.
Liquid
308 Cyclohexyl acetate
No.
EN 12285-1:2003 (E)
44
131
141
49
142
151
143
171
165
135
135
176
3
°C
Boiling point
1,23
0,05
0,02
1,05
0,04
0,04
0,04
0,02
0,02
0,07
0,07
0,04
4
mbar
at 50°C
Vapour pressure
AI
A II
A II
AI
A II
A II
A II
A II
A II
B
A III
5
class
0,78
0,95
0,95
0,75
0,92
0,88
0,87
0,99
0,88
0,87
0,87
0,97
6
kg/l
Danger Density
Table B.2 (continued)
---+++
++++++
++++++
++++++
------
---+++
---+++
---+++
++++++
++++++
++++++
++++++
7
N
AC
BC
M1N
N
N
CT
AC
8
++++++
++++++
++++++
++++++
------
---+++
---+++
---+++
++++++
++++++
++++++
++++++
9
B
M1N
N
N
BCT
C1
10
conditions
conditions
A B C D E F
A B C D E F
Qualifying Group of tank Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
------
---+++
---+++
---+++
++++++
++++++
++++++
++++++
11
A B C D E F
Group of tank
B
M1N
N
N
BCT
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1148 1148
329 Diacetone alcohol, pure
330 Diacetone alcohol, technical grade, ctg.
acetone, with a f.p. of 21 to 55°C
2383
328 Di-n-propylamine
167
168
105
120
2372
174
327 1,2-bis(dimethylamino)ethane
2247
325 n-decane
187
197
1147
324 trans-decahydronaphthalene
195
A III
0,05
0,17
AI
B
A II
1
A II
A III
A III
A II
5
0,94
0,94
0,74
0,77
0,87
0,73
0,87
0,9
0,89
0,89
6
kg/l
Danger Density class
0,03
0,02
0,03
189
0,04
134
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
326 Dehydrolinalool
1147
1147
323 cis-decahydronaphthalene
with a f.p. over 55°C
322 Decahydronaphthalene, isomer mixture,
with a f.p. of 55°C max.
1147
321 Decahydronaphthalene, isomer mixture,
2
1
2051
UNNo.
Liquid
320 Deanol
No.
Table B.2 (continued)
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
---+++
7
BG
BG
A
A
A
A
A
A5N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
9
A B C D E F
Qualifying Group of tank
B
B
A5BN
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
11
61
D
D
A5DN
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
2258
334 1,2-diaminopropane, with a f.p. over -18
2686
339 N,N-diethylethanolamine
62
2684
2373
2373
338 N,N-diethyl-1,3-propanediamine
-18°C
337 Diethoxymethane, with a f.p. below
below 21°C
336 Diethoxymethane, with a f.p. of -18 to
55°C
335 1,2-diaminopropane, with a f.p. of 21 to
2258
1783
333 1,6-diaminohexane, aq. soln.
to below 21°C
2079
332 2,2'-diaminodiethylamine
acetone, with a f.p. below 21°C
1148
UNNo.
Liquid
331 Diacetone alcohol, technical grade, ctg.
No.
EN 12285-1:2003 (E)
162
159
88
88
119
0,02
0,02
0,29
0,29
AI
AI
A II
0,89
0,83
0,84
0,84
0,87
0,87
119
0,96
0,94
AI
B
6
0,05
5
kg/l
Danger Density class
207
166
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
---+++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
------
++++++
++++++
7
A5N
AC
AC
AG
8
conditions
A B C D E F
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
A5BN
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A B C D E F
Group of tank
A5DN
D
D
D
D
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2049
343 Diethylbenzene, isomer mixture, with a
2049 2366 2579
347 1,4-diethylbenzene
348 Diethyl carbonate
349 1,4-diethylenediamine, 65% aq. soln.,
350 N,N-diethylethylenediamine
2685
2049
346 1,3-diethylbenzene
melted
2049
345 1,2-diethylbenzene
f.p. over 55°C
344 Diethylbenzene, isomer mixture, with a
2049
2432
342 N,N-diethylaniline
f.p. of 21 to 55°C
1154
341 Diethylamine
2
1 1155
UNNo.
Liquid
340 Diethyl ether
No.
144
0,04
A III
A II
A II
0,07
A II
A III
A II
B
AI
5
0,83
0,98
0,86
0,86
0,87
0,94
0,71
0,72
6
kg/l
Danger Density class
126
184
181
184
0,87
1,76
217
56
35
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
------
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
GH5K4
AC
AC
AC
AC
AC
AC
A
BG
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
BH5K4
AB
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
63
D
DH5K4
B
D
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1156 1993 1594 2375 2359 2372 2873 1149
353 Diethyl ketone
354 3,3-diethylpentane
355 Diethyl sulfate
356 Diethyl sulfide
357 Diallylamine
358 1,2-bis(dimethylamino)ethane
359 Dibutylethanolamine
360 Dibutyl ether, isomer mixture, with a f.p.
1590 1590
362 2,3-dichloroaniline, liq.
363 2,4-dichloroaniline, liq.
64
1590
361 Dichloroaniline, isomer mixture, liq.
21°C min.
2079
352 Diethylenetriamine
2
1 1165
UNNo.
Liquid
351 1,4-diethylene dioxide
No.
EN 12285-1:2003 (E)
242
252
1,37 1,37
0,86
0,77
0,79
0,84
1,18
0,75
0,81
0,96
1,03
6
kg/l
A II
B
AI
AI
AI
AI
B
5
class
Danger Density
1
0,15
0,25
0,05
0,11
0,17
4
mbar
at 50°C
Vapour pressure
222
120
112
92
208
146
102
207
101
3
°C
Boiling point
Table B.2 (continued)
------
------
------
++++++
0 0 0 0 0 0
++++++
--+--+
0 0 0 0 0 0
---+++
++++++
++++++
++++++
---+++
7
A
BG
GH
ACT
A
AC
AG
EN
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
---+++
++++++
--+--+
++++++
---+++
++++++
++++++
++++++
---+++
9
A B C D E F
Qualifying Group of tank
EH5
E
E
A5BN
B
BH
AT
B
N
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
11
EH5
E
E
A5DN
D
B
D
N
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
1590 1590 1591 2362 1184 1916 1150 1150 1150 1152 1152 2206 1279
365 2,6-dichloroaniline, liq.
366 3,5-dichloroaniline, liq.
367 1,2-dichlorobenzene
368 1,1-dichloroethane
369 1,2-dichloroethane
370 2,2'-dichloroethyl ether
371 cis-1,2-dichloroethylene
372 trans-1,2-dichloroethylene
373 1,2-dichloroethylene, isomer mixture
374 Dichloropentane, isomer mixture
375 1,5-dichloropentane
376 3,4-dichlorophenyl isocyanate, liq.
377 1,2-dichloropropane, technical grade
2
1 1590
UNNo.
Liquid
364 2,5-dichloroaniline, liq.
No.
97
238
0,21
A II
180
A II
AI
AI
AI
1,1
AI
A II
0,72
AI
0,33
1,16
1,39
1,11
1,26
1,28
1,22
1,26
1,18
1,31
AI
1,37
0,8
1,37
A III
1,37
6
5
kg/l
Danger Density class
49
60
178
83
58
179
266
200
251
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
---+++
++++++
++++++
++++++
++++++
++++++
------
++++++
------
++++++
------
------
------
7
AC
CET
AC
AC
AI
AI
AI
E
AC
8
conditions
A B C D E F
------
++-+++
------
------
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
0 0 0 0 0 0
------
------
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
CEH5T
EH5
EH5
EH5
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++-+++
------
------
++++++
++++++
++++++
---+++
---+++
--+--+
------
++++++
++++++
++++++
11
65
AC
CEH5T
AI
AI
AI
ET
ET
EH2
EH5
EH5
EH5
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
2047
380 1,3-dichloropropene, isomer mixture of
1993 1993 2565 2264 2048 1202 1993 2361
382 1,1-dichloro-1-propene
383 2,3-dichloro-1-propene
384 Dicyclohexylamine
385 N,N-dicyclohexylamine
386 Dicyclopentadiene
387 Diesel fuel, DK type
388 Diisobutyl ether
389 Diisobutylamine
66
1993
381 3,3-dichloropropene
the cis and trans forms
1993
379 1,2-dichloropropene, trans isomer
f.p. of 21°C min.
2047
UNNo.
Liquid
378 Dichloropropene, isomer mixture, with a
No.
EN 12285-1:2003 (E)
139
0,05
0,09
121
0,03
A II
AI
A III
A II
A II
A III
0,03
AI
AI
AI
A II
AI
A II
5
0,75
0,76
0,98
0,85
0,91
1,21
1,17
1,18
1,18
6
kg/l
Danger Density class
0,28
0,43
167
159
256
94
76
0,33
84
0,43
77
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
G
A
BG
AC
AC
AC
AC
AC
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
------
------
------
------
------
------
9
A B C D E F
Qualifying Group of tank
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
------
------
------
------
------
------
11
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
1234 1595 1164
398 Dimethoxymethane
399 Dimethyl sulfate
400 Dimethyl sulfide
-18°C
397 1,1-dimethoxyethane, with a f.p. below
2377
2377
396 1,1-dimethoxyethane, with a f.p. of -18
to below 21°C
2252
395 1,2-dimethoxyethane
37
188
42
65
65
85
69
1159
394 Diisopropyl ether
84
AI
A III
1,63
B
B
B
B
AI
B
A II
A II
5
0,85
1,34
0,86
0,85
0,85
0,87
0,73
0,87
0,72
0,81
6
kg/l
Danger Density class
1,35
0,64
0,64
0,28
0,55
0,34
191
1158
0,02
168
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
393 N,N-diisopropylethanolamine
392 Diisopropylamine
methyl butyl ether
1993
391 Diisopentyl ether, mixture of 2- and 3-
2
1 1157
UNNo.
Liquid
390 Diisobutyl ketone
No.
Table B.2 (continued)
++++++
---+++
++++++
---+++
---+++
---+++
++++++
0 0 0 0 0 0
++++++
0 0 0 0 0 0
++++++
C
CT
AC
CN
CN
CN
A
AC
8
++++++
---+++
++++++
++++++
++++++
---+++
++++++
---+++
++++++
++++++
++++++
9
conditions A B C D E F
A B C D E F
7
Qualifying Group of tank
CT
N
A5BN
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
---+++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
11
67
CT
N
A5DN
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2707 2707 1993 1993 1106 2266 1160 1160 1160 1160
404 2,5-dimethyl-1,4-dioxane
405 4,4-dimethyl-1,3-dioxane
406 2,3-dimethyl-3-ethylpentane
407 2,4-dimethyl-3-ethylpentane
408 2,2-dimethyl-1-propylamine
409 Dimethyl-N-propylamine
410 Dimethylamine, 25% soln. in water
411 Dimethylamine, 40% soln. in water
412 Dimethylamine, 60% soln. in water
413 Dimethylamine, aq. soln., with a f.p. of
68
2288
403 3,3-dimethyl-1-butene
-18 to below 21°C and a b.p. over 35°C.
2288
402 2,3-dimethyl-2-butene
2
1 2288
UNNo.
Liquid
401 2,3-dimethyl-1-butene
No.
EN 12285-1:2003 (E)
0,48
0,41
0,05
0,04
0,1
0,1
1,48
0,47
0,9
77
81
137
142
117
118
41
73
56
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
B
B
B
B
B
B
AI
AI
A II
AI
AI
AI
AI
5
0,83
0,9
0,95
0,75
0,75
0,74
0,75
0,95
0,93
0,66
0,71
0,69
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
---+++
---+++
---+++
7
G
G
G
G
G
G
A
A
N
N
N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
B
N
N
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
++++++
++++++
++++++
11
D
D
D
D
D
D
N
N
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
2253 1711 1711 1711 1711 1711 1711 2619 1105
417 Dimethylaniline, isomer mixture, liq.
418 2,3-dimethylaniline, liq.
419 2,4-dimethylaniline, liq.
420 2,5-dimethylaniline, liq.
421 2,6-dimethylaniline, liq.
422 3,5-dimethylaniline, liq.
423 N,N-dimethylbenzylamine
424 2-methylbutan-2-ol
1160
416 N,N-dimethylaniline
below -18°C and a b.p. over 35°C
415 Dimethylamine, aq. soln., with a f.p.
and a p(50) of 3 bar max.
below -18°C and a b.p. of 35°C max.
2924
UNNo.
Liquid
414 Dimethylamine, aq. soln., with a f.p.
No.
102
0,11
A II
185
A III
B
A III
A III
A III
A III
A III
A III
B
B
5
0,81
0,9
0,96
6
kg/l
Danger Density class
193
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
ABC
BG
A
G
G
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
69
B
D
D
D
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1161 2263 2263 2263 2263 2263 2263 2263 2263 2707
428 Dimethyl carbonate
429 1,1-dimethylcyclohexane
430 cis-1,2-dimethylcyclohexane
431 cis-1,3-dimethylcyclohexane
432 cis-1,4-dimethylcyclohexane
433 trans-1,2-dimethylcyclohexane
434 trans-1,4-dimethylcyclohexane
435 1,2-dimethylcyclohexane, isomer mixture
436 1,3-dimethylcyclohexane, isomer mixture
437 Dimethyldioxanes with a f.p. of -18 to
70
2379
427 1,3-dimethylbutylamine
below 21°C
2457
426 2,3-dimethylbutane
2
1 1208
UNNo.
Liquid
425 2,2-dimethylbutane
No.
EN 12285-1:2003 (E)
0,11
120
0,11
0,11
0,11
0,11
0,11
0,11
0,23
0,15
0,79
1,03
120
123
124
120
129
120
90
106
58
50
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
AI
AI
AI
AI
AI
AI
AI
AI
AI
B
AI
AI
5
0,95
0,76
0,77
0,78
0,78
0,8
0,78
1,07
0,75
0,67
0,65
6
kg/l
Danger Density class
Table B.2 (continued)
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
A
A
A
A
A
A
A
A
AC
G
A
A
8
conditions
A B C D E F
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
N
A
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
N
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
2265 1920 1993 1920 1920 1920 1920 1920
442 N,N-dimethylformamide
443 2,3-dimethylheptane
444 2,4-dimethylheptane
445 2,5-dimethylheptane
446 2,6-dimethylheptane
447 3,3-dimethylheptane
448 3,5-dimethylheptane
449 4,4-dimethylheptane
135
136
137
135
136
134
141
153
134
2051
441 N,N-dimethylethanolamine
120
120
2707
120
0,06
0,06
0,05
0,06
0,06
0,06
0,05
0,03
0,04
0,11
0,11
0,11
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
440 Dimethyldioxanes with a f.p. over 61°C
up to 61°C
439 Dimethyldioxanes with a f.p. over 55°C
55°C
2707
UNNo.
Liquid
438 Dimethyldioxanes with a f.p. of 21 to
No.
A II
A II
A II
A II
A II
A II
A II
A III
A III
A II
5
0,72
0,72
0,73
0,71
0,72
0,71
0,73
0,95
0,89
0,95
0,95
0,95
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
A
A
A
A
A
A
A
A1G
A5N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
---+++
---+++
9
A B C D E F
Qualifying Group of tank
A5BN
N
N
N
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
---+++
---+++
11
71
A5DN
N
N
N
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1262 1262 1262 1262 2382 1163 1993 1665 1665 1665 1665 1665
452 2,4-dimethylhexane
453 2,5-dimethylhexane
454 3,3-dimethylhexane
455 3,4-dimethylhexane
456 N,N'-dimethylhydrazine
457 N-N-dimethylhydrazine
458 2,6-cis-dimethylmorpholine
459 Dimethylnitrobenzene, isomer mixture, liq.
460 2,3-dimethylnitrobenzene, liq.
461 2,4-dimethylnitrobenzene, liq.
462 2,5-dimethylnitrobenzene, liq.
463 2,6-dimethylnitrobenzene, liq.
72
1262
451 2,3-dimethylhexane
2
1 1262
UNNo.
Liquid
450 2,2-dimethylhexane
No.
EN 12285-1:2003 (E)
225
241
244
245
1,13 1,13 1,11
A III
1,14
0,94
0,79
0,83
0,72
0,71
0,69
0,7
0,71
0,7
6
A III
A II
142
AI
AI
AI
AI
AI
AI
AI
B
0,32
0,11
0,13
0,14
0,14
0,11
0,15
5
kg/l
Danger Density class
0,63
63
80
118
112
109
109
116
107
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
---+++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
7
C
C
C
C
C
T
A
A
A
A
A
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1993 1993 1993 1993 1206 1206 1206 1206 2261 2261 2261 1106 2924
465 2,3-dimethyloctane
466 2,5-dimethyloctane
467 2,7-dimethyloctane
468 4,5-dimethyloctane
469 2,2-dimethylpentane
470 2,3-dimethylpentane
471 2,4-dimethylpentane
472 3,3-dimethylpentane
473 Dimethylphenol, isomer mixture, liq.
474 2,4-dimethylphenol, liq.
475 2,6-dimethylphenol, liq.
476 1,1-dimethylpropylamine
477 1,2-dimethylpropylamine
2
1 1665
UNNo.
Liquid
464 3,4-dimethylnitrobenzene, liq.
No.
82
0,41
0,48
77
0,32
0,37
0,29
0,42
0,03
86
81
90
79
162
0,03
160
0,03
164
244
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
B
B
A III
A III
AI
AI
AI
AI
A II
AI
A II
AI
5
0,76
0,75
0,69
0,68
0,7
0,67
0,76
0,73
0,75
1,14
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
------
------
------
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
G
G
A
A
A
A
A
A
A
A
C
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
73
D
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2733
481 N,N-dimethyltrimethylenediamine, with a
1596 1597 1597 1597 1597 1599
484 Dinitroanilines, liq.
485 1,2-dinitrobenzene, liq.
486 1,3-dinitrobenzene, liq.
487 1,4-dinitrobenzene, liq.
488 Dinitrobenzenes, isomer mixture, liq.
489 2,4-dinitrophenol, aq. soln.
74
1598
483 4,6-dinitro-o-cresol, liq., pure
f.p. of 21 to 55°C
482 N,N-dimethyltrimethylenediamine, with a
2733
2267
480 Dimethylthiophosphoryl chloride
f.p. of 0 to below 21°C
1993
479 1,1-dimethylpropyl methyl ether
2
1 2266
UNNo.
Liquid
478 N,N-dimethylpropylamine
No.
EN 12285-1:2003 (E)
1,31 1,36 1,4
298
302
318
1,62
300
0,82
0,81
1,31
0,77
0,75
6
1,4
0,04
AI
A III
0,04
AI
B
0,36
0,48
5
kg/l
Danger Density class
312
134
134
170
85
77
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
------
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
------
0 0 0 0 0 0
++++++
ACH8
ACH8
ACH8
ACH8
AH6
G
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
9
A B C D E F
Group of tank
H8
H8
H8
H8
BH6
BH8
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
++++++
++++++
11
A B C D E F
H8
H8
H8
H8
BH6
BH8
D
D
EH1T
D
12
conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1166 2052 1993
493 Dioxolane
494 Dipentene, isomer mixture
495 Dipentyl ether, technical grade, mixture of
1993 2565 2586
499 Dodecadiphenylamine
500 Dodecylbenzenesulfonic acid, pure
2489
498 Dodecaethyl pentasilicate
technical grade, liq.
497 Diphenylmethane 4,4'-diisocyanate,
isomer mixture, liq.
496 Diphenylmethane 4,4'-diisocyanate,
2489
1165
492 Dioxane
di-n-amyl ether and diisoamyl ether
1600
491 Dinitrotoluene, isomer mixture, melted
2
1 2038
UNNo.
Liquid
490 Dinitrotoluene, isomer mixture, liq.
No.
230
256
160
300
A III
A II
A II
A II
B
B
5
1,06
0,91
1,06
1,24
1,07
1,03
6
kg/l
Danger Density class
0,46
74
0,17
101
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
------
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
0 0 0 0 0 0
---+++
++++++
++++++
7
EN
CH8K4
C
8
conditions
A B C D E F
0 0 0 0 0 0
++++++
++++++
---+++
---+++
++++++
++++++
---+++
---+++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
BCT
BCT
N
N
H8KA
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
---+++
---+++
++++++
++++++
---+++
---+++
++++++
++++++
11
75
B
BCT
BCT
N
N
H8KA
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1170 1170
504 Ethanol
505 Ethanol, aq. soln. ctg. over 24% up to
2491 2363 2335
509 Ethanolamine soln.
510 Ethanethiol
511 3-ethoxy-1-propene
76
2491
508 Ethanolamine
of ethanol
507 Ethanol, aq. soln. ctg. not more than 24%
ethanol
506 Ethanol, aq. soln. ctg. more than 70% of
1170
1280
503 1,2-epoxypropane, stabilized
70% of ethanol
3022
502 1,2-epoxybutane, stabilized
2
1 2023
UNNo.
Liquid
501 Epichlorohydrin
No.
EN 12285-1:2003 (E)
65
0,66
1,72
35
169
0,31
1,71
0,56
0,09
78
34
63
116
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
AI
B
B
AI
AI
A II
5
0,77
0,85
1,02
0,79
0,84
0,84
1,18
6
kg/l
Danger Density class
Table B.2 (continued)
0 0 0 0 0 0
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
-----+
-----+
++++++
7
AH
BC
BC
BC
BC
EK1MN
EK1MN
AC
8
conditions
A B C D E F
0 0 -0 0 +
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
-----+
------
9
A B C D E F
Qualifying Group of tank
H3N
B
B
B
B
EMN
EMN
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
0 0 -0 0 +
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
-----+
++++++
11
H3N
B
B
B
B
EMN
EMN
E
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
b.p. over 35°C
50%, a f.p. of -18 to below 0°C and a
2924
521 Ethylamine, aq. soln. with a conc. Below
0,66
B
AI
AI
A III
0,18
AI
0,3
65
2335
520 Ethyl allyl ether
77
98
1173
517 Ethyl acetate
1,07
250
1917
2311
516 4-ethoxyaniline
519 Ethyl acrylate, stabilized
2311
515 3-ethoxyaniline
0,77
0,92
1,03
0,9
1,05
A III
0,98
0,93
6
kg/l
233
181
2311
514 2-ethoxyaniline
5
class
Danger Density
A II
0,35
4
mbar
at 50°C
Vapour pressure
0,03
156
135
3
°C
Boiling point
518 Ethyl acetoacetate
1172
513 2-ethoxyethyl acetate
2
1 1171
UNNo.
Liquid
512 2-ethoxyethanol
No.
Table B.2 (continued)
++++++
0 0 0 0 0 0
--+--+
--+--+
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
7
BG
CM
CH
AC
A
8
conditions
A B C D E F
++++++
0 0 -0 0 +
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
H3N
M
C
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
0 0 -0 0 +
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
77
B
H3N
M
C
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
78
a b.p. over 35°C
to 70%, a f.p. of -18 to below 21°C and
526 Ethylamine, aq. soln., with a conc. of 50
70% and a p(50) of 3 bar max.
525 Ethylamine, aq. soln., with a conc. Over
35°C
70%, a f.p. below -18°C and a b.p. over
524 Ethylamine, aq. soln., with a conc. up to
over 35°C
50%, a f.p. of 21 to 55°C and a b.p.
523 Ethylamine, aq. soln., with a conc. Below
b.p. over 35°C
50%, a f.p. of 0 to below 21°C and a
2270
1036
2270
2920
2924
UNNo.
Liquid
522 Ethylamine, aq. soln., with a conc. Below
No.
EN 12285-1:2003 (E)
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
B
B
B
B
5
6
kg/l
Danger Density class
Table B.2 (continued)
------
++++++
++++++
++++++
++++++
7
BG
BG
BG
BG
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
11
B
B
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2288 1177 2275 2733
536 2-ethyl-1-butene
537 2-ethyl-n-butyl acetate
538 2-ethylbutyl alcohol
539 N-ethylbutylamine
109
149
162
65
149
2275
535 2-ethylbutanol
136
314
1175
532 Ethylbenzene, technical
A II
AI
A II
0,11
AI
0,7
0,74
0,83
0,88
0,7
0,83
A II
1,05 1,03
A III
0,87
0,96
0,98
0,94
0,95
6
AI
0,06
A II
A III
205
2274
1175
531 Ethylbenzene, chemically pure
A III
210
534 N-ethyl-N-benzylaniline
2272
530 N-ethylaniline
A III
217
213
2273
529 2-ethylaniline
A III
221
5
kg/l
Danger Density class
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
533 Ethyl benzoate
2754
528 4-(ethylamino)toluene
2
1
2754
UNNo.
Liquid
527 3-(ethylamino)toluene
No.
Table B.2 (continued)
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
BG
BC
AC
N
BC
E
AF
AF
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
C1
B
E
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
79
B
B
E
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1993 1993 1920 1262 1262 2385 2300 1993
546 3-ethyl-2,4-dimethylpentane
547 4-ethyl-2-methylhexane
548 4-ethyl-3-methylhexane
549 3-ethyl-2-methylpentane
550 3-ethyl-3-methylpentane
551 Ethyl-2-methylpropanoate
552 5-ethyl-2-methylpyridine
553 Ethyl pentanoate
80
1993
545 3-ethyl-2,3-dimethylpentane
A II
A III
178
AI
AI
A II
AI
AI
AI
0,11
0,12
0,05
0,06
0,05
0,04
AI
A III
0,35
A II
AI
0,07
AI
0,27
5
0,92
0,87
0,73
0,72
0,74
0,72
0,74
0,75
0,93
0,92
0,88
0,82
0,76
6
kg/l
Danger Density class
0,12
110
118
116
140
134
137
142
135
1171
544 Ethyl cellosolve
122 193
1180
542 Ethyl butyrate
117
91
4
mbar
°C
3
Vapour pressure at 50°C
Table B.2 (continued) Boiling point
543 2-ethylbutyric acid
1178
541 2-ethylbutyraldehyde
2
1 1179
UNNo.
Liquid
540 Ethyl n-butyl ether
No.
EN 12285-1:2003 (E)
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
7
C
A
A
A
A
A
A
C
AC
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
C1
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2734 2810 1604
562 N-ethylcyclohexylamine
563 Ethylenecyanohydrin
564 Ethylenediamine
116
228
165
206
85
2252
2666
561 Ethyl cyanoacetate
137
567 Ethylene glycol dimethyl ether
1862
560 Ethyl crotonate
126
121
2366
559 Ethyl carbonate
217
1153
2754
558 N-ethyl-p-toluidine
221
566 Ethylene glycol diethyl ether
2754
557 N-ethyl-m-toluidine
64
204
2615
556 Ethyl-n-propyl ether
178
95
A III
0,28
0,14
B
0,87
0,84
0,84
1,04
0,88
1,06
0,92
0,9
A II
A II
AI
0,98
0,94
0,95
0,74
0,92
0,72
6
0,08
0,02
0,07
A II
A III
0,07
AI
A III
0,64
AI
5
kg/l
Danger Density class
0,21
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
565 Ethylene glycol di-n-butyl ether
2300
555 5-ethyl-2-picoline
2
1 2287
UNNo.
Liquid
554 3-ethyl-2-pentene
No.
Table B.2 (continued)
---+++
---+++
++++++
------
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
0 0 0 0 0 0
---+++
7
CN
CN
A
C
CH
AC
A
N
8
conditions
A B C D E F
---+++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
N
N
B
C
C1
AB
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
---+++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
81
N
N
D
C
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1189 1185 2983
573 Ethylene glycol monomethyl ether acetate
574 Ethyleneimine, stabilized, pure
575 Ethylene oxide and propylene oxide,
1920
577 4-ethylheptane
82
1190
576 Ethyl formate
ethylene oxide
mixture ctg. not more than 30% of
1188
572 Ethylene glycol monomethyl ether
f.p. over 61°C
571 Ethylene glycol monobutyl ether with a
2369
2369
570 Ethylene glycol monobutyl ether with a
f.p.of 61°C max.
1172
569 Ethylene glycol monoethyl ether acetate
2
1 1171
UNNo.
Liquid
568 Ethylene glycol monoethyl ether
No.
EN 12285-1:2003 (E)
141
0,05
0,93
54
0,79
0,05
0,07
0,03
0,35
57
145
125
171
171
156
135
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
AI
AI
AI
A II
5
0,73
0,93
0,83
1,01
0,97
0,9
0,9
0,98
0,93
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
------
++++++
++++++
++++++
++++++
++++++
++++++
7
A
AC
C2H7N
A
A
8
conditions
A B C D E F
++++++
++++++
-----+
------
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
HK1N
C2H7N
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
-----+
------
++++++
++++++
++++++
++++++
++++++
++++++
11
HK1N
C2H7N
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
229 169
2276 2385 2615 1192 2277
581 2-ethylhexyl acrylate, stabilized
582 2-ethylhexylamine
583 Ethyl isobutyrate
584 Ethyl isopropyl ether
585 Ethyl lactate
586 Ethyl methacrylate, stabilized
201 167
1993 1993 1206
588 Ethyl octadecanoate
589 3-ethyloctane
590 4-ethyloctane
591 3-ethylpentane
94
164
220
587 Ethyl nonanoate
117
154
63
110
183
119
176
A III
0,24
0,03
0,03
AI
A II
A II
A III
AI
AI
AI
0,1
0,02
0,65
0,12
A II
A III
0,02
AI
A II
0,1
5
0,7
0,75
0,75
1,06
0,87
0,91
1,03
0,72
0,87
0,79
0,89
0,83
0,71
0,85
6
kg/l
Danger Density class
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
580 2-ethylhexanol
1262
579 3-ethylhexane
2
1 1191
UNNo.
Liquid
578 Ethylhexaldehyde
No.
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
7
A
A
A
C
A
C
BC
A
C
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
M
C1
C1
B
M
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
11
83
M
D
M
B
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
84
b.p. over 50°C
n.i.l., with a f.p. over -18 up to 0°C and a
599 Extracts, flavourings in alcoholic solution,
f.p. over 61°C
598 N-ethyltoluidine, isomer mixture with a
f.p. of 21 to 61°C
1197
2754
2754
0,28
597 N-ethyltoluidine, isomer mixture with a
91
0,17
B
A III
A II
B
AI
A II
1106
595 1-ethylpropylamine
99
AI
5
class
1,06
0,75
0,89
1,06
0,83
6
kg/l
Danger Density
0,05
4
mbar
at 50°C
Vapour pressure
201
1195
594 Ethyl propionate
160
131
3
°C
Boiling point
Table B.2 (continued)
596 Ethyl stearate
1993
593 Ethyl polysilicate
2
1 2386
UN-No.
Liquid
592 N-ethylpiperidine
No.
EN 12285-1:2003 (E)
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
G
C
G
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
U
D
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
and a b.p. over 100°C
n.i.l., with a f.p. over 61°C up to 100°C
603 Extracts, flavourings in alcoholic soln.,
a b.p. over 100°C
n.i.l., with a f.p. over 55 up to 61°C and
602 Extracts, flavourings in alcoholic soln.,
over 50°C
n.i.l., with a f.p. of 21 to 55°C and a b.p.
601 Extracts, flavourings in alcoholic soln.,
a b.p. over 50°C
n.i.l., with a f.p. of 0 to below 21°C and
1197
1197
1197
UNNo.
Liquid
600 Extracts, flavourings in alcoholic soln.,
No.
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
B
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
11
85
U
U
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
86
boiling point over 50°C
n.i.l., with a f.p. of 55 to 61°C and a
607 Extracts, perfumes in alcoholic soln.,
boiling point over 100°C
n.i.l., with a f.p. of 21 to 55°C and a
606 Extracts, perfumes in alcoholic soln.,
a boiling point over 50°C
n.i.l., with a f.p. of 0 to below 21°C and
605 Extracts, perfumes in alcoholic soln.,
a boiling point over 50°C
n.i.l., with a f.p. of -18 to below 0°C and
1169
1169
1169
1169
UNNo.
Liquid
604 Extracts, perfumes in alcoholic soln.,
No.
EN 12285-1:2003 (E)
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
B
B
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
11
A B C D E F
Group of tank
U
U
U
U
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
2387 1777 2388 2388 2388 1198
610 Fluorobenzene
611 Fluorosulfonic acid
612 2-fluorotoluene
613 3-fluorotoluene
614 4-fluorotoluene
615 Formaldehyde, aq. soln., with a
methanol content of 10 to 15%
formaldehyde content of 37% and a
1271
609 FAM standard mineral spirit, A type
a boiling point over 50°C
n.i.l., with a f.p. over 21 up to 55°C and
608 Extracts, perfumes in alcoholic soln.,
No.
0,11
0,11
0,12
0,02
0,31
117
116
114
163
85
0,71
65
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
AI
AI
AI
AI
AI
5
class
1
1
1,01
1,74
1,03
0,71
6
kg/l
Danger Density
Table B.2 (continued)
------
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
0 0 0 0 0 0
7
AC
AC
AC
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
+ + + + ++
++++++
9
A B C D E F
Qualifying Group of tank
C3C5
AC
AC
AC
AC
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
0 0 -0 0 +
++++++
++++++
++++++
11
87
C3
AC
AC
AC
H3T
AC
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1779 1779
620 Formic acid, ctg. 70 to 85% of pure acid
621 Formic acid, ctg. 85 to 97% of pure acid
88
1779
2209
1198
619 Formic acid, ctg. 50 to 70% of pure acid
over 61°C
methanol content of 15% max. and a b.p
formaldehyde content of 5 % min. a
618 Formaldehyde, aq. soln., with a
methanol content of 15% max. and a b.p. of 21 to 61°C
formaldehyde content of 5 % min. a
617 Formaldehyde, aq. soln., with a
f.p. over 100°C
2209
UNNo.
Liquid
formaldehyde content below 5% and a
616 Formaldehyde, aq. soln., with a
No.
EN 12285-1:2003 (E)
101
106
101
0,18
0,18
0,18
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
5
class
----------------
------
------
------
7
8
conditions
A B C D E F
------
------
------
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
C3C5
C3C5
C3C5
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
= 1,17
6
kg/l
Danger Density
Table B.2 (continued)
Qualifying
++++++
--+--+
--+--+
++++++
++++++
++++++
11
H2
H2
C3
C3
C3
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
1199 2874 2526 1202
629 Furfuraldehyde, with a f.p. over 55°C
630 Furfuryl alcohol
631 Furfurylamine
632 Gas oil, with a f.p. of 21 to 55°C and a
b.p. over 100°C
2389
628 Furan
A II
A II
A III
0,03
A III
AI
A III
A III
A III
A III
5
1,05
1,13
1,16
0,94
0 0 0 0 0 0
---+++
------
------
0 0 0 0 0 0
++++++
++++++
++++++
++++++
------
------
7
GN
A
A
A
8
conditions
A B C D E F
0 0 0 0 0 0
---+++
---+++
---+++
---+++
++++++
++++++
------
++++++
------
++++++
9
A B C D E F
Qualifying Group of tank
BN
CN
N
N
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
6
kg/l
Danger Density class
0,02
146
171
162
1,96
627 Fuel oil, medium 31
626 Fuel oil, light
1202
624 Fuel oil, EL-01 type
625 Fuel oil, S-03 type
0,18
1202
1779
101
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
acid
623 Formic acid ctg. less than 50% of pure
acid
1779
UNNo.
Liquid
622 Formic acid ctg. more than 97% of pure
No.
Table B.2 (continued)
++++++
---+++
---+++
---+++
---+++
++++++
++++++
++++++
++++++
--+--+
++++++
11
89
DN
CN
N
N
H2
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
2810
636 Glutaraldehyde, aq. soln., with a f.p. over
90
a f.p. of -18 to below 0°C and a b.p. over 35°C
637 Gutta-percha, in flammable liq., n.i.l., with
61°C
2789
635 Glacial acetic acid, purity 99,7% min.
a b.p over 100°C
634 Gas oil, with a f.p. of 61°C to 100°C and
and a b.p. over 100°C
1202
UNNo.
Liquid
633 Gas oil, with a f.p. over 55 up to 61°C,
No.
EN 12285-1:2003 (E)
0,08
118
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
AI
A III
A III
5
class
1,06
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
------
------
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
--+--+
0 0 0 0 0 0
0 0 0 0 0 0
9
A B C D E F
Qualifying Group of tank
U
C
BH1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
11
U
C
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
3056 1206 1206 1110 2710
642 n-heptaldehyde
643 Heptane, isomer mixture
644 n-heptane
645 2-heptanone
646 4-heptanone
a f.p. over 61 up to 100°C, and a b.p. over 100°C
641 Gutta-percha, in flammable liq., n.i.l., with
a f.p. over 55 up to 61°C, and a b.p. over 100°C
640 Gutta-percha, in flammable liq., n.i.l., with
a f.p. of 21 to 55°C, and a b.p. over 50°C
639 Gutta-percha, in flammable liq., n.i.l., with
a f.p. of 0°C to below 21°C and a b. p over 50°C.
638 Gutta-percha, in flammable liq., n.i.l., with
No.
144
150
A II
A II
0,04
AI
AI
A II
A III
A III
A II
AI
5
class
0,82
0,82
0,68
0,82
6
kg/l
Danger Density
0,2
98
153
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
AC
AC
A
A
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
91
U
U
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1993 1993 1993 2279 2646 2458
650 cis-3-heptene
651 trans-2-heptene
652 trans-3-heptene
653 Hexachlorobutadiene
654 Hexachlorocyclopentadiene
655 Hexadiene, isomer mixture, with a f.p. of
92
657 1,2-hexadiene
below -18°C
656 Hexadiene, isomer mixture, with a f.p.
2458
2458
1993
649 cis-2-heptene
-18 to 21°C
1993
648 3-heptene, mixture of cis and trans forms
2
1 2278
UNNo.
Liquid
647 1-heptene
No.
EN 12285-1:2003 (E)
76
0,51
AI
AI
0,72
AI
1,72
215
0,7
0,7
0,7
239
AI
AI
AI
0,71
0,7
6
kg/l
1,68
0,21
0,2
0,21
AI
AI
AI
5
class
Danger Density
96
98
96
0,2
98
0,23
4
mbar
at 50°C
Vapour pressure
94
3
°C
Boiling point
Table B.2 (continued)
---+++
---+++
---+++
++++++
++++++
---+++
---+++
---+++
---+++
---+++
---+++
7
N
N
N
AC
AC
N
N
N
N
N
N
8
conditions
A B C D E F
++++++
++++++
++++++
------
------
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
E
E
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
2458
660 2,4-hexadiene, mixture of cis and trans
2458 2401 1207 1993 2281 2493 1208 1208 2282
661 trans-1,3-hexadiene
662 Hexahydropyridine
663 Hexaldehyde
664 1,1,1,3,3,3-hexamethyldisilazane
665 Hexamethylene diisocyanate
666 Hexamethyleneimine
667 Hexane, isomer mixture
668 n-hexane
669 Hexanol
isomers
2458
659 1,5-hexadiene
isomers
2458
UNNo.
Liquid
658 1,4-hexadiene, mixture of cis and trans
No.
149
AI A III
AI
B
AI
A II
B
AI
AI
AI
AI
5
0,83
0,66
0,67
0,88
1,05
0,78
0,82
0,86
0,71
0,69
6
kg/l
Danger Density class
0,56
69
0,05
0,08
0,07
0,14
139
250
126
129
106
0,51
73
0,81
60
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
---+++
---+++
---+++
---+++
7
BC
A
A
AC
BG
N
N
N
N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
---+++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
BCT
T
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
---+++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
11
93
B
D
BCT
T
D
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
94
hydrazine
677 Hydrazine, aq. soln., ctg. over 64% of
hydrazine
676 Hydrazine, aq. soln., ctg. 64% of
hydrazine
675 Hydrazine, aq. soln., ctg. 51% of
64% of hydrazine
674 Hydrazine, aq. soln., ctg. over 36% up to
hydrazine
673 Hydrazine, aq. soln., ctg. 36% max. of
2029
2030
2030
2030
2030
2030
672 Hydrazine, aq. soln., ctg. 15% of
hydrazine
2029
671 Hydrazine, anhydrous
2
1 2370
UNNo.
Liquid
670 1-hexene
No.
EN 12285-1:2003 (E)
0,09
0,65
114
64
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
A II
A II
A II
A II
A III
AI
AI
5
1,01
0,68
6
kg/l
Danger Density class
Table B.2 (continued)
------
------
------
------
------
------
------
---+++
7
N
8
conditions
A B C D E F
---+++
---+++
---+++
---+++
---+++
---+++
---+++
++++++
9
A B C D E F
Qualifying Group of tank
K1N
K1N
K1N
K1N
K1N
K1N
K1N
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
0 0 0 0 0 0
------
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
-18°C and a b.p. over 50°C
684 Hydrocarbons, u.o.n., with a f.p. below
-18°C and a b.p. over 35°C
683 Hydrocarbons, u.o.n., with a f.p. below
-18°C and a b.p. of 35°C max.
1993
1993
682 Hydrocarbons, u.o.n., with a f.p. below
1993
1993
1993
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
681 Hydrocarbons, u.o.n., with a f.p. over 61 up to 100°C and a b.p. over 100°C
up to 61°C and a b.p. over 100°C
680 Hydrocarbons, u.o.n., with a f.p. over 55
55°C and a b.p. over 100°C
679 Hydrocarbons, u.o.n., with a f.p. of 21 to
to below 21°C and a b.p. over 50°C
1993
UNNo.
Liquid
678 Hydrocarbons, u.o.n., with a f.p. of -18
No.
AI
AI
AI
A III
A III
A II
AI
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B1
B1
B1
B1
B1
B1
B1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
95
B1
B1
B1
B1
B1
B1
B1
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
96
below -18°C and a b.p. of 35°C max.
690 Hydrocarbon mixture, u.o.n., with a f.p.
over 61 up to 100°C and a b.p. over 100°C
689 Hydrocarbon mixture, u.o.n., with a f.p.
100°C
over 55 up to 61°C and a b.p. over
688 Hydrocarbon mixture, u.o.n., with a f.p.
of 21 to 55°C and a b.p. over 100°C
687 Hydrocarbon mixture, u.o.n., with a f.p.
50°C
of -18 to below 21°C and a b.p. over
686 Hydrocarbon mixture, u.o.n., with a f.p.
u.o.n., with a f.p over 100°C
1993
1993
1993
1993
UNNo.
Liquid
685 Hydrocarbons, not toxic and corrosive,
No.
EN 12285-1:2003 (E)
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
A III
A III
A II
AI
5
6
kg/l
Danger Density class
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B1
B1
B1
B1
B1
B1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
11
B1
B1
B1
B1
B1
B1
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
2662 1760 1148 2821 2839 2810
695 N-(2-hydroxethyl)ethylenediamine
696 4-hydroxy-4-methyl-2-pentanone
697 Hydroxybenzene, aq. soln., not alkaline
698 3-hydroxybutanal
699 3-hydroxypropionitrile
1993
694 Hydroquinone, aq. soln.
corrosive, u.o.n., with a f.p. over 100°C
693 Hydrocarbon mixture, not toxic and
below -18°C and a b.p. over 50°C
692 Hydrocarbon mixture, u.o.n., with a f.p.
below -18°C and a b.p. over 35°C
1993
UNNo.
Liquid
691 Hydrocarbon mixture, u.o.n., with a f.p.
No.
228
182
1,11 1,04
0,94
168
A III
1,04
244
6
kg/l
AI
AI
5
class
Danger Density
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
Table B.2 (continued)
++++++
++++++
------
++++++
++++++
------
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
A
AC
8
conditions
A B C D E F
++++++
++++++
------
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B1
B1
B1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
97
BH6
B1
B1
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1213 2527 1212 1214 2709 2393 1920 2528 2486 1993 2283
702 Isobutyl acetate
703 Isobutyl acrylate, stabilized
704 Isobutyl alcohol
705 Isobutylamine
706 Isobutylbenzene
707 Isobutyl formate
708 Isobutylisoamyl
709 Isobutyl isobutyrate
710 Isobutyl isocyanate
711 Isobutyl isovalerate
712 Isobutyl methacrylate, stabilized
98
1208
701 Isohexane
from 21 to 55°C
1993
UNNo.
Liquid
700 Isodecane, isomer mixture, with a f.p.
No.
EN 12285-1:2003 (E)
155
171
102
142
135
98
173
66
108
133
117
A II
A II
0,03
AI
A II
A II
AI
A II
B
A II
A II
AI
AI
A II
5
0,89
0,87
0,89
0,88
0,71
0,89
0,87
0,74
0,81
0,9
0,87
0,66
6
kg/l
Danger Density class
0,15
0,03
0,06
0,19
0,02
0,55
0,08
0,14
0,09
0,73
60
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
--+--+
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
7
CM
AC
AC
A
AC
EC
BG
BC
CM
AC
A
A
8
conditions
A B C D E F
--+--+
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
M
BCT
C1
AC1
B
B
C1M
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
--+--+
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
11
M
BCT
B
M
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2530 2284 2810 2286 2287
716 Isobutyric anhydride
717 Isobutyronitrile
718 3-isocyanatotoluene
719 Isododecane
720 Isoheptene, isomer mixture, with a f.p. of
50°C max.
722 Isohexene, isomer mixture, with a b.p. of
below -18°C
721 Isoheptene, isomer mixture, with a f.p.
2288
2287
2529
715 Isobutyric acid
-18 to below 21°C
2045
714 Isobutyraldehyde
2
1 2394
UNNo.
Liquid
713 Isobutyl propionate
No.
0,04
150
AI
AI
AI
A II
A III
189
AI
A III
A II
AI
A II
5
class
0,75
1,06
0,96
0,96
0,79
0,87
6
kg/l
Danger Density
0,08
0,02
0,63
0,07
4
mbar
at 50°C
Vapour pressure
183
155
65
137
3
°C
Boiling point
Table B.2 (continued)
---+++
---+++
---+++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
------
++++++
7
N
N
N
A
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
---+++
++++++
0 0 0 0 0 0
--+--+
---+++
++++++
9
A B C D E F
Qualifying Group of tank
BCT
H
CN
A
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
---+++
++++++
++++++
++++++
---+++
++++++
11
99
BCT
N
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1216 1265 2371 1104
725 Isooctene
726 Isopentane
727 Isopentene, isomer mixture
728 Isopentyl acetate, mixture of 2- and 3-
2341 2620 1107 1109 1113
730 Isopentyl bromide
731 Isopentyl butyrate
732 Isopentyl chloride
733 Isopentyl formate
734 Isopentyl nitrite, pure
100
1105
729 Isopentyl alcohol
methylbutyl acetate
1177
724 Isohexyl acetate
over 50°C
2288
UNNo.
Liquid
723 Isohexene, isomer mixture, with a b.p.
No.
EN 12285-1:2003 (E)
0,08
AI
A II
AI
A III
0,22
A II
A II
A II
AI
AI
0,09
124
99
179
121
0,04
131
2,06
AI
28
102
A II
AI
5
0,88
0,87
0,87
1,26
0,81
0,62
0,72
0,88
6
kg/l
Danger Density class
162
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
0 0 0 0 0 0
++++++
--+--+
++++++
++++++
++++++
++++++
---+++
++++++
---+++
++++++
---+++
7
AC
ACH2
AC
AC
ABC
AC
AN
A
N
AC
N
8
conditions
A B C D E F
++++++
++++++
------
++++++
------
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
A
B
C1
A
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
------
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A
A
B
A
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2290 1218 1219 2403 1220 1219 1221 2405 2356 2284 2561 1281 1993
736 Isophorone diisocyanate
737 Isoprene, stabilized
738 Isopropanol
739 Isopropenyl acetate
740 Isopropyl acetate
741 Isopropyl alcohol
742 Isopropylamine
743 Isopropyl butyrate
744 Isopropyl chloride
745 Isopropyl cyanide
746 Isopropylethylene
747 Isopropyl formate
748 4-isopropylheptane
2
1 2289
UNNo.
Liquid
735 Isophoronediamine
No.
159
68
0,03
0,53
2,71
20
1,61
0,07
2,1
0,24
0,26
0,22
0,24
1,72
A II
AI
AI
AI
AI
AI
B
B
AI
AI
B
AI
0,75
0,87
0,64
0,87
0,86
0,69
0,79
0,87
0,92
0,79
0,69
1,06
6 0,92
5
kg/l
Danger Density class
35
130
32
82
88
97
82
34
280
247
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
---+++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
0 0 0 0 0 0
0 0 0 0 0 0
7
A
AC
AN
AC
AC
BG
C
AC
AC
C
AN
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
++++++
9
A B C D E F
Qualifying Group of tank
C1
C1
N
BCT
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
++++++
11
101
C
N
BCT
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2046 1222 2409 1223 1223 1223
751 4-isopropylmethylbenzene
752 Isopropyl nitrate
753 Isopropyl propionate
754 Kerosine
755 Kerosine, with a f.p. of 21 to 55°C
756 Kerosine, with a f.p. over 55 up to 61°C
102
35°C max. and a p(50) of 3 bar max.
759 Ligroin, with a f.p. below -18°C, a b.p. of
and a b.p. over 50°C
758 Ligroin, with a f.p. of -18 to below 21°C
and a b.p. over 35°C
757 Ligroin, with a f.p. of -18 to below 21°C
2483
750 Isopropyl isocyanate
2
1 2406
UNNo.
Liquid
749 Isopropyl isobutyrate
No.
EN 12285-1:2003 (E)
0,14
AI
AI
AI
A III
A II
A II
a ii
AI
A II
0,16
AI
AI
5
0,87
1,04
0,86
0,88
0,84
6
kg/l
Danger Density class
0,39
0,13
109
101
176
75
119
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
7
A
A
A
A
A
AC
AC
A
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
9
A B C D E F
Qualifying Group of tank
C1
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
11
BCT
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
2679
763 Lithium hydroxide, aq. soln., ctg. not
2052 1229 2396 2531 2614 1230
764 dl-p-mentha-1,8-diene, isomer mixture
765 Mesityl oxide
766 Methacrylaldehyde, stabilized
767 Methacrylic acid, stabilized
768 Methallyl alcohol
769 Methanol
more than 11% of LiOH
2052
762 dl-limonene, isomer mixture
b.p. over 50°C
761 Ligroin, with a f.p. below -18°C and a
b.p. over 35°C
760 Ligroin, with a f.p. below -18°C and a
No.
65
115
161
69
130
0,56
0,11
0,54
0,07
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
B
A II
B
A II
A II
A II
AI
AI
5
class
0,8
0,86
1,02
0,85
0,86
6
kg/l
Danger Density
Table B.2 (continued)
++++++
++++++
--+--+
0 0 0 0 0 0
++++++
------
------
------
++++++
++++++
7
EC
AM
A
A
8
conditions
A B C D E F
++++++
++++++
--+--+
-----+
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
M
MN
H5
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
--+--+
-----+
++++++
++++++
++++++
++++++
++++++
++++++
11
103
M
MN
H5
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1188 1189 2810 2431 2708 1231 1848
773 2-methoxyethanol
774 2-methoxyethyl acetate
775 m-methoxyaniline
776 o-methoxyaniline
777 Methoxybutyl acetate
778 Methyl acetate
779 Methylacetic acid, pure, 99,8% min.
104
below 80% of pure acid
780 Methylacetic acid, aq. soln., ctg. 50 to
2293
1993
772 4-methoxy-4-methylpentan-2-one
up to 61°C
771 Methanol, aq. soln., with a f.p. over 55
55°C
1993
UNNo.
Liquid
770 Methanol, aq. soln., with a f.p. of 21 to
No.
EN 12285-1:2003 (E)
0,03
0,77
B
A III
1
0,93
0,96
1,09
0,03
1,1
0,97
1
6
1,01
A III
A II
5
kg/l
Danger Density class
0,05
0,07
141
57
166
225
251
145
125
147
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
------
------
++++++
++++++
------
------
++++++
++++++
++++++
++++++
++++++
7
C
AC
A
AC
8
conditions
A B C D E F
------
------
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
--+--+
0 0 +0 0 +
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
H
H3
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
1919 1235
786 Methyl acrylate, stabilized
787 Methylamine, 40% aq. soln.
methanol, methyl acetate and acetone 0,35
80
785 Methylacetone, anhydrous mixture of
170
1848
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
784 Methyl acetoacetate
min. of pure acid, with a f.p. over 61°C
783 Methylacetic acid, aq. soln., ctg. 80%
max.
min. of pure acid, with a f.p. of 61°C
782 Methylacetic acid, aq. soln., ctg. 80%
50% of pure acid 1848
UNNo.
Liquid
781 Methylacetic acid, aq. soln., ctg. less than
No.
B
AI
AI
A III
5
0,96
1,08
6
kg/l
Danger Densit y class
Table B.2 (continued)
++++++
--+--+
++++++
--+--+
------
------
------
BG
M
C
CH
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
--+--+
++++++
++++++
------
------
--+--+
9
A B C D E F
Group of tank
B
M
C1
C
H2
10
conditions
Qualifying
1.4306, 1.4541
Material No.
Qualifying
++++++
--+--+
++++++
++++++
0 0 +0 0 +
0 0 +0 0 +
++++++
11
105
D
M
C
H3
H3
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1708 1708 1708 2938
793 Methylaniline, isomer mixture, liq.
794 2-methylaniline, liq.
795 3-methylaniline, liq.
796 Methyl benzoate
106
2294
1235
1235
2924
792 N-methylaniline
40% min. and a f.p. of -18°C min.
791 Methylamine, aq. soln., with a conc. of
40% max.
790 Methylamine, aq. soln., with a conc. of
-18°C and a b.p. over 35°C
789 Methylamine, aq. soln., with a f.p. below
of 3 bar max.
-18°C, a b.p. of 35°C max. and a p(50)
2924
UNNo.
Liquid
788 Methylamine, aq. soln., with a f.p. below
No.
EN 12285-1:2003 (E)
A III A III A III
199
203
200
A III
A III
B
B
B
B
5
1,09
1
1
0,99
6
kg/l
Danger Density class
195
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
E
G
BG
BG
BG
BG
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
D
D
D
D
D
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1111 1105 1105 1105 1105 1105
799 3-methyl-1-butanethiol
800 1-methyl-1-butanol
801 2-methyl-1-butanol
802 2-methyl-2-butanol
803 3-methyl-1-butanol
804 3-methyl-1-butanol, ctg. fractions of 2,2-
1105 2397 2459 2460 2561
805 3-methyl-2-butanol
806 3-methyl-2-butanone
807 2-methyl-1-butene
808 2-methyl-2-butene
809 3-methyl-1-butene
dimethyl-1-propanol
1111
798 2-methyl-2-butanethiol
2
1 1111
UNNo.
Liquid
797 2-methyl-1-butanethiol
No.
20
39
31
94
113
129
131
102
128
119
2,71
1,51
1,85
0,23
0,04
0,05
0,04
0,11
0,05
0,05
0,13
118
0,13
118
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
AI
AI
AI
A II
A II
A II
B
A II
A II
AI
AI
AI
5
0,64
0,67
0,66
0,81
0,82
0,81
0,81
0,81
0,82
0,81
0,84
0,85
6
kg/l
Danger Density class
Table B.2 (continued)
---+++
---+++
---+++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
0 0 +0 0 +
0 0 +0 0 +
0 0 +0 0 +
7
AN
AN
AN
ABC
ABC
ABC
ABC
ABC
ABC
AH3
AH3
AH3
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
107
B
B
B
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1106 1106 1106 2620 1113 2924 1237 2398 2295 2296 2297 2297
812 2-methylbutylamine
813 3-methylbutylamine
814 2-methyl-2-butylamine
815 3-methylbutyl butyrate
816 3-methylbutyl nitrite, pure
817 3-methyl-2-butylamine
818 Methyl butyrate
819 Methyl-tert-butyl ether
820 Methyl chloroacetate
821 Methylcyclohexane
822 2-methylcyclohexanone
823 3-methylcyclohexanone
108
1106
811 1-methylbutylamine
2
1 1105
UNNo.
Liquid
810 2-methylbutan-2-ol
No.
EN 12285-1:2003 (E)
169
162
101
130
55
102
82
AI A II A II
A II
AI
AI
B
0,21
0,06
0,92
0,15
0,41
AI
A III
179
B
B
B
B
B
0,28
0,28
0,28
0,11
5
0,92
0,93
0,77
1,24
0,76
0,9
0,76
= 0,89
0,87
0,75
0,75
0,74
0,74
0,81
6
kg/l
Danger Density class
0,48
77
95
95
92
102
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
7
A
C
G
AC
G
G
G
G
ABC
8
conditions
A B C D E F
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
A
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
AC
D
A
D
D
D
D
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2298 2381 1593 2288 1993 1920 1193 1262 1262 2300 1243
826 Methylcyclopentane
827 Methyldithiomethane
828 Methylene chloride
829 3-methylenepentane
830 2-methyl-4-ethylhexane
831 3-methyl-4-ethylhexane
832 Methyl ethyl ketone
833 2-methyl-3-ethylpentane
834 3-methyl-2-ethylpentane
835 2-methyl-5-ethylpyridine
836 Methyl formate
4-methylcyclohexanone
2297
825 Methylcyclohexanone, mixture of 3- and
2
1 2297
UNNo.
Liquid
824 4-methylcyclohexanone
No.
32
178
118
116
80
140
134
65
40
110
B
A III
1,95
AI
AI
AI
A II
AI
AI
AI
AI
0,11
0,12
0,38
0,05
0,06
0,7
1,45
0,13
0,5
72
A II
169 A II
5
0,98
0,92
0,73
0.72
0,81
0,74
0,72
0,7
1,34
1,06
0,75
0,92
6
kg/l
Danger Density class
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
0 0 0 0 0 0
++++++
++++++
---+++
++++++
++++++
---+++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
7
C
A
A
N
A
A
N
AC
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
11
109
ACH1
B
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1262 1206 1206 2302 2287 2287 1993 1245 1993 2477 2400 1993
839 4-methylheptane
840 2-methylhexane
841 3-methylhexane
842 5-methyl-2-hexanone
843 2-methyl-1-hexene
844 3-methyl-1-hexene
845 Methyl-2-hydroxypropionate
846 Methyl isobutyl ketone
847 Methyl isopropyl ether
848 Methyl isothiocyanate, liq.
849 Methyl isovalerate
850 Methyl lactate
110
1262
838 3-methylheptane
2
1 1262
UNNo.
Liquid
837 2-methylheptane
No.
EN 12285-1:2003 (E)
144
116
118
32
116
144
84
91
144
91
90
118
119
118
0,03
0,1
0,1
2,11
0,1
0,03
0,33
0,23
0,05
0,26
0,28
0,1
0,1
0,1
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
AI
A II
AI
AI
A II
AI
AI
A II
AI
AI
AI
AI
AI
5
1,09
0,88
1,07
0,74
0,8
1,09
0,69
0,7
0,81
0,69
0,68
0,72
0,71
0,7
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
++++++
------
++++++
---+++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
7
AC
AC
A
AC
N
N
AC
A
A
A
A
R
8
conditions
A B C D E F
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
AC1
C1
AC1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
C1
ET
C1
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
1993 1920 1920 1920
857 2-methyloctane
858 3-methyloctane
859 4-methyloctane
2535
2535
2535
2535
856 2-methylnonane
min.
855 N-methylmorpholine, with a f.p. of 21°C
min.
854 4-methylmorpholine, with a f.p. of 21°C
21°C
853 N-methylmorpholine, with a f.p. below
21°C
852 4-methylmorpholine, with a f.p. below
stabilized
1247
UNNo.
Liquid
851 Methyl methacrylate, monomeric,
No.
142
144
143
167
114
114
113
113
101
0,05
0,08
0,08
0,03
0,1
0,1
0,1
0,1
0,18
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
A II
A II
A II
A II
A II
AI
AI
AI
5
0,72
0,72
0,71
0,74
0,92
0,92
0,92
0,92
0,95
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
7
A
A
A
A
BG
BG
BG
BG
AM
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
9
A B C D E F
Qualifying Group of tank
B
B
B
B
M
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
11
111
D
D
D
D
M
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1208 2367 1993 2288 2288 2288 2288 2288 2288 1229 1233 1709
862 3-methylpentane
863 2-methylpentanal
864 Methyl pentanoate
865 2-methyl-1-pentene
866 2-methyl-2-pentene
867 3-methyl-1-pentene
868 3-methyl-2-pentene, cis/trans mixture
869 4-methyl-1-pentene
870 4-methyl-2-pentene, cis/trans mixture
871 4-methyl-3-pentene-2-one
872 4-methylpentyl-2-acetate
873 4-methyl-1,3-phenylenediamine, liq.
112
1208
861 2-methylpentane
2
1 1280
UNNo.
Liquid
860 Methyloxirane, stabilized
No.
EN 12285-1:2003 (E)
0,04
146
0,07
130
0,9
54
0,9
0,64
54
67
0,7
62
0,1
0,66
0,73
1,71
118
63
60
34
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
A II
AI
AI
AI
AI
AI
AI
A II
AI
AI
AI
AI
5
0,86
0,86
0,67
0,67
0,69
0,69
0,81
0,67
0,66
0,84
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
---+++
---+++
---+++
---+++
---+++
---+++
++++++
++++++
++++++
++++++
-----+
7
AE
AC
N
N
N
N
N
N
AC
AC
A
A
EK1MN
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
9
A B C D E F
Qualifying Group of tank
EMN
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
11
EMN
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
1993 1993 1993 2347 2347 1120 1248 2612 1249 1249 2313 2313 2313
875 2-methylpiperidine
876 3-methylpiperidine
877 4-methylpiperidine
878 2-methyl-1-propanethiol
879 2-methyl-2-propanethiol
880 2-methyl-2-propanol
881 Methyl propionate
882 Methyl propyl ether
883 Methyl propyl ketone, pure
884 Methyl propyl ketone, technical
885 2-methylpyridine
886 3-methylpyridine
887 4-methylpyridine
2
1 2399
UNNo.
Liquid
874 1-methylpiperidine
No.
145
144
0,06
0,06
0,06
128
0,1
1,49
0,35
0,25
0,65
0,28
0,07
0,08
0,11
0,15
102
39
80
83
64
88
125
126
118
106
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
A II
AI
AI
AI
AI
AI
AI
AI
B
B
B
B
5
0,96
0.96
0,95
0,82
0,74
0,92
0,79
0,82
0,84
0,84
0,85
0,84
0,82
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
------
++++++
++++++
++++++
++++++
7
A
C
BC
G
G
G
G
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
113
B
D
D
D
D
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1271 2057
891 Mineral spirit, A type
892 C9-monoolefin mixture, with a f.p. of -18
2077 1650 2810
895 1-naphthylamine, liq.
896 2-naphthylamine, liq.
897 alpha-naphthyl isocyanate
114
-18°Cand a b.p. over 35°C
898 Natural gas condensate, with a f.p. below
2054
894 Morpholine
to 55°C
893 C9-monoolefin mixture, with a f.p. of 21
2057
2403
890 1-methylvinyl acetate
to below 21°C
2367
889 2-methylvaleraldehyde
2
1 2303
UNNo.
Liquid
888 alpha-methylstyrene, stabilized
No.
EN 12285-1:2003 (E)
1,18
269
1,06
306
AI
1,13
299
0,7
0,92
0,81
0,91
6
1,01
A II
A II
AI
AI
AI
AI
A II
5
kg/l
Danger Density class
0,06
128
0,76
0,22
0,1
0,03
60
97
118
165
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
------
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
--+--+
7
ACS
AC
AC
CM
8
conditions
A B C D E F
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
9
A B C D E F
Qualifying Group of tank
BC
BCT
M
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
--+--+
11
BC
BCT
M
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
1796
904 Nitrating acid, mixtures, ctg. over 30% up
sulfuric acid
to 40% of nitric acid and up to 70% of
1658
903 Nicotine sulfate, aq. soln., 40% max.
and a b.p. over 50°C
902 Natural gasolene, with a f.p. below -18°C
and a b.p. over 35°C
901 Natural gasolene, with a f.p. below -18°C
3 bar max.
and a b.p.of 35°C max. and a p(50) of
900 Natural gasolene, with a f.p. below -18°C
-18°C and a b.p. over 50°C
899 Natural gas condensate, with a f.p. below
No.
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
AI
AI
AI
AI
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
7
ACS
ACS
ACS
ACS
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
BC
BC
BC
BC
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
11
115
BC
BC
BC
BC
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
116
sulfuric acid, and 15% max. of water
to 60% of nitric acid, 25% min. of
909 Nitrating acid, mixtures, ctg. over 50 up
8% of nitric acid and sulfuric acid
908 Nitrating acid, mixtures, ctg. over 5 up to
sulfuric acid
to 50% of nitric acid and 30% max. of
907 Nitrating acid, mixtures, ctg. over 40% up
sulfuric acid and 5% max. of water
to 50% of nitric acid, over 15% of
906 Nitrating acid, mixtures, ctg. over 30 up
to 50% of nitric acid and sulfuric acid
1796
1796
1796
1796
1796
UNNo.
Liquid
905 Nitrating acid, mixtures, ctg. over 30 up
No.
EN 12285-1:2003 (E)
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
5
class
6
kg/l
Danger Density
Table B.2 (continued)
------
------
0 0 0 0 0 0
------
------
7
8
conditions
A B C D E F
--+--+
------
++++++
--+--+
--+--+
9
A B C D E F
Qualifying Group of tank
H2
H2
H2
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
--+--+
++++++
++++++
++++++
11
H2
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
sulfuric acid
30% of nitric acid and 80% max. of
914 Nitrating acid, mixtures, ctg. over 8 up to
30% of nitric acid and sulfuric acid
913 Nitrating acid, mixtures, ctg. over 8 up to
to 90% nitric acid and sulfuric acid
912 Nitrating acid, mixtures, ctg. over 50 up
sulfuric acid
to 80% of nitric acid and 30% max. of
911 Nitrating acid, mixtures, ctg. over 50 up
acid, and 5% max. of water
to 80% nitric acid, 15% max. of sulfuric
1796
1796
1796
1796
1796
UNNo.
Liquid
910 Nitrating acid, mixtures, ctg. over 50 up
No.
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
------
------
0 0 0 0 0 0
------
7
8
conditions
A B C D E F
++++++
--+--+
--+--+
++++++
--+--+
9
A B C D E F
Qualifying Group of tank
H2
H2
H2
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
11
117
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
118
and 20% max. of water
of nitric acid, 50% min. of sulfuric acid
918 Nitrating acid, mixtures, ctg. 30% max.
and 25% max. of water
of nitric acid, 65% min. of sulfuric acid
917 Nitrating acid, mixtures, ctg. 10% max.
sulfuric acid
to 97% of nitric acid and 3% min. of
916 Nitrating acid, mixtures, ctg. over 95 up
acid
to 95% nitric acid and 5% min of sulfuric
1796
1796
1796
1796
UNNo.
Liquid
915 Nitrating acid, mixtures, ctg. over 90 up
No.
EN 12285-1:2003 (E)
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
5
class
1,76
6
kg/l
Danger Density
Table B.2 (continued)
------
------
------
------
7
8
conditions
A B C D E F
0 0 0 0 0 0
0 0 0 0 0 0
------
--+--+
9
A B C D E F
Qualifying Group of tank
H2
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
0 0 0 0 0 0
0 0 0 0 0 0
--+--+
++++++
11
H2
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
2031 1661 1662 1663 2608 2608 2608 1664 1664 1664 1665
920 Nitric acid with 65% max. of pure acid
921 Nitroanilines, isomer mixture, liq.
922 Nitrobenzene
923 Nitrophenol, isomer mixture, melted
924 Nitropropane, isomer mixture
925 1-nitropropane
926 2-nitropropane
927 Nitrotoluene, isomer mixture, liq.
928 2-nitrotoluene, liq.
929 3-nitrotoluene, liq.
930 Nitroxylene, isomer mixture, liq.
sulfuric acid and 15% max. of water
to 50% of nitric acid, 25% min. of
1796
UNNo.
Liquid
919 Nitrating acid, mixtures, ctg. over 30% up
No.
232
A III
A III
222
A III
A II
A II
0,16
0,06
120
131
A II
1,16
1,16
0,99
1
1,2
211
A III
6
5
kg/l
Danger Density class
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
------
------
7
C
C
C
C
A
A
A
AH6K4
A
AH6
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
9
A B C D E F
Qualifying Group of tank
BH8K4
BH6
E
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
11
119
BH8K4
BH6
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1665 1665 1920 1920
934 4-nitro-2-xylene, liq.
935 4-nitro-3-xylene, liq.
936 n-Nonane
937 Nonane, isomer mixture, with a f.p. of 21
120
941 n-octane
1262
1262
940 Octane, isomer mixture, with a f.p. of -12
to 12°C
2309
939 1,7-octadiene
21°C
938 Nonane, isomer mixture, with a f.p. below
1993
1665
933 3-nitro-2-xylene, liq.
to 31°C
1665
932 2-nitro-3-xylene, liq.
2
1 1665
UNNo.
Liquid
931 Nitro-4-xylene, liq.
No.
EN 12285-1:2003 (E)
126
= 99
= 116
A
AI
0,08
AI
AI
A II
0,7
0,72
1,13
A II
1,14
0,03
1,14
1,11
A III
6 1,13
5
kg/l
Danger Density class
151
244
244
245
225
241
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
A
A
A
A
A
A
C
C
C
C
C
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
f.p. over 61°C and a b.p. over 100°C
active substance, in solvents, n.i.l., with a
948 Parathion-methyl with more than 12% of
f.p. of 21 to 61°C and a b.p. over 50°C
active substance, in solvents, n.i.l., with a
947 Parathion-methyl, ctg. more than 12% of
61°C
946 C12-olefin mixture , with a f.p. over 55 to
3018
3017
2850
2850
945 C12-olefin mixture , with a f.p. of 21 to
55°C
1216
944 iso-octene
= 100
= 100
102
162
2271
3
943 3-octanone
2
1
°C
Boiling point
195
UNNo.
Liquid
942 1-octanol
No.
A II
A III
A II
A III
AI
A II
A III
0,06
5
class
0,72
0,82
0,83
6
kg/l
Danger Density
4
mbar
at 50°C
Vapour pressure
Table B.2 (continued)
------
------
0 0 0 0 0 0
0 0 0 0 0 0
---+++
++++++
++++++
7
N
AC
BC
8
conditions
A B C D E F
--+--+
--+--+
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
HU
HU
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
--+--+
--+--+
++++++
++++++
++++++
++++++
++++++
11
121
HU
HU
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1669 2401 2058 1265 2810 2310
952 Pentachloroethane
953 Pentamethyleneimine
954 Pentanal
955 n-pentane
956 Pentanedial, aq. soln., with a f.p. over 61°C
957 2,4-pentanedione
122
3017
3018
951 Parathion-methyl, pure, liq.
f.p. over 61°C and a b.p. over 100°C
active substance, in solvents, n.i.l., with a
950 Parathion-methyl, with 1,2% to 12% of
f.p. up to 61°C and a b.p. over 50°C
active substance, in solvents, n.i.l., with a
3017
UNNo.
Liquid
949 Parathion-methyl, with 1,2% to 12% of
No.
EN 12285-1:2003 (E)
0,07
140
1,6
36
0,14
0,03
106
161
200
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
A II
AI
AI
B
A II
A III
A II
5
class
0,98
0,63
0,86
1,68
1,23
6
kg/l
Danger Density
Table B.2 (continued)
------
------
++++++
++++++
++++++
---+++
------
------
------
7
A
C
BG
ACN
8
conditions
A B C D E F
---+++
++++++
++++++
++++++
++++++
------
--+--+
--+--+
--+--+
9
A B C D E F
Qualifying Group of tank
AN
C
A
B
H
HU
HU
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
---+++
++++++
++++++
++++++
++++++
------
--+--+
--+--+
--+--+
11
AN
C
A
D
H
HU
HU
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1111 1111 1111 1111 1105 1105 1105 1249 1249 1108 1104
960 sec-pentanethiol
961 1-pentanethiol
962 2-pentanethiol
963 3-pentanethiol
964 1-pentanol
965 2-pentanol
966 3-pentanol
967 2-pentanone, pure
968 2-pentanone/3-pentanone mix (3:1)
969 1-pentene
970 Pentyl acetate, technical grade, with a
f.p. of -18 to below 21°C
1111
959 Pentanethiol, isomer mixture
2
1 1111
UNNo.
Liquid
958 Pentanethiol, active form
No.
105
0,16
ß950
30
0,1
0,07
0,05
0,03
0,21
0,13
0,08
102
116
119
138
105
113
127
0,13
113
0,13
118
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
AI
AI
AI
A II
A II
A II
AI
AI
AI
AI
AI
AI
5
0,88
0,65
0,82
0,82
0,81
0,82
0,84
0,83
0,86
0,83
0,85
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
---+++
++++++
++++++
++++++
++++++
++++++
0 0 +0 0 +
0 0 +0 0 +
0 0 +0 0 +
0 0 +0 0 +
0 0 +0 0 +
0 0 +0 0 +
7
AC
N
ABC
ABC
ABC
AH3
AH3
AH3
AH3
AH3
AH3
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
C1
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
123
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
124
978 1-pentylamine
of 21 to 55°C
977 Pentylamine, isomer mixture, with a f.p.
of -18 to below 21°C
976 Pentylamine, isomer mixture, with a f.p.
with a f.p. of 21 to 55°C
975 Pentyl alcohol, synthetic isomer mixture,
with a f.p. of 0 to below 21°C
974 Pentyl alcohol, synthetic isomer mixture,
1106
1106
1106
1105
1105
1105
973 Pentyl alcohol, primary, mixture of
pentan-1-ol and 2-methyl-butan-1-ol
1105
972 Pentyl alcohol, optically act.
f.p. of 21 to 55°C
1104
UNNo.
Liquid
971 Pentyl acetate, technical grade, with a
No.
EN 12285-1:2003 (E)
104
0,15
0,05
0,04
4
mbar
at 50°C
Vapour pressure
128
121
3
°C
Boiling point
B
B
B
A II
AI
A II
A II
A II
5
class
0,76
0,82
0,88
6
kg/l
Danger Density
Table B.2 (continued)
++++++
++++++
++++++
------
------
++++++
++++++
++++++
7
G
G
G
ABC
ABC
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
B
B
C1
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
D
D
B
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2841 2620 1107 1107 1993 1109 1112 1113 1993 1266
981 Di-n-pentylamine
982 n-pentyl butyrate
983 Pentyl chloride, active form
984 Pentyl chloride, isomer mixture
985 Di-n-pentyl ether
986 Pentyl formate
987 Pentyl nitrate, isomer mixture
988 n-pentyl nitrite, pure
989 n-pentyl propionate
990 Perfume products, with flammable
0°C and a b.p. over 35°C
solvents, n.i.l., with a f.p. of -18 to below
1106
980 3-pentylamine
2
1 1106
UNNo.
Liquid
979 2-pentylamine
No.
A II
AI A II
165
0,03
169
0,08
130
188
AI
A II
AI
A II
AI
A II
202
B B
0,28
5
0,88
0,89
0,79
0,88
0,78
0,75
0,74
6
kg/l
Danger Density class
0,28
91
92
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
0 0 0 0 0 0
++++++
0 0 0 0 0 0
++++++
++++++
0 0 0 0 0 0
--+--+
--+--+
++++++
++++++
++++++
++++++
7
AC
C
AC
ACH2
ACH2
AC
G
G
G
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
------
------
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
A
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
------
------
++++++
++++++
++++++
++++++
11
125
U
A
D
D
D
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
126
to 61°C and a b.p. over 100°C
solvents, n.i.l., with a f.p. over 55°C up
994 Perfume products, with flammable
and a b.p. over 50°C
solvents, n.i.l., with a f.p. of 21 to 55°C
993 Perfume products, with flammable
21°C and a b.p. over 50°C
solvents, n.i.l., with a f.p. of 0 to below
992 Perfume products, with flammable
below 0°C and a b.p. over 50°C
solvents, n.i.l., with a f.p. of -18°C to
1266
1266
1266
1266
UNNo.
Liquid
991 Perfume products, with flammable
No.
EN 12285-1:2003 (E)
1,100
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
A III
A II
AI
AI
5
class
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
11
U
U
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
1203 1203 1268
998 Petrol, premium plus, SP type, unleaded
999 Petrol, regular, N type, unleaded
1000 Petroleum distillate, u.o.n., with a f.p. of
100°C
over 55°C up to 61°C and a b.p. over
1002 Petroleum distillate, u.o.n., with a f.p.
21 to 55°C and a b.p. over 100°C
1001 Petroleum distillate, u.o.n., with a f.p. of
1268
1268
1203
997 Petrol, premium, S type, unleaded
-18 to below 21°C and a b.p. over 50°C
1203
996 Petrol, premium, S type, leaded
to 100°C and a b.p. over 100°C
solvents, n.i.l., with a f.p. over 61°C up
995 Perfume products, with flammable
No.
AI
40
0,2
AI
40
A III
A II
AI
AI
40
AI
A III
5
0,77
0,79
0,79
0,78
6
kg/l
Danger Density class
40
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
7
CS
CS
CS
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
127
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
128
below 21°C and a b.p. over 50°C
1009 Petroleum ether, with a f.p. of -18 to
below 21°C and a b.p. over 35°C
1008 Petroleum ether, with a f.p. of -18 to
over 100°C, not toxic and not corrosive
1007 Petroleum distillate, u.o.n., with a f.p.
below -18°C and a b.p. over 50°C
1006 Petroleum distillate, u.o.n., with a f.p.
below -18°C and a b.p. over 35°C
1005 Petroleum distillate, u.o.n., with a f.p.
below -18°C and a b.p. of 20 to 35°C
1004 Petroleum distillate, u.o.n., with a f.p.
over 61°C up to 100°C and a b.p. over 100°C
1268
1268
1268
UNNo.
Liquid
1003 Petroleum distillate, u.o.n., with a f.p.
No.
EN 12285-1:2003 (E)
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
AI
AI
AI
AI
A III
5
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
A
A
CS
CS
CS
CS
CS
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
2821 2922
1017 Phenol, aq. soln., not alkaline
1018 Phenol, aq. alkaline soln. with a density of
1,3 kg/l max.
2311
1016 p-phenetidine
250
1,07
1,05
A III
2311
1015 o-phenetidine
233
2311
1014 m-phenetidine
AI
AI
6
kg/l
AI
AI
5
class
Danger Density
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
1013 Petroleum ether, A type
and a b.p. over 50°C
1012 Petroleum ether, with a f.p. below -18°C
and a b.p. over 35°C
1011 Petroleum ether, with a f.p. below -18°C
a b.p. of 35°C max. and a p(50) of 3 bar max.
1010 Petroleum ether, with a f.p. below -18°C,
No.
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
++++++
7
H5
H5
A
A
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
H5
H5
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A B C D E F
Group of tank
129
H5
H5
12
conditions
Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1805
1022 Phosphoric acid, aq. soln., ctg. less than
130
pure acid
1026 Phosphoric acid, aq. soln., ctg. 85% of
pure acid
1025 Phosphoric acid, aq. soln., ctg. 80% of
pure acid
1024 Phosphoric acid, aq. soln., ctg. 75% of
75% of pure acid
1023 Phosphoric acid, aq. soln., ctg. 25% to
1805
1805
1805
1805
2303
1021 2-phenylpropene, stabilized
25% of pure acid
2487
1020 Phenyl isocyanate
1,5 kg/l max.
2922
UNNo.
Liquid
1019 Phenol, aq. alkaline soln. with a density of
No.
EN 12285-1:2003 (E)
0,03
165
0,02
165
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A II
A II
5
0,91
1,1
6
kg/l
Danger Density class
Table B.2 (continued)
------
------
------
------
------
--+--+
0 0 0 0 0 0
++++++
7
CM
H5
8
conditions
A B C D E F
------
------
------
------
------
--+--+
---+++
++++++
9
A B C D E F
Qualifying Group of tank
M
BCT
H5
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
--+--+
---+++
++++++
11
BF
BF
BF
BF
BF
M
BCT
H5
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
2368 2579 2401 2427
1029 2-pinene
1030 Piperazine, 65% aq. soln., melted
1031 Piperidine
1032 Potassium chlorate, aq. soln., with a
1814
1035 Potassium hydroxide, aq. soln., with a
conc. of 50% max.
1036 Potassium hydroxide, aq. soln., with a
1814
1812
1034 Potassium fluoride, aq. soln.
conc. of 20% max.
1680
1033 Potassium cyanide, aq. soln.
conc. of 30% max. of potassium chlorate
1224
1028 Pinacolone
85% of pure acid
1805
UNNo.
Liquid
1027 Phosphoric acid, aq. soln., ctg. more than
No.
0,14
106
0,03
0,11
0,03
155
106
213
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
B
A II
AI
5
1,5
0,86
0,86
0,81
1,88
6
kg/l
Danger Density class
Table B.2 (continued)
0 0 0 0 0 0
++++++
0 0 0 0 0 0
------
------
++++++
++++++
0 0 0 0 0 0
------
------
7
H5
BG
GH5K4
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
--+--+
++++++
++++++
++++++
++++++
------
9
A B C D E F
Qualifying Group of tank
BCH
B
BH5K4
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
131
BC
D
DH5K4
BF
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
1274 1219 1098 1098 2334 1993 1275 1848
1039 1-propanol
1040 2-propanol
1041 2-propen-1-ol, with a f.p. of 21 to below 23°C
1042 2-propen-1-ol, with a f.p. of 23°C min.
1043 2-propenylamine
1044 Propenylidene dichloride
1045 Propionaldehyde
1046 Propionic acid, pure,
132
50% of pure acid
1047 Propionic acid, aq. soln., ctg. less than
2402
1038 2-propanethiol
2
1 2402
UNNo.
Liquid
1037 1-propanethiol
No.
EN 12285-1:2003 (E)
0,03
1,11
0,43
0,93
0,15
0,15
0,24
0,13
0,94
0,56
4
mbar
at 50°C
Vapour pressure
141
49
76
53
97
97
82
97
53
68
3
°C
Boiling point
A II
AI
AI
B
A II
A II
B
B
AI
AI
5
class
1
0,81
1,17
0,76
0,85
0,85
0,79
0,8
0,83
0,85
6
kg/l
Danger Density
Table B.2 (continued)
------
------
------
++++++
--+--+
++++++
++++++
++++++
++++++
------
------
7
AC
GH
EC
EC
C
C
8
conditions
A B C D E F
--+--+
------
---+++
------
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
H2
CN
BH
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
0 0 +0 0 +
---+++
------
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
11
H3
CN
BH
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
2
1
2404 1276 1277 2364 2850
1052 Propionitrile
1053 n-propyl acetate
1054 n-propylamine
1055 n-propylbenzene
1056 Propylene tetramer, with a f.p. of min. 21
up to 55°C
2496
1848
1051 Propionic anhydride
of pure acid, with a f.p. over 61°C
1050 Propionic acid, aq. soln., ctg. 80% min.
of pure acid, with a f.p. of 61°C max.
1049 Propionic acid, aq. soln., ctg. 80% min.
below 80% of pure acid 1848
UNNo.
Liquid
1048 Propionic acid, aq. soln., ctg. 50% to
No.
0,03
1,11
0,16
0,21
159
48
102
97
167
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
A II
A II
B
AI
B
A III
5
class
0,86
0,72
0,89
0,79
1,02
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
------
------
------
7
A
BG
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
------
------
------
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
0 0 +0 0 +
0 0 +0 0 +
--+--+
11
133
B
H3
H3
H
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
2384
1061 Di-n-propyl ether, with a f.p. of -18 to
1282
1064 Pyridine, pure
134
1281
1063 n-propyl formate
-18°C
1062 Di-n-propyl ether, with a f.p. below
2384
1760
1060 n-propylethanolamine
below 21°C
2057
2057
1059 Propylene trimer, with a f.p. of 21 to 55°C
below 21°C
1058 Propylene trimer, with a f.p. of -18 to
up to 61°C
2850
UNNo.
Liquid
1057 Propylene tetramer, with a f.p. of min. 55
No.
EN 12285-1:2003 (E)
114
81
90
90
180
0,11
0,35
0,27
0,27
0,04
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
B
AI
AI
AI
A II
AI
A III
5
class
0,99
0,91
0,75
0,75
0,9
= 1,00
6
kg/l
Danger Density
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
A7
AC
A
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
2656 1866
1068 Quinoline, with a f.p. over 61°C
1069 Resins, in hydrocarbons or alcohols, n.i.l.,
50°C
with a f.p. of 21 to 55°C and a b.p. over
1071 Resins, in hydrocarbons or alcohols, n.i.l,.
over 50°C
with a f.p. of 0 to below 21°C and a b.p.
1070 Resins, in hydrocarbons or alcohols, n.i.l.,
over 35°C
1866
1866
2656
1067 Quinoline, with a f.p. of 61°C max.
with a f.p. of -18 to below 0°C and a b.p.
1922
1066 Pyrrolidine
of methylpyridines
1282
UNNo.
Liquid
1065 Pyridine, technical grade, with admixture
No.
A III
237
A II
AI
AI
A III
237
B
B
0,11
5
1,1
1,1
0,86
0,99
6
kg/l
Danger Density class
0,37
87
115
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
------
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
E
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
11
135
U
U
U
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
136
to 100°C and a b.p. over 150°C
1077 Road asphalt, liq., with a f.p. over 61 up
to 61°C and a b.p. over 150°C
1076 Road asphalt, liq., with a f.p. over 55 up
55°C and a b.p. over 100°C
1075 Road asphalt, liq., with a f.p. of 21 to
below 21°C and a b.p. over 50°C
1074 Road asphalt, liq., with a f.p. of -18 to
b.p. over 100°C
with a f.p. over 61 up to 100°C and a
1073 Resins, in hydrocarbons or alcohols, n.i.l.,
over 100°C
with a f.p. over 55 up to 61°C and a b.p.
1999
1999
1999
1866
UNNo.
Liquid
1072 Resins, in hydrocarbons or alcohols, n.i.l.,
No.
EN 12285-1:2003 (E)
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
A III
A III
A II
AI
A III
A III
5
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
7
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
11
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
below 21°Cand a b.p. over 50°C
1085 Road tar, viscous, with a f.p. of -18 to
1999
1999
1999
1999
1084 Road tar, liq., with a f.p. over 100°C
100°C and a b.p. over 150°C
1083 Road tar, liq., with a f.p over 61 up to
61°C and ab.p. over 150°C
1082 Road tar, liq., with a f.p. over 55 up to
and a b.p. over 100°C
1081 Road tar, liq., with a f.p. of 21 to 55°C
21°C and a b.p. over 50°C
1080 Road tar, liq., with a f.p. of -18 to below
-18°C to below 21°C and a b.p over 50°C
1079 Road asphalt, viscous, with a f.p. of
1999
mbar
°C
1078 Road asphalt, liq., with a f.p. over 100°C
2
1
Vapour pressure at 50°C
Boiling point
4
UNNo.
Liquid
3
No.
AI
A III
A III
A II
AI
AI
5
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
ABC
ABC
ABC
ABC
ABC
ABC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
137
B
B
B
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1819
1093 Sodium-meta-aluminate, aq. soln.
138
2749
1288
1288
1288
1288
1092 Silicon tetramethyl
and a b.p. over 100°C
1091 Shale oil, with a f.p. over 61 to 100°C
and a b.p. over 100°C
1090 Shale oil, with a f.p. over 55 up to 61°C
b.p. over 100°C
1089 Shale oil, with a f.p. of 21 to 55°C and a
a b.p. over 50°C
1088 Shale oil, with a f.p. 0 to below 21°C and
and a b.p. over 50°C
1087 Shale oil, with a f.p. of -18 to below 0°C
and a b.p. over 35°C
1288
UNNo.
Liquid
1086 Shale oil, with a f.p. of -18 to below 0°C
No.
EN 12285-1:2003 (E)
2,21
26
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
A III
A III
A II
AI
AI
AI
5
0,65
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
7
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
max. of NaOH
1101 Sodium hydroxide, aq. soln., ctg. 5%
1824
1719
1100 Sodium hydrogen sulfide, aq. soln., ctg.
30% of NaHS
1690
1689
1908
1686
1099 Sodium fluoride, aq. soln.
of 1,2 kg/l max.
1098 Sodium cyanide, aq. soln. with a density
5% of active chlorine
1097 Sodium chlorite, aq. soln., ctg. more than
than 5% of active chlorine
1096 Sodium chlorite, aq. soln., ctg. not more
1095 Sodium arsenite, aq. soln., toxic
health
1686
UNNo.
Liquid
1094 Sodium arsenite, aq. soln., injurious to
No.
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
5
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
------
------
------
++++++
++++++
7
8
conditions
A B C D E F
++++++
++++++
------
0 0 +0 0 +
------
------
++++++
++++++
9
A B C D E F
Qualifying Group of tank
H3
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
--+--+
0 0 +0 0 +
++++++
++++++
++++++
++++++
11
139
CH1
H3
C2
C2
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
140
with a f.p. of 21 to 61°C
1108 Sodium methoxide, alcoholic soln., n.i.l.,
with a f.p. of -18 to below 21°C
1107 Sodium methoxide, alcoholic soln., n.i.l.,
methanol
1106 Sodium methoxide, soln., 30%, in
max. of NaOH
1105 Sodium hydroxide, aq. soln., ctg. 50%
max. of NaOH
1104 Sodium hydroxide, aq. soln., ctg. 33%
max. of NaOH
1289
1289
1289
1824
1824
1824
1103 Sodium hydroxide, aq. soln., ctg. 20%
2
1 1824
UNNo.
Liquid
1102 Sodium hydroxide, aq. soln., ctg. 10% max. of NaOH
No.
EN 12285-1:2003 (E)
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
B
B
5
class
0,97
6
kg/l
Danger Density
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
---+++
++++++
++++++
++++++
++++++
7
N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
1136
1114 Solvent naphtha, heavy, C10-Ar type,
below 0°C
1116 Solvent naphtha, with a f.p. of -18 to
a f.p. over 61 up to 100°C
1115 Solvent naphtha, heavy, C10-Ar type,with
1256
1136
1113 Solvent naphtha, light, C9-Ar type
with a f.p. over 55 up to 61°C
1849
1289
1289
1112 Sodium sulfide, aq. soln.
with a f.p. of 21 to 61°C
1111 Sodium methylate, alcoholic soln., n.i.l.,
with a f.p. of -18 to below 21°C
1110 Sodium methylate, alcoholic soln., n.i.l.,
methanol
1289
UNNo.
Liquid
1109 Sodium methylate, soln., 30%, in
No.
80
0,37
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
A III
A III
A II
B
B
5
0,88
0,97
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
------
0 0 0 0 0 0
0 0 0 0 0 0
---+++
7
ACS
AC
AC
AC
N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
------
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
141
U
U
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
1271 1271 1271 2055 1830
1121 Special boiling point spirit, 2-A type
1122 Special boiling point spirit, 2-B type
1123 Special boiling point spirit, 3 type
1124 Styrene, monomeric, stabilized
1125 Sulfuric acid, ctg. over 90% up to 92%
142
1126 Sulfuric acid, ctg. over 98% of pure acid
1830
1271
1120 Special boiling point spirit, 1-B type
of pure acid
1271
1256
1119 Special boiling point spirit, 1-A type
55°C
1118 Solvent naphtha, with a f.p. of 21 to
21°C
1256
UNNo.
Liquid
1117 Solvent naphtha, with a f.p. of 0 to below
No.
EN 12285-1:2003 (E)
280
300
0,04
145
0,51
0,51
0,76
0,76
0,37
0,37
4
mbar
at 50°C
Vapour pressure
80
80
60
60
80
80
3
°C
Boiling point
A II
AI
AI
AI
AI
AI
A II
AI
5
class
1,85
1,83
0,91
0,7
0,7
0,68
0,68
0,88
0,88
6
kg/l
Danger Density
Table B.2 (continued)
-++-++
-++-++
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
7
BCM
ACS
ACS
8
conditions
A B C D E F
------
------
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
M
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
0 ++0 ++
0 ++0 ++
--+--+
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
BT1
BT1
M
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
over 61 up to 100°C and a b.p. over 150°C
1132 Tar, in petroleum distillate, liq., with a f.p.
150°C
over 55 up to 61°C and a b.p. over
1131 Tar, in petroleum distillate, liq., with a f.p.
of 21 to 55°C and a b.p. over 100°C
1130 Tar, in petroleum distillate, liq., with a f.p.
50°C
1999
1999
1999
1129 Tar, in petroleum distillate, liq., with a f.p.
of -18 to below 21°C and a b.p. over
1272
1128 Tall oil
acid
1830
UNNo.
Liquid
1127 Sulfuric acid, ctg. 92% to 98% of pure
No.
4
mbar
at 50°C
Vapour pressure
300
3
°C
Boiling point
A III
A III
A II
AI
A III
5
class
1,84
6
kg/l
Danger Density
Table B.2 (continued)
++++++
++++++
++++++
++++++
0 0 0 0 0 0
-++-++
7
ABC
ABC
ABC
ABC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
------
9
A B C D E F
Qualifying Group of tank
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
0 ++0 ++
11
143
B
B
B
B
BT1
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
144
166
1292
1140 Tetraethyl orthosilicate
120
254
1897
2319
2319
0,02
A II
0,93
0,76
0,120
1,200
6
1,63 A III
A III
A III
A II
AI
5
kg/l
Danger Density class
0,1
4
mbar
°C
3
Vapour pressure at 50°C
Table B.2 (continued) Boiling point
1139 n-tetradecane
1138 Tetrachloroethylene
to 100°C and a b.p. over 100°C
1137 Terpenes, u.o.n., with a f.p. over 61 up
61°C and a b.p. over 100°C
1136 Terpenes, u.o.n.,with a f.p. over 55 up to
55°C and a b.p. over 50°C
1135 Terpenes, u.o.n., with a f.p. of 21 to
over 100°C
1134 Tar, in petroleum distillate, liq., with a f.p.
over 50°C
a f.p. of -18 to below 21°C, and a b.p.
1999
UNNo.
Liquid
1133 Tar, in petroleum distillate, viscous, with
No.
EN 12285-1:2003 (E)
++++++
++++++
--+--+
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
7
A
ACH
ABC
ABC
8
conditions
A B C D E F
++++++
++++++
------
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
AC
B
B
B
B
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1262 1993 1993 1993 2749 2413 2785
1146 2,2,3,3-tetramethylbutane
1147 2,2,3,3-tetramethylpentane
1148 2,2,3,4-tetramethylpentane
1149 2,3,3,4-tetramethylpentane
1150 Tetramethylsilane
1151 Tetrapropyl orthotitanate
1152 4-thiapentanal, with a f.p. over 55 up to 61°C
2,21
0,04
0,06
0,05
0,12
A III
A II
AI
AI
AI
AI
AI
AI
A III
0,09
B
AI
A II
5
0,65
0,75
0,74
0,76
0,82
1
0,97
0,89
0,89
6
kg/l
Danger Density class
0,63
26
142
133
140
107
121
2412
1145 Tetrahydrothiophene
64 206
2056
0,63
64
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
1144 Tetrahydronaphthalene
1143 Tetrahydrofuran, with a f.p. below -18°C
below 21°C
2056
1142 Tetrahydrofuran, with a f.p. of -18 to
2
1 2498
UNNo.
Liquid
1141 1,2,3,6-tetrahydrobenzaldehyde
No.
Table B.2 (continued)
------
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
A
A
A
A
A
A
A
A
AC
8
conditions
A B C D E F
7
Qualifying
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Group of tank
B
10
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
A B C D E F
conditions
145
B
12
conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
Qualifying
1.4306, 1.4541
Material No.
EN 12285-1:2003 (E)
2337 1293
1156 Thiophenol
1157 Tinctures, pharmaceutical, in alcoholic
146
and a b.p. over 50°C
solvents, n.i.l., with a f.p. of 21 to 55°C
1159 Tinctures, pharmaceutical, in alcoholic
21°C and a b.p. over 50°C
solvents, n.i.l., with a f.p. of 0 to below
1158 Tinctures, pharmaceutical, in alcoholic
0°C and a b.p. over 50°C
1293
1293
2414
1155 Thiophene
solvents, n.i.l., with a f.p. of -18 to below
1940
1154 Thioglycolic acid
2
1 2785
UNNo.
Liquid
1153 4-thiapentanal, with a f.p. over 61°C
No.
EN 12285-1:2003 (E)
A II
169
B
B
AI
A III
5
class
1,08
1,06
1,33
6
kg/l
Danger Density
0,32
84
200
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
------
++++++
0 0 +0 0 +
------
7
C
AH3
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
0 0 +0 0 +
++++++
9
A B C D E F
Qualifying Group of tank
U
U
U
H3
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
U
U
U
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
2078
1164 2,4-tolylene diisocyanate and isomer
1710 2226
1166 Trichloroethylene
1167 Trichloromethylbenzene
stabilized
1165 Trichloroacetaldehyde, anhydrous,
2075
1709
1163 2,4-tolylenediamine, liq.
mixtures, liq.
1294
1162 Toluene
100°C and a b.p. over 100°C
solvents, n.i.l., with a f.p. over 61 up to
1161 Tinctures, pharmaceutical, in alcoholic
61°C and a b.p. over 100°C
solvents, n.i.l., with a f.p. over 55 up to
1293
UNNo.
Liquid
1160 Tinctures, pharmaceutical, in alcoholic
No.
221
85
1,38
1,51
0,87
6
1,47
AI
5
kg/l
Danger Density class
0,29
98
111
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
0 0 -0 0 +
--+--+
---+++
0 0 0 0 0 0
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
7
CEH3T
ACH
ET
AE
AC
8
conditions
A B C D E F
------
0 0 0 0 0 0
0 0 0 0 0 0
---+++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
BCT
U
U
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
Qualifying
0 0 -0 0 +
++++++
------
---+++
++++++
++++++
++++++
++++++
11
147
CEH3T
AC
EH2
BCT
U
U
12
A B C D E F conditions
Group of tank
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2810 2338 1993 1993 1297 1297
1171 Triethyl phosphate
1172 Trifluoromethylbenzene
1173 Trimethoxymethane
1174 Trimethoxyvinylsilane, stabilized
1175 Trimethylamine, 45% aq. soln.
1176 Trimethylamine, aq. soln., with a conc.
148
over 50% and a p(50) of 3 bar max.
1178 Trimethylamine, aq. soln., with a conc.
30% max. and a b.p. over 35°C
1177 Trimethylamine, aq. soln., with a conc. of
2924
1297
2259
1170 Triethylenetetraamine
over 30% up to 50% and a b.p. of 35°C max.
1296
1169 Triethylamine
2
1 2524
UNNo.
Liquid
1168 Triethoxymethane
No.
EN 12285-1:2003 (E)
0,09
123
0,17
B
B
B
B
A II
B
AI
1,13
1,2
1,07
0,73
0,89
6
0,98
B
A II
5
kg/l
Danger Density class
0,02
0,32
0,03
102
215
260
89
146
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
++++++
++++++
0 0 0 0 0 0
0 0 0 0 0 0
++++++
0 0 0 0 0 0
++++++
++++++
------
7
BG
BG
BG
BG
AC
BG
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
-----+
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
B
B
B
MT
B
A
BC
B
B
B
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
-----+
++++++
++++++
++++++
++++++
++++++
++++++
11
MT
B
A
BC
D
B
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
1993 2325 1206 2287 1993 2328 1993 1920 1920 1920 1993 1262 1262
1180 1,2,4-trimethylbenzene
1181 1,3,5-trimethylbenzene
1182 2,2,3-trimethylbutane
1183 2,3,3-trimethyl-1-butene
1184 2,5,5-trimethylheptane
1185 Trimethylhexamethylene diisocyanate
1186 2,2,5-trimethylhexane
1187 2,3,3-trimethylhexane
1188 2,3,4-trimethylhexane
1189 3,3,4-trimethylhexane
1190 Trimethyl orthoformate
1191 2,2,3-trimethylpentane
1192 2,2,4-trimethylpentane
2
1 1993
UNNo.
Liquid
1179 1,2,3-trimethylbenzene
No.
99
0,21
0,15
110
0,05
0,05
0,06
0,08
0,04
0,42
0,39
0,02
0,02
AI
AI
B
A II
A II
A II
AI
A II
AI
AI
A II
A II
A II
141
139
138
124
200
151
78
81
165
169
176
5
0,69
0,72
0,74
0,74
0,73
0,71
1,01
0,74
0,71
0,7
0,87
0,88
0,88
6
kg/l
Danger Density class
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
Table B.2 (continued)
++++++
++++++
0 0 0 0 0 0
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
---+++
++++++
++++++
++++++
++++++
7
A
A
A
A
A
A
A
N
A
A
A
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
B
BCT
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
---+++
++++++
++++++
++++++
++++++
++++++
++++++
11
149
B
BCT
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2050 2329 1264 1299 1300
1196 2,2,4-trimethyl-2-pentene
1197 Trimethyl phosphite
1198 2,4,6-trimethyl-1,3,5-trioxane
1199 Turpentine
1200 Turpentine spirit, with a f.p. of -18 to
150
to 61°C and a b.p. over 100°C
1202 Turpentine spirit, with a f.p. over 55 up
55°C and a b.p. over 100°C
1201 Turpentine spirit, with a f.p. of 21 to
1300
1300
2050
1195 2,2,4-trimethyl-1-pentene
below 21°C and a b.p. over 50°C
1262
1194 2,3,4-trimethylpentane
2
1 1262
UNNo.
Liquid
1193 2,3,3-trimethylpentane
No.
EN 12285-1:2003 (E)
A III
A II
AI
A II
A II
A II
0,07
AI
AI
AI
AI
5
class
1
1,05
0,72
0,72
0,72
0,73
6
kg/l
Danger Density
0,18
0,23
0,13
0,13
4
mbar
at 50°C
Vapour pressure
124
112
105
101
114
115
3
°C
Boiling point
Table B.2 (continued)
0 0 0 0 0 0
0 0 0 0 0 0
0 0 0 0 0 0
++++++
++++++
++++++
---+++
---+++
++++++
++++++
7
A
C
A
N
N
A
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
UNNo.
2
Liquid
1
1301 1993 1300 1300 1300 1300
1205 Vinyl acetate, stabilized
1206 Vinyltrimethoxysilane, stabilized
1207 White spirit, 1 type
1208 White spirit, 2 type
1209 White spirit, 3 type
1210 White spirit, 4 type, with a f.p. over 55
1300 1230
1212 White spirit, 5 type
1213 Wood alcohol
up to 100°C
1211 White spirit, 4 type, with a f.p. over 61
up to 61°C
2330
1204 Undecane
to 100°C and a b.p. over 100°C
1203 Turpentine spirit, with a f.p. over 61 up
No.
65
130
180
180
150
140
130
123
72
0,56
0,11
0,07
0,07
0,07
0,07
0,11
0,09
0,45
196
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
B
A II
A III
A III
A II
A II
A II
A II
AI
A III
A III
5
0,8
0,75
0,8
0,8
0,75
0,75
0,75
1,13
0,93
0,74
6
kg/l
Danger Density class
Table B.2 (continued)
---+++
++++++
++++++
++++++
++++++
++++++
++++++
0 0 0 0 0 0
++++++
++++++
0 0 0 0 0 0
7
N
C
A
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
MT
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
-----+
++++++
++++++
++++++
11
151
MT
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
2
1
152
to below 21°C
1221 Xylene, isomer mixture, with a f.p. of 1
and toluene, with a f.p. of 21 to 55°C
1220 Xylene, ctg. small fractions of benzene
and toluene, with a f.p. of 0 to below 21°C
1219 Xylene, ctg. small fractions of benzene
and toluene, with a f.p. of -18 to below 0°C
1307
1307
1217 p-xylene
1218 Xylene, ctg. small fractions of benzene
1307
1993
1216 m-xylene
55 up to 61°C
1215 Wood alcohol, aq. soln., with a b.p. over
to 55°C
1993
UNNo.
Liquid
1214 Wood alcohol, aq. soln., with a b.p. of 21
No.
EN 12285-1:2003 (E)
80
80
80
138
139
0,37
0,37
0,37
0,05
0,05
4
mbar
°C
3
Vapour pressure at 50°C
Boiling point
AI
A II
AI
AI
A II
A II
A III
A II
5
0,88
0,88
0,88
0,86
0,86
6
kg/l
Danger Density class
Table B.2 (continued)
++++++
++++++
++++++
++++++
++++++
++++++
---+++
---+++
7
AC
ACS
ACS
ACS
AC
AC
N
N
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
++++++
++++++
++++++
++++++
11
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
2
1
1307 1136
1224 o-xylene, with a f.p. of 21 to 55°C
1225 Solvent xylene (C8H10 type), with a f.p.
of 21 to 55°C
1307
1223 o-xylene, with a f.p. of 17 to below 21°C
to 55°C
1307
UNNo.
Liquid
1222 Xylene, isomer mixture, with a f.p. of 21
No.
0,07
144
0,07
144
4
mbar
at 50°C
Vapour pressure
3
°C
Boiling point
A II
A II
AI
A II
5
class
0,88
0,88
6
kg/l
Danger Density
Table B.2 (concluded)
++++++
++++++
++++++
++++++
7
AC
AC
AC
AC
8
conditions
A B C D E F
++++++
++++++
++++++
++++++
9
A B C D E F
Qualifying Group of tank
10
conditions
Qualifying
1.4306, 1.4541
Group of tank
1.0425
1.0116, 1.0144, 1.0345,
1.0036, 1.0037, 1.0038,
Material No.
++++++
++++++
++++++
++++++
11
153
12
A B C D E F conditions
Group of tank Qualifying
1.4435
1.4571, 1.4401, 1.4404,
EN 12285-1:2003 (E)
EN 12285-1:2003 (E)
Appendix 1 to annex B: Example of a Form for the approval of liquid-material combination Approval of the following liquid-material-combination under the following conditions It is approved that there have been positive experiences over a min. period of 5 years for the qualification of the following liquid-material-combination considering the following conditions:
chemical name of the liquid or data for unambigouos identification
............................................................................................................................................................................
flash point
boiling point °C
density . . . . . . . . . . . . . . . . . . . . kg/m ; storage temperatures . . . . . . . . . . . . . . . . . . .°C
material of the shell in contact with the liquid (in case of double-skin tanks: material of the inner skin)
name according to material standard
wall thickness (in case of double-skin tanks from the inner skin) . . . . . . . . . . . . . mm
installation and operation-conditions of the tank
°C
3
underground
light coating of the outside shell
above ground
insulation thickness . . . . . . . mm
in building
heating temp. . . . . . . .°C
cooling temp. . . . . . . . . . .°C
period during which the liquid has been stored in the tank
from . . . . . . . .
number of internal coatings............
testing institution ...........................
to ...................
.....................................................
...................................................
Company, place, date
Place, date
Signed by the customer to guarantee the
Signed by an expert acredited to the
above data
relevant national authority for approval of suitability
154
EN 12285-1:2003 (E)
Annex C (informative) A-devitations
A-deviation: National deviation due to regulations, the alteration of which is for the time being outside the competence of the CEN/CENELEC member. This European Standard does not fall under any Directive of the EC. In the relevant CEN/CENELEC countries these A-deviations are valid instead of the provisions of the European Standard until they have been removed. C.1
Finland
Clause
Deviation
National legislative/
Requirements for storage of flammable liquids are given in the Finishlaw 313/85 with amendments (Kauppa- ja teollisuusministeriön päätös palavista nesteistä) where the provisions of the national standard SFS 2736 (Palavien nesteiden varastointi ja käsittely. Teräksinen maanalainen lieriömäinen makaava säiliö.) are given an obligatory status.
administrative deviations
6.12 Stiffening rings
In accordance with the regulations 39 – 45 § of the Finnish law 313/85 and the standard SFS 2736 the following additional requirements are obligatory concerning stiffening rings in tanks for flammable liquids: In the event that the tank is provided with stiffenings rings, these rings shall be continuously welded. Stiffening rings shall not be located on a plate joint. The lowest point of the stiffening ring shall be provided with a flow opening.
7 Additional
In accordance with the regulations 39 – 45 § of the Finnish law 313/85 and
requirements for internal
the standard SFS 2736 the following additional requirements are
coating
obligatory concerning internal coating in tanks for flammable liquids:
A tank for storage of flammable liquids shall be provided with internal coating in accordance with the requirements of SFS 2736 clause 6.2. 7.3 Types of joints
In accordance with regulations 39 - 45 § of the Finnish law 313/85 and the standard SFS 2736 the following additional requirements are obligatory concerning types of joints in tanks for flammable liquids: Tank plates (shell and dished ends) shall be welded on both sides with square butt joints. Plate misalignment shall not exceed 0,25 s. The weld joint types 2 a, 2 b, 3a, 3b, 7b and 8 are not allowed.
C.2
Netherlands
Reference to legal requirements
Belsuit van 15 januari 1993, houdende regels met betrekking tot het opslaan van vloeistoffen in ondergrondse tanks (Besluit opslaan in ondergrondse tanks);
Belsuit van 12 maart 1996, houdende regels voor tuinbouwbedrijven met bedekte teelt (Besluit tuinbouwbedrijven met bedekte teelt milieubeheer);
Commissie Preventie van Rampen door Gevaarlijke Stoffen CPR 9-1;
Commissie Preventie van Rampen door Gevaarlijke Stoffen CPR 9-6;
Beoordelingsrichtlijn BRL-K747/01 d.d. 1996-11-01 "Horizontale cilindrische stalen tanks voor de drukloze opslag van vloeistoffen van ten hoogste 150 155
in the Netherlands
EN 12285-1:2003 (E)
m³".In addition to the requirements in clause 7.3 "Joggle joint weld construction" of this European Standard, the following will be applicable in the Netherlands:
Weld inspection
The circumferential and longitudinal welds of the tank shell and the shell to the dished ends shall be welded on both sides. The weld joint type 2a as detailed in Table 6 of EN 12285 is not acceptable for the inner skin of a double skin tank or for single skin tanks.
A new paragraph 7.4a "Additional requirements for the performance of welds" shall be added to this European Standard, as follows for the Netherlands:
Visual inspection The weld shall be inspected visually. Porosity and intermittent welds are not allowed. Undercutting is only allowed to a limited extent as indicated in Table 1. Radiographic inspection The longitudinal and circumferential welds shall be randomly inspected by means of radiographic inspection. The acceptance criteria for evaluation of the weld quality shall be as detailed in Table 1 and the number and method of sampling used shall be as detailed in Table II. The personnel responsible for the radiographic inspection shall be qualified to at least level 1 for making the photographs and to level 2 for the interpretation of the photographs.
156
EN 12285-1:2003 (E)
Table C.1 — Acceptation levels for welded butt joints Description
Sketch
Acceptance level
Cracks
---
not permitted
Crater cracks
permitted provided l ≤ 2 mm
Lack of fusion not breaking the surface (see note 1)
permitted provided l ≤ 10 mm
Lack of root penetration (see note 1)
permitted provided l ≤ 10 mm
Gas and Slag inclusions (see note 1)
permitted provided l ≤ 10 mm and w < 1,5 mm
Through thickness (e. g. wormhole, etc.)
permitted provided: Individual pores: ≤ 5 mm0/
porosity
Localized ≤ 4 % by area (see note 2)
Undercut
permitted provided:
h < 0,5 mm is always acceptable; 0,5 ≤ h ≤ 1,0 mm maximum if l ≤ 10 % of length of weld Symobls:
h = height of imperfection
l = length of imperfection
w = width of imperfection
NOTE 1 Short imperfections are one or more imperfections of total length not greater than 25 mm in any 100 mm length of weld or a maximum of 25 % of the weld length for a weld shorter than 100 mm. Long imperfections are one or more imperfections of total length greater than 25 mm in any 100 mm length of the weld or a minimum of 25 % of the weld length for a weld shorter than 100 mm. Long imperfections constituting lack of fusion, lack of root penetration and/or slag inclusions are not acceptable. NOTE 2
The area to be considered should be the length of weld affected by porosity times the maximum width of the weld.
157
EN 12285-1:2003 (E)
Table C.2 — Sampling ispection of welds for Steel storage tanks Start at level 10 Level
Minimum photo frequency
1
2 photos per 27 tanks
2
2 photos per 24 tanks
3
2 photos per 21 tanks
4
2 photos per 18 tanks
5
2 photos per 15 tanks
6
2 photos per 13 tanks
7
2 photos per 11 tanks
8
2 photos per 10 tanks
9
2 photos per 9 tanks
10
2 photos per 8 tanks
The two photos are to be made of the weld T-crossings from a randomly selected tank. One photo whereby the longitudinal weld at the T-crossing has been photographed and one photo whereby the circumferential weld as the T-crossing has been photographed. Manufacturers producing less than 2 tanks per week should radiograph all tanks. Due to the low production rate the use of sampling inspection is not allowed. For determining the production rate, the number of tanks produced during the last two months will be used. New certificate holders must photograph every tank during the starting up phase. The photo frequency level may be changed depending on the number of rejected photographs as follows: 0 rejected photos
1 level lower
1 or 2 rejected photos
same level
3 or 4 rejected photos
1 level higher
5 rejected photos or more
100 % inspection (see note)
The change in frequency may only be affected after 8 tanks have been photographed. NOTE When the number of defects is high, all the tanks should be photographed. In this case, in addition to the two photos of the T-crossings, two extra photographs need to be taken - one of the longitudinal weld and one of the circumferential weld. When the cause of the poor weld quality has been ascertained - determined by 0 rejected photos after 8 tanks have been photographed - the frequency can be set at level 10.
Rejected photos: All defects found are to be repaired. When carrying out repairs, the adjoining area also has to be photographed. In the event that in these areas faults are found, the 100 % of that particular weld needs to be photographed. Photographs of repairs are not to be counted in determining the weld frequency level.
158
EN 12285-1:2003 (E)
Bibliography
EN 10028–2, Flat products made of steels for pressure purposes — Part 2: Non-alloy and alloy steels with specified elevated temperature properties. EN 10055, Hot rolled steel equal flange tees with radiused root and toes — Dimensions and tolerances on shape and dimensions. EN 10088–1, Stainless steels — Part 1: List of stainless steels.
159
BS EN 12285-1:2003
BSI — British Standards Institution BSI is the independent national body responsible for preparing British Standards. It presents the UK view on standards in Europe and at the international level. It is incorporated by Royal Charter. Revisions British Standards are updated by amendment or revision. Users of British Standards should make sure that they possess the latest amendments or editions. It is the constant aim of BSI to improve the quality of our products and services. We would be grateful if anyone finding an inaccuracy or ambiguity while using this British Standard would inform the Secretary of the technical committee responsible, the identity of which can be found on the inside front cover. Tel: +44 (0)20 8996 9000. Fax: +44 (0)20 8996 7400. BSI offers members an individual updating service called PLUS which ensures that subscribers automatically receive the latest editions of standards. Buying standards Orders for all BSI, international and foreign standards publications should be addressed to Customer Services. Tel: +44 (0)20 8996 9001. Fax: +44 (0)20 8996 7001. Email: [email protected]. Standards are also available from the BSI website at http://www.bsi-global.com. In response to orders for international standards, it is BSI policy to supply the BSI implementation of those that have been published as British Standards, unless otherwise requested. Information on standards BSI provides a wide range of information on national, European and international standards through its Library and its Technical Help to Exporters Service. Various BSI electronic information services are also available which give details on all its products and services. Contact the Information Centre. Tel: +44 (0)20 8996 7111. Fax: +44 (0)20 8996 7048. Email: [email protected]. Subscribing members of BSI are kept up to date with standards developments and receive substantial discounts on the purchase price of standards. For details of these and other benefits contact Membership Administration. Tel: +44 (0)20 8996 7002. Fax: +44 (0)20 8996 7001. Email: [email protected]. Information regarding online access to British Standards via British Standards Online can be found at http://www.bsi-global.com/bsonline. Further information about BSI is available on the BSI website at http://www.bsi-global.com. Copyright Copyright subsists in all BSI publications. BSI also holds the copyright, in the UK, of the publications of the international standardization bodies. Except as permitted under the Copyright, Designs and Patents Act 1988 no extract may be reproduced, stored in a retrieval system or transmitted in any form or by any means – electronic, photocopying, recording or otherwise – without prior written permission from BSI.
BSI 389 Chiswick High Road London W4 4AL
This does not preclude the free use, in the course of implementing the standard, of necessary details such as symbols, and size, type or grade designations. If these details are to be used for any other purpose than implementation then the prior written permission of BSI must be obtained. Details and advice can be obtained from the Copyright & Licensing Manager. Tel: +44 (0)20 8996 7070. Fax: +44 (0)20 8996 7553. Email: [email protected].