UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
1001 |
Acetylene, dissolved |
4 F |
only in battery-vehicles and MEGCs composed of receptacles |
||||
1002 |
Air, compressed |
1 A |
see 4.3.3.2.1 |
||||
1003 |
Air, refrigerated liquid |
3 O |
see 4.3.3.2.4 |
||||
1005 |
Ammonia, anhydrous |
2 TC |
2.6 |
26 |
2.9 |
29 |
0.53 |
1006 |
Argon, compressed |
1 A |
see 4.3.3.2.1 |
||||
1008 |
Boron trifluoride |
2 TC |
22.5 |
225 |
22.5 |
225 |
0.715 |
30 |
300 |
30 |
300 |
0.86 |
|||
1009 |
Bromotrifluoromethane (Refrigerant gas R13B1) |
2 A |
12 |
120 |
1.50 |
||
4.2 |
42 |
1.13 |
|||||
12 |
120 |
1.44 |
|||||
25 |
250 |
1.60 |
|||||
1010 |
BUTADIENES, STABILIZED (1,2- butadiene) or |
2 F |
1 |
10 |
1 |
10 |
0.59 |
1010 |
BUTADIENES, STABILIZED (1,3- butadiene) or |
2 F |
1 |
10 |
1 |
10 |
0.55 |
1010 |
BUTADIENES AND HYDROCARBON, MIXTURE, STABILIZED |
2 F |
1 |
10 |
1 |
10 |
0.50 |
1011 |
Butane |
2 F |
1 |
10 |
1 |
10 |
0.51 |
1012 |
1-butylene or |
2 F |
1 |
10 |
1 |
10 |
0.53 |
1012 |
trans-2-butylene or |
2 F |
1 |
10 |
1 |
10 |
0.54 |
1012 |
cis-2-butylene or |
2 F |
1 |
10 |
1 |
10 |
0.55 |
1012 |
butylenes mixture |
2 F |
1 |
10 |
1 |
10 |
0.50 |
1013 |
Carbon dioxide |
2 A |
19 |
190 |
0.73 |
||
22.5 |
225 |
0.78 |
|||||
19 |
190 |
0.66 |
|||||
25 |
250 |
0.75 |
|||||
1016 |
Carbon monoxide, compressed |
1 TF |
see 4.3.3.2.1 |
||||
1017 |
Chlorine |
2 TOC |
1.7 |
17 |
1.9 |
19 |
1.25 |
1018 |
Chlorodifluoromethane (Refrigerant gas R22) |
2 A |
2.4 |
24 |
2.6 |
26 |
1.03 |
1020 |
Chloropentafluoroethane (Refrigerant gas R115) |
2 A |
2 |
20 |
2.3 |
23 |
1.08 |
1021 |
1-chloro-1,2,2,2- tetrafluoroethane (Refrigerant gas R124) |
2 A |
1 |
10 |
1.1 |
11 |
1.2 |
1022 |
Chlorotrifluoromethane (Refrigerant gas R13) |
2 A |
12 |
120 |
0.96 |
||
22.5 |
225 |
1.12 |
|||||
10 |
100 |
0.83 |
|||||
12 |
120 |
0.90 |
|||||
19 |
190 |
1.04 |
|||||
25 |
250 |
1.10 |
|||||
1023 |
Coal gas, compressed |
TF |
see 4.3.3.2.1 |
||||
1026 |
Cyanogen |
2 TF |
10 |
100 |
10 |
100 |
0.70 |
1027 |
Cyclopropane |
2 F |
1.6 |
16 |
1.8 |
18 |
0.53 |
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
1028 |
Dichlorodifluoromethane (Refrigerant gas R12) |
2 A |
1.5 |
15 |
1.6 |
16 |
1.15 |
1029 |
Dichlorofluoromethane (Refrigerant gas R21) |
2 A |
1 |
10 |
1 |
10 |
1.23 |
1030 |
1,1-difluoroethane (Refrigerant gas R152a) |
2 F |
1.4 |
14 |
1.6 |
16 |
0.79 |
1032 |
Dimethylamine, anhydrous |
2 F |
1 |
10 |
1 |
10 |
0.59 |
1033 |
Dimethyl ether |
2 F |
1.4 |
14 |
1.6 |
16 |
0.58 |
1035 |
Ethane |
2 F |
12 |
120 |
0.32 |
||
9.5 |
95 |
0.25 |
|||||
12 |
120 |
0.29 |
|||||
30 |
300 |
0.39 |
|||||
1036 |
Ethylamine |
2 F |
1 |
10 |
1 |
10 |
0.61 |
1037 |
Ethyl chloride |
2 F |
1 |
10 |
1 |
10 |
0.8 |
1038 |
Ethylene, refrigerated liquid |
3 F |
see 4.3.3.2.4 |
||||
1039 |
Ethyl methyl ether |
2 F |
1 |
10 |
1 |
10 |
0.64 |
1040 |
Ethylene oxide with nitrogen up to a total pressure of 1MPa (10 bar) at 50 °C |
2 TF |
1.5 |
15 |
1.5 |
15 |
0.78 |
1041 |
Ethylene oxide and carbon dioxide mixture, with more than 9% but not more than 87% ethylene oxide |
2 F |
2.4 |
24 |
2.6 |
26 |
0.73 |
1046 |
Helium, compressed |
1 A |
see 4.3.3.2.1 |
||||
1048 |
Hydrogen bromide, anhydrous |
2 TC |
5 |
50 |
5.5 |
55 |
1.54 |
1049 |
Hydrogen, compressed |
1 F |
see 4.3.3.2.1 |
||||
1050 |
Hydrogen chloride, anhydrous |
2 TC |
12 |
120 |
0.69 |
||
10 |
100 |
0.30 |
|||||
12 |
120 |
0.56 |
|||||
15 |
150 |
0.67 |
|||||
20 |
200 |
0.74 |
|||||
1053 |
Hydrogen sulphide |
2 TF |
4.5 |
45 |
5 |
50 |
0.67 |
1055 |
Isobutylene |
2 F |
1 |
10 |
1 |
10 |
0.52 |
1056 |
Krypton, compressed |
1 A |
see 4.3.3.2.1 |
||||
1058 |
Liquefied gases, non flammable, charged with nitrogen, carbon dioxide or air |
2 A |
1.5 filling pressure see 4.3.3.2.2 or 4.3.3.2.3 |
||||
1060 |
Methylacetylene and propadiene mixture, stabilized: |
2 F |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
mixture P1 |
2 F |
2.5 |
25 |
2.8 |
28 |
0.49 |
|
mixture P2 |
2 F |
2.2 |
22 |
2.3 |
23 |
0.47 |
|
propadiene with 1% to 4% methylacetylene |
2 F |
2.2 |
22 |
2.2 |
22 |
0.50 |
|
1061 |
Methylamine, anhydrous |
2 F |
1 |
10 |
1.1 |
11 |
0.58 |
1062 |
Methyl bromide with not more than 2% chloropicrin |
2 T |
1 |
10 |
1 |
10 |
1.51 |
1063 |
Methyl chloride (Refrigerant gas R40) |
2 F |
1.3 |
13 |
1.5 |
15 |
0.81 |
1064 |
Methyl mercaptan |
2 TF |
1 |
10 |
1 |
10 |
0.78 |
1065 |
Neon, compressed |
1 A |
see 4.3.3.2.1 |
||||
1066 |
Nitrogen, compressed |
1 A |
see 4.3.3.2.1 |
||||
1067 |
Dinitrogen tetroxide (nitrogen dioxide) |
2 TOC |
only in battery-vehicles and MEGCs composed of receptacles |
||||
1070 |
Nitrous oxide |
2 O |
22.5 |
225 |
0.78 |
||
18 |
180 |
0.68 |
|||||
22.5 |
225 |
0.74 |
|||||
25 |
250 |
0.75 |
|||||
1071 |
Oil gas, compressed |
1 TF |
see 4.3.3.2.1 |
||||
1072 |
Oxygen, compressed |
1 O |
see 4.3.3.2.1 |
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
1073 |
Oxygen, refrigerated liquid |
3 O |
see 4.3.3.2.4 |
||||
1075 |
Petroleum gases, liquefied |
2 F |
See 4.3.3.2.2 or 4.3.3.2.3 |
||||
1076 |
Phosgene |
2 TC |
only in battery-vehicles and MEGCs composed of receptacles |
||||
1081 |
Tetrafluoroethylene, stabilized |
2 F |
only in battery-vehicles and MEGCs composed of seamless receptacles |
||||
1077 |
Propylene |
2 F |
2.5 |
25 |
2.7 |
27 |
0.43 |
1078 |
Refrigerant gases, n.o.s. such as: |
2 A |
|||||
mixture F1 |
2 A |
1 |
10 |
1.1 |
11 |
1.23 |
|
mixture F2 |
2 A |
1.5 |
15 |
1.6 |
16 |
1.15 |
|
mixture F3 |
2 A |
2.4 |
24 |
2.7 |
27 |
1.03 |
|
other mixtures |
2 A |
see 4.3.3.2.2 or 4.3.3.2.3 |
|||||
1079 |
Sulphur dioxide |
2 TC |
1 |
10 |
1.2 |
12 |
1.23 |
1080 |
Sulphur hexafluoride |
2 A |
12 |
120 |
1.34 |
||
7 |
70 |
1.04 |
|||||
14 |
140 |
1.33 |
|||||
16 |
160 |
1.37 |
|||||
1082 |
Trifluorochloroethylene, stabilized (Refrigerant gas R1113) |
2 TF |
1.5 |
15 |
1.7 |
17 |
1.13 |
1083 |
Trimethylamine, anhydrous |
2 F |
1 |
10 |
1 |
10 |
0.56 |
1085 |
Vinyl bromide, stabilized |
2 F |
1 |
10 |
1 |
10 |
1.37 |
1086 |
Vinyl chloride, stabilized |
2 F |
1 |
10 |
1.1 |
11 |
0.81 |
1087 |
Vinyl methyl ether, stabilized |
2 F |
1 |
10 |
1 |
10 |
0.67 |
1581 |
Chloropicrin and methyl bromide mixture with more than 2% chloropicrin |
2 T |
1 |
10 |
1 |
10 |
1.51 |
1582 |
Chloropicrin and methyl chloride mixture |
2 T |
1.3 |
13 |
1.5 |
15 |
0.81 |
1612 |
Hexaethyl tetraphosphate and compressed gas mixture |
1 T |
see 4.3.3.2.1 |
||||
1749 |
Chlorine trifluoride |
2 TOC |
3 |
30 |
3 |
30 |
1.40 |
1858 |
Hexafluoropropylene (Refrigerant gas R 1216) |
2A |
1.7 |
17 |
1.9 |
19 |
1.11 |
1859 |
Silicon tetrafluoride |
2 TC |
20 30 |
200 300 |
20 30 |
200 300 |
0.74 1.10 |
1860 |
Vinyl fluoride, stabilized |
2 F |
12 |
120 |
0.58 |
||
22.5 |
225 |
0.65 |
|||||
25 |
250 |
0.64 |
|||||
1912 |
Methyl chloride and methylene chloride mixture |
2 F |
1.3 |
13 |
1.5 |
15 |
0.81 |
1913 |
Neon, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
1951 |
Argon, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
1952 |
Ethylene oxide and carbon dioxide mixture, with not more than 9% ethylene oxide |
2 A |
19 |
190 |
19 |
190 |
0.66 |
25 |
250 |
25 |
250 |
0.75 |
|||
1953 |
1 TF |
see 4.3.3.2.1 or 4.3.3.2.2 |
|||||
1954 |
Compressed gas, flammable n.o.s. |
1 F |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
1955 |
Compressed gas, toxic, n.o.s.a |
1 T |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
1956 |
Compressed gas, n.o.s. |
1 A |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
1957 |
Deuterium, compressed |
1 F |
see 4.3.3.2.1 |
||||
1958 |
1,2-dichloro-1,1,2,2-tetrafluoroethane (Refrigerant gas R114) |
2 A |
1 |
10 |
1 |
10 |
1.3 |
1959 |
1,1-difluoroethylene (Refrigerant gas R1132a) |
2 F |
12 |
120 |
0.66 |
||
22.5 |
225 |
0.78 |
a Allowed if LC50 equal to or greater than 200 ppm.
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
25 |
250 |
0.77 |
|||||
1961 |
Ethane, refrigerated liquid |
3 F |
see 4.3.3.2.4 |
||||
1962 |
Ethylene |
2 F |
12 |
120 |
0.25 |
||
22.5 |
225 |
0.36 |
|||||
22.5 |
225 |
0.34 |
|||||
30 |
300 |
0.37 |
|||||
1963 |
Helium, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
1964 |
Hydrocarbon gas mixture, compressed, n.o.s. |
1 F |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
1965 |
Hydrocarbon gas mixture, liquefied, n.o.s.: |
2 F |
|||||
Mixture A |
2 F |
1 |
10 |
1 |
10 |
0.50 |
|
Mixture A01 |
2 F |
1.2 |
12 |
1.4 |
14 |
0.49 |
|
Mixture A02 |
2 F |
1.2 |
12 |
1.4 |
14 |
0.48 |
|
Mixture A0 |
2 F |
1.2 |
12 |
1.4 |
14 |
0.47 |
|
Mixture A1 |
2 F |
1.6 |
16 |
1.8 |
18 |
0.46 |
|
Mixture B1 |
2 F |
2 |
20 |
2.3 |
23 |
0.45 |
|
Mixture B2 |
2 F |
2 |
20 |
2.3 |
23 |
0.44 |
|
Mixture B |
2 F |
2 |
20 |
2.3 |
23 |
0.43 |
|
Mixture C |
2 F |
2.5 |
25 |
2.7 |
27 |
0.42 |
|
Other mixtures |
2 F |
see 4.3.3.2.2 or 4.3.3.2.3 |
|||||
1966 |
Hydrogen, refrigerated liquid |
3 F |
see 4.3.3.2.4 |
||||
1967 |
Insecticide gas, toxic, n.o.s.a |
2 T |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
1968 |
Insecticide gas, n.o.s. |
2 A |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
1969 |
Isobutane |
2 F |
1 |
10 |
1 |
10 |
0.49 |
1970 |
Krypton, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
1971 |
Methane, compressed or natural gas, compressed with high methane content |
1 F |
see 4.3.3.2.1 |
||||
1972 |
Methane, refrigerated liquid or natural gas, refrigerated liquid with high methane content |
3 F |
see 4.3.3.2.4 |
||||
1973 |
Chlorodifluoromethane and chloropentafluoroethane mixture with fixed boiling point, with approximately 49% chlorodifluoromethane (Refrigerant gas R502) |
2 A |
2.5 |
25 |
2.8 |
28 |
1.05 |
1974 |
Chlorodifluorobromomethane (Refrigerant gas R12B1) |
2 A |
1 |
10 |
1 |
10 |
1.61 |
1976 |
Octafluorocyclobutane (Refrigerant gas RC318) |
2 A |
1 |
10 |
1 |
10 |
1.34 |
1977 |
Nitrogen, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
1978 |
Propane |
2 F |
2.1 |
21 |
2.3 |
23 |
0.42 |
1982 |
Tetrafluoromethane (Refrigerant gas R14) |
2 A |
20 |
200 |
20 |
200 |
0.62 |
30 |
300 |
30 |
300 |
0.94 |
|||
1983 |
1-chloro-2,2,2-trifluoroethane (Refrigerant gas R133a) |
2 A |
1 |
10 |
1 |
10 |
1.18 |
1984 |
Trifluoromethane (Refrigerant gas R23) |
2 A |
19 |
190 |
0.92 |
||
25 |
250 |
0.99 |
|||||
19 |
190 |
0.87 |
|||||
25 |
250 |
0.95 |
|||||
2034 |
Hydrogen and methane mixture, compressed |
1 F |
see 4.3.3.2.1 |
||||
2035 |
1,1,1-trifluoroethane (Refrigerant gas R143a) |
2 F |
2.8 |
28 |
3.2 |
32 |
0.79 |
2036 |
Xenon |
2 A |
12 |
120 |
1.30 |
||
13 |
130 |
1.24 |
|||||
2044 |
2,2-dimethylpropane |
2 F |
1 |
10 |
1 |
10 |
0.53 |
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
2073 |
Ammonia solutions, relative density less than 0.880 at 15 °C in water: |
4 A |
|||||
with more than 35% and not more than 40% ammonia |
4 A |
1 |
10 |
1 |
10 |
0.80 |
|
with more than 40% and not more than 50% ammonia |
4 A |
1.2 |
12 |
1.2 |
12 |
0.77 |
|
2187 |
Carbon dioxide, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
2189 |
Dichlorosilane |
2 TFC |
1 |
10 |
1 |
10 |
0.90 |
2191 |
Sulfuryl fluoride |
2 T |
5 |
50 |
5 |
50 |
1.1 |
2193 |
Hexafluoroethane (Refrigerant gas R116) |
2 A |
16 |
160 |
1.28 |
||
20 |
200 |
1.34 |
|||||
20 |
200 |
1.10 |
|||||
2197 |
Hydrogen iodide, anhydrous |
2 TC |
1.9 |
19 |
2.1 |
21 |
2.25 |
2200 |
Propadiene, stabilized |
2 F |
1.8 |
18 |
2.0 |
20 |
0.50 |
2201 |
Nitrous oxide, refrigerated liquid |
3 O |
see 4.3.3.2.4 |
||||
2203 |
2 F |
22.5 |
225 |
22.5 |
225 |
0.32 |
|
25 |
250 |
25 |
250 |
0.36 |
|||
2204 |
Carbonyl sulphide |
2 TF |
2.7 |
27 |
3.0 |
30 |
0.84 |
2417 |
Carbonyl fluoride |
2 TC |
20 |
200 |
20 |
200 |
0.47 |
30 |
300 |
30 |
300 |
0.70 |
|||
2419 |
Bromotrifluoroethylene |
2 F |
1 |
10 |
1 |
10 |
1.19 |
2420 |
Hexafluoroacetone |
2 TC |
1.6 |
16 |
1.8 |
18 |
1.08 |
2422 |
Octafluorobut-2-ene (Refrigerant gas R1318) |
2 A |
1 |
10 |
1 |
10 |
1.34 |
2424 |
Octafluoropropane (Refrigerant gas R218) |
2 A |
2.1 |
21 |
2.3 |
23 |
1.07 |
2451 |
Nitrogen trifluoride |
2 O |
20 |
200 |
20 |
200 |
0.50 |
30 |
300 |
30 |
300 |
0.75 |
|||
2452 |
Ethylacetylene, stabilized |
2 F |
1 |
10 |
1 |
10 |
0.57 |
2453 |
Ethyl fluoride (Refrigerant gas R161) |
2 F |
2.1 |
21 |
2.5 |
25 |
0.57 |
2454 |
Methyl fluoride (Refrigerant gas R41) |
2 F |
30 |
300 |
30 |
300 |
0.36 |
2517 |
1-chloro-1,1-difluoroethane (Refrigerant gas R142b) |
2 F |
1 |
10 |
1 |
10 |
0.99 |
2591 |
Xenon, refrigerated liquid |
3 A |
see 4.3.3.2.4 |
||||
2599 |
Chlorotrifluoromethane and trifluoromethane, azeotropic mixture with approximately 60% chlorotrifluoromethane (Refrigerant gas R503) |
2 A |
3.1 |
31 |
3.1 |
31 |
0.11 |
4.2 |
42 |
0.21 |
|||||
10 |
100 |
0.76 |
|||||
4.2 |
42 |
0.20 |
|||||
10 |
100 |
0.66 |
|||||
2601 |
Cyclobutane |
2 F |
1 |
10 |
1 |
10 |
0.63 |
2602 |
Dichlorodifluoromethane and difluoro-1,1 ethane, azeotropic mixture with approximately 74% dichlorodifluoromethane (Refrigerant gas R500) |
2 A |
1.8 |
18 |
2 |
20 |
1.01 |
2901 |
Bromine chloride |
2 TOC |
1 |
10 |
1 |
10 |
1.50 |
3057 |
Trifluoroacetyl chloride |
2 TC |
1.3 |
13 |
1.5 |
15 |
1.17 |
3070 |
Ethylene oxide and dichlorodifluoromethane mixture with not more than 12.5% ethylene oxide |
2 A |
1.5 |
15 |
1.6 |
16 |
1.09 |
3083 |
Perchloryl fluoride |
2 TO |
2.7 |
27 |
3.0 |
30 |
1.21 |
3136 |
Trifluoromethane, refigerated liquid |
3 A |
See 4.3.3.2.4 |
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
3138 |
Ethylene, acetylene propylene in mixture, refrigerated liquid, containing at least 71.5% ethylene with not more than 22.5% acetylene and not more than 6% propylene |
3 F |
see 4.3.3.2.4 |
||||
3153 |
Perfluoro(methyl vinyl ether) |
2 F |
1.4 |
14 |
1.5 |
15 |
1.14 |
3154 |
Perfluoro(ethyl vinyl ether) |
2 F |
1 |
10 |
1 |
10 |
0.98 |
3156 |
Compressed gas, oxidizing, n.o.s. |
1 O |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
3157 |
Liquefied gas, oxidizing, n.o.s. |
2 O |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3158 |
Gas, refrigerated liquid, n.o.s. |
3 A |
see 4.3.3.2.4 |
||||
3159 |
1,1,1,2-tetrafluoroethane (Refrigerant gas R134a) |
2 A |
1.6 |
16 |
1.8 |
18 |
1.04 |
3160 |
2 TF |
see 4.3.3.2.2 or 4.3.3.2.3 |
|||||
3161 |
Liquefied gas, flammable, n.o.s. |
2 F |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3162 |
Liquefied gas, toxic, n.o.s. a |
2 T |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3163 |
Liquefied gas, n.o.s. |
2 A |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3220 |
Pentafluoroethane (Refrigerant gas R125) |
2 A |
4.1 |
41 |
4.9 |
49 |
0.95 |
3252 |
Difluoromethane (Refrigerant gas R32) |
2 F |
3.9 |
39 |
4.3 |
43 |
0.78 |
3296 |
Heptafluoropropane (Refrigerant gas R227) |
2 A |
1.4 |
14 |
1.6 |
16 |
1.20 |
3297 |
Ethylene oxide and chlorotetrafluoroethane mixture, with not more than 8.8% ethylene oxide |
2 A |
1 |
10 |
1 |
10 |
1.16 |
3298 |
Ethylene oxide and pentafluoroethane mixture, with not more than 7.9% ethylene oxide |
2 A |
2.4 |
24 |
2.6 |
26 |
1.02 |
3299 |
Ethylene oxide and tetrafluoroethane mixture, with not more than 5.6% ethylene oxide |
2 A |
1.5 |
15 |
1.7 |
17 |
1.03 |
3300 |
Ethylene oxide and carbon dioxide mixture, with more than 87% ethylene oxide |
2 TF |
2.8 |
28 |
2.8 |
28 |
0.73 |
3303 |
Compressed gas, toxic, oxidizing, n.o.s.a |
1 TO |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
3304 |
Compressed gas, toxic, corrosive, n.o.s.a |
1 TC |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
3305 |
Compressed gas, toxic, flammable, corrosive, n.o.s. a |
1 TFC |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
3306 |
Compressed gas, toxic, oxidizing, corrosive, n.o.s. a |
1 TOC |
see 4.3.3.2.1 or 4.3.3.2.2 |
||||
3307 |
Liquefied gas, toxic, oxidizing, n.o.s. a |
2 TO |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3308 |
Liquefied gas, toxic, corrosive, n.o.s. a |
2 TC |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3309 |
Liquefied gas, toxic, flammable, corrosive, n.o.s. a |
2 TFC |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3310 |
Liquefied gas, toxic, oxidizing, corrosive, n.o.s. a |
2 TOC |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3311 |
Gas, refrigerated liquid, oxidizing, n.o.s. |
3 O |
see 4.3.3.2.4 |
||||
3312 |
Gas, refrigerated liquid, flammable, n.o.s. |
3 F |
see 4.3.3.2.4 |
||||
3318 |
Ammonia solutions, relative density less than 0.880 at 15 °C in water, with more than 50% ammonia |
4 TC |
see 4.3.3.2.2 |
||||
3337 |
Refrigerant gas R404A |
2 A |
2.9 |
29 |
3.2 |
32 |
0.84 |
3338 |
Refrigerant gas R407A |
2 A |
2.8 |
28 |
3.2 |
32 |
0.95 |
3339 |
Refrigerant gas R407B |
2 A |
3.0 |
30 |
3.3 |
33 |
0.95 |
a Allowed if LC50 equal to or greater than 200 ppm.
UN No. |
Name |
Classification code |
Minimum test pressure for tanks |
Maximum permissible mass of contents per litre of capacity |
|||
With thermal insulation |
Without thermal insulation |
||||||
MPa |
bar |
MPa |
bar |
kg |
|||
3340 |
Refrigerant gas R407C |
2 A |
2.7 |
27 |
3.0 |
30 |
0.95 |
3354 |
Insecticide gas, flammable, n.o.s. |
2 F |
see 4.3.3.2.2 or 4.3.3.2.3 |
||||
3355 |
Insecticide gas, toxic, flammable, n.o.s.a |
2 TF |
see 4.3.3.2.2 or 4.3.3.2.3 |
(Reserved)
The actual holding time shall be determined for
each journey of a tank-container carrying a
refrigerated liquefied gas on the basis of the
following:
(a) The reference holding time for the
refrigerated liquefied gas to be carried (see
6.8.3.4.10) as indicated on the plate referred
to in 6.8.3.5.4;
(b) The actual filling density;
(c) The actual filling pressure;
(d) The lowest set pressure of the pressure
limiting device(s);
(e) The deterioration of the insulation4.
NOTE: ISO 21014:2006 ‘Cryogenic vessels –
Cryogenic insulation performance’ details methods
of determining the insulation performance of
cryogenic vessels and provides a method of
calculating the holding time.
The date at which the actual holding time ends shall
be entered in the transport document (see 5.4.1.2.2.
(d)).
Tank-containers shall not be offered for carriage:
(a) In an ullage condition liable to produce an
unacceptable hydraulic force due to surge
within the shell;
(b) When leaking;
(c) When damaged to such an extent that the
integrity of the tank-container or its lifting or
securing arrangements may be affected;
(d) Unless the service equipment has been
examined and found to be in good working
order;
(e) Unless the actual holding time for the
refrigerated liquefied gas being carried has
been determined;
(f) Unless the duration of carriage, after taking
into consideration any delays which might be
encountered, does not exceed the actual
holding time;
(g) Unless the pressure is steady and has been
lowered to a level such that the actual holding
time may be achieved4.
|
Part |
Description |
Tank code |
1 |
Types of tank |
L = tank for substances in the liquid state (liquids or solids handed over for carriage in the molten state);
S = tank for substances in the solid state (powdery or granular). |
2 |
Calculation pressure |
G = minimum calculation pressure according to the general requirements of 6.8.2.1.14; or
1.5; 2.65; 4; 10; 15 or 21= minimum calculation pressure in bar (see 6.8.2.1.14). |
3 |
Openings (see 6.8.2.2.2) |
A = tank with bottom-filling or bottom-discharge openings with 2 closures; |
B = tank with bottom-filling or bottom-discharge openings with 3 closures;
C = tank with top-filling and discharge openings with only cleaning openings below the surface of the liquid;
D = tank with top-filling and discharge openings with no openings below the surface of the liquid. |
||
4 |
Safety valves/devices |
V = tank with a breather device, according to 6.8.2.2.6, but no device protecting against the propagation of a flame; or non-explosion pressure shock resistant tank ;
F = tank with a breather device, according to 6.8.2.2.6, fitted with a device protecting against the propagation of a flame; or explosion pressure shock resistant tank ;
N = tank without a breather device according to 6.8.2.2.6 and not hermetically closed; |
B = tank with bottom-filling or bottom-discharge openings with 3 closures;
C = tank with top-filling and discharge openings with only cleaning openings below the surface of the liquid;
D = tank with top-filling and discharge openings with no openings below the surface of the liquid. |
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
LIQUIDS LGAV |
3 |
F2 |
III |
9 |
M9 |
III |
|
LGBV |
4.1 |
F2 |
II, III |
5.1 |
O1 |
III |
|
9 |
M6 |
III |
|
M11 |
III |
||
and groups of permitted substances for tank code LGAV |
|||
LGBF |
3 |
F1 |
II vapour pressure at 50 °C ≤ 1.1 bar |
F1 |
III |
||
D |
II vapour pressure at 50 °C ≤ 1.1 bar |
||
D |
III |
||
and groups of permitted substances for tank codes LGAV and LGBV |
|||
L1.5BN |
3 |
F1 |
II vapour pressure at 50 °C > 1.1 bar |
F1 |
III flash-point < 23 °C, viscous, vapour pressure at 50 °C > 1.1 bar boiling point > 35 °C |
||
D |
II vapour pressure at 50 °C > 1.1 bar |
||
and groups of permitted substances for tank codes LGAV, LGBV and LGBF |
|||
L4BN |
3 |
F1 |
I, III boiling point ≤ 35 °C |
FC |
III |
||
D |
I |
||
5.1 |
O1 |
I, II |
|
OT1 |
I |
||
8 |
C1 |
II, III |
|
C3 |
II, III |
||
C4 |
II, III |
||
C5 |
II, III |
||
C7 |
II, III |
||
C8 |
II, III |
||
C9 |
II, III |
||
C10 |
II, III |
||
CF1 |
II |
||
CF2 |
II |
||
CS1 |
II |
||
CW1 |
II |
||
CW2 |
II |
||
CO1 |
II |
||
CO2 |
II |
||
CT1 |
II, III |
||
CT2 |
II, III |
||
CFT |
II |
||
9 |
M11 |
III |
and groups of permitted substances for tank codes LGAV, LGBV, LGBF and L1.5BN
Rationalized approach |
|||
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
L4BH |
3 |
FT1 |
II, III |
FT2 |
II |
||
FC |
II |
||
FTC |
II |
||
6.1 |
T1 |
II, III |
|
T2 |
II, III |
||
T3 |
II, III |
||
T4 |
II, III |
||
T5 |
II, III |
||
T6 |
II, III |
||
T7 |
II, III |
||
TF1 |
II |
||
TF2 |
II, III |
||
TF3 |
II |
||
TS |
II |
||
TW1 |
II |
||
TW2 |
II |
||
TO1 |
II |
||
TO2 |
II |
||
TC1 |
II |
||
TC2 |
II |
||
TC3 |
II |
||
TC4 |
II |
||
TFC |
II |
||
6.2 |
I3 |
II |
|
I4 |
|||
9 |
M2 |
II |
|
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN and L4BN |
|||
L4DH |
4.2 |
S1 |
II, III |
S3 |
II, III |
||
ST1 |
II, III |
||
ST3 |
II, III |
||
SC1 |
II, III |
||
SC3 |
II, III |
||
4.3 |
W1 |
II, III |
|
WF1 |
II, III |
||
WT1 |
II, III |
||
WC1 |
II, III |
||
8 |
CT1 |
II, III |
|
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN and L4BH |
|||
L10BH |
8 |
C1 |
I |
C3 |
I |
||
C4 |
I |
||
C5 |
I |
||
C7 |
I |
||
C8 |
I |
||
C9 |
I |
||
C10 |
I |
||
CF1 |
I |
||
СF2 |
I |
||
CS1 |
I |
||
СW1 |
I |
||
СW2 |
I |
||
CO1 |
I |
||
CO2 |
I |
||
CT1 |
I |
||
CT2 |
I |
||
COT |
I |
||
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN, and L4BH |
Rationalized approach |
|||
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
L10CH |
3 |
FT1 |
I |
FT2 |
I |
||
FC |
I |
||
FTC |
I |
||
6.1* |
T1 |
I |
|
T2 |
I |
||
T3 |
I |
||
T4 |
I |
||
T5 |
I |
||
T6 |
I |
||
T7 |
I |
||
TF1 |
I |
||
TF2 |
I |
||
TF3 |
I |
||
TS |
I |
||
TW1 |
I |
||
TO1 |
I |
||
TC1 |
I |
||
TC2 |
I |
||
TC3 |
I |
||
TC4 |
I |
||
TFC |
I |
||
TFW |
I |
||
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN, L4BH, and L10BH |
|||
* Substances with an LC50 lower than or equal to 200 ml/m3 and saturated vapour concentration greater than or equal to 500 LC50 shall be assigned to tank code L15CH. |
|||
L10DH |
4.3 |
W1 |
I |
WF1 |
I |
||
WT1 |
I |
||
WC1 |
I |
||
WFC |
I |
||
5.1 |
OTC |
I |
|
8 |
CT1 |
I |
|
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN, L4BH, L4DH, L10BH and L10CH |
|||
L15CH |
3 |
FT1 |
I |
6.1** |
T1 |
I |
|
T4 |
I |
||
TF1 |
I |
||
TW1 |
I |
||
TO1 |
I |
||
TC1 |
I |
||
TC3 |
I |
||
TFC |
I |
||
TFW |
I |
||
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN, L4BH, L10BH and L10CH |
|||
** Substances with an LC50 lower than or equal to 200 ml/m3 and saturated vapour concentration greater than or equal to 500 LC50 shall be assigned to this tank code. |
|||
L21DH |
4.2 |
S1 |
I |
S3 |
I |
||
SW |
I |
||
ST3 |
I |
||
and groups of permitted substances for tank codes LGAV, LGBV, LGBF, L1.5BN, L4BN, L4BH, L4DH, L10BH, L10CH, L10DH and L15CH |
Rationalized approach |
|||
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
SOLIDS SGAV |
4.1 |
F1 |
III |
F3 |
III |
||
4.2 |
S2 |
II, III |
|
S4 |
III |
||
5.1 |
O2 |
II, III |
|
8 |
C2 |
II, III |
|
C4 |
III |
||
C6 |
III |
||
C8 |
III |
||
C10 |
II, III |
||
СT2 |
III |
||
9 |
M7 |
III |
|
M11 |
II, III |
||
SGAN |
4.1 |
F1 |
II |
F3 |
II |
||
FT1 |
II, III |
||
FT2 |
II, III |
||
FC1 |
II, III |
||
FC2 |
II, III |
||
4.2 |
S2 |
II |
|
S4 |
II, III |
||
ST2 |
II, III |
||
ST4 |
II, III |
||
SC2 |
II, III |
||
SC4 |
II, III |
||
4.3 |
W2 |
II, III |
|
WF2 |
II |
||
WS |
II, III |
||
WT2 |
II, III |
||
WC2 |
II, III |
||
5.1 |
O2 |
II, III |
|
OT2 |
II, III |
||
OC2 |
II, III |
||
8 |
C2 |
II |
|
С4 |
II |
||
С6 |
II |
||
С8 |
II |
||
С10 |
II |
||
CF2 |
II |
||
CS2 |
II |
||
CW2 |
II |
||
CO2 |
II |
||
CT2 |
II |
||
9 |
M3 |
III |
|
and groups of permitted substances for tank codes SGAV |
|||
SGAH |
6.1 |
T2 |
II, III |
T3 |
II, III |
||
T5 |
II, III |
||
T7 |
II, III |
||
T9 |
II |
||
TF3 |
II |
||
TS |
II |
||
TW2 |
II |
||
TO2 |
II |
||
TC2 |
II |
||
TC4 |
II |
||
9 |
M1 |
II, III |
|
and groups of permitted substances for tanks codes SGAV and SGAN |
Rationalized approach |
|||
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
S4AH |
6.2 |
I3 |
II |
9 |
M2 |
II |
|
and groups of permitted substances for tanks codes SGAV, SGAN and SGAH |
|||
S10AN |
8 |
C2 |
I |
C4 |
I |
||
C6 |
I |
||
C8 |
I |
||
C10 |
I |
||
CF2 |
I |
||
CS2 |
I |
||
CW2 |
I |
||
CO2 |
I |
||
CT2 |
I |
||
and groups of permitted substances for tank codes SGAV and SGAN |
|||
S10AH |
6.1 |
T2 |
I |
T3 |
I |
||
T5 |
I |
||
T7 |
I |
||
TS |
I |
||
TW2 |
I |
||
TO2 |
I |
||
TC2 |
I |
||
TC4 |
I |
||
and groups of permitted substances for tank codes SGAV, SGAN, SGAH and S10AN |
Rationalized approach |
|||
Tank code |
Group of permitted substances |
||
Class |
Classification code |
Packing group |
|
S4AH |
6.2 |
I3 |
II |
9 |
M2 |
II |
|
and groups of permitted substances for tanks codes SGAV, SGAN and SGAH |
|||
S10AN |
8 |
C2 |
I |
C4 |
I |
||
C6 |
I |
||
C8 |
I |
||
C10 |
I |
||
CF2 |
I |
||
CS2 |
I |
||
CW2 |
I |
||
CO2 |
I |
||
CT2 |
I |
||
and groups of permitted substances for tank codes SGAV and SGAN |
|||
S10AH |
6.1 |
T2 |
I |
T3 |
I |
||
T5 |
I |
||
T7 |
I |
||
TS |
I |
||
TW2 |
I |
||
TO2 |
I |
||
TC2 |
I |
||
TC4 |
I |
||
and groups of permitted substances for tank codes SGAV, SGAN, SGAH and S10AN |
Hierarchy of tanks
Tanks with tank codes different from those indicated in this table or in Table A of Chapter 3.2 may also be used provided that any element (number or letter) of parts 1 to 4 of these tank codes correspond to a level of safety at least equivalent to the corresponding element of the tank code indicated in Table A of Chapter 3.2, according to the following increasing order:
Part 1: Types of tanks S L
Part 2: Calculation pressure
G 1.5 2.65 4 10 15 21 bar
Part 3: Openings A B C D
Part 4: Safety valves/devices V F N H
For example:
A tank with the tank code L10CN is authorized for the carriage of a substance to which the tank code L4BN has been assigned;
A tank with the tank code L4BN is authorized for the carriage of a substance to which the tank code SGAN has been assigned.
E: The hierarchy does not take account of any special provisions for each entry (see 4.3.5 and
.8.4).