[Code of Federal Regulations]
[Title 49, Volume 2]
[Revised as of October 1, 2004]
From the U.S. Government Printing Office via GPO Access
[CITE: 49CFR173.32]

[Page 446-450]
 
                        TITLE 49--TRANSPORTATION
 
 CHAPTER I--RESEARCH AND SPECIAL PROGRAMS ADMINISTRATION, DEPARTMENT OF 
                             TRANSPORTATION
 
PART 173_SHIPPERS_GENERAL REQUIREMENTS FOR SHIPMENTS AND PACKAGINGS--Table 
of Contents
 
     Subpart B_Preparation of Hazardous Materials for Transportation
 
Sec. 173.32  Requirements for the use of portable tanks.

    (a) General requirements. No person may offer a hazardous material 
for transportation in a portable tank except as authorized by this 
subchapter.
    (1) Except as otherwise provided in this subpart, no person may use 
a portable tank for the transportation of a hazardous material unless it 
meets the requirements of this subchapter.
    (2) No person may fill and offer for transportation a portable tank 
when the prescribed periodic test or inspection under subpart G of part 
180 of this subchapter has become due until the test or inspection has 
been successfully completed. This requirement does not apply to any 
portable tank filled prior to the test or inspection due date.
    (3) When a portable tank is used as a cargo tank motor vehicle, it 
must conform to all the requirements prescribed for cargo tank motor 
vehicles. (See Sec. 173.33.)
    (b) Substitute packagings. A particular Specification portable tank 
may be substituted for another portable tank as follows:
    (1) An IM or UN portable tank may be used whenever an IM or UN 
portable tank having less stringent requirements is authorized provided 
the portable tank meets or exceeds the requirements for pressure-relief 
devices, bottom outlets and any other special provisions specified in 
Sec. 172.102(c)(7)(vi) of this subchapter.
    (2) Where a Specification IM101 or IM102 portable tank is 
prescribed, a UN portable tank or Specification 51 portable tank 
otherwise conforming to the special commodity requirements of Sec. 
172.102(c)(7) of this subchapter for the material to be transported may 
be used.
    (3) A DOT Specification 51 portable tank may be used whenever a DOT 
Specification 56, 57, or 60 portable tank is authorized. A DOT 
Specification 60 portable tank may be used whenever a DOT Specification 
56 or 57 portable tank is authorized. A higher integrity tank used 
instead of a specified portable tank must meet the same design profile; 
for example, a DOT Specification 51 portable tank must be lined if used 
instead of a lined DOT Specification 60 portable tank.
    (c) Grandfather provisions for portable tanks--(1) Continued use of 
Specification 56 and 57 portable tanks. Continued use of an existing 
portable tank constructed to DOT Specification 56 or 57 is authorized 
only for a portable tank constructed before October 1, 1996. A stainless 
steel portable tank internally lined with polyethylene that was 
constructed on or before October 1, 1996, and that meets all 
requirements of DOT Specification 57 except for being equipped with a 
polypropylene discharge ball valve and polypropylene secondary discharge 
opening closure, may be marked as a Specification 57 portable tank and 
used in accordance with the provisions of this section.
    (2) A DOT Specification 51, IM 101, or IM 102 portable tank may not 
be manufactured after January 1, 2003; however, such tanks may continue 
to be used for the transportation of a hazardous material provided they 
meet the requirements of this subchapter, including the specification 
requirements and the requirements of this subchapter for the 
transportation of the particular hazardous material according to the T 
codes in effect on September 30, 2001 or the new T codes in Sec. 
172.102(c)(7)(i) (see Sec. 171.14(d)(4) for transitional provisions 
applicable to T codes), and provided

[[Page 447]]

the portable tanks conform to the periodic inspection and tests 
specified for the particular portable tank in subpart G of part 180 of 
this subchapter. After January 1, 2003, all newly manufactured portable 
tanks must conform to the requirements for the design, construction and 
approval of UN portable tanks as specified in Sec. Sec. 178.273, 
178.274, 178.275, 178.276, 178.277 and part 180, subpart G, of this 
subchapter.
    (3) A DOT Specification portable tank manufactured prior to January 
1, 1992 that is equipped with a non-reclosing pressure relief device may 
continue in service for the hazardous materials for which it is 
authorized. Except for a DOT Specification 56 or 57 portable tank, a DOT 
Specification portable tank manufactured after January 1, 1992, used for 
materials meeting the definition for Division 6.1 liquids, Packing Group 
I or II, Class 2 gases, or Class 3 or 4 liquids, must be equipped with a 
reclosing pressure relief valve having adequately sized venting capacity 
unless otherwise specified in this subchapter (see Sec. Sec. 
178.275(f)(1) and 178.277 of this subchapter).
    (4) Any portable tank container constructed prior to May 15, 1950, 
complying with the requirements of either the ASME Code for Unfired 
Pressure Vessels, 1946 Edition, or the API ASME Code for Unfired 
Pressure Vessels, 1943 Edition, may be used for the transportation of 
liquefied compressed gas, provided it fulfills all the requirements of 
the part and specifications for the particular gas or gases to be 
transported. Such portable tanks must be marked ``ICC Specification 
51X'' on the plate required by the specification, except as modified by 
any or all of the following:
    (i) Portable tanks designed and constructed in accordance with Pars. 
U-68, U-69, or U-201 of the ASME Code, 1943 and 1946 editions, may be 
used. Portable tanks designed and constructed in accordance with Par. U-
68 or Par. U-69 may be re-rated at a working pressure 25 percent in 
excess of the design pressure for which the portable tank was originally 
constructed. If the portable tank is re-rated, the re-rated pressure 
must be marked on the plate as follows: ``Re-rated working pressure--
psig''.
    (ii) Loading and unloading accessories, valves, piping, fittings, 
safety and gauging devices, do not have to comply with the requirements 
for the particular location on the portable tank.
    (5) Any ICC Specification 50 portable tank fulfilling the 
requirements of that specification may be continued in service for 
transportation of a liquefied petroleum gas if it is retested every five 
years in accordance with the requirements in Sec. 180.605 of this 
subchapter. Use of existing portable tanks is authorized. New 
construction is not authorized.
    (d) Determination of an authorized portable tank. Prior to filling 
and offering a portable tank for transportation, the shipper must ensure 
that the portable tank conforms to the authorized specification and 
meets the applicable requirements in this subchapter for the hazardous 
material. The shipper must ensure that the MAWP, design pressure or test 
pressure of the portable tank, as applicable, is appropriate for the 
hazardous material being transported. Determination of the applicable 
pressure must take into account the maximum pressure used to load or 
unload the hazardous material, the vapor pressure, static head and surge 
pressures of the hazardous material and the temperatures that the 
hazardous material will experience during transportation.
    (e) External inspection prior to filling. Each portable tank must be 
given a complete external inspection prior to filling. Any unsafe 
condition must be corrected prior to its being filled and offered for 
transportation. The external inspection shall include a visual 
inspection of:
    (1) The shell, piping, valves and other appurtenances for corroded 
areas, dents, defects in welds and other defects such as missing, 
damaged, or leaking gaskets;
    (2) All flanged connections or blank flanges for missing or loose 
nuts and bolts;
    (3) All emergency devices for corrosion, distortion, or any damage 
or defect that could prevent their normal operation;
    (4) All required markings on the tank for legibility; and

[[Page 448]]

    (5) Any device for tightening manhole covers to ensure such devices 
are operative and adequate to prevent leakage at the manhole cover.
    (f) Loading requirements. (1) A hazardous material may not be loaded 
into a portable tank if the hazardous material would:
    (i) Damage the portable tank;
    (ii) React with the portable tank; or
    (iii) Otherwise compromise its product retention capability.
    (2) A hazardous material may not be loaded in a DOT Specification 
51, DOT Specification 60, an IM or UN portable tank unless the portable 
tank has a pressure relief device that provides total relieving capacity 
meeting the requirements of this subchapter.
    (3) Except during a pressure test, a portable tank may not be 
subjected to a pressure greater than its marked maximum allowable 
working pressure or, when appropriate, its marked design pressure.
    (4) A portable tank may not be loaded to a gross mass greater than 
the maximum allowable gross mass specified on its identification plate.
    (5) Except for a non-flowable solid or a liquid with a viscosity of 
2,680 centistokes (millimeters squared per second) or greater at 20 
[deg]C (68 [deg]F), an IM or UN portable tank, or compartment thereof, 
having a volume greater than 7,500 L (1,980 gallons) may not be loaded 
to a filling density of more than 20% and less than 80% by volume. This 
filling restriction does not apply if a portable tank is divided by 
partitions or surge plates into compartments of not more than 7,500 L 
(1,980 gallons) capacity; this portable tank must not be offered for 
transportation in an ullage condition liable to produce an unacceptable 
hydraulic force due to surge.
    (6) The outage for a portable tank may not be less than 2% at a 
temperature of 50 [deg]C (122 [deg]F) unless otherwise specified in this 
subchapter. For UN portable tanks, the applicable maximum filling limits 
apply as specified according to the assigned TP codes in Column (7) of 
the Sec. 172.101 Table of this subchapter except when transported 
domestically.
    (7) Each tell-tale indicator or pressure gauge located in the space 
between a frangible disc and a safety relief valve mounted in series 
must be checked after the tank is filled and prior to transportation to 
ensure that the frangible disc is leak free. Any leakage through the 
frangible disc must be corrected prior to offering the tank for 
transportation.
    (8) During filling, the temperature of the hazardous materials shall 
not exceed the limits of the design temperature range of the portable 
tank.
    (9) The maximum mass of liquefied compressed gas per liter (gallon) 
of shell capacity (kg/L or lbs./gal.) may not exceed the density of the 
liquefied compressed gas at 50 [deg]C (122 [deg]F). The portable tank 
must not be liquid full at 60 [deg]C (140 [deg]F).
    (g) Additional requirements for specific modal transport. In 
addition to other applicable requirements, the following apply:
    (1) A portable tank containing a hazardous material may not be 
loaded onto a highway or rail transport vehicle unless loaded entirely 
within the horizontal outline of the vehicle, without overhang or 
projection of any part of the tank assembly.
    (2) An IM or UN portable tank used for the transportation of 
flammable liquids by rail may not be fitted with non-reclosing pressure 
relief devices except in series with reclosing pressure relief valves.
    (3) A portable tank or Specification 106A or 110A multi-unit tank 
car containing a hazardous material may not be offered for 
transportation aboard a passenger vessel unless:
    (i) The vessel is operating under a change to its character of 
vessel certification as defined in Sec. 171.8 of this subchapter; and
    (ii) The material is permitted to be transported aboard a passenger 
vessel in the Sec. 172.101 Table of this subchapter.
    (h) Additional general commodity-specific requirements. In addition 
to other applicable requirements, the following requirements apply:
    (1) Each uninsulated portable tank used for the transportation of a 
liquefied compressed gas must have an exterior surface finish that is 
significantly reflective, such as a light-reflecting color if painted, 
or a bright reflective metal or other material if unpainted.

[[Page 449]]

    (2) If a hazardous material is being transported in a molten state, 
the portable tank must be thermally insulated with suitable insulation 
material of sufficient thickness that the overall thermal conductance is 
not more than 0.080 Btu per hour per square foot per degree Fahrenheit 
differential.
    (3) No person may offer a liquid hazardous material of Class 3, PG I 
or II, or PG III with a flash point of less than 100 [deg]F (38 [deg]C); 
Division 5.1, PG I or II; or Division 6.1, PG I or II, in an IM or UN 
portable tank that is equipped with a bottom outlet as authorized in 
Column (7) of the Sec. 172.101 Table of this subchapter by assignment 
of a T Code in the appropriate proper shipping name entry, for unloading 
to a facility while it remains on a transport vehicle with the power 
unit attached unless--
    (i) The tank outlets conform to Sec. 178.275(d)(3) of this 
subchapter; or
    (ii) The facility at which the IM or UN portable tank is to be 
unloaded conforms to the requirements in Sec. 177.834(o) of this 
subchapter.
    (i) Additional requirements for portable tanks other than IM 
specification and UN portable tanks. (1) The bursting strength of any 
piping and fittings must be at least four times the design pressure of 
the tank, and at least four times the pressure to which, in any 
instance, it may be subjected in service by the action of a pump or 
other device (not including safety relief valves) that may subject 
piping to pressures greater than the design pressure of the tank.
    (2) Pipe joints must be threaded, welded or flanged. If threaded 
pipe is used, the pipe and pipe fittings must not be lighter than 
Schedule 80 weight. Where copper tubing is permitted, joints must be 
brazed or be of equally strong metal union type. The melting point of 
brazing material may not be lower than 1,000 [deg]F (537.8 [deg]C). The 
method of joining tubing must not decrease the strength of the tubing 
such as by the cutting of threads.
    (3) Non-malleable metals may not be used in the construction of 
valves or fittings.
    (4) Suitable provision must be made in every case to allow for 
expansion, contraction, jarring and vibration of all pipe. Slip joints 
may not be used for this purpose.
    (5) Piping and fittings must be grouped in the smallest practicable 
space and must be protected from damage as required by the 
specification.
    (6) All piping, valves and fittings on every portable tank must be 
leakage tested with gas or air after installation and proved tight at 
not less than the design pressure of the portable tank on which they are 
used. In the event of replacement, all such piping, valves, or fittings 
must be tested in accordance with the requirements of this section 
before the portable tank is returned to transportation service. The 
requirements of this section apply to all hoses used on portable tanks, 
except that hoses may be tested either before or after installation on 
the portable tank.
    (7) All materials used in the construction of portable tanks and 
their appurtenances may not be subject to destructive attack by the 
contents of the portable tank.
    (8) No aluminum, copper, silver, zinc nor their alloys may be used. 
Brazed joints may not be used. All parts of a portable tank and its 
appurtenances used for anhydrous ammonia must be steel.
    (9) Each outlet of a portable tank used for the transportation of 
non-refrigerated liquefied compressed gases, except carbon dioxide, must 
be provided with a suitable automatic excess-flow valve (see definition 
in Sec. 178.337-1(g) of this subchapter). The valve must be located 
inside the portable tank or at a point outside the portable tank where 
the line enters or leaves the portable tank. The valve seat must be 
located inside the portable tank or may be located within a welded 
flange or its companion flange, or within a nozzle or within a coupling. 
The installation must be made in such a manner as to reasonably assure 
that any undue strain which causes failure requiring functioning of the 
valve shall cause failure in such a manner that it will not impair the 
operation of the valve.
    (i) A safety device connection or liquid level gauging device that 
is constructed so that the outward flow of the tank contents will not 
exceed that passed by an opening of 0.1397 cm (0.0550 inches) is not 
required to be equipped with excess-flow valves.

[[Page 450]]

    (ii) An excess-flow valve must close automatically if the flow 
reaches the rated flow of gas or liquid specified by the original valve 
manufacturer when piping mounted directly on the valve is sheared off 
before the first valve, pump, or fitting downstream from the excess flow 
valve.
    (iii) An excess-flow valve may be designed with a by-pass, not to 
exceed a 0.1016 cm (0.040 inches) diameter opening to allow equalization 
of pressure.
    (iv) Filling and discharge lines must be provided with manually 
operated shut-off valves located as close to the tank as practical. 
Unless this valve is manually operable at the valve, the line must also 
have a manual shut-off valve. The use of ``Stop-Check'' valves to 
satisfy with one valve the requirements of this section is forbidden. 
For portable tanks used for refrigerated liquefied gases, a ``stop 
check'' valve may be used on the vapor side of the pressure buildup 
circuit.
    (10) Each portable tank used for carbon dioxide or nitrous oxide 
must be lagged with a suitable insulation material of such thickness 
that the overall thermal conductance is not more than 0.08 Btu per 
square foot per degree Fahrenheit differential in temperature per hour. 
The conductance must be determined at 60 [deg]Fahrenheit. Insulation 
material used on portable tanks for nitrous oxide must be 
noncombustible.
    (11) Refrigerating or heating coils must be installed in portable 
tanks used for carbon dioxide and nitrous oxide. Such coils must be 
tested externally to at least the same pressure as the test pressure of 
the portable tank. The coils must also be tested internally to at least 
twice the working pressure of the heating or refrigerating system to be 
used, but in no case less than the test pressure of the portable tank. 
Such coils must be securely anchored. In the event of leakage, the 
refrigerant or heating medium to be circulated through the coil or coils 
must have no adverse chemical reaction with the portable tank or its 
contents.
    (12) Excess flow valves are not required for portable tanks used for 
the transport of refrigerated liquefied gases.

[66 FR 33427, June 21, 2001, as amended at 67 FR 15743, Apr. 3, 2002; 68 
FR 32413, May 30, 2003; 68 FR 57632, Oct. 6, 2003; 68 FR 75742, 75743, 
Dec. 31, 2003; 69 FR 54046, Sept. 7, 2004]