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371 

Pipeline and Haz. Matls. Safety Admin., DOT 

§ 172.102 

the ‘‘T’’ Code. If a frangible disc is re-
quired in series with the reclosing pres-
sure relief device for the specified port-
able tank, the alternative portable 
tank must be fitted with a frangible 
disc in series with the reclosing pres-
sure relief device; and 

(D) With regard to bottom openings— 
(

1

) When two effective means are 

specified, the alternative portable tank 
is fitted with bottom openings having 
two or three effective means of closure 
or no bottom openings; or 

(

2

) When three effective means are 

specified, the portable tank has no bot-
tom openings or three effective means 
of closure; or 

(

3

) When no bottom openings are au-

thorized, the alternative portable tank 
must not have bottom openings. 

(vi) Except when an organic peroxide 

is authorized under § 173.225(g), if a haz-
ardous material is not assigned a port-
able tank ‘‘T’’ Code, the hazardous ma-
terial may not be transported in a 
portable tank unless approved by the 
Associate Administrator. 

(8) 

‘‘TP’’ codes. 

(i) These provisions 

apply to the transportation of haz-
ardous materials in IM and UN Speci-
fication portable tanks. Portable tank 
special provisions are assigned to cer-
tain hazardous materials to specify re-
quirements that are in addition to 
those provided by the portable tank in-
structions or the requirements in part 
178 of this subchapter. Portable tank 
special provisions are designated with 
the abbreviation TP (tank provision) 
and are assigned to specific hazardous 
materials in Column (7) of the § 172.101 
Table. 

(ii) The following is a list of the port-

able tank special provisions: 

Code/Special Provisions 

TP1

The maximum degree of filling must 

not exceed the degree of filling determined 
by the following: 

Degree of filling

=

+

(

)


⎝⎜


⎠⎟

97

1

α

t

t

r

f

.

Where: 

t

r

is the maximum mean bulk temperature 

during transport, and t

f

is the tempera-

ture in degrees celsius of the liquid dur-
ing filling. 

TP2

a. The maximum degree of filling 

must not exceed the degree of filling deter-
mined by the following: 

Degree of filling

=

+

(

)


⎝⎜


⎠⎟

95

1

α

t

t

r

f

.

Where: 

t

r

is the maximum mean bulk temperature 

during transport, 

t

f

is the temperature in degrees celsius of the 

liquid during filling, and 

is the mean coefficient of cubical expan-

sion of the liquid between the mean tem-
perature of the liquid during filling (t

f

and the maximum mean bulk tempera-
ture during transportation (t

r

) both in 

degrees celsius. 

b. For liquids transported under ambient 

conditions 

may be calculated using the for-

mula: 

α =

d

d

d

15

50

50

35

Where: 

d

15

and d

50

are the densities (in units of mass 

per unit volume) of the liquid at 15 

°

C (59 

°

F) and 50 

°

C (122 

°

F), respectively. 

TP3

The maximum degree of filling (in %) 

for solids transported above their melting 
points and for elevated temperature liquids 
shall be determined by the following: 

Degree of filling = 95

d

d

r

f


⎝⎜


⎠⎟

.

Where: d

f

and d

r

are the mean densities of the 

liquid at the mean temperature of the liquid 
during filling and the maximum mean bulk 
temperature during transport respectively. 

TP4

The maximum degree of filling for 

portable tanks must not exceed 90%. 

TP5

For a portable tank used for the 

transport of flammable refrigerated liquefied 
gases or refrigerated liquefied oxygen, the 
maximum rate at which the portable tank 
may be filled must not exceed the liquid flow 
capacity of the primary pressure relief sys-
tem rated at a pressure not exceeding 120 
percent of the portable tank’s design pres-
sure. For portable tanks used for the trans-
port of refrigerated liquefied helium and re-
frigerated liquefied atmospheric gas (except 
oxygen), the maximum rate at which the 
tank is filled must not exceed the liquid flow 
capacity of the pressure relief device rated 
at 130 percent of the portable tank’s design 
pressure. Except for a portable tank con-
taining refrigerated liquefied helium, a port-
able tank shall have an outage of at least 
two percent below the inlet of the pressure 
relief device or pressure control valve, under 

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