AU2002232050A1 - Transportation of liquefiable petroleum gas - Google Patents

Transportation of liquefiable petroleum gas

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Publication number
AU2002232050A1
AU2002232050A1 AU2002232050A AU2002232050A AU2002232050A1 AU 2002232050 A1 AU2002232050 A1 AU 2002232050A1 AU 2002232050 A AU2002232050 A AU 2002232050A AU 2002232050 A AU2002232050 A AU 2002232050A AU 2002232050 A1 AU2002232050 A1 AU 2002232050A1
Authority
AU
Australia
Prior art keywords
pressure vessel
petroleum gas
assembly
liquefiable petroleum
vessel assembly
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
AU2002232050A
Other versions
AU2002232050B2 (en
Inventor
Donegal Harold Victor Carroll
Graham Christopher Pye
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
African Oxygen Ltd
Original Assignee
African Oxygen Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by African Oxygen Ltd filed Critical African Oxygen Ltd
Priority claimed from PCT/IB2002/000427 external-priority patent/WO2002065015A2/en
Publication of AU2002232050A1 publication Critical patent/AU2002232050A1/en
Application granted granted Critical
Publication of AU2002232050B2 publication Critical patent/AU2002232050B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

TRANSPORTATION OF LIQUEFIABLE PETROLEUM GAS
THIS INVENTION relates to the transportation of liquefiable petroleum
gas (LPG) . In particular, it relates to a transportable pressure vessel assembly for
housing liquefiable petroleum gas, to a vehicle which includes such a pressure
vessel assembly, and to a method of transporting liquefiable petroleum gas.
According to one aspect of the invention, there is provided a
transportable pressure vessel assembly for housing liquefiable petroleum gas,
which includes a pressure vessel that is generally cylindrical, having a circular
cross-sectional profile, and being dimensioned such that a value (R) expressed by
r?=(— ).10 D'
is smaller than approximately 8 megapascals, wherein
e is a thickness of a cylindrical wall of the pressure vessel, in meters;
f is a design strength of a material from which the pressure vessel is made,
in megapascals; and
D is an internal diameter of the pressure vessel, in meters.
The design strength of the material is defined as the minimum of either the yield strength divided by 1 , 5 or the tensile strength divided by 2,5. The
yield strength and tensile strength for the material are as per recognized material
standard specifications.
The term "transportable pressure vessel assembly" as used herein is
intended to mean any pressure vessel assembly which is designed and/or
configured for transport by a land transport vehicle, such as a road transport
vehicle, a train, or the like.
Typically, the thickness (e) of the wall of the pressure vessel is 0,003
to 0,01 1 m, while the internal diameter (D) of the pressure vessel may be 1 to
2,6m. A pressure vessel having these dimensions should be readily transportable
by conventional road transport vehicles, such as heavy transport trucks.
The pressure vessel assembly may include a temperature control
means operatively associated with the pressure vessel, to control the temperature
of LPG in the pressure vessel.
The term "temperature control means" as used herein is intended to
include any arrangement for permitting, at least, an increased degree of control
over the temperature of LPG in the pressure vessel, or for reducing or inhibiting the
rate of change of temperature of LPG in the pressure vessel. The temperature
control means thus includes insulation means, cooling means, and the like. In a particular embodiment of the invention, the temperature control
means is an insulation means for insulating the pressure vessel to inhibit heat
transfer between the atmosphere and the interior of the pressure vessel.
The insulation means may be a thermal insulation jacket provided on
the pressure vessel. Advantageously, the thermal insulation jacket may be of a fire
resistant material. In one such embodiment, the insulation jacket includes a
number of continuous circumferentially extending layers of ceramic fibre blanket,
the layers being located radially outwardly of the pressure vessel.
The pressure vessel assembly may, in addition, have a
circumferentially extending layer of cladding around the insulation jacket, so that
the insulation jacket is sandwiched between the wall of the pressure vessel and the
layer of cladding, the layer of cladding defining the outer surface of the pressure
vessel assembly.
In another embodiment of the invention, the temperature control
means is in the form of a cooling means for cooling liquefiable petroleum gas in the
pressure vessel. The cooling means may, for instance, be a refrigeration plant
which includes a cooling element operatively connected to the refrigeration plant
and located within the pressure vessel, for refrigerating liquefiable petroleum gas in the pressure vessel.
According to another aspect of the invention, there is provided a land transport vehicle which includes a transportable pressure vessel assembly as
described above.
The vehicle may, for instance, be a road transport vehicle, such as a
heavy transport vehicle.
According to a further aspect of the invention, there is provided a
method of transporting a liquefiable petroleum gas, which method includes the
steps of housing liquefiable petroleum gas in a pressure vessel assembly as
described above, and transporting the pressure vessel to a desired location.
Typically, the method includes the step of controlling the temperature
of the liquefiable petroleum gas in the pressure vessel.
The step of controlling the temperature of the liquefiable petroleum
gas may include cooling the liquefiable petroleum gas.
The invention will now be further described, by way of example, with
reference to the accompanying diagrammatic drawings, in which
Figure 1 is a schematic side-elevation of a vehicle in accordance with the invention; and
Figure 2 is a schematic cross-section of a pressure vessel assembly forming
part of the vehicle of Figure 1 , on an enlarged scale, taken at ll-ll in Figure 1 ; and
Figure 3 is a schematic side-elevation of a further embodiment of a vehicle in accordance with the invention.
In Figures 1 and 2 of the drawings, reference numeral 1 0 generally
indicates a vehicle in accordance with the invention. The vehicle is a road
transport vehicle in the form of a transport tanker 1 0. The tanker 1 0 includes a
horse or truck 1 2, which is connected to a trailer 14 on which a load is supported,
the load being a pressure vessel assembly 1 9 for housing liquefiable petroleum gas
(LPG) 24. The assembly 1 9 includes a pressure vessel 20 that is cylindrical,
having a circular cross-sectional profile, with hemispherical ends 22 closing off the
cylindrical portion to form an enclosed storage space 21 . It will be appreciated
that, in other embodiments of the invention, the ends can be ellipsoidal, or can
have any other suitable shape.
In this example, the liquefiable petroleum gas 24 contained in the
pressure vessel 20 is a mixture of propane and butane. At conventional operating
temperatures, the LPG 24 is partly liquid 30 and partly gas 32. The volume of the
storage space 21 occupied by the gas phase LPG 32 is referred to as the ullage.
A cylindrical wall 26 of the pressure vessel 20 is of plate steel having
a constant thickness (e) . The pressure vessel 20 is covered by an insulation jacket
40 of a thermal insulation material. In this case, the thermal insulation jacket 40
includes two circumferentially extending continuous layers 28 of 64 kg/m^ ceramic
fibre blanket, each layer 28 being approximately 25 mm thick, and the inner layer
28 being in contact with the radially outwardly facing surface of the pressure vessel wall 26. A radially outer, circumferentially extending layer of stainless steel
cladding 38 is provided around the insulation jacket 40. This insulation jacket 40
thus not only provides thermal insulation to the pressure vessel 20, but also offers
protection against the impingement of fire on the pressure vessel 20.
In use, the insulation jacket 40 inhibits heat transfer between the
atmosphere and the interior of the pressure vessel 20, as the combination of the pressure vessel wall 26 and the insulation jacket 40 has a considerably higher
coefficient of thermal conductivity than the pressure vessel walls of conventional
LPG tankers, which often comprise only steel plate. An outer surface 42 of the
cladding 38 also has a relatively high coefficient of surface absorptivity, to inhibit
the absorption of heat from solar radiation. Conventionally, refrigerated LPG is
loaded into a transportable pressure vessel assembly which is then transported to
a desired location, the temperature of the LPG in the tanker gradually increasing
owing to heat transfer between the interior of the pressure vessel and the
atmosphere, which is usually at a higher temperature.
As a result of the insulation jacket 40, the rate of increase of the
temperature of the LPG 24 in the pressure vessel 20 will be less than that of LPG
housed in a conventional uninsulated pressure vessel. During a test conducted by
the Applicant, the tanker 1 0 and a conventional uninsulated tanker were exposed
to extreme operating conditions. After exposure to these conditions for a particular
amount of time, the temperature of the LPG 24 in the insulated vessel 20 was
approximately 40°C, compared to approximately 53°C for the LPG in the control tanker. As a result of its lower temperature, the pressure of the gas portion 32 of
the LPG 24 in the pressure vessel 20 was also lower, being about 1 ,35 Mpa
(absolute), as opposed to about 1 , 8 Mpa (absolute) of the control tanker.
Conventionally, a maximum expected temperature (design
temperature), or a corresponding maximum expected gas pressure (design
pressure), of LPG in a pressure vessel is used as a point of departure for calculating
the dimensions of the pressure vessel according to a standardised design code.
An eventual thickness (e) of a wall of the pressure vessel is directly proportional
to the design pressure, while an internal diameter (D) of the pressure vessel is
inversely proportional to the design pressure.
The Applicant has found that a lower design pressure, or a lower
design temperature, can be used for calculating the dimensions of the pressure
vessel 20 when it is provided with the insulation jacket 40. This lower design
temperature results in the pressure vessel 40 being designed to have a smaller wall
thickness (e) and/or a larger internal diameter (D) than would normally be the case.
The Applicant has thus found that the dimensions of the pressure vessel 20 can
be designed in accordance with a standardised design code by using the reduced
design pressure as a point of departure, such that a value (R) which is expressed
by
D'
is equal to or smaller than about 8 megapascals, which is not the case with conventional transportable pressure vessels. In this case, the design codes used were BS5500 and BS71 22, although similar results will follow from using other
standard design codes such as ASME 8 or AS 1 21 0.
The pressure vessel 20 was designed in accordance with this
approach, using a reduced design pressure of 1 ,3 MPa (gauge pressure) . The
calculated thickness (e) of the steel plate forming the wall 26 of the pressure
vessel 20 is approximately 0,0084 m, the steel having a design strength of about
208 Mpa. The internal diameter (D) of the pressure vessel 20 is 2,44 m.
Consequently, the value of R is about 7, 1 6 Mpa.
The wall thickness (e) thus calculated is smaller than would have been
the case with a conventional design approach. This reduced thickness (e) leads to
a considerable reduction in the tare mass of the tanker 1 0. The truck 1 2 thus has
a lighter load to tow, and transport costs are reduced due to improved efficiency.
In cases where the amount of LPG 24 which can be carried by a tanker is limited
by the power of the truck, more LPG can be carried by the tanker if it is provided
with the transportable pressure vessel 20 having the insulation jacket 40.
Naturally, this will only be the case if the insulation jacket 40 has a mass which is
lower than the difference in mass between a conventional pressure vessel and the
pressure vessel 20 with a reduced wall thickness. If a different design approach
is followed, the pressure vessel 21 can be designed to have a larger internal
diameter (D), leading to obvious advantages. The Applicant has further found that, with the insulated pressure
vessel 20, a smaller ullage is required than is the case with conventional pressure vessels.
In Figure 3 of the drawings, reference numeral 50 indicates a further
embodiment of a LPG tanker in accordance with the invention, with like reference
numerals indicating like parts in the embodiment of Figures 1 and 2, and the
embodiment of Figure 3.
The tanker 50 has a pressure vessel 54 and insulation jacket 40
similar to that of the tanker 1 0 of Figures 1 and 2, but the tanker 50 includes a
cooling means in the form of a refrigeration plant 52 carried on the trailer 14 and
operatively associated with the pressure vessel 20 to cool the LPG 24 in the
pressure vessel 54. To this end, the refrigeration plant 52 is provided with a
cooling element 56 comprising a number of coils located in the storage space 21
of the pressure vessel 20.
In use, the refrigeration plant 52, via the cooling element 56, cools the
LPG 24 in the pressure vessel 20, thus limiting the temperature of the LPG 24 to
a predetermined value. Although the insulation jacket 40 assists in controlling the
temperature of the LPG 24 by inhibiting heat transfer through the pressure vessel
wall 26, it will be appreciated that the insulation jacket 40 can be omitted, if
desired. Due to the operation of the refrigeration plant 52, the temperature of the
LPG 24 in the pressure vessel 54 will not rise above the predetermined value, so that the dimensions of the pressure vessel 54 can be calculated accordingly, using said predetermined temperature as design temperature.

Claims (19)

CLAIMS:
1 . A transportable pressure vessel assembly for housing liquefiable
petroleum gas, which includes a pressure vessel that is generally cylindrical, having
a circular cross-sectional profile, and being dimensioned such that a value (R)
expressed by
/?=(— ).10
D ' is smaller than approximately 8 megapascals, wherein
e is a thickness of a cylindrical wall of the pressure vessel, in meters;
f is a design strength of a material from which the pressure vessel is made,
in megapascals; and
D is an internal diameter of the pressure vessel, in meters.
2. A pressure vessel assembly as claimed in claim 1 , in which the
thickness (e) of the wall of the pressure vessel is between 0,003 and 0,01 1 m.
3. A pressure vessel assembly as claimed in claim 1 or claim 2, in which the internal diameter (D) of the pressure vessel is between 1 and 2,6 m.
4. A pressure vessel assembly as claimed in any one of the preceding
claims, which includes a temperature control means operatively associated with the pressure vessel.
5. A pressure vessel assembly as claimed in claim 4, in which the
temperature control means is an insulation means for insulating the pressure vessel
to inhibit heat transfer between the atmosphere and the interior of the pressure
vessel.
6. A pressure vessel assembly as claimed in claim 5, in which the
insulation means is a thermal insulation jacket provided on the pressure vessel.
7. A pressure vessel assembly as claimed in claim 6, in which the
thermal insulation jacket is of a fire resistant material.
8. A pressure vessel assembly as claimed in claim 6 or claim 7, in which
the insulation jacket includes a number of continuous circumferentially extending
layers of ceramic fibre blanket, the layers being located radially outwardly of the
pressure vessel.
9. A pressure vessel assembly as claimed in claim 6, claim 7, or claim
8, which includes a circumferentially extending layer of cladding around the
insulation jacket, so that the insulation jacket is sandwiched between the wall of
the pressure vessel and the layer of cladding.
1 0. A pressure vessel assembly as claimed in any one of claims 4 to 9
inclusive, in which the temperature control means is in the form of a cooling means for cooling liquefiable petroleum gas in the pressure vessel.
1 1 . A pressure vessel assembly as claimed in claim 1 0, in which the
cooling means is a refrigeration plant which includes a cooling element operatively
connected to the refrigeration plant and located within the pressure vessel, for
refrigerating liquefiable petroleum gas in the pressure vessel.
1 2. A land transport vehicle which includes a transportable pressure vessel
assembly as claimed in any one of claims 1 to 1 1 inclusive.
1 3. A vehicle as claimed in claim 1 2, which is a road transport vehicle.
1 4. A method of transporting a liquefiable petroleum gas, which method
includes the steps of housing liquefiable petroleum gas in a pressure vessel
assembly as claimed in any one of claims 1 to 1 1 inclusive, and transporting the
pressure vessel assembly to a desired location.
1 5. A method as claimed in claim 14, which includes the step of
controlling the temperature of the liquefiable petroleum gas in the pressure vessel.
1 6. A method as claimed in claim 1 5, in which the step of controlling the
temperature of the liquefiable petroleum gas includes cooling the liquefiable petroleum gas.
1 7. A transportable pressure vessel assembly for housing liquefiable
petroleum gas, substantially as described herein with reference to the
accompanying drawings.
1 8. A land transport vehicle for liquefiable petroleum gas, substantially as
described herein with reference to the accompanying drawings.
1 9. A method of transporting a liquefiable petroleum gas, substantially as
described herein with reference to the accompanying drawings.
AU2002232050A 2001-02-13 2002-02-13 Transportation of liquefiable petroleum gas Expired - Fee Related AU2002232050B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
ZA2001/1227 2001-02-13
ZA200101227 2001-02-13
PCT/IB2002/000427 WO2002065015A2 (en) 2001-02-13 2002-02-13 Transportation of liquefiable petroleum gas

Publications (2)

Publication Number Publication Date
AU2002232050A1 true AU2002232050A1 (en) 2003-02-20
AU2002232050B2 AU2002232050B2 (en) 2007-01-25

Family

ID=25589066

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2002232050A Expired - Fee Related AU2002232050B2 (en) 2001-02-13 2002-02-13 Transportation of liquefiable petroleum gas

Country Status (4)

Country Link
US (1) US7024868B2 (en)
AU (1) AU2002232050B2 (en)
GB (1) GB2389411B (en)
WO (1) WO2002065015A2 (en)

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US7538275B2 (en) 2005-02-07 2009-05-26 Rockbestos Surprenant Cable Corp. Fire resistant cable
US9759383B2 (en) * 2011-07-08 2017-09-12 Capat Llc Multi-stage compression and storage system for use with municipal gaseous supply
KR200487398Y1 (en) 2014-08-04 2018-09-12 현대중공업 주식회사 Cargo reliquefaction apparatus of lpg ship
CN106122756A (en) * 2016-08-16 2016-11-16 中科赛德(北京)科技有限公司 A kind of liquefied natural gas tank car reclaiming BOG
CN106090597A (en) * 2016-08-16 2016-11-09 中科赛德(北京)科技有限公司 A kind of zero evaporation liquefied natural gas tank car
CN106440655A (en) * 2016-08-16 2017-02-22 中科赛德(北京)科技有限公司 Skid-mounted liquefying device for recycling BOG (Boil of gas) of LNG (liquefied natural gas) tank car
CN106196882B (en) * 2016-08-29 2019-05-14 中科赛德(北京)科技有限公司 A kind of cool-storage type gas liquefaction equipment
US11559964B2 (en) * 2019-06-06 2023-01-24 Northrop Grumman Systems Corporation Composite structures, composite storage tanks, vehicles including such composite storage tanks, and related systems and methods
FR3107701B1 (en) * 2020-03-02 2022-09-02 Etablissements Magyar Device for holding an inner tank of a cryogenic liquid transport tank

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