IP Library Granted Patent US 10,006,589
Granted Patent B2
US 10,006,589 · App. 15/084,279 · Granted Jun 26, 2018

Method and system for storage and transport of liquefied petroleum gases

Inventor: Carl Jørgen Rummelhoff (Moss, NO)
Assignee: WÄRTSILÄ OIL & GAS SYSTEMS AS
F17C9/02F17C13/004F25J1/0025F25J1/0236F25J1/0271F25J1/0277F17C2205/013F17C2205/0338F17C2221/035F17C2223/0153F17C2227/0135F17C2227/0157F17C2227/0164F17C2227/0339F17C2227/0341F17C2227/0351F17C2227/0388F17C2250/01F17C2260/013F17C2265/017F17C2265/034F17C2270/0105F25J2215/64F25J2215/66F25J2290/62
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Quick Facts
Patent No.
US 10,006,589
App. No.
15/084,279
Granted
Jun 26, 2018
Kind
B2
Abstract

A method for storage and transport of LPG on LPG carriers, in particular two cargoes of different LPG types on same shipment, having reliquefaction units in which vaporized gases are condensed and then returned into at least one cargo tank for the respective LPG cargo type. The method is further comprising: using the reliquefaction units, at a minimum one running, as to condense vapor from the first cargo type; passing the condensed vapor through a heat exchanger; simultaneously flowing vapor from the second cargo type through the heat exchanger as to condense vapor by means of heat exchanging with the condensed vapor; and returning the condensed vapors leaving the heat exchanger back into the respective cargo types. The present invention is also disclosing a system for storage and transport of LPG on LPG carriers.

Claims (16)

1. A method for storage and transport of liquefied petroleum gas (LPG) on LPG carriers, including two cargoes of different LPG types on same shipment, having reliquefaction units in which vaporized gases are condensed and then returned into at least one cargo tank for the respective LPG cargo type, the method comprising:

using the reliquefaction units containing a first refrigerant, at a minimum one running, so as to condense vapor from a first one of the two cargo types (first LPG type) to yield a first condensed vapor using the first refrigerant;

passing the first condensed vapor through a heat exchanger;

simultaneously flowing vapor from a second one of the two cargo types (second LPG type) through the heat exchanger so as to condense the vapor from the second LPG type to yield a second condensed vapor using the first condensed vapor as a second refrigerant;

returning the first and second condensed vapors leaving the heat exchanger back into the respective cargo types; and

throttling the first condensed vapor from the reliquefaction units upstream or downstream of the heat exchanger as to meet pressure requirements,

wherein the first refrigerant, the first LPG type, and the second LPG type are separate from each other and have different flow paths.

2. The method according to claim 1 , further comprising: throttling the condensed vapor in two stages as to meet the pressure requirements.

3. A system for storage and transport of liquefied petroleum gas (LPG) on LPG carriers, including two cargoes of different LPG types on same shipment, having reliquefaction units in which vaporized gases are condensed and then returned into at least one cargo tank for the respective LPG cargo type, comprising:

reliquefaction units containing a first refrigerant and configured, at a minimum one running, to condense first vapor from a first one of the two cargo types (first LPG type) using the first refrigerant;

a heat exchanger configured to let the first condensed vapor pass therethrough;

the heat exchanger being further configured to allow vapor from a second one of the two cargo types (second LPG type) to simultaneously flow therethrough to condense the vapor from the second LPG type to yield a second condensed vapor using the first condensed vapor as a second refrigerant;

the heat exchanger having an outlet enabling the first and second condensed vapors leaving the heat exchanger to return back into the respective cargo types;

the first condensed vapor from the reliquefaction units being throttled using a throttle valve arranged in flow lines upstream or downstream of the heat exchanger, respectively, and

the first refrigerant, the first LPG type, and the second LPG type being separate from each other and having different flow paths.

4. The system according to claim 3 , wherein the first condensed vapor from the reliquefaction units is throttled in two stages.

Assignments (3)
CHANGE OF NAME Recorded Mar 5, 2025
From: WÄRTSILÄ OIL & GAS SYSTEMS AS
To: WÄRTSILÄ GAS SOLUTIONS NORWAY AS
Reel/Frame 070419/0041 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 30, 2018
From: RUMMELHOFF, CARL JØRGEN
To: HAMWORTHY OIL & GAS SYSTEMS AS
Reel/Frame 044778/0412 →
CHANGE OF NAME Recorded Jan 30, 2018
From: HAMWORTHY OIL & GAS SYSTEMS AS
To: WÄRTSILÄ OIL & GAS SYSTEMS AS
Reel/Frame 045196/0607 →
Priority Claims (1)
NO 20092477 · Jun 30, 2009 · national
Continuity (2)
Division 13143023
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