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Fuel supply system for marine structure having reliquefaction apparatus and high-pressure natural gas injection engine

a technology of reliquefaction apparatus and fuel supply system, which is applied in the direction of machines/engines, lighting and heating apparatus, and container discharging methods, etc., can solve the problems of low liquefaction efficiency, flash gas may be generated, and low reliquefaction efficiency, so as to reduce the load, efficiently supply, and minimize the energy consumption of the reliquefaction apparatus

Inactive Publication Date: 2014-03-06
DAEWOO SHIPBUILDING & MARINE ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention provides a fuel supply system for a high-pressure natural gas injection engine. The system uses the excess gas (BOG) generated in a liquefied gas storage tank as fuel for the engine. The BOG is compressed to a medium pressure and then liquefied using a reliquefaction apparatus. The liquefied BOG is then sent to the engine. This system has several technical benefits: efficient fuel supply, minimized energy consumption, reduced load on the reliquefaction apparatus, reduced thermal stress, reduced size of the apparatus, and reduced power requirements. The system also uses a nonflammable mixed refrigerant for safer and more efficient reliquefaction of the BOG.

Problems solved by technology

The generated natural gas may increase the internal pressure of the storage tank and accelerate the flow of the natural gas due to the rocking of the vessel, causing structural problems.
However, the LNG stored in the storage tank is maintained at an ambient pressure state, and therefore, if a pressure of the liquefied BOG is excessively high, flash gas may be generated when the BOG is returned to the storage tank.
Consequently, the BOG needs to be compressed to the above-mentioned low pressure of about 4 to 8 bara, in spite of low reliquefaction efficiency.
Also, it is well known in the art that it is technically inappropriate to compress BOG to a pressure higher than the above-mentioned pressure.
Meanwhile, since the nitrogen refrigeration cycle uses nitrogen gas (N2) as a refrigerant, the liquefaction efficiency is low.
Also, the mixed refrigerant cycle uses a refrigerant mixed with nitrogen and hydrocarbon gases as a refrigerant, the stability is low.
The nitrogen reverse Brayton cycle used for the offshore LNG liquefaction apparatus is relatively simple in the configuration of the apparatus and thus is advantageous to a limited vessel or offshore plant, but has low efficiency.
The mixed-refrigerant Joule-Thomson refrigeration cycle used for the onshore LNG liquefaction plant has relatively high efficiency but is complicated in the configuration of the apparatus because a separator needs to be used for separating a mixed refrigerant when a gaseous state and a liquid state coexist due to the feature of the mixed refrigerant.

Method used

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  • Fuel supply system for marine structure having reliquefaction apparatus and high-pressure natural gas injection engine
  • Fuel supply system for marine structure having reliquefaction apparatus and high-pressure natural gas injection engine
  • Fuel supply system for marine structure having reliquefaction apparatus and high-pressure natural gas injection engine

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first embodiment

Modified Example of First Embodiment

[0090]FIG. 3B illustrates a fuel supply system according to a modified example of the first embodiment of the present invention. Since the modified example of the first embodiment is partially different from the first embodiment in terms of the configurations of a BOG compression unit 13 and a liquefaction apparatus 20, only the difference therebetween will be described below.

[0091]The modified example of the first embodiment illustrated in FIG. 3B is substantially identical to the first embodiment illustrated in FIG. 3A in that the BOG compressing unit 13 includes five BOG compressors 14, but is different from the first embodiment in that an intermediate cooler 15 is not disposed between the first and second BOG compressors and between the second and third BOG compressors included in the BOG compression unit 13. According to the present invention, the intermediate cooler 15 may or may not be disposed between every two BOG compressors 14.

[0092]Als...

second embodiment

Modified Example of Second Embodiment

[0117]FIG. 7B is a configuration diagram illustrating a fuel supply system according to a modified example of the second embodiment of the present invention. As described in the modified example of the first embodiment, the modified example of the second embodiment is partially different from the second embodiment in terms of the configurations of a BOG compression unit 13 and a reliquefaction apparatus 20.

[0118]That is, the modified example of the second embodiment is substantially identical to the second embodiment in that the BOG compression unit 13 includes five BOG compressors 14, but is different from the second embodiment in that an intermediate cooler 15 is not disposed between the first and second BOG compressors and between the second and third BOG compressors included in the BOG compression unit 13. According to the present invention, the intermediate cooler 15 may or may not be disposed between every two BOG compressors 14.

[0119]Like ...

third embodiment

Modified Example of Third Embodiment

[0125]FIG. 8B is a configuration diagram illustrating a fuel supply system according to a modified example of the third embodiment of the present invention. The modified example of the third embodiment is partially different from the third embodiment in terms of the configuration of a reliquefaction apparatus 20.

[0126]That is, like the reliquefaction apparatus 20 according to the modified example of the first embodiment illustrated in FIG. 3B, the reliquefaction apparatus 20 according to the modified example of the third embodiment includes a cold box 21 configured to exchange heat between a refrigerant and BOG, a compression unit configured to compress the refrigerant that is heated and at least partially gasified by the cold box 21, an expansion unit configured to expand the compressed refrigerant to reduce the temperature thereof, and a gas-liquid refrigerant separator configured to separate the gaseous refrigerant and the liquid refrigerant.

[0...

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Abstract

Provided is a fuel supply system for a marine structure. The fuel supply system includes a BOG compression unit configured to receive and compress BOG generated in a storage tank, a reliquefaction apparatus configured to receive and liquefy the BOG compressed by the BOG compression unit, a high-pressure pump configured to compress the liquefied BOG generated by the reliquefaction apparatus, and a high-pressure gasifier configured to gasify the liquefied BOG compressed by the high-pressure pump. The fuel supply system includes a recondenser installed at an upstream side of the high-pressure pump and configured to recondense a portion or all of the generated BOG by using liquefied gas received from the storage tank. The BOG compression unit compresses BOG to a pressure of about 12 to 45 bara such that the BOG is liquefied under the compression pressure of the BOG compression unit.

Description

TECHNICAL FIELD[0001]The present invention relates to a fuel supply system for a high-pressure natural gas injection engine, and more particularly, to a fuel supply system for a marine structure such as a liquefied natural gas (LNG) carrier having a boil-off gas (BOG) reliquefaction apparatus and a high-pressure natural gas injection engine (e.g., a MAN Electronic-Gas Injection (ME-GI) engine), which can efficiently supply fuel to the high-pressure natural gas injection engine and minimize energy consumption in the BOG reliquefaction apparatus.BACKGROUND ART[0002]Recently, the consumption of natural gas, such as liquefied natural gas (LNG) or liquefied petroleum gas (LPG), has been rapidly increasing throughout the world. Liquefied gas is transported in a gaseous state through onshore or offshore gas pipelines, or transported to a remote consumption place while being stored in a liquefied state inside a liquefied gas carrier. Liquefied gas, such as LNG or LPG, is obtained by cooling...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): F25J1/00
CPCF25J1/0025F02M21/0227F02M21/0245F02M21/0287F25J1/0052F25J1/0097F25J1/0212F25J1/023F25J1/0254F25J1/0277F25J1/0278F25J1/0291F25J2220/62F25J2230/08F25J2230/30F25J2230/60F25J2235/60F25J2290/62F17C13/004F17C2201/052F17C2221/033F17C2223/0161F17C2265/034F17C2265/037F17C2265/066F17C2270/0105F17C2270/0113F25J1/0045F25J2205/30Y02T10/30F25J2215/02F25J2205/90F17C5/04
Inventor JUNG, SEUNG KYOJUNG, JE HEONLEE, JUNG HANLEE, SUNG JUNSHIN, HYUN JUNCHOI, DONG KYU
Owner DAEWOO SHIPBUILDING & MARINE ENG CO LTD
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