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System for supplying fuel to high-pressure natural gas injection engine having excess evaporation gas consumption means

a high-pressure natural gas and fuel supply technology, which is applied in the direction of machines/engines, liquefaction, lighting and heating apparatus, etc., can solve the problems of low liquefaction efficiency, low reliquefaction efficiency, flash gas generation, etc., and achieves a decrease in liquefaction energy, liquefaction energy consumption in reliquefaction, and the effect of increasing the liquefaction point of the bog

Inactive Publication Date: 2014-02-27
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 is about a fuel supply system for a high-pressure natural gas injection engine that uses excess boil-off gas (BOG). The system compresses the BOG to a medium pressure and then reliquefies it, reducing the energy consumed during the process. By using a nonflammable refrigerant and overcooling the liquefied BOG, the system becomes more efficient and safe. Overall, the invention prevents the generation of flash gas and reduces the size and power requirement of the high-pressure pump.

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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  • System for supplying fuel to high-pressure natural gas injection engine having excess evaporation gas consumption means
  • System for supplying fuel to high-pressure natural gas injection engine having excess evaporation gas consumption means
  • System for supplying fuel to high-pressure natural gas injection engine having excess evaporation gas consumption means

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first embodiment

Modified Example of First Embodiment

[0086]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.

[0087]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.

[0088]Als...

second embodiment

Modified Example of Second Embodiment

[0113]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.

[0114]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.

[0115]Like ...

third embodiment

Modified Example of Third Embodiment

[0121]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.

[0122]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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PUM

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Abstract

Provided is a fuel supply system for a high-pressure natural gas injection engine. The fuel supply system includes: a BOG compression unit configured to receive BOG, which is generated in a storage tank, from the storage tank and compress the received BOG to a pressure of 12 to 45 bara; a reliquefaction apparatus configured to receive and liquefy the BOG compressed by the BOG compression unit; a high-pressure pump configured to compress the BOG liquefied by the reliquefaction apparatus; a high-pressure gasifier configured to gasify the BOG compressed by the high-pressure pump and supply the gasified BOG to the high-pressure natural gas injection engine; and an excess BOG consumption unit configured to consume excess BOG corresponding to a difference between an amount of BOG generated in the storage tank and an amount of BOG required as fuel for the high-pressure natural gas injection engine.

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 high-pressure natural gas injection engine having an excess boil-off gas (BOG) consumption unit, which can consume excess BOG corresponding to a difference between an amount of BOG generated in the storage tank and an amount of BOG required as fuel for the high-pressure natural gas injection engine, when a larger amount of BOG than required as fuel for the high-pressure natural gas injection engine is generated.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,...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): F25J1/00
CPCF25J1/0025F02M21/0215F02M21/0245F02M21/0287F02M25/08F02D19/0605F25J1/0052F25J1/0097F25J1/0212F25J1/023F25J1/0254F25J1/0277F25J1/0278F25J1/0291F25J2220/62F25J2230/08F25J2230/30F25J2235/60F25J2290/62F17C2221/033F17C2221/035F17C2223/0153F17C2223/0161F17C2223/033F17C2265/034F17C2265/036F17C2265/037F17C2265/066F17C2270/0105F25J1/0045Y02T10/30F25J2215/02F25J2205/90F25J2230/60
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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