Ship

Patent metadata

Field	Value
Publication number	US-12005999-B2
Application number	US-201616090120-A
Country	US
Kind code	B2
Filing date	Oct 21, 2016
Priority date	Mar 31, 2016
Publication date	Jun 11, 2024
Grant date	Jun 11, 2024

Abstract

A ship comprises: a liquefied gas storage tank; a multi-stage compressor for compressing a boil-off gas discharged from a storage tank and comprising a plurality of compression cylinders; a second heat exchanger for heat exchanging a fluid, which has been compressed by the multi-stage compressor, and thus cooling same; a first decompressing device for expanding a flow (“flow a 1 ”) partially branched from the flow (“flow a”) that has been cooled by the second heat exchanger; a third heat exchanger for heat exchanging, by “flow a 1 ” which has been expanded by the first decompressing device as a refrigerant, the remaining flow (“flow a 2 ”) of “flow a” after excluding “flow a 1 ” that has been branched and thus cooling same; and a second decompressing device for expanding “flow a 2 ” which has been cooled by the third heat exchanger.

First claim

The invention claimed is:

1. A ship comprising:
a storage tank configured to store liquefied gas;
a multistage compressor comprising a plurality of compressors connected in series and configured to compress boil-off gas (BOG) discharged from the storage tank to provide compressed BOG;
a first heat exchanger configured to cool and liquefy at least part of the compressed BOG, which provides a first flow of cooled compressed BOG;
a second heat exchanger configured to further cool the first flow of cooled compressed BOG;
a first decompressor configured to expand a first portion of the first flow, which further cools the first portion and provides an expanded flow;
a third heat exchanger configured to cool a second portion of the first flow with the expanded flow from the first decompressor for further cooling the second portion; and
a second decompressor configured to expand the cooled second portion, which provides a liquefied flow to a liquefied gas return line connecting between the second decompressor and the storage tank,
wherein the second heat exchanger is on the liquefied gas return line and interposed between the second decompressor and the storage tank,
wherein the second heat exchanger is configured to heat-exchange the liquefied flow returning to the storage tank in the liquefied gas return line with the first flow of cooled compressed BOG from the first heat exchanger such that the liquefied flow flowing back to the storage tank from the second decompressor is heated in the liquefied gas return line prior to arriving at the storage tank and such that the first flow of cooled compressed BOG is further cooled prior to arriving the first decompressor and the second decompressor.

2. The ship according to claim 1 , wherein the third heat exchanger is configured to return the expanded flow to the multistage compressor such that the expanded flow is compressed to provide at least part of the compressed BOG.

3. A boil-off gas reliquefaction method for use in a ship having a storage tank storing liquefied gas, the boil-off gas reliquefaction method comprising:
compressing, by a multi-stage compressor comprising a plurality of compressors connected in series, boil-off gas (BOG) discharged from the storage tank to provide compressed BOG;
cooling and liquefying, by a first heat exchanger, at least part of the compressed BOG to provide a first flow of cooled compressed BOG;
further cooling, at a second heat exchanger, the first flow of the cooled compressed BOG;
expanding and further cooling, by a first decompressor, a first portion of the first flow to provide an expanded flow;
heat-exchanging, at a third heat exchanger, a second portion of the first flow with the expanded flow from the first decompressor for further cooling the second portion; and
expanding, at a second decompressor, the cooled second portion to provide a liquefied flow to a liquefied gas return line connecting between the second decompressor and the storage tank,
wherein the second heat exchanger is on the liquefied gas return line and interposed between the second decompressor and the storage tank,
wherein the method further comprises heat-exchanging, at the second heat exchanger, the liquefied flow returning to the storage tank in the liquefied gas return line with the first flow of cooled compressed BOG from the first heat exchanger such that the liquefied flow flowing back to the storage tank from the second decompressor is heated in the liquefied gas return line prior to arriving at the storage tank and such that the first flow of cooled compressed BOG is further cooled prior to arriving the first decompressor and the second decompressor.

4. The boil-off gas reliquefaction method according to claim 3 , wherein the method further comprises:
returning, from the third heat exchanger, the expanded flow to the multi-stage compressor such that the expanded flow is compressed to provide at least part of the compressed BOG.

Assignees

• Daewoo Shipbuilding & Marine
• Hanwha Ocean Co Ltd

Inventors

• Lee Seung Chul
• Kim Seon Jin

Classifications

• F17C2270/0105

  Ships · CPC title

• F17C2265/033

  with cooling · CPC title

• F17C2227/0358

  by expansion · CPC title

• F17C2227/0351

  using seawater · CPC title

• F17C2227/0185

  comprising several pumps or compressors · CPC title