JP2015506454A5 - - Google Patents
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- JP2015506454A5 JP2015506454A5 JP2014548840A JP2014548840A JP2015506454A5 JP 2015506454 A5 JP2015506454 A5 JP 2015506454A5 JP 2014548840 A JP2014548840 A JP 2014548840A JP 2014548840 A JP2014548840 A JP 2014548840A JP 2015506454 A5 JP2015506454 A5 JP 2015506454A5
- Authority
- JP
- Japan
- Prior art keywords
- stream
- heat exchanger
- external heat
- refrigerant stream
- separation vessel
- 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.)
- Ceased
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- 239000003507 refrigerant Substances 0.000 claims 40
- 238000000034 method Methods 0.000 claims 25
- 239000007788 liquid Substances 0.000 claims 17
- 238000000926 separation method Methods 0.000 claims 17
- 238000001816 cooling Methods 0.000 claims 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 4
- 239000007789 gas Substances 0.000 claims 3
- 230000000694 effects Effects 0.000 claims 2
- 239000003345 natural gas Substances 0.000 claims 2
- 238000005057 refrigeration Methods 0.000 claims 2
- 230000000452 restraining effect Effects 0.000 claims 2
- 230000001629 suppression Effects 0.000 claims 2
Claims (15)
a.分離容器、ここで該分離容器は、冷媒流を分離しそれにより気体冷媒流と液体冷媒流を生成するものであり、
b.前記液体冷媒流を前記分離容器から外部の熱交換器コアに送達するための気液冷媒パイプ、
c.少なくとも1つの外部熱交換器コア、ここで前記液体冷媒流およびより暖かいプロセス流が前記外部熱交換器コアにおいて間接的な熱交換を受け、それにより、冷却されたプロセス流および気化した冷媒流を生成し、
d.前記部分気化冷媒を前記外部熱交換器コアから前記分離容器に送達するための部分気化冷媒パイプ、
を含む該システム。 A system for cooling or liquefying process gas in a moving environment,
a. A separation vessel, wherein the separation vessel separates the refrigerant stream and thereby generates a gaseous refrigerant stream and a liquid refrigerant stream;
b. A gas-liquid refrigerant pipe for delivering the liquid refrigerant stream from the separation vessel to an external heat exchanger core;
c. At least one external heat exchanger core, wherein the liquid refrigerant stream and warmer process stream undergo indirect heat exchange in the external heat exchanger core, thereby reducing the cooled process stream and the vaporized refrigerant stream. Generate
d. A partially vaporized refrigerant pipe for delivering the partially vaporized refrigerant from the external heat exchanger core to the separation vessel;
Including the system.
a.分離容器に冷(refrigeration)を導入し、それにより気体冷媒流と液体冷媒流を生成すること、
b.前記液体冷媒流を外部熱交換器コアの底近傍に導入すること、
c.より暖かいプロセス流を前記液体冷媒流の上部の位置で前記外部熱交換器コアに導入すること、
d.前記より暖かいプロセス流を前記外部熱交換器コアにおいて前記液体冷媒流との間接的熱交換により冷却し、それにより冷却されたプロセス流と部分気化冷媒流とを生成すること、
e.前記冷却されたプロセス流と前記部分気化冷媒流とを前記外部熱交換器から取り出すこと、
を含む該方法。 A method for liquefying natural gas in a moving environment,
a. Introducing refrigeration into the separation vessel, thereby producing a gas refrigerant stream and a liquid refrigerant stream;
b. Introducing the liquid refrigerant stream near the bottom of the external heat exchanger core;
c. Introducing a warmer process stream into the external heat exchanger core at a position above the liquid refrigerant stream;
d. Cooling the warmer process stream by indirect heat exchange with the liquid refrigerant stream in the external heat exchanger core, thereby producing a cooled process stream and a partially vaporized refrigerant stream;
e. Removing the cooled process stream and the partially vaporized refrigerant stream from the external heat exchanger;
The method comprising.
a.分離容器、ここで該分離容器は複数の動き抑制バッフルを含み、該分離容器は、高圧冷媒流を分離しそれにより気体冷媒流と液体冷媒流を生成するものであり、
b.前記液体冷媒流を前記分離容器から外部の熱交換器コアに送達するための気液冷媒パイプ、
c.少なくとも1つの外部熱交換器コア、ここで該外部熱交換器コアは、ケトルの外部にあり、前記液体冷媒流およびより暖かいプロセス流が前記外部熱交換器コアにおいて間接的な熱交換を受け、それにより、冷却されたプロセス流および気化した冷媒流を生成し、前記冷却されたプロセス流は、前記外部熱交換器コアの外部の位置に送達されるものであり、
d.前記部分気化冷媒を前記外部熱交換器コアから前記分離容器に送達するための部分気化冷媒パイプ、ここで前記部分気化冷媒パイプは最小の圧力降下を提供し、前記部分気化冷媒パイプは、熱サイフォン効果が維持されるのを保証するものである、
を含む該システム。 A system for cooling or liquefying process gas in a moving environment,
a. A separation vessel, wherein the separation vessel includes a plurality of motion-suppressing baffles, the separation vessel separating a high-pressure refrigerant stream and thereby generating a gaseous refrigerant stream and a liquid refrigerant stream;
b. A gas-liquid refrigerant pipe for delivering the liquid refrigerant stream from the separation vessel to an external heat exchanger core;
c. At least one external heat exchanger core, wherein the external heat exchanger core is external to the kettle, and the liquid refrigerant stream and warmer process stream undergo indirect heat exchange in the external heat exchanger core; Thereby producing a cooled process stream and a vaporized refrigerant stream, wherein the cooled process stream is delivered to a location external to the external heat exchanger core;
d. A partially vaporized refrigerant pipe for delivering the partially vaporized refrigerant from the external heat exchanger core to the separation vessel, wherein the partially vaporized refrigerant pipe provides a minimum pressure drop, and the partially vaporized refrigerant pipe is a thermosyphon Guarantees that the effect is maintained,
Including the system.
a.冷(refrigeration)を分離容器に導入し、それにより気体冷媒流と液体冷媒流を生成すること、ここで、前記分離容器は、複数の動き抑制バッフルを含み、
b.前記液体冷媒流を外部熱交換器コアの底近傍に導入すること、
c.より暖かいプロセス流を前記液体冷媒流の上部の位置で前記外部熱交換器コアに導入すること、
d.前記より暖かいプロセス流を前記液体冷媒流との間接的熱交換により冷却し、それにより冷却されたプロセス流と部分気化冷媒流とを生成すること、
e.前記冷却されたプロセス流と部分気化冷媒流とを前記外部熱交換器から取り出すこと、
f.前記部分気化冷媒流を前記分離容器に送達すること、
g.前記冷却されたプロセス流を前記外部熱交換器の外部の位置に送達すること、
を含む該方法。 A method for liquefying natural gas in a moving environment,
a. Introducing refrigeration into the separation vessel, thereby producing a gaseous refrigerant stream and a liquid refrigerant stream, wherein the separation vessel comprises a plurality of motion-reducing baffles;
b. Introducing the liquid refrigerant stream near the bottom of the external heat exchanger core;
c. Introducing a warmer process stream into the external heat exchanger core at a position above the liquid refrigerant stream;
d. Cooling the warmer process stream by indirect heat exchange with the liquid refrigerant stream, thereby producing a cooled process stream and a partially vaporized refrigerant stream;
e. Removing the cooled process stream and the partially vaporized refrigerant stream from the external heat exchanger;
f. Delivering the partially vaporized refrigerant stream to the separation vessel;
g. Delivering the cooled process stream to a location external to the external heat exchanger;
The method comprising.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201161578085P | 2011-12-20 | 2011-12-20 | |
US61/578,085 | 2011-12-20 | ||
PCT/US2012/070647 WO2013096464A1 (en) | 2011-12-20 | 2012-12-19 | Liquefying natural gas in a motion environment |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2015506454A JP2015506454A (en) | 2015-03-02 |
JP2015506454A5 true JP2015506454A5 (en) | 2015-11-12 |
Family
ID=48653241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2014548840A Ceased JP2015506454A (en) | 2011-12-20 | 2012-12-19 | Natural gas liquefaction in a moving environment |
Country Status (8)
Country | Link |
---|---|
US (1) | US20130160487A1 (en) |
EP (1) | EP2795214A4 (en) |
JP (1) | JP2015506454A (en) |
CN (1) | CN104011487B (en) |
AP (1) | AP2014007703A0 (en) |
AU (1) | AU2012359032A1 (en) |
RU (1) | RU2620310C2 (en) |
WO (1) | WO2013096464A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
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AU2015225689B2 (en) * | 2014-03-07 | 2019-01-03 | Conocophillips Company | Heat exchanger system with mono-cyclone inline separator |
AU2015252986B2 (en) | 2014-05-01 | 2019-07-11 | Conocophillips Company | Liquid drains in core-in-shell heat exchanger |
CN106024074A (en) * | 2016-05-11 | 2016-10-12 | 中广核研究院有限公司 | Nuclear power plant voltage stabilizer for inhibiting liquid level sloshing |
CN105957565B (en) * | 2016-06-23 | 2018-05-29 | 中广核研究院有限公司 | Constrain pond and the containment with the constrain pond |
CN114777412B (en) * | 2022-04-01 | 2023-03-24 | 中国科学院理化技术研究所 | Hydrogen liquefying plant with thermal siphon type hydrogen subcooler |
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-
2012
- 2012-12-19 WO PCT/US2012/070647 patent/WO2013096464A1/en unknown
- 2012-12-19 EP EP12860640.7A patent/EP2795214A4/en not_active Withdrawn
- 2012-12-19 RU RU2014129588A patent/RU2620310C2/en not_active IP Right Cessation
- 2012-12-19 CN CN201280063729.2A patent/CN104011487B/en not_active Expired - Fee Related
- 2012-12-19 AP AP2014007703A patent/AP2014007703A0/en unknown
- 2012-12-19 AU AU2012359032A patent/AU2012359032A1/en not_active Abandoned
- 2012-12-19 JP JP2014548840A patent/JP2015506454A/en not_active Ceased
- 2012-12-19 US US13/719,902 patent/US20130160487A1/en not_active Abandoned
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