JPS54121347A - Utilization of low temperature of liquefied natural gas - Google Patents
Utilization of low temperature of liquefied natural gasInfo
- Publication number
- JPS54121347A JPS54121347A JP2846978A JP2846978A JPS54121347A JP S54121347 A JPS54121347 A JP S54121347A JP 2846978 A JP2846978 A JP 2846978A JP 2846978 A JP2846978 A JP 2846978A JP S54121347 A JPS54121347 A JP S54121347A
- Authority
- JP
- Japan
- Prior art keywords
- natural gas
- expander
- evaporator
- low temperature
- compressor
- 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.)
- Pending
Links
- 239000003949 liquefied natural gas Substances 0.000 title abstract 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 8
- 239000003345 natural gas Substances 0.000 abstract 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- 229910001873 dinitrogen Inorganic materials 0.000 abstract 2
- 230000006835 compression Effects 0.000 abstract 1
- 238000007906 compression Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
PURPOSE: To increase generated power and reduce the equipment cost of a low temperature utilizing system, by utilizing the low temperature of liquefied natural gas to evaporate it with an evaporator.
CONSTITUTION: To reduce power necessary for compression by a compressor C, nitrogen gas is cooled by the LNG evaporator V to the vicinity of the lowest temperature of the LNG and compressed by the compressor C to predetermined pressure and heat-exchanged by a heat recovery unit R with the outlet gas of an expander E so that the nitrogen gas is heated. The evaporator V can handle three fluides. A natural gas expander E' is connected to the compressor C, the expander E and an electric generator G. The natural gas evaporated by the evaporator V is expanded by the expander E' to obtain power. The natural gas discharged from the expander E' is heat-exchanged again by the evaporator V so that the natural gas is supplied through an outlet pipe Lo.
COPYRIGHT: (C)1979,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2846978A JPS54121347A (en) | 1978-03-13 | 1978-03-13 | Utilization of low temperature of liquefied natural gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2846978A JPS54121347A (en) | 1978-03-13 | 1978-03-13 | Utilization of low temperature of liquefied natural gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS54121347A true JPS54121347A (en) | 1979-09-20 |
Family
ID=12249501
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2846978A Pending JPS54121347A (en) | 1978-03-13 | 1978-03-13 | Utilization of low temperature of liquefied natural gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS54121347A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7272932B2 (en) * | 2002-12-09 | 2007-09-25 | Dresser, Inc. | System and method of use of expansion engine to increase overall fuel efficiency |
US11408675B2 (en) * | 2013-03-27 | 2022-08-09 | Highview Enterprises Limited | Method and apparatus in a cryogenic liquefaction process |
-
1978
- 1978-03-13 JP JP2846978A patent/JPS54121347A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7272932B2 (en) * | 2002-12-09 | 2007-09-25 | Dresser, Inc. | System and method of use of expansion engine to increase overall fuel efficiency |
US11408675B2 (en) * | 2013-03-27 | 2022-08-09 | Highview Enterprises Limited | Method and apparatus in a cryogenic liquefaction process |
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