Straightforward method and once-through apparatus for gas liquefaction

• US 5,931,021 A
• Filed: 06/24/1997
• Issued: 08/03/1999
• Est. Priority Date: 06/24/1997
• Status: Expired due to Fees

• Current Assignee: Dan Weiner, Giora Meron, Isaac Shnaid, Shmuel Olek
• Original Assignee: Dan Weiner, Giora Meron, Isaac Shnaid, Shmuel Olek
• Inventors: Weiner, Dan, Olek, Shmuel, Shnaid, Isaac, Meron, Giora
• Primary Examiner(s): CAPOSSELA, RONALD C
• Application Number:
  US08/880,306
• Time in Patent Office: 770 Days
• Field of Search: 62/612, 62/613, 62/51.2
• US Class Current: 62/613
• CPC Class Codes: F25J 1/0012 Primary atmospheric gases, e.g. air
• CPC Class Codes: F25J 1/0015 Nitrogen
• CPC Class Codes: F25J 1/0017 Oxygen
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/0045 by vaporising a liquid return stream
• CPC Class Codes: F25J 1/005 by expansion of a gaseous refrigerant stream with extraction of work
• CPC Class Codes: F25J 1/0201 using only internal refrigeration means, i.e. without external refrigeration
• CPC Class Codes: F25J 1/0204 as a single flow SCR cycle
• CPC Class Codes: F25J 1/0212 as a single flow MCR cycle
• CPC Class Codes: F25J 1/0221 using the cold stored in an external cryogenic component in an open refrigeration loop
• CPC Class Codes: F25J 1/0245 Different modes, i.e. 'runs', of operation; Process control
• CPC Class Codes: F25J 1/0247 start-up of the process
• CPC Class Codes: F25J 1/0254 controlling particular process parameter, e.g. pressure, temperature
• CPC Class Codes: F25J 2210/40 Air or oxygen enriched air, i.e. generally less than 30mol% of O2
• CPC Class Codes: F25J 2240/10 the fluid being air
• CPC Class Codes: F25J 2270/16 with mutliple gas expansion loops of the same refrigerant
• CPC Class Codes: F25J 2290/10 Mathematical formulae, modeling, plot or curves; Design methods
• CPC Class Codes: F25J 2290/34 Details about subcooling of liquids

Abstract

The invention relates to methods and systems for liquefaction of gases whose critical temperature is lower than the ambient temperature, such as, for instance, natural gas, air, nitrogen, oxygen, etc. Compressed to supercritical pressure gas to be liquefied is cooled by external refrigerator means to a predetermined final temperature that is lower than the saturation temperature of the liquefied gas, and then is throttled to a subcritical pressure. As a result, all gas supplied to the apparatus is liquefied without generating any flash gas, and controlled rate of liquefied gas subcooling is achieved. Three modifications of the apparatus for gas liquefaction employing refrigerator means, based on reversed gas cycles, are introduced. Another modification of the apparatus with refrigerator means applying open air cycle and Compressed Air Energy Storage (CAES) is also developed.

Claims

1. Once-Through-Apparatus for Gas Liquefaction comprising:

a device for thermodynamic conditioning of the gas to be liquefied to achieve the gas supercritical pressure and minimal temperature consistent with ambient conditions;

an inlet line to supply the gas to the device for thermodynamic conditioning of the gas;

external refrigerator means generating distributed variable temperature heat sinks in heat absorbing means, to cool the supercritical pressure gas to a final temperature that is lower than the saturation temperature of the liquefied gas;

a throttling device to expand the cooled supercritical pressure gas without work performance to the prescribed subcritical pressure of the liquefied gas;

a low temperature heat transfer unit comprising said heat absorbing means of said refrigerator means and main heat transfer means, connected by a line to said device for thermodynamic conditioning of the gas and by another line to said throttling device;

said heat absorbing means being in thermal contact with said main heat transfer means thereby ensuring transfer of heat from the gas to said heat absorbing means;

an outlet line to supply the liquefied gas to the consumer;

means for transferring the liquefied gas from said throttling device to said outlet line.

2. Once-Through-Apparatus for Gas Liquefaction according to claim 1 wherein:

auxiliary heat transfer means are introduced in said low temperature heat transfer unit;

said auxiliary heat transfer means being in thermal contact at least with said main heat transfer means;

the means for transferring the liquefied gas comprises a line connected to said throttling device, an interconnection element connected in series with the line and a line with a valve connecting the interconnection element with the outlet line;

the auxiliary heat transfer means are connected by a line with a valve to the interconnection element.

3. Once-Through-Apparatus for Gas Liquefaction according to claim 1 wherein said refrigerator means comprises connected in series by lines the following elements:

compressing and cooling device combining compressor means for compressing gaseous refrigerant with appropriate heat exchanger means for cooling compressed refrigerant by the ambient heat sinks;

expander means for expanding the compressed gaseous refrigerant with performance of work;

heat absorbing means for extracting heat from the supercritical pressure gas by a flow of expanded gaseous refrigerant.

4. Once-Through-Apparatus for Gas Liquefaction according to claim 1 wherein said refrigerator means comprises

compressing and cooling device combining compressor means for compressing gaseous refrigerant with appropriate heat exchanger means for cooling compressed refrigerant by the ambient heat sinks to produce at least two flows of compressed and cooled refrigerant;

at least two expander means for expanding the flows of compressed refrigerant with performance of work;

the heat absorbing means having at least two sections for extracting heat from the supercritical pressure gas by the flows of expanded gaseous refrigerant;

at least one regenerative heat exchanger having a high pressure side and a low pressure side;

lines creating at least two circuits for the flows of refrigerant;

the first circuit includes connected in series compressing and cooling device, the first expander means and the first section of the heat absorbing means;

the second circuit includes connected in series compressing and cooling device, the high pressure side of the heat exchanger, the second expander means, the second section of the heat absorbing means, and the low pressure side of the heat exchanger, while the flows of refrigerant leaving the first section of the heat absorbing means and the low pressure side of the heat exchanger are united into one flow entering the compressing and cooling device.

5. Once-Through-Apparatus for Gas Liquefaction according to claim 1 wherein said refrigerator means comprises

compressing and cooling device combining compressor means for compressing gaseous refrigerant with appropriate heat exchanger means for cooling compressed refrigerant by the ambient heat sinks to produce at least two flows of compressed and cooled refrigerant;

at least two expander means for expanding the flows of compressed refrigerant with performance of work;

the heat absorbing means for extracting heat from the supercritical pressure gas by the flows of expanded gaseous refrigerant;

an outlet line connecting the heat absorbing means with inlet of compressing and cooling device;

at least one regenerative heat exchanger having a high pressure side being in heat contact with said heat absorbing means;

lines creating at least two circuits for the flows of refrigerant;

the first circuit includes connected in series compressing and cooling device, the first expander means and the expander exhaust line connected with an intermediate point of the heat absorbing means;

the second circuit includes connected in series compressing and cooling device, the high pressure side of the heat exchanger, the second expander means, and low temperature part of the heat absorbing means.

6. Once-Through-Apparatus for Gas Liquefaction according to claim 1 wherein said refrigerator means comprise:

compressing and cooling device to compress and cool atmospheric air;

an electric motor to drive the compressing and cooling device;

a line connecting the compressing and cooling device with the atmosphere;

an air purifying device to extract from the compressed air mechanical particles, water drops and to dry the compressed air;

lines with valves for connecting said compressing and cooling device with said air purifying device and with a Compressed Air Energy Storage;

expander means to expand compressed air with performance of work and connected by a line with said air purifying device;

electric generator driven by said expander means;

the heat absorbing means supplied through a line by expanded air and connected by a line with the atmosphere.

7. Straightforward Method of Gas Liquefaction comprising the following steps:

thermodynamic conditioning of a gas to be liquefied that comprises compressing said gas to a supercritical pressure and cooling the gas by ambient heat sinks;

refrigerating said supercritical pressure gas by external refrigerator means to a final temperature which is lower than the saturation temperature of the liquefied gas;

throttling said refrigerated supercritical pressure gas to the prescribed subcritical pressure of the liquefied gas.

8. Straightforward Method of Gas Liquefaction according to claim 7, wherein final temperature of the refrigerated supercritical pressure gas is varied, thus controlling rate of subcooling of said liquefied gas.

9. Straightforward Method of Gas Liquefaction according to claim 7, wherein said external refrigerator means generate distributed variable temperature heat sinks disposed for refrigerating said supercritical pressure gas.

10. Straightforward Method of Gas Liquefaction according to claim 7, wherein said external refrigerator means produce at least one flow of cold gas disposed for refrigerating said supercritical pressure gas.

11. Straightforward Method of Gas Liquefaction according to claim 7, wherein said external refrigerator means generate at least one flow of multicomponent refrigerant boiling at variable temperature and disposed for refrigerating said supercritical pressure gas.