Arrangement and method for the production of liquid natural gas

• US 4,456,459 A
• Filed: 01/07/1983
• Issued: 06/26/1984
• Est. Priority Date: 01/07/1983
• Status: Expired due to Term

• Current Assignee: Exxonmobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Brundige, Virgil L. Jr.
• Primary Examiner(s): Sever, Frank
• Application Number:
  US06/456,234
• Time in Patent Office: 536 Days
• Field of Search: 62/9, 62/11, 62/38, 62/39, 62/36, 62/45, 62/52, 62/54, 62/55
• US Class Current: 62/613
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/0042 by liquid expansion with extraction of work
• CPC Class Codes: F25J 1/0248 Stopping of the process, e.g. defrosting or deriming, maintenance; Back-up mode or systems
• CPC Class Codes: F25J 2220/62 Separating low boiling components, e.g. He, H2, N2, Air
• CPC Class Codes: F25J 2240/40 Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval

Abstract

An arrangement and a method for the increase in the production of liquid natural gas and the conservation of energy and reduction of flash gas in a liquid natural gas manufacturing installation and, more particularly, the reduction in the quantity of formed flash gas through the novel utilization of a hydraulic expander in the installation for extracting work from the flow of liquid natural gas prior to flashing thereof.

Claims

1. In a liquid natural gas manufacturing facility, an arrangement for improving liquid natural gas production, reducing flash gas production and conserving energy, comprising:

means operating to reduce the pressure of a super-cooled stream of liquid natural gas feed from a main exchanger of the liquid natural gas manufacturing facility, to extract work from both a liquid phase and a vapor phase formed during the reduction in pressure, and to separate the liquid and vapor phases into streams of liquid natural gas and flash gas;

said means consisting of a hydraulic expander designed to extract work from both the liquid phase and vapor phase formed during the reduction in pressure, a low pressure flash means for separating the liquid and vapor phases, and a first flow conduit for feeding the super-cooled stream of liquid natural gas from the main exchanger to the hydraulic expander and for feeding the liquid and vapor phases exiting from an outlet of the hydraulic expander directly to an inlet of the low pressure flash means.

2. An arrangement as claimed in claim 1, further comprising:

means to enable the liquid natural gas manufacturing facility to be continuously operated without interruption when the hydraulic expander is out of service;

said means consisting of a second flow conduit connecting into said first flow conduit upstream and downstream of said hydraulic expander to form a parallel bypass flowpath for the liquid natural gas stream between the main exchanger and the low pressure flash means, and a Joule-Thomson valve interposed in said second flow conduit, said Joule-Thomson valve being selectively closable to preclude flow of liquid natural gas when the hydraulic expander is in service and openable to allow flow of liquid natural gas and effect a reduction in the pressure of the gas when the hydraulic expander is out of service.

3. An arrangement as claimed in claim 1, said hydraulic expander comprising a turboexpander.

4. An arrangement as claimed in claim 1, said hydraulic expander being connected to means for converting the work extracted from the liquid and vapor phases into mechanical or electrical energy.

5. An arrangement as claimed in claim 1, said stream of flash gas formed in the flash means being employable as fuel in said manufacturing facility.

6. In a method for producing liquified natural gas, a method for improving liquid natural gas production, reducing flash gas production and conserving energy, comprising:

feeding a stream of super-cooled and pressurized liquid natural gas from a main exchanger of a liquid natural gas manufacturing facility to a hydraulic expander means;

conducting the stream through the hydraulic expander to reduce the pressure of the stream and to further cool the stream, said stream forming gas and vapor phases during the pressure reduction;

extracting work from both the liquid and vapor phases during the pressure reduction by means of said hydraulic expander;

feeding the liquid and vapor phases from an outlet of the hydraulic expander directly to a low-pressure flash means without further treatment; and

flashing the liquid and vapor phases in the low pressure flash means in order to form separate streams of liquid natural gas and flash gas.

7. A method as claimed in claim 6, further comprising providing a parallel flow path for the liquid natural gas stream between the main exchanger and the flash means bypassing said hydraulic expander, and a Joule-Thomson valve interposed in said second flow path, said Joule-Thomson valve being selectively closable to preclude flow of liquid natural gas when the hydraulic expander is in service and openable to allow flow of liquid natural gas and effect a reduction in the pressure of the gas when the hydraulic expander is out of service, thereby enabling the liquid natural gas manufacturing facility to be continuously operated without interruption when the hydraulic expander is out of service.

8. A method as claimed in claim 6, said hydraulic expander comprising a turboexpander.

9. A method as claimed in claim 6, further comprising connecting said hydraulic expander to means for converting the work extracted from the liquid and vapor phases into mechanical or electrical energy.

10. A method as claimed in claim 6, further comprising employing the stream of flash gas formed in the low pressure flash means as fuel in the manufacturing facility.