Core-in-shell heat exchangers for multistage compressors

• US 5,651,270 A
• Filed: 07/17/1996
• Issued: 07/29/1997
• Est. Priority Date: 07/17/1996
• Status: Expired due to Term

• Current Assignee: Conocophillips Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: Campbell, Kenneth C., Low, William R.
• Primary Examiner(s): CAPOSSELA, RONALD C
• Application Number:
  US08/682,463
• Time in Patent Office: 377 Days
• Field of Search: 62/612, 62/613, 62/657
• US Class Current: 62/613
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/0082 Methane
• CPC Class Codes: F25J 1/0085 Ethane; Ethylene
• CPC Class Codes: F25J 1/0087 Propane; Propylene
• CPC Class Codes: F25J 1/0207 as at least a three level SCR refrigeration cascade
• CPC Class Codes: F25J 1/0244 Operation; Control and regulation; Instrumentation F25J1/0279 takes precedence
• CPC Class Codes: F25J 1/0262 Details of the cold heat exchange system constructional details F25J5/00, construction of cold-exchangers in general F28
• CPC Class Codes: F25J 2250/02 Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
• CPC Class Codes: F25J 5/005 in a reboiler-condenser, e.g. within a column
• CPC Class Codes: F28F 9/22 Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates

Abstract

In multistage refrigeration compression, where liquid refrigerant withdraw from a core-in-shell type heat exchanger connected to a high compression stage is passed to a similar exchanger connected to a lower compression stage, liquid level stability in the higher compression stage exchanger is improved by providing an enlarged surge volume. A baffle plate transversing a lower portion of the shell divides the shell into a cooling zone that contains the cores, and a discharge zone that is part of the surge volume. The height of the baffle is selected to facilitate maintenance of at least a minimum functional liquid level in the shell. Liquid refrigerant withdraw from the discharge zone of the high-stage shell is supplied to the cooling zone of a shell connected to a lower compression stage. The liquid level in the shell is maintained by manipulating flow to liquid refrigerant that is flashed into the cooling zone of the higher compression stage shell. A refrigerant compressor may employ two or more compression stages, where the higher stage shells are typically much smaller than the lower stage shells, and the described scheme prevent major liquid level upsets in the shell of a higher stage resulting from minor liquid level upsets in the lower stage shells.

Claims

1. Apparatus for cooling a normally gaseous feed stream, comprising:

(a) a multistage compressor having at least a high-stage section and a low-stage section;

(b) heat exchange means for condensing refrigerant gas compressed in said multistage compressor to produce a liquid refrigerant;

(c) an elongated high-stage heat exchange shell associated with said high-stage section of said multistage compressor, said high-stage heat exchange shell having a volume sufficient for handling vapor-compression refrigeration service for said high-stage compressor section, and additionally having a surge volume;

(d) at least one high-stage plate-fin-core disposed in said high-stage shell, said core being operable over a range of liquid levels in said high-stage shell;

(e) a baffle plate transversely disposed in said high-stage shell so as to facilitate maintenance of a minimum liquid level for said plate fin core;

(f) means for flashing said liquid refrigerant into said high-stage shell and producing a first mixture of gas and liquid in which said feed gas stream passes in indirect heat exchange through said high-stage plate-fin-core;

(g) means for separating said first mixture of gas and liquid and providing said gas to an inlet of said high-stage compressor section, and holding sufficient liquid in said high-stage shell to provide at least a minimum functional liquid level for said high-stage core;

(h) an elongated low-stage heat exchange shell associated with said low-stage section of said multistage compressor, said low-stage heat exchange shell containing at least one low-stage plate-fin-core, said low-stage shell having a volume sufficient for handling vapor-compression refrigeration service for said low-stage compressor section;

(i) means for flashing said liquid refrigerant withdrawn from said surge volume into said low-stage shell to produce a second mixture of gas and liquid in which said feed gas stream passes in indirect heat exchange through said low-stage plate-fin-core;

(j) means for separating said second mixture of gas and liquid in said low-stage shell and providing said gas to an inlet of said low-stage compressor section and holding sufficient liquid in said low-stage shell to provide at least a minimum functional liquid level for said low-stage core; and

(k) wherein said surge volume in said high-stage shell is a volume equal to a level fluctuation in said low-stage shell of about four inches to about eight inches.

2. Apparatus in accordance with claim 1, wherein said high-stage shell includes an additional volume defined by said baffle plate and the nearest end wall of said high-stage shell, and wherein said surge volume is defined by said additional volume in combination with the volume defined by said liquid level range in said high-stage shell.

3. Apparatus according to claim 1, wherein said cores in said plate-fin-core-in-shell heat exchanger comprise brazed-aluminum-plate-fin cores, and said elongated high-stage heat exchange shell contains a plurality of said cores.

4. Apparatus according to claim 1, wherein said multistage compressor comprises at least three compression stages.

5. Apparatus in accordance with claim 1, wherein said normally gaseous feed stream comprises natural gas.

6. Apparatus in accordance with claim 4, wherein said surge volume comprises a volume equal to a fluctuation in the largest downstream shell of from about five inches to about seven inches and preferably about six inches.

7. Apparatus in accordance with claim 1, wherein said refrigerant comprises propane, and said apparatus additionally includes multistage compressors and associated plate-fin-in-core heat exchanger for ethylene and methane refrigerants in a cascade cooling operation.

8. Apparatus in accordance with claim 7, wherein said liquid refrigerant is flashed into said elongated low-stage shell from said surge volume, said apparatus additionally comprising:

means for controlling the liquid level in said surge volume by manipulating the flow rate of said liquid refrigerant flashed into said elongated high-stage shell.

9. A method for cooling a normally gaseous material which comprises the step of providing a process stream of said normally gaseous material to an apparatus comprising:

(a) a multistage compressor having at least a high-stage section and a low-stage section;

(b) a heat exchange means for condensing refrigerant gas compressed in said multistage compressor to produce a liquid refrigerant;

(c) an elongated high-stage heat exchange shell associated with said high-stage section of said multistage compressor, said high-stage heat exchange shell having a volume sufficient for handling vapor compression refrigeration service for said high-stage compressor section, and having a surge volume;

(d) at least one high-stage plate-fin-core, said core being operable over a range of liquid levels in said high-stage shell;

(e) a baffle plate transversely disposed in said high-stage shell to facilitate maintenance of a minimum liquid level for said high-stage plate-fin-cores;

(f) means for flashing said liquid refrigerant into said high-stage shell to produce a first mixture of gas and liquid in which said feed gas stream passes in indirect heat exchange through said high-stage plate-fin-core;

(g) means for separating said first mixture of gas and liquid and providing said gas to an inlet of said high stage compressor section, and holding sufficient liquid in said high-stage shell to provide at least a minimum functional liquid level for said high-stage core;

(h) an elongated low-stage heat exchange shell associated with said low-stage section of said multistage compressor, said low-stage heat exchange shell containing at least one low-stage plate-fin-core, said low-stage shell having a volume sufficient for handling the vapor- compression refrigeration service for said low-stage compressor section;

(i) means for flashing said liquid refrigerant withdrawn from said surge volume into said low-stage shell to produce a second mixture of gas and liquid in which said feed gas stream passes in indirect heat exchange through said low-stage plate-fin-core;

(j ) means for separating said second mixture of gas and liquid in said low-stage shell and providing said gas to an inlet of said low-stage compressor section and holding sufficient liquid to provide a level in said low-stage shell; and

(k) wherein said surge volume in said high-stage shell is a volume equal to a level fluctuation in said low-stage shell of about four inches to about eight inches.

10. A method in accordance with claim 9, wherein said refrigerant is propane, said method additionally comprising the step of:

controlling the liquid level in said surge volume by manipulating flow of said liquid refrigerant into said high-stage shell.

11. A method in accordance with claim 9, wherein said normally gaseous feed stream comprises natural gas, and said refrigerant comprises propane.

12. A method in accordance with claim 11, additionally comprising the following step:

providing a cascade cooling scheme for said feed stream, wherein said feed stream is first cooled by propane in said multistage compressor, followed by a cooling cycle using ethylene refrigerant and finally a cooling cycle using methane refrigerant to liquefy said feed stream.

13. A method in accordance with claim 12, wherein said multistage compressor comprises at least three compression stages, and said elongated heat exchange shell associated with said high-stage compression section includes a plurality of said cores.

14. A method in accordance with claim 13, wherein said high-stage shell contains a first, a second and a third plate-fin-core, said method additionally comprising:

passing said feed stream through said first plate-fin-core for indirect heat exchange with said first mixture of gas and liquid;

passing ethylene refrigerant through said second plate-fin-core for indirect heat exchange with said first mixture of gas and liquid; and

passing methane refrigerant through said third plate-fin-core for indirect heat exchange with said first mixture of gas and liquid.