Heat exchanger for a liquefied natural gas facility

Patent metadata

Field	Value
Publication number	US-11435138-B2
Application number	US-201514633307-A
Country	US
Kind code	B2
Filing date	Feb 27, 2015
Priority date	Mar 4, 2014
Publication date	Sep 6, 2022
Grant date	Sep 6, 2022

Abstract

A method of constructing a plate fin heat exchanger includes joining a first side bar formed from a nickel-iron alloy to a first end of a fin element formed from a nickel-iron alloy through a first nickel-iron alloy bond, and joining a second side bar formed from a nickel-iron alloy to a second end of the fin element through a second nickel-iron alloy bond to create a first layer of the plate fin heat exchanger. The fin element defines a fluid passage.

First claim

What is claimed is:

1. A cryogenic gas processing system comprising:
a chiller;
a low temperature separator (LTS) including an inlet fluidically connected to the chiller, a first outlet and a second outlet;
a flash drum including an inlet fluidically connected to the LTS and a plurality of conduits;
a heat exchanger fluidically connected to the second outlet of the LTS and the plurality of conduits of the flash drum, the heat exchanger comprising:
a first side bar formed from a nickel-iron alloy;
a second side bar formed from the nickel-iron alloy, the second side bar being spaced from the first side bar;
a fin element formed from the nickel-iron alloy extending between the first side bar and the second side bar forming a first layer of the heat exchanger, the fin element including an inner passage, thereby defining a fluid passage, the fin element formed from the nickel-iron alloy;
a first nickel-iron alloy bond joining the fin element and the first side bar; and
a second nickel-iron alloy bond joining the fin element and the second side bar,
wherein the nickel content of the nickel-iron alloy is between about 32% and 42%; and

a pump disposed between the heat exchanger and the second outlet of the LTS to convey an outlet fluid from the second outlet of the LTS directly into the heat exchanger.

2. The cryogenic gas processing system according to claim 1 , further comprising: a parting sheet extending between, and connected to, the first side bar and the second side bar, the parting sheet being formed from the nickel-iron alloy.

3. The cryogenic gas processing system according to claim 2 , wherein the parting sheet is joined to each of the first and second side bars through a corresponding nickel-iron alloy bond.

4. The cryogenic gas processing system according to claim 3 , wherein the corresponding nickel-iron alloy bond comprises a diffusion bond.

5. The cryogenic gas processing system according to claim 1 , wherein each of the first nickel-iron alloy bond and the second nickel-iron alloy bond comprises a diffusion bond.

6. The cryogenic gas processing system according to claim 1 , wherein the heat exchanger includes a first portion connected to a second portion, the first portion including a first inlet plenum configured and disposed to receive a first cryogenic fluid and the second portion including a second inlet plenum configured and disposed to receive a second cryogenic fluid.

7. A heat exchanger comprising:
a first side bar formed from a nickel-iron alloy, wherein the nickel content of the nickel-iron alloy is between about 32% and 42%;
a second side bar formed from the nickel-iron alloy, the second side bar being spaced from the first side bar;
a fin element formed from the nickel-iron alloy extending between the first side bar and the second side bar forming a first layer of the heat exchanger, the fin element including an inner passage, thereby defining a fluid passage, the fin element formed from the nickel-iron alloy;
a first nickel-iron alloy bond joining the fin element and the first side bar; and
a second nickel-iron alloy bond joining the fin element and the second side bar; and
a fluid inlet fluidically connected directly to an outlet of a low temperature separator via a pump.

8. The heat exchanger according to claim 6 , further comprising: a parting sheet extending between, and connected to, the first side bar and the second side bar, the parting sheet being formed from the nickel-iron alloy.

9. The heat exchanger according to claim 8 , wherein the parting sheet is joined to each of the first and second side bars through a corresponding nickel-iron alloy bond.

10. The heat exchanger according to claim 9 , wherein the corresponding nickel-iron alloy bond comprises a diffusion bond.

11. The heat exchanger according to claim 7 , wherein each of the first nickel-iron alloy bond and the second nickel-iron alloy bond comprises a diffusion bond.

12. The heat exchanger according to claim 7 , further comprising: a first heat exchange portion connected to a second heat exchange portion, the first heat exchange portion including a first inlet plenum configured and disposed to receive a first cryogenic fluid and the second heat exchange portion including a second inlet plenum configured and disposed to receive a second cryogenic fluid.

13. The heat exchanger according to claim 7 , further comprising: a conditioning flow inlet plenum having a conditioning flow inlet and a conditioning flow outlet plenum having a conditioning flow outlet, the conditioning flow inlet plenum being configured and disposed to direct a cryogenic fluid across the fin element formed from the nickel-iron alloy.

14. The cryogenic gas processing system according to claim 1 , wherein the iron content of the nickel-iron alloy is between about 34% and 38%.

15. The cryogenic gas processing system according to claim 1 , wherein each of the first nickel-iron alloy bond and the second nickel-iron alloy bond comprises application of additional nickel-iron alloy material.

16. The cryogenic gas processing system according to claim 3 , wherein the corresponding nickel-iron alloy bond comprises application of additional nickel-iron alloy material.

17. The heat exchanger according to claim 7 , wherein the iron content of the nickel-iron alloy is between about 34% and 38%.

18. The heat exchanger according to claim 7 , wherein each of the first nickel-iron alloy bond and the second nickel-iron alloy bond comprises application of additional nickel-iron alloy material.

19. The heat exchanger according to claim 9 , wherein the corresponding nickel-iron alloy bond comprises application of additional nickel-iron alloy material.

20. A cryogenic gas processing system comprising:
a chiller;
a low temperature separator (LTS) including an inlet fluidically connected to the chiller, a first outlet and a second outlet;
a flash drum including an inlet fluidically connected to the LTS and a plurality of outlet conduits;
a heat exchanger fluidically connected to the second outlet of the LTS and the plurality of outlet conduits of the flash drum, the heat exchanger comprising:
a first side bar formed from a nickel-iron alloy;
a second side bar formed from the nickel-iron alloy, the second side bar being spaced from the first side bar;
a fin element formed from the nickel-iron alloy extending between the first side bar and the second side bar forming a first layer of the heat exchanger, the fin element including an inner passage defining a fluid passage; and

a pump disposed between the heat exchanger and the second outlet of the LTS to convey an outlet fluid from the second outlet of the LTS directly into the heat exchanger.

Assignees

• Conocophillips Co

Inventors

• Wilson Stuart L
• Qualls Wesley R
• Gentry Matthew C
• Leger Paula A
• Boulanger Robert L

Classifications

• Y02P80/10

  Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier · CPC title

• F28D9/0062

  the conduits for one heat-exchange medium being formed by spaced plates with inserted elements (F28D9/0012, F28D9/0025, F28D9/0081, F28D9/04 take precedence) · CPC title

• F25J1/0085

  Ethane; Ethylene · CPC title

• B23K20/233

  without ferrous layer · CPC title

• F25J3/0209

  Natural gas or substitute natural gas · CPC title