Method for removal of carbon dioxide from a carrier liquid

Patent metadata

Field	Value
Publication number	US-10537823-B2
Application number	US-201715433185-A
Country	US
Kind code	B2
Filing date	Feb 15, 2017
Priority date	Feb 15, 2017
Publication date	Jan 21, 2020
Grant date	Jan 21, 2020

Abstract

A method for removing carbon dioxide from a carrier liquid using a heat exchanger. A carrier liquid, containing carbon dioxide, is heated through the heat exchanger, causing the carbon dioxide to vaporize. The carrier liquid and the carbon dioxide gas pass to a liquid removal vessel. The carrier liquid is removed and the carbon dioxide gas is compressed. The compressed carbon dioxide gas is provided to the heat exchanger, cooling the carbon dioxide gas opposite the carrier liquid, producing a carbon dioxide liquid.

First claim

The invention claimed is:

1. A method of removing carbon dioxide from a carrier liquid comprising:
providing a heat exchanger with a cooling side and a heating side to conduct a heat exchange process between the carrier liquid and a compressed carbon dioxide gas; the cooling side of the heat exchanger having a cooling input port and a cooling output port; the heating side of the heat exchanger having a heating input port and a heating output port;
conveying the carrier liquid to the heating input port, the carrier liquid being at a first temperature and a first pressure where the carbon dioxide is a carbon dioxide liquid;
heating the carrier liquid through the heat exchanger, causing the carbon dioxide and a portion of the carrier liquid to vaporize as the carrier liquid and the carbon dioxide are brought to a second temperature where the carbon dioxide vaporizes to a carbon dioxide gas;
passing the carrier liquid and the carbon dioxide gas through the heating output port to a feed inlet of a liquid removal vessel;
removing a carbon dioxide depleted carrier liquid from the bottom of the liquid removal vessel;
compressing the carbon dioxide gas from the liquid removal vessel through a compression process by raising the carbon dioxide gas to a second pressure at which the carbon dioxide gas is now the compressed carbon dioxide gas;
sending the compressed carbon dioxide gas to the cooling input port; and
cooling the compressed carbon dioxide gas by the heat exchange process with the carrier liquid through the heat exchanger, bringing the compressed carbon dioxide gas to a third temperature, by which process the carbon dioxide gas cools to a pure carbon dioxide liquid;
wherein, given a pressure-temperature curve for carbon dioxide, the first temperature and the first pressure are located in a liquid phase area of the pressure-temperature curve for carbon dioxide; the second temperature is shifted from the first temperature to the second temperature, the second temperature being higher than the first temperature, and the combination of the first pressure and the second temperature being located in a gas phase area of the pressure-temperature curve for carbon dioxide that also allows for the compression from the first pressure to the second pressure to keep the carbon dioxide gas as a gas; and the third temperature being lower than the second temperature, the third temperature and second pressure being in the liquid phase area; and,
wherein the compression process is sized to allow the heat exchange process to be efficient by avoiding an inflection region that occurs between a heat-temperature curve of the cooling side of the heat exchanger and a heat-temperature curve of the heating side of the heat exchanger;
whereby carbon dioxide is removed from the carrier liquid.

2. The method of claim 1 , wherein the heat exchanger is operated as a counter-current heat exchanger.

3. The method of claim 2 , wherein the heat exchanger is a shell and tube style heat exchanger containing a shell enclosing a tube, wherein the tube has a varying diameter.

4. The method of claim 1 , wherein the heat exchanger is operated as a co-current heat exchanger.

5. The method of claim 1 , wherein the heat exchanger comprises a brazed plate, aluminum plate, shell and tube, plate, plate and frame, plate and shell, spiral, or plate fin style heat exchanger.

6. The method of claim 1 , wherein any surface of the heat exchanger exposed to the compressed carbon dioxide gas or the carrier liquid comprises aluminum, stainless steel, polymers, carbon steel, ceramics, polytetrafluoroethylene, polychlorotrifluoroethylene, natural diamond, man-made diamond, chemical-vapor deposition diamond, polycrystalline diamond, or combinations thereof.

7. The method of claim 1 , wherein the liquid removal vessel contains packing materials.

8. The method of claim 7 , wherein the packing materials comprise structured or unstructured packing in the top third of the liquid removal vessel.

9. The method of claim 8 , wherein the feed inlet of the liquid removal vessel is no higher than halfway up the liquid removal vessel.

10. The method of claim 7 , wherein the packing materials are made of a material comprising stainless steel, hastelloy, titanium, nickel, copper, carbon steel, alumina, ceramics, polypropylene, polyethylene, polyvinylchloride, polyvinylidene fluoride, polyfluoroethylenepropylene, ethylene chlorotrifluoroethylene, polytetrafluoroethylene, polychlorotrifluoroethylene, natural diamond, man-made diamond, chemical-vapor deposition diamond, polycrystalline diamond, or combinations thereof.

11. The method of claim 1 , wherein any surface of the liquid removal vessel exposed to the carrier liquid and the carbon dioxide gas comprises aluminum, stainless steel, polymers, carbon steel, ceramics, polytetrafluoroethylene, polychlorotrifluoroethylene, natural diamond, man-made diamond, chemical-vapor deposition diamond, polycrystalline diamond, or combinations thereof.

12. The method of claim 1 , wherein the carrier liquid comprises 1,1,3-trimethylcyclopentane, 1,4-pentadiene, 1,5-hexadiene, 1-butene, 1-methyl-1-ethylcyclopentane, 1-pentene, 2,3,3,3-tetrafluoropropene, 2,3-dimethyl-1-butene, 2-chloro-1,1,1,2-tetrafluoroethane, 2-methylpentane, 3-methyl-1,4-pentadiene, 3-methyl-1-butene, 3-methyl-1-pentene, 3-methylpentane, 4-methyl-1-hexene, 4-methyl-1-pentene, 4-methylcyclopentene, 4-methyl-trans-2-pentene, bromochlorodifluoromethane, bromodifluoromethane, bromotrifluoroethylene, chlorotrifluoroethylene, cis 2-hexene, cis-1,3-pentadiene, cis-2-hexene, cis-2-pentene, dichlorodifluoromethane, difluoromethyl ether, trifluoromethyl ether, dimethyl ether, ethyl fluoride, ethyl mercaptan, hexafluoropropylene, isobutane, isobutene, isobutyl mercaptan, isopentane, isoprene, methyl isopropyl ether, methylcyclohexane, methylcyclopentane, methylcyclopropane, n,n-diethylmethylamine, octafluoropropane, pentafluoroethyl trifluorovinyl ether, propane, sec-butyl mercaptan, trans-2-pentene, trifluoromethyl trifluorovinyl ether, vinyl chloride, bromotrifluoromethane, chlorodifluoromethane, dimethyl silane, ketene, methyl silane, perchloryl fluoride, propylene, vinyl fluoride, or combinations thereof.

13. The method of claim 1 , wherein the first temperature is between 56.5° C. and −30° C., the second temperature is between 10° C. and 45° C. higher than the first temperature, and the third temperature is between the first temperature and the second temperature.

14. The method of claim 1 , wherein the compression process is conducted by a compressor.

15. The method of claim 14 , wherein the compressor comprises a reciprocating, scroll, screw, rotary, sorbent, or centrifugal style compressor.

16. The method of claim 14 , wherein any surface of the compressor exposed to the carbon dioxide gas comprises stainless steel, ceramics, cast aluminum, wrought aluminum, bronze, graphite resin, or combinations thereof.

17. The method of claim 14 , wherein the two compressors comprise reciprocating, scroll, screw, rotary, sorbent, centrifugal, or a combination of styles of compressors thereof.

18. The method of claim 14 , wherein any surface of the compressor exposed to the carbon dioxide gas comprises stainless steel, ceramics, cast aluminum, wrought aluminum, bronze, graphite resin, or combinations thereof.

19. The method of claim 1 , wherein the compression step is conducted by two compressors in series.

20. The method of claim 1 , wherein the carbon dioxide in the carrier liquid comprises dissolved carbon

Assignees

• Baxter Larry
• Hoeger Christopher
• Mansfield Eric
• Stitt Kyler
• Burt Stephanie
• Davis Nathan
• Hall Labs Llc

Inventors

• Baxter Larry
• Hoeger Christopher
• Mansfield Eric
• Stitt Kyler
• Burt Stephanie
• Davis Nathan

Classifications

• B01D19/0036

  Flash degasification (the other groups take precedence) · CPC title

• B01D1/00 Primary

  Evaporating ({evaporation in general, e.g. of liquids for gas phase reactions B01B1/005} ; removal of incrustation B08B; preparation of starch C08B30/00; sugar industry C13; prevention of incrustation C23F; drying solid materials or objects by evaporating liquids therefrom F26) · CPC title

• B01D19/00

  Degasification of liquids · CPC title

• B01D1/0041 Primary

  Use of fluids · CPC title

• Y02C20/40

  of CO2 · CPC title