Hydrocyclone for cryogenic gas-vapor separation

Patent metadata

Field	Value
Publication number	US-10328384-B2
Application number	US-201715439177-A
Country	US
Kind code	B2
Filing date	Feb 22, 2017
Priority date	Feb 22, 2017
Publication date	Jun 25, 2019
Grant date	Jun 25, 2019

Abstract

A hydrocyclone for separating a vapor from a carrier gas is disclosed. The hydrocyclone comprises one or more nozzles. A cryogenic liquid is injected to a tangential feed inlet at a velocity that induces a tangential flow and a cyclone vortex in the hydrocyclone. The carrier gas is injected into the cryogenic liquid, causing the vapor to dissolve, condense, desublimate, or a combination thereof, forming a vapor-depleted carrier gas and a vapor-enriched cryogenic liquid. The vapor-depleted carrier gas is drawn through a vortex finder and the vapor-enriched cryogenic liquid is drawn through an apex nozzle outlet. In this manner, the vapor is removed from the carrier gas.

First claim

The invention claimed is:

1. A hydrocyclone for separating a vapor from a carrier gas, the apparatus comprising:
a vessel having a generally cylindrical shape with a generally circular cross-section;
a tangential feed inlet for a cryogenic liquid, attached to a cylindrical wall of the vessel on an upper end of the vessel, wherein the cryogenic liquid is injected to the tangential feed inlet at a velocity that induces a tangential flow and a cyclone vortex in the hydrocyclone;
at least a portion of a wall of the hydrocyclone comprising one or more nozzles, wherein the carrier gas is injected into the cryogenic liquid, causing the vapor to desublimate, forming a vapor-depleted carrier gas and a vapor-enriched cryogenic liquid, wherein the one or more nozzles have injection points that are flush with an inner side of the wall of the hydrocyclone, and wherein any surface of the injection points exposed to the cryogenic liquid comprise a material that inhibits adsorption of gases, prevents deposition of solids, or a combination thereof;
a vortex finder outlet on a top of the inner vessel, perpendicular to the tangential feed inlet, through which the vapor-depleted gas is drawn;
a lower section of the inner vessel that tapers conically down in size to an apex nozzle outlet through which the vapor-enriched cryogenic liquid is drawn; and,
the vessel, the tangential feed inlet, the vortex finder, the lower section, and the apex nozzle outlet sized to cause a gas/liquid separation;
whereby the vapor is removed from the carrier gas.

2. The apparatus of claim 1 , wherein the vapor comprises carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, hydrocarbons with a freezing point above 0° C., or combinations thereof.

3. The apparatus of claim 1 , wherein the carrier gas comprises combustion flue gas, syngas, natural gas, steam reforming gas, any hydrocarbon that has higher volatility than water, or combinations thereof.

4. The apparatus of claim 1 , wherein the cryogenic liquid comprises any compound or mixture of compounds with a freezing point below a temperature at which a solid forms from the vapor.

5. The apparatus of claim 1 , wherein the vessel, the tangential feed inlet, the vortex finder, the lower section, and the apex nozzle outlet comprise aluminum, stainless steel, polymers, ceramics, or combinations thereof.

6. The apparatus of claim 1 , wherein the material comprises ceramics, polytetrafluoroethylene, polychlorotrifluoroethylene, natural diamond, man-made diamond, chemical-vapor deposition diamond, polycrystalline diamond, or combinations thereof.

7. A hydrocyclone for separating a vapor from a carrier gas, the apparatus comprising:
a vessel having a generally cylindrical shape with a generally circular cross-section;
a tangential feed inlet for a cryogenic liquid, attached to a cylindrical wall of the vessel on an upper end of the vessel, wherein the cryogenic liquid is injected to the tangential feed inlet at a velocity that induces a tangential flow and a cyclone vortex in the hydrocyclone;
at least a portion of a wall of the hydrocyclone comprising one or more nozzles, wherein the carrier gas is injected into the cryogenic liquid, causing the vapor to desublimate, forming a vapor-depleted carrier gas and a vapor-enriched cryogenic liquid, wherein the one or more nozzles have injection points that are flush with an inner side of the wall of the hydrocyclone, and wherein the one or more nozzles are attached parallel to the tangential feed inlet to cause a tangential carrier gas stream to inject with the tangential flow of the cryogenic liquid;
a vortex finder outlet on a top of the inner vessel, perpendicular to the tangential feed inlet, through which the vapor-depleted gas is drawn;
a lower section of the inner vessel that tapers conically down in size to an apex nozzle outlet through which the vapor-enriched cryogenic liquid is drawn; and,
the vessel, the tangential feed inlet, the vortex finder, the lower section, and the apex nozzle outlet sized to cause a gas/liquid separation;
whereby the vapor is removed from the carrier gas.

8. The apparatus of claim 7 , wherein the vapor comprises carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, hydrocarbons with a freezing point above 0° C., or combinations thereof.

9. The apparatus of claim 7 , wherein the carrier gas comprises combustion flue gas, syngas, natural gas, steam reforming gas, any hydrocarbon that has higher volatility than water, or combinations thereof.

10. The apparatus of claim 7 , wherein the cryogenic liquid comprises any compound or mixture of compounds with a freezing point below a temperature at which a solid forms from the vapor.

11. The apparatus of claim 7 , wherein the vessel, the tangential feed inlet, the vortex finder, the lower section, and the apex nozzle outlet comprise aluminum, stainless steel, polymers, ceramics, or combinations thereof.

12. The apparatus of claim 7 , wherein any surface of the injection points exposed to the cryogenic liquid comprise a material that inhibits adsorption of gases, prevents deposition of solids, or a combination thereof.

13. The apparatus of claim 12 , wherein the material comprises ceramics, polytetrafluoroethylene, polychlorotrifluoroethylene, natural diamond, man-made diamond, chemical-vapor deposition diamond, polycrystalline diamond, or combinations thereof.

14. A hydrocyclone for separating a vapor from a carrier gas, the apparatus comprising:
a vessel having a generally cylindrical shape with a generally circular cross-section;
a tangential feed inlet for a cryogenic liquid, attached to a cylindrical wall of the vessel on an upper end of the vessel, wherein the cryogenic liquid is injected to the tangential feed inlet at a velocity that induces a tangential flow and a cyclone vortex in the hydrocyclone;
at least a portion of a wall of the hydrocyclone comprising one or more nozzles, wherein the carrier gas is injected into the cryogenic liquid, causing the vapor to desublimate, forming a vapor-depleted carrier gas and a vapor-enriched cryogenic liquid, wherein the one or more nozzles have injection points that are flush with an inner side of the wall of the hydrocyclone, and wherein the one or more nozzles are attached anti-parallel to the tangential feed inlet to cause a tangential carrier gas stream to inject against the tangential flow of the cryogenic liquid;
a vortex finder outlet on a top of the inner vessel, perpendicular to the tangential feed inlet, through which the vapor-depleted gas is drawn;
a lower section of the inner vessel that tapers conically down in size to an apex nozzle outlet through which the vapor-enriched cryogenic liquid is drawn; and,
the vessel, the tangential feed inlet, the vortex finder, the lower section, and the apex nozzle outlet sized to cause a gas/liquid separation;
whereby the vapor is removed from the carrier gas.

15. The apparatus of claim 14 , wherein the vapor comprises carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, hydrocarbons with a freezing point above 0° C., or combinations thereof.

16. The apparatus of claim 14 , wherein the carrier gas comprises combustion flue gas, syngas, natural gas, steam reforming gas, any hydrocarbon that has higher volatility than water, or combinations thereof.

17. The apparatus of claim 14 , wherein the cryogenic liquid comprises any compound o

Assignees

• Baxter Larry
• Hoeger Christopher
• Sayre Aaron
• Chamberlain Skyler
• Stitt Kyler
• Mansfield Eric
• Burt Stephanie
• Baxter Andrew
• Chamberlain Jacom
• Davis Nathan
• Sustainable Energy Solutions Llc

Inventors

• Baxter Larry
• Hoeger Christopher
• Sayre Aaron
• Chamberlain Skyler
• Stitt Kyler
• Mansfield Eric
• Burt Stephanie
• Baxter Andrew
• Chamberlain Jacom
• Davis Nathan

Classifications

• B01D53/002

  by condensation · CPC title

• F25J3/061

  Natural gas or substitute natural gas · CPC title

• B01D53/18 Primary

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• F25J3/0695

  Start-up or control of the process; Details of the apparatus used · CPC title

• F25J2205/10

  using combined expansion and separation, e.g. in a vortex tube, "Ranque tube" or a "cyclonic fluid separator", i.e. combination of an isentropic nozzle and a cyclonic separator; Centrifugal separation · CPC title