US4822394A
Expired / Lapsed
US
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Method and apparatus for the production and liquefaction of gases
Assignee: BOW VALLEY RESOURCE SERVICES Inc A CORP OF
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Filing: 1987-09-14
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Granted: 1989-04-18
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Expires: 2007-09-14
Abstract
Abstract The present invention provides a method and apparatus for collecting and liquefying off-gases, particularly carbon dioxide, generated by a wet oxidation of organic matter and for the on sight gasification of liquid oxygen for use as an oxidant in the wet oxidation reaction. Through a series of separation and pressurization operations, high pressure off-gases are introduced into a heat exchanger at substantially the same time as liquid oxygen. The liquid oxygen and compressed off-gases are in heat exchange relation in the heat exchanger but are isolated from one another. Heat is transferred from the compressed off-gases to the liquid oxygen whereby the off-gases are liquified and the liquid oxygen is gasified. The liquified off-gases may then be stored in appropriate storage units. The gaseous oxygen is used as the oxidant for the wet oxidation reaction. In another aspect, odor-producing compounds are removed from the off-gases by a condensation process wherein the odor-producing compounds are separated from the off-gases by condensation. In still another aspect, these odor-producing compounds are removed from the off-gases after liquefaction by a chemical stripping operation which chemically strips the odor-producing compounds from the liquefied off-gases.
Inventors
- 👤 Joseph E. Zeigler
- 👤 Hermann W. Peterscheck
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 23:17
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/06; F25J3/063; F25J3/067; B; B01; B01D; B01D5/00; B01D5/0033; B01D5/0039; B01D5/0057; B01D5/0069; B01D53/00; B01D53/002; B01D53/34; B01D53/46; B01D53/72; C; C02; C02F; C02F11/00; C02F11/06; C02F11/08; C02F11/083; F17; F17C; F17C9/00; F17C9/02; F17C9/04; F25J1/00; F25J1/0002; F25J1/0027; F25J1/02; F25J1/0221; F25J2210/00; F25J2210/50; F25J2210/70; F25J2220/00; F25J2220/80; F25J2220/82; F25J2220/84; F25J2270/00; F25J2270/90; F25J2270/904; Y; Y02; Y02C; Y02C20/00; Y02C20/40; Y02P; Y02P70/00; Y02P70/10; Y10; Y10S; Y10S62/00; Y10S62/928
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
125 words
A method for liquefying off-gas and gasifying liquid oxygen comprising the following steps performed in sequence: generating off-gas by wet oxidation reaction; flowing the off-gas into a heat-exchanger; flowing the liquid oxygen into the heat exchanger such that the off-gas and the liquid oxygen are in direct heat transfer relation with each other within said heat exchanger; allowing a sufficient quantity of heat to flow from said off-gas to said liquid oxygen such that said off-gas is liquified to form a liquid product and so that said liquid oxygen is converted to gaseous oxygen; flowing said liquid product out of said heat exchanger; flowing said gaseous oxygen out of said heat exchanger; and using said gaseous oxygen as an oxidant in said wet oxidation reaction.
Claim 2
Independent Claim
125 words
A method for liquefying off-gas and gasifying liquid oxygen comprising the following steps performed in sequence: generating off-gas by wet oxidation reaction; flowing the off-gas into a heat-exchanger; flowing the liquid oxygen into the heat exchanger such that the off-gas and the liquid oxygen are in direct heat transfer relation with each other within said heat exchanger; allowing a sufficient quantity of heat to flow from said off-gas to said liquid oxygen such that said off-gas is liquified to form a liquid product and so that said liquid oxygen is converted to gaseous oxygen; flowing said liquid product out of said heat exchanger; flowing said gaseous oxygen out of said heat exchanger; and using said gaseous oxygen as an oxidant in said wet oxidation reaction.
Claim 3
Dependent Claim
34 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 1 further including the step of increasing the pressure of said off-gas before the step of flowing said off-gas into said heat-exchanger.
Claim 4
Dependent Claim
51 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 3 wherein the temperature of said off-gas is raised during said pressure increasing step such that the temperature of said off-gas after said pressure increasing step is greater than the temperature of said off-gas before said pressure increasing step.
Claim 5
Dependent Claim
59 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 3 further including the step of flowing said off-gas through a cooler before said off-gas is flowed into said heat-exchanger and cooling said off-gas in said cooler to a temperature less than the temperature to which said off-gas is allowed to rise during said pressure increasing step.
Claim 6
Dependent Claim
45 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 4 wherein said off-gas includes water vapor and further including the steps of condensing said water vapor during said cooling step to form liquid water and separating said liquid water from said off-gas.
Claim 7
Dependent Claim
41 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 1 wherein said off-gas generation step includes producing an effluent by said wet oxidation reaction, said effluent containing said off-gas and water, and separating said off-gas from said effluent.
Claim 8
Dependent Claim
26 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 6, wherein said off-gas generation step further includes separating said water from said effluent.
Claim 9
Dependent Claim
21 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 6, wherein said off-gas is a mixture of gases.
Claim 10
Dependent Claim
35 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 8 wherein the principal constituent of said mixture of gases is carbon dioxide and wherein said liquid product is principally liquid carbon dioxide.
Claim 11
Dependent Claim
36 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 8, wherein non-condensed off-gas is associated with said liquid product and further including the step of separating said non-condensed off-gas from said liquid product.
Claim 12
Dependent Claim
23 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 10, further including the step of incinerating said separated non-condensed off-gas.
Claim 13
Dependent Claim
25 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 1, wherein said wet oxidation reaction includes the wet oxidation of municipal waste.
Claim 14
Dependent Claim
51 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 5, wherein said off-gas mixture includes unsaturated hydrocarbon compounds and further including the steps of condensing and separating said unsaturated hydrocarbon compounds from said off-gas mixture prior to said step of flowing said off-gas mixture into said heat exchanger.
Claim 15
Dependent Claim
38 words
The method for liquefying off-gas and gasifying liquid oxygen recited in claim 5, wherein said liquid product includes unsaturated hydrocarbon compounds and further including the steps of stripping and separating said unsaturated hydrocarbon compounds from said liquid product.
Claim 16
Independent Claim
254 words
An apparatus which produces and liquifies gases, comprising: a reaction apparatus for oxidizing organic matter in an aqueous medium at high temperature and pressure to substantially oxidize said organic matter producing an effluent which includes an ash, water and off-gases; a separator for receiving said effluent and for separating said off-gases from said effluent; means for flowing said effluent from said reaction apparatus to said separator; a compressor for receiving said off-gases from said separator and for compressing said off-gases to produce a gas pressure greater than the pressure at which said off-gases reside in said separator; means for flowing said off-gases from said separator to said compressor; a cooler for receiving said pressurized off-gases from said compressor and for cooling said pressurized off-gases to a temperature less than the temperature of said off-gases in said compressor; means for flowing said pressurized off-gases from said compressor to said cooler; supply means for containing a supply of liquid oxygen; a heat-exchanger for receiving said pressurized off-gases from said cooler and for receiving said liquid oxygen contemporaneous with said pressurized off-gases, said heat exchanger having means for allowing the separate flow of said pressurized off-gases and said liquid oxygen therethrough such that heat is transferred from said off-gases to said liquid oxygen at a rate which liquefies said off-gases to form a liquid product and gasifies said liquid oxygen; means for flowing said gaseous oxygen to said reaction apparatus for use in oxidizing said organic matter; and means for flowing said liquid product from said heat-exchanger.
Claim 17
Independent Claim
254 words
An apparatus which produces and liquifies gases, comprising: a reaction apparatus for oxidizing organic matter in an aqueous medium at high temperature and pressure to substantially oxidize said organic matter producing an effluent which includes an ash, water and off-gases; a separator for receiving said effluent and for separating said off-gases from said effluent; means for flowing said effluent from said reaction apparatus to said separator; a compressor for receiving said off-gases from said separator and for compressing said off-gases to produce a gas pressure greater than the pressure at which said off-gases reside in said separator; means for flowing said off-gases from said separator to said compressor; a cooler for receiving said pressurized off-gases from said compressor and for cooling said pressurized off-gases to a temperature less than the temperature of said off-gases in said compressor; means for flowing said pressurized off-gases from said compressor to said cooler; supply means for containing a supply of liquid oxygen; a heat-exchanger for receiving said pressurized off-gases from said cooler and for receiving said liquid oxygen contemporaneous with said pressurized off-gases, said heat exchanger having means for allowing the separate flow of said pressurized off-gases and said liquid oxygen therethrough such that heat is transferred from said off-gases to said liquid oxygen at a rate which liquefies said off-gases to form a liquid product and gasifies said liquid oxygen; means for flowing said gaseous oxygen to said reaction apparatus for use in oxidizing said organic matter; and means for flowing said liquid product from said heat-exchanger.
Claim 18
Dependent Claim
22 words
The apparatus recited in claim 15, wherein said separator is pressurized and adapted for the separation of said water from said effluent.
Claim 19
Dependent Claim
16 words
The apparatus recited in claim 15, wherein said reaction apparatus is a down-hole, wet-oxidation reaction apparatus.
Claim 20
Dependent Claim
57 words
The apparatus recited in claim 15, wherein non-condensed off-gases are associated with said liquid product and further including a second separator for receiving said liquid product with associated non-condensed off-gases and for separating said non-condensable off-gases from said liquid product, said separator being in flow communication with said means for flowing said liquid product from said heat-exchanger.
Claim 21
Dependent Claim
44 words
The apparatus recited in claim 15 wherein said off-gases include unsaturated hydrocarbon compounds and further including condenser means for receiving said off-gases with said unsaturated hydrocarbon compounds and for separating said unsaturated hydrocarbon compounds from said off-gases by preferentially condensing said unsaturated hydrocarbon compounds.
Claim 22
Dependent Claim
43 words
The apparatus recited in claim 15 wherein said liquid product includes unsaturated hydrocarbon compounds and further including stripper means for receiving said liquid product with said unsaturated hydrocarbon compounds and for separating said unsaturated hydrocarbon compounds from said liquid product by chemical stripping.
References Cited (Backward Citations)
US4272383A
Cited
US4704146A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-04-17 | 1992-10-17 | 1993-04-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-04-17 | 1996-10-17 | 1997-04-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-04-17 | 2000-10-17 | 2001-04-18 | $7700.00 | Window Closed / Lapsed |