US4101635A
Expired / Lapsed
US
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Method for regenerating and recycling catalyst for oxidation of sulfur dioxide
Assignee: Eneos Corp
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Filing: 1977-02-28
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Granted: 1978-07-18
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Expires: 1997-02-28
Abstract
Abstract In a method for oxidizing sulfur dioxide by contacting a sulfur dioxide-containing gas and an oxygen-containing gas with an aqueous solution containing pentavalent vanadium and divalent manganese as a catalyst, the method for regenerating and recycling the oxidation catalyst which comprises adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the aqueous solution catalyst used in the oxidation reaction, separating the resulting gypsum, and recycling the recovered aqueous solution catalyst for use in the oxidation of sulfur dioxide.
Inventors
- 👤 Masao Nambu
- 👤 Syunichi Yamamoto
- 👤 Yoshihisa Koiwai
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 23:10
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8603; B01D53/8609; B01J; B01J27/00; B01J27/28; B01J27/30; B01J37/00; B01J37/12; C; C01; C01B; C01B17/00; C01B17/69; C01B17/74; C01B17/76; C01B17/775; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
215 words
A process for removing sulfur dioxide from a gas stream containing the same prior to passing said gas stream to the ambient atmosphere comprising oxidizing the sulfur dioxide with an oxygen-containing gas in a low temperature, liquid phase catalytic reaction to produce sulfuric acid wherein said reaction between sulfur dioxide and oxygen is carried out in the presence of an acidic aqueous solution containing, as oxidation catalyst, at least 3ppm each of pentavalent vanadium ion and divalent manganese ion and regenerating and recycling the oxidation catalyst by the steps of: adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the aqueous catalyst solution used in the oxidation reaction and containing sulfuric acid to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum, by first adding the calcium compound to the aqueous catalyst solution and thereafter adding the oxygen-containing gas to the aqueous catalyst solution wherein the amount of calcium compound added is sufficient to maintain the pH of the aqueous catalyst solution at at least 7.0, separating the resulting gypsum, and recycling the recovered aqueous solution catalyst for use in the oxidation of sulfur dioxide.
Claim 2
Dependent Claim
215 words
A process for removing sulfur dioxide from a gas stream containing the same prior to passing said gas stream to the ambient atmosphere comprising oxidizing the sulfur dioxide with an oxygen-containing gas in a low temperature, liquid phase catalytic reaction to produce sulfuric acid wherein said reaction between sulfur dioxide and oxygen is carried out in the presence of an acidic aqueous solution containing, as oxidation catalyst, at least 3ppm each of pentavalent vanadium ion and divalent manganese ion and regenerating and recycling the oxidation catalyst by the steps of: adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the aqueous catalyst solution used in the oxidation reaction and containing sulfuric acid to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum, by first adding the calcium compound to the aqueous catalyst solution and thereafter adding the oxygen-containing gas to the aqueous catalyst solution wherein the amount of calcium compound added is sufficient to maintain the pH of the aqueous catalyst solution at at least 7.0, separating the resulting gypsum, and recycling the recovered aqueous solution catalyst for use in the oxidation of sulfur dioxide.
Claim 3
Dependent Claim
32 words
The method of claim 1 wherein the concentration of pentavalent vanadium in the aqueous solution catalyst is 3 to 8,000 ppm, and the concentration of divalent manganese is 3 to 200 ppm.
Claim 4
Dependent Claim
23 words
The methos of claim 1 wherein at least 3 ppm of trivalent iron is caused to be present in the aqueous solution catalyst.
Claim 5
Dependent Claim
22 words
The method of claim 1 wherein soot is added to the aqueous solution catalyst prior to the oxidation reaction of sulfur dioxide.
Claim 6
Dependent Claim
208 words
A process for removing sulfur dioxide from a gas stream containing the same prior to passing said gas stream to the ambient atmosphere comprising oxidizing the sulfur dioxide with an oxygen-containing gas in a low temperature, liquid phase catalytic reaction to produce sulfuric acid wherein said reaction between sulfur dioxide and oxygen is carried out in the presence of an acidic aqueous solution containing, as oxidation catalyst, at least 3 ppm each of pentavalent vanadium ion and divalent manganese ion, and regenerating and recycling the oxidation catalyst by the steps of: adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the aqueous catalyst solution used in the oxidation reaction and containing sulfuric acid to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum, by simultaneously adding the calcium compound and the oxygen-containing gas to the aqueous catalyst solution wherein the amount of the calcium compound is sufficient to maintain the pH of the aqueous catalyst solution at at least 2.0, separating the resulting gypsum, and recycling the recovered aqueous solution catalyst for use in the oxidation of dioxide.
Claim 7
Dependent Claim
208 words
A process for removing sulfur dioxide from a gas stream containing the same prior to passing said gas stream to the ambient atmosphere comprising oxidizing the sulfur dioxide with an oxygen-containing gas in a low temperature, liquid phase catalytic reaction to produce sulfuric acid wherein said reaction between sulfur dioxide and oxygen is carried out in the presence of an acidic aqueous solution containing, as oxidation catalyst, at least 3 ppm each of pentavalent vanadium ion and divalent manganese ion, and regenerating and recycling the oxidation catalyst by the steps of: adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the aqueous catalyst solution used in the oxidation reaction and containing sulfuric acid to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum, by simultaneously adding the calcium compound and the oxygen-containing gas to the aqueous catalyst solution wherein the amount of the calcium compound is sufficient to maintain the pH of the aqueous catalyst solution at at least 2.0, separating the resulting gypsum, and recycling the recovered aqueous solution catalyst for use in the oxidation of dioxide.
Claim 8
Dependent Claim
32 words
The method of claim 5 wherein the concentration of pentavalent manganese in the aqueous solution catalyst is 3 to 8,000 ppm, and the concentration of divalent vanadium is 3 to 200 ppm.
Claim 9
Dependent Claim
23 words
The method of claim 5 wherein at least 3 ppm of trivalent iron is caused to be present in the aqueous solution catalyst.
Claim 10
Dependent Claim
22 words
The method of claim 5 wherein soot is added to the aqueous solution catalyst prior to the oxidation reaction of sulfur dioxide.
Claim 11
Independent Claim
154 words
A method for regenerating an oxidation catalyst comprising an acidic aqueous solution of pentavalent vanadium divalent manganese and sulfuric acid and having an initial pH of less than 7.0 in which at least a portion of the pentavalent vanadium has been converted to tetravalent vanadium, comprising adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the acidic aqueous catalyst solution used in an oxidation reaction to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum by first adding the calcium compound to the aqueous catalyst solution and thereafter adding the oxygen-containing gas to the aqueous catalyst solution wherein the amount of calcium compound added is sufficient to mainain the pH of the aqueous catalyst solution at at least 7.0, and separating the resulting gypsum.
Claim 12
Independent Claim
154 words
A method for regenerating an oxidation catalyst comprising an acidic aqueous solution of pentavalent vanadium divalent manganese and sulfuric acid and having an initial pH of less than 7.0 in which at least a portion of the pentavalent vanadium has been converted to tetravalent vanadium, comprising adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the acidic aqueous catalyst solution used in an oxidation reaction to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum by first adding the calcium compound to the aqueous catalyst solution and thereafter adding the oxygen-containing gas to the aqueous catalyst solution wherein the amount of calcium compound added is sufficient to mainain the pH of the aqueous catalyst solution at at least 7.0, and separating the resulting gypsum.
Claim 13
Independent Claim
147 words
A method for regenerating an oxidation catalyst comprising an acidic aqueous solution of pentavalent vanadium, divalent manganese and sulfuric acid and having an initial pH of less than 2.0 in which at least a portion of the pentavalent vanadium has been converted to tetravalent vanadium, comprising adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the acidic aqueous catalyst solution used in an oxidation reaction to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum by simultaneously adding the calcium compound and the oxygen-containing gas to the aqueous catalyst solution wherein the amount of the calcium compound is sufficient to maintain the pH of the aqueous catalyst solution at at least 2.0, and separating the resulting gypsum.
Claim 14
Independent Claim
147 words
A method for regenerating an oxidation catalyst comprising an acidic aqueous solution of pentavalent vanadium, divalent manganese and sulfuric acid and having an initial pH of less than 2.0 in which at least a portion of the pentavalent vanadium has been converted to tetravalent vanadium, comprising adding at least one calcium compound selected from the group consisting of calcium oxide, calcium hydroxide and calcium carbonate and an oxygen-containing gas as an oxidizing agent to at least a part of the acidic aqueous catalyst solution used in an oxidation reaction to thereby oxidize tetravalent vanadium contained therein to pentavalent vanadium and convert sulfuric acid to gypsum by simultaneously adding the calcium compound and the oxygen-containing gas to the aqueous catalyst solution wherein the amount of the calcium compound is sufficient to maintain the pH of the aqueous catalyst solution at at least 2.0, and separating the resulting gypsum.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-07-17 | 1982-01-16 | 1982-07-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-17 | 1986-01-16 | 1986-07-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-17 | 1990-01-16 | 1990-07-18 | $7700.00 | Window Closed / Lapsed |