US4666852A
Expired / Lapsed
US
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Photosynthetic bioconversion sulfur removal
Assignee: Gas Technology Institute
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Filing: 1982-07-26
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Granted: 1987-05-19
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Expires: 2002-07-26
Abstract
Abstract This invention relates to a process for sulfur removal from gas streams by contacting an active culture of photosynthetic sulfur bacteria with reductive sulfur compounds and carbon oxides in the gas stream under substantially anaerobic conditions with irradiation by electromagnetic energy and cultivating the bacteria to form elemental sulfur and organic carbon compounds. The process is particularly suited for removal of hydrogen sulfide from acid-gas streams and from natural or raw pipeline gas with greater than 95 percent and usually greater than about 98 percent sulfur removal from gas streams. The process is operable with gas streams of very low hydrogen sulfide content of about 0.1 and less Mole percent and gas streams of high hydrogen sulfide content. The process utilizes Chlorobium bacteria to produce elemental sulfur and organic carbon compounds which may be advantageously utilized to produce hydrocarbon fuels.
Inventors
- 👤 Douglas J. Cork
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 09:10
CPC Classifications
B; B01; B01D; B01D53/00; C; C10; C10K; C10K1/00; C10K1/20; C12; C12N; C12N13/00; C12P; C12P3/00; C12M; C12M21/00; C12M21/02; C12M47/00; C12M47/18; Y; Y02; Y02W; Y02W10/00; Y02W10/30; Y02W10/37; Y10; Y10S; Y10S435/00; Y10S435/801; Y10S435/813; Y10S435/8215; Y10S435/822
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
161 words
A photosynthetic bioconversion process for removal of sulfur compounds from a gas stream comprising carbon oxide and reductive sulfur compounds, comprising the steps: contacting said gas stream comprising carbon oxide compounds and reductive sulfur compounds with an active culture of photosynthetic bacteria capable of utilizing said reductive sulfur compound as its sole source of reducing electrons and said carbon oxides as its sole source of carbon for growth under substantially anaerobic conditions with electromagnetic radiation wherein said reductive sulfur compound provides the sole source of reducing electrons and said carbon oxides provide the sole source of carbon for growth and cultivating said bacteria to form elemental sulfur and organic carbon compounds; passing said formed elemental sulfur and organic carbon compounds together with said photosynthetic sulfur bacteria to a dark phase reactor for further metabolism of said organic carbon compounds to form and excrete from said bacteria predominately lower organic acids; and separately removing said elemental sulfur and said lower oganic acids.
Claim 2
Dependent Claim
161 words
A photosynthetic bioconversion process for removal of sulfur compounds from a gas stream comprising carbon oxide and reductive sulfur compounds, comprising the steps: contacting said gas stream comprising carbon oxide compounds and reductive sulfur compounds with an active culture of photosynthetic bacteria capable of utilizing said reductive sulfur compound as its sole source of reducing electrons and said carbon oxides as its sole source of carbon for growth under substantially anaerobic conditions with electromagnetic radiation wherein said reductive sulfur compound provides the sole source of reducing electrons and said carbon oxides provide the sole source of carbon for growth and cultivating said bacteria to form elemental sulfur and organic carbon compounds; passing said formed elemental sulfur and organic carbon compounds together with said photosynthetic sulfur bacteria to a dark phase reactor for further metabolism of said organic carbon compounds to form and excrete from said bacteria predominately lower organic acids; and separately removing said elemental sulfur and said lower oganic acids.
Claim 3
Dependent Claim
20 words
The process of claim 1 wherein the hydraulic detention time in the dark phase is about 12 to 36 hours.
Claim 4
Dependent Claim
21 words
The process of claim 1 wherein the hydraulic detention time in the dark phase is about 20 to about 30 hours.
Claim 5
Dependent Claim
12 words
The process of claim 1 wherein said photosynthetic sulfur bacteria are Chlorobium.
Claim 6
Dependent Claim
30 words
The process of claim 1 wherein said reducing sulfur compounds are predominantly hydrogen sulfide and said carbon oxides are predominantly carbon dioxide, said carbon dioxide being present in stoichiometric excess.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein said bacteria are Chlorobium thiosulfatophilum.
Claim 8
Dependent Claim
18 words
The process of claim 1 wherein said cultivating is at temperatures of about 25° to about 45° C.
Claim 9
Dependent Claim
18 words
The process of claim 1 wherein said cultivating is at a pH of about 6 to about 8.
Claim 10
Dependent Claim
21 words
The process of claim 1 wherein said Chlorobium are present in concentrations of about 0.5 to about 1.5 grams per liter.
Claim 11
Dependent Claim
17 words
The process of claim 1 wherein the hydraulic detention time is about 12 to about 36 hours.
Claim 12
Dependent Claim
21 words
The process of claim 1 wherein said irradiation is with electromagnetic energy at wave1engths of about 300 to about 1200 nm.
Claim 13
Dependent Claim
20 words
The process of claim 1 wherein said process is carried out at pressures of about ambient to about 5 atmospheres.
Claim 14
Dependent Claim
36 words
The process of claim 1 wherein said hydrogen sulfide comprises less than 10 mole percent of said gas stream and greater than 95 percent of the sulfur of said hydrogen sulfide is converted to elemental sulfur.
Claim 15
Dependent Claim
27 words
The process of claim 1 wherein said hydrogen sulfide is introduced in a concentration of about 0.045 to about 0.080 Mole H 2 S per gram bacteria.
Claim 16
Dependent Claim
110 words
The process of claim 4 wherein said cultivating is at temperatures of about 25° to about 45° C., pH about 6 to about 8, said Chlorobium are present in concentrations of about 0.5 to about 1.5 grams per liter, hydraulic detention time is about 12 to about 36 hours, said irradiation is with electromagnetic energy at wavelengths of about 400 to about 1000 nm, said hydrogen sulfide is introduced in a concentration of about 0.045 to about 0.080 Mole H 2 S per gram bacteria; and the hydraulic detention time is about 12 to about 36 hours converting greater than about 95 percent of the hydrogen sulfide to elemental sulfur.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1990-05-18 | 1990-11-17 | 1991-05-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-05-18 | 1994-11-17 | 1995-05-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-05-18 | 1998-11-17 | 1999-05-19 | $7700.00 | Window Closed / Lapsed |