Patent US4629608A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4629608A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the removal of H2 S from geothermal steam and the conversion to sulfur

Assignee: Dow Chemical Co
•
Filing: 1985-06-24
•
Granted: 1986-12-16
•
Expires: 2005-06-24
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Process for removing H2S from the exhaust steam in a geothermal power plant wherein the H2S containing steam is contacted with an aqueous solution containing a ferric chelate and a cationic polymeric catalyst such as poly(dimethyldiallyl ammonium chloride). The conversion of H2S to sulfur is accelerated by the use of a small amount of the catalyst.

Inventors

  • 👤 Robert D. Lampton, Jr.
  • 👤 II Thomas M. Hopkins

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 06:14
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05; B; B01; B01D; B01D53/00; B01D53/14; F; F03; F03G; F03G4/00; F03G4/074

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 145 words
A process for removing H 2 S from a geothermal fluid stream containing H 2 S which comprises (A) contacting said H 2 S stream in a first reaction zone with an aqueous solution at a pH range suitable for removing H 2 S wherein said solution contains (1) an effective amount of at least one ferric chelate, and (2) an effective amount of one or more water soluble cationic polymeric catalysts whereby the conversion of H 2 S to free sulfur is accelerated in the presence of said polymeric catalyst and said ferric chelate is reduced to ferrous chelate, (B) contacting said solution containing ferrous chelate in a second reaction zone with an oxygen containing gas stream whereby said ferrous chelate is reoxidized to form a ferric chelate containing solution, and (C) recirculating said ferric chelate containing solution back to said first reaction zone.
Claim 2
Dependent Claim 145 words
A process for removing H 2 S from a geothermal fluid stream containing H 2 S which comprises (A) contacting said H 2 S stream in a first reaction zone with an aqueous solution at a pH range suitable for removing H 2 S wherein said solution contains (1) an effective amount of at least one ferric chelate, and (2) an effective amount of one or more water soluble cationic polymeric catalysts whereby the conversion of H 2 S to free sulfur is accelerated in the presence of said polymeric catalyst and said ferric chelate is reduced to ferrous chelate, (B) contacting said solution containing ferrous chelate in a second reaction zone with an oxygen containing gas stream whereby said ferrous chelate is reoxidized to form a ferric chelate containing solution, and (C) recirculating said ferric chelate containing solution back to said first reaction zone.
Claim 3
Dependent Claim 22 words
The process as set forth in claim 1 wherein said aqueous solution has a pH in the range from 5 to 10.
Claim 4
Dependent Claim 57 words
The process as set forth in claim 1 wherein the amount of ferric chelate is sufficient to provide a mol ratio of iron to H 2 S in the range from 2:1 to 4:1 and the amount of polymeric catalyst sufficient to provide a weight ratio of iron to catalyst in the range from 0.2:1 to 10:1.
Claim 5
Dependent Claim 28 words
The process as set forth in claim 3 wherein said chelate is the ferric chelate of N-hydroxyethyl ethylene diaminetriacetic acid and said polymeric catalyst is poly(dimethyldiallyl ammonium chloride).
Claim 6
Dependent Claim 41 words
The process as set forth in claim 1 wherein said ferric chelate has a chelating agent selected from the group consisting of nitrilotriacetic acid, N-hydroxyethyl aminodiacetic acid, ethylenediaminetetraacetic acid, N-hydroxyethylethylenediamine triacetic acid, diethylenetriaminepentaacetic acid, cyclohexene diamine tetraacetic acid, and triethylenetetraaminehexaacetic acid.
Claim 7
Dependent Claim 35 words
The process as set forth in claim 1 wherein said polymeric catalyst is selected from the group consisting of polyethylene amines, poly(2-hydroxypropyl-1-N-methyl ammonium chloride), poly(2-hydroxypropyl-1,1-N-dimethyl ammonium chloride), poly(N-dimethylaminomethyl)-acrylamide, poly(2-vinylimidazolimum bisulfate), poly(diallyldimethyl ammonium chloride), and poly(N-dimethylaminopropyl)-methacrylamide.
Claim 8
Dependent Claim 92 words
In a process for removing H 2 S from a geothermal stream containing H 2 S by contacting the H 2 S stream with an aqueous solution containing at least one ferric chelate to convert H 2 S to free sulfur and reduce ferric chelate to ferrous chelate and regenerating the ferrous chelate with an oxygen containing gas stream, the improvement which comprises accelerating the conversion of H 2 S to free sulfur by having an effective amount of one or more water soluble cationic polymeric catalysts present during said contacting step.
Claim 9
Dependent Claim 92 words
In a process for removing H 2 S from a geothermal stream containing H 2 S by contacting the H 2 S stream with an aqueous solution containing at least one ferric chelate to convert H 2 S to free sulfur and reduce ferric chelate to ferrous chelate and regenerating the ferrous chelate with an oxygen containing gas stream, the improvement which comprises accelerating the conversion of H 2 S to free sulfur by having an effective amount of one or more water soluble cationic polymeric catalysts present during said contacting step.
Claim 10
Dependent Claim 33 words
The process as set forth in claim 7 wherein the amount of said polymeric catalyst is sufficient to provide a weight ratio of iron to catalyst in the range from 0.2:1 to 10:1.
Claim 11
Dependent Claim 15 words
The process as set forth in claim 8 wherein said catalyst is poly(dimethyldiallyl ammonium chloride).

References Cited (Backward Citations)

US4218342A Cited
US4076621A Cited
US4374104A Cited
US4361487A Cited
US4382918A Cited
US4414817A Cited
US4468929A Cited
US4528817A Cited
US4421733A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-12-15 1990-06-16 1990-12-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-12-15 1994-06-16 1994-12-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-12-15 1998-06-16 1998-12-16 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag