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US3607036A Expired / Lapsed US ⏱️ 0.0 years remaining

Recovery of sulfur from gypsum

Assignee: Cities Service Co
•
Filing: 1968-02-09
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Granted: 1971-09-21
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Expires: 1988-02-09
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Abstract

Abstract The sulfur values are recovered from calcium sulfate principally in the form of sulfur dioxide by a two-stage reduction process. The calcium sulfate to be decomposed and the reducing gases pass countercurrently through the two-stage system in which the solids are maintained in a fluidized state. Temperatures within the range of from about 600* C. to about 900* C. may be employed. Steam may be condensed out of the product gas stream to provide a product gas containing a major proportion of sulfur dioxide and a minor proportion of carbon dioxide. The calcium sulfate is first reduced to calcium sulfide and is then further reduced in the second stage to calcium oxide. Sand may be mixed with the calcium sulfate being decomposed in order to minimize agglomeration of the solids.

Inventors

  • 👤 Ralph M Foecking
  • 👤 Robert D Austin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 22:51
CPC Classifications
C; C01; C01F; C01F11/00; C01F11/02; C01F11/10; C01B; C01B17/00; C01B17/48; C01B17/50; C01B17/501; C01B17/506

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 23 words
The process of claim 1 in which the temperature in each stage is maintained at from about 600* C. to about 900* C.
Claim 2
Dependent Claim 29 words
The process of claim 1 in which the reducing gases are passed upwardly through each stage at a velocity sufficient to maintain said calcium solids in a fluidized state.
Claim 3
Dependent Claim 29 words
The process of claim 1 in which steam is present in step c in an amount of from about 2 to about 6 moles per mole of reducing gas.
Claim 4
Dependent Claim 137 words
A process for converting calcium sulfate which comprises: a. drying gypsum to a substantially anhydrous form, b. contacting the substantially anhydrous gypsum with hydrogen sulfide in a first stage at a temperature of from 600* C. to about 900* C. to form calcium sulfide and a gas stream containing sulfur dioxide, c. recovering the sulfur-dioxide-containing gas stream, d. contacting said calcium sulfide with gas selected from the group consisting of hydrogen, carbon monoxide, methane, natural gas, primary reform gas and mIxtures thereof, and from about 2 to 6 moles of steam per mole of said gas in a second stage at a temperature of from 600* C. to 900* C. to form calcium oxide and a hydrogen-sulfide-containing gas stream, e. recovering said hydrogen-sulfide-containing gas stream and recycling said hydrogen sulfide stream for use in said first stage.

References Cited (Backward Citations)

US616391A Cited
US1678630A Cited
GB643479A Cited
GB694036A Cited
US2740691A Cited
US3129063A Cited
US2893839A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-09-20 1975-03-22 1975-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-09-20 1979-03-22 1979-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-09-20 1983-03-22 1983-09-21 $7700.00 Window Closed / Lapsed

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