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US4503018A Expired / Lapsed US ⏱️ 0.0 years remaining

Desulfurization of phosphogypsum

Assignee: Davy McKee Corp
•
Filing: 1983-02-14
•
Granted: 1985-03-05
•
Expires: 2003-02-14
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Abstract

Abstract Phosphogypsum is mixed with fine coal, balled, and charged to a travelling grate where the charge is heated under reducing conditions to evolve sulfur and/or sulfur dioxide for conversion into sulfuric acid.

Inventors

  • 👤 Samuel A. Gardner
  • 👤 Thomas E. Ban

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 15:57
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/06; C01B17/48; C01B17/50; C01B17/52; C01F; C01F11/00; C01F11/02; C01F11/08

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 104 words
A process for producing sulfur and/or sulfur dioxide from gypsum comprising the steps of: forming a mixture of fine carbon material and fine gypsum material, balling the mixture to form pellets, charging the pellets to a travelling grate, moving the travelling grate to carry the charge of pellets successively through firing and post firing zones, heating the charge on the grate in the firing zone under non-oxidizing conditions to produce a gaseous effluent containing sulfur dioxide or sulfur or both sulfur and sulfur dioxide, and passing a portion of the gaseous effluent from the firing zone through the charge in the post firing zone.
Claim 2
Dependent Claim 104 words
A process for producing sulfur and/or sulfur dioxide from gypsum comprising the steps of: forming a mixture of fine carbon material and fine gypsum material, balling the mixture to form pellets, charging the pellets to a travelling grate, moving the travelling grate to carry the charge of pellets successively through firing and post firing zones, heating the charge on the grate in the firing zone under non-oxidizing conditions to produce a gaseous effluent containing sulfur dioxide or sulfur or both sulfur and sulfur dioxide, and passing a portion of the gaseous effluent from the firing zone through the charge in the post firing zone.
Claim 3
Dependent Claim 17 words
A process as claimed in claim 1 wherein the carbon material is coal, coke or petroleum coke.
Claim 4
Dependent Claim 38 words
A process as claimed in claim 1 wherein the fixed carbon material and gypsum material are mixed in a ratio to produce a ratio of gypsum to fixed carbon of about 92-97% gypsum to about 8-3% fixed carbon.
Claim 5
Dependent Claim 20 words
A process as claimed in claim 1 wherein the heating is in the range from 980° C. to 1200° C.
Claim 6
Dependent Claim 13 words
A process as claimed in claim 1 wherein the gypsum material is phosphogypsum.
Claim 7
Dependent Claim 106 words
A process as claimed in claim 1 wherein the forming of the mixture of fine carbon material and fine gypsum includes forming a moist mixture; the moving of the travelling grate includes carrying the charge of pellets successively through predrying and drying zones prior to the firing zone and carrying the charge through a cooling zone after the post firing zone; and there is further included the steps of subjecting the charge in the predrying zone to air heated by heat exchange from the gaseous effluent, and subjecting the charge in the drying zone to air heated by passing through the charge in the cooling zone.
Claim 8
Dependent Claim 54 words
A process as claimed in claim 1 wherein the portion of gaseous effluent passed through the charge in the post firing zone is combined with the gaseous effluent from the firing zone, and the portion of gaseous effluent being passed through the charge in the post firing zone is taken from the combined effluent.
Claim 9
Dependent Claim 107 words
A process as claimed in claim 7 wherein the forming of the mixture of fine carbon material and fine gypsum includes forming a moist mixture; the moving of the travelling grate includes carrying the charge of pellets successively through the predrying and drying zones prior to the firing zone and carrying the charge through a cooling zone after the post firing zone; and there is further included the steps of subjecting the charge in the predrying zone to air heated by heat exchange from the gaseous effluent, and subjecting the charge in the drying zone to air heated by passing through the charge in the cooling zone.
Claim 10
Dependent Claim 181 words
A process for producing sulfur and/or sulfur dioxide from phosphogypsum comprising the steps of forming a mixture of fine high-sulfur content coal and fine phosphogypsum so that the mixture includes at least about 3 to 8 parts by weight fixed carbon content for every 92 to 97 parts by weight gypsum content, balling the mixture to form pellets having a diameter of about 13 mm, charging the pellets to a circular travelling grate to form a layer of pellets on the grate, moving the grate and layer of pellets successively through drying, firing, post firing and cooling zones in a sealed hood arrangement, burning high sulfur content fuel in a fixed bed gas producer to produce a hot raw low BTU gas, feeding the hot gas to the firing zone to heat the pellets to about 1200° C. to produce a product gas containing sulfur or sulfur dioxide or both sulfur and sulfur dioxide from the pellets, removing the product gas from the firing zone, and passing a portion of the product gas through the charge in the post firing zone.
Claim 11
Dependent Claim 181 words
A process for producing sulfur and/or sulfur dioxide from phosphogypsum comprising the steps of forming a mixture of fine high-sulfur content coal and fine phosphogypsum so that the mixture includes at least about 3 to 8 parts by weight fixed carbon content for every 92 to 97 parts by weight gypsum content, balling the mixture to form pellets having a diameter of about 13 mm, charging the pellets to a circular travelling grate to form a layer of pellets on the grate, moving the grate and layer of pellets successively through drying, firing, post firing and cooling zones in a sealed hood arrangement, burning high sulfur content fuel in a fixed bed gas producer to produce a hot raw low BTU gas, feeding the hot gas to the firing zone to heat the pellets to about 1200° C. to produce a product gas containing sulfur or sulfur dioxide or both sulfur and sulfur dioxide from the pellets, removing the product gas from the firing zone, and passing a portion of the product gas through the charge in the post firing zone.
Claim 12
Dependent Claim 46 words
A process as claimed in claim 9 wherein the mixture includes an excess amount of carbon above the stoichiometric amount of carbon for reacting with the gypsum, the heating of the pellets produces combustibles in the effluent, and the combustibles are then burned in an incinerator.
Claim 13
Dependent Claim 46 words
A process as claimed in claim 10 wherein a portion of the hot raw low BTU gas is fed to an incinerator to which the product gas is fed along with stoichiometric amounts of oxygen containing gas to burn any residual combustibles in the product gas.
Claim 14
Dependent Claim 91 words
A process as claimed in claim 9 wherein the forming of the mixture of fine carbon material and fine phosphogypsum includes forming a moist mixture; the moving of the travelling grate includes carrying the charge of pellets through a predrying zone prior to the drying zone; and there is further included the steps of subjecting the charge in the predrying zone to air heated by heat exchange from the product gas, and subjecting the charge in the drying zone to air heated by passing through the charge in the cooling zone.
Claim 15
Dependent Claim 54 words
A process as claimed in claim 9 wherein the portion of product gas passed through the charge in the post firing zone is combined with the product gas from the firing zone, and the portion of product gas being passed through the charge in the post firing zone is taken from the combined gas.
Claim 16
Dependent Claim 91 words
A process as claimed in claim 13 wherein the forming of the mixture of fine carbon material and fine phosphogypsum includes forming a moist mixture; the moving of the travelling grate includes carrying the charge of pellets through a predrying zone prior to the drying zone; and there is further included the steps of subjecting the charge in the predrying zone to air heated by heat exchange from the product gas, and subjecting the charge in the drying zone to air heated by passing through the charge in the cooling zone.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-03-04 1988-09-03 1989-03-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-03-04 1992-09-03 1993-03-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-03-04 1996-09-03 1997-03-05 $7700.00 Window Closed / Lapsed

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