Patent US4108677A successfully refreshed from Google Patents.
US4108677A
Expired / Lapsed
US
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Process for treating waste sludge from combustion plant desulfurization units and cementitious product of the process
Assignee: Individual
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Filing: 1976-11-24
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Granted: 1978-08-22
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Expires: 1996-11-24
Abstract
Abstract Aqueous alkaline desulfurization treating units for combustion gases generate as a product an aqueous sludge containing sulfur compounds of calcium. Many such sludge products contain more than 30 percent by weight (of the solids) of calcium sulfite hemihydrate. These waste products are in part calcined at a temperature from 250°C to 650°C to produce a moisture-free, cementitious product which is thereafter recombined with uncalcined aqueous sludge to produce a cementitious product which can be profitably utilized or which may be conveniently discarded as a landfill. If desired, fly ash or bottom ash produced in the combustion process can be combined with the cementitious product.
Inventors
- 👤 Richard E. Valiga
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 10:30
CPC Classifications
C; C04; C04B; C04B28/00; C04B28/14; C04B28/142; C04B28/144; C04B18/00; C04B18/04; C04B18/06; C04B18/062; C04B18/064; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/91
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
154 words
A method for hardening inorganic aqueous waste sludge which comprises as its non-aqueous ingredient calcium salts selected from the class consisting of calcium sulfate and calcium sulfite and wherein at least 30 percent by weight of the solids are calcium sulfite hemihydrate, including the steps of: (1) thickening the said sludge by removing at least a portion of the liquid content; (2) withdrawing a first portion of the thickened sludge, removing volatile liquids from the said first portion and calcining the residual solids from said first portion at 250° to 650° C to produce a dry, calcined intermediate product which comprises essentially dry, cementitious ingredients selected from the class consisting of calcium sulfate soluble anhydrite, calcium sulfate anhydrite and anhydrous calcium sulfite; (3) withdrawing a second portion of the thickened sludge, and (4) mixing the said partially dewatered sludge and at least a portion of the said intermediate product to produce a hardenable product.
Claim 2
Independent Claim
154 words
A method for hardening inorganic aqueous waste sludge which comprises as its non-aqueous ingredient calcium salts selected from the class consisting of calcium sulfate and calcium sulfite and wherein at least 30 percent by weight of the solids are calcium sulfite hemihydrate, including the steps of: (1) thickening the said sludge by removing at least a portion of the liquid content; (2) withdrawing a first portion of the thickened sludge, removing volatile liquids from the said first portion and calcining the residual solids from said first portion at 250° to 650° C to produce a dry, calcined intermediate product which comprises essentially dry, cementitious ingredients selected from the class consisting of calcium sulfate soluble anhydrite, calcium sulfate anhydrite and anhydrous calcium sulfite; (3) withdrawing a second portion of the thickened sludge, and (4) mixing the said partially dewatered sludge and at least a portion of the said intermediate product to produce a hardenable product.
Claim 3
Dependent Claim
38 words
The method of claim 1 wherein the said first portion constitutes 1 to 90 weight percent of the thickened sludge solids and the said second portion constitutes from 10 to 99 weight percent of the thickened sludge solids.
Claim 4
Dependent Claim
16 words
The method of claim 1 wherein inert particulate aggregates are added to the said hardenable sludge.
Claim 5
Dependent Claim
12 words
The method of claim 3 wherein the said aggregates comprise fly ash.
Claim 6
Dependent Claim
12 words
The method of claim 3 wherein the said aggregates comprise bottom ash.
Claim 7
Dependent Claim
10 words
A hardened solidified product of the process of claim 1.
Claim 8
Dependent Claim
33 words
The process of claim 1 wherein the said calcining step is at temperatures from 250° to 350° C and the said calcined intermediate product includes more anhydrous calcium sulfite than calcium sulfite hemihydrate.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-08-21 | 1982-02-20 | 1982-08-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-08-21 | 1986-02-20 | 1986-08-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-08-21 | 1990-02-20 | 1990-08-22 | $7700.00 | Window Closed / Lapsed |