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US3966633A Expired / Lapsed US ⏱️ 0.0 years remaining

Waste water processing

Assignee: Cogas Development Co
•
Filing: 1974-09-23
•
Granted: 1976-06-29
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Expires: 1994-09-23
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Abstract

Abstract Waste water formed in the gasification of coal and containing ammonia, H 2 S, and phenolic compounds is treated to remove H 2 S and a substantial proportion of its ammonia, while leaving sufficient ammonia in the water to maintain a pH of at least 8 (such as up to about 10.5, preferably about 8.5 to 9), the ammoniacal water is then flashed into a stream of superheated steam being fed to gasification zone. At the high temperatures in the gasification zone the organic impurities are decomposed.

Inventors

  • 👤 Louis D. Friedman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 15:52
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/54; C01; C01B; C01B17/00; C01B17/16; C01B17/167; C01B3/00; C01B3/02; C01B3/22; C01B3/24; C01B3/28; C01C; C01C1/00; C01C1/02; C01C1/10; C10J3/48; C10J3/482; C10J3/58; C10J3/60; C10J3/62; C10K; C10K1/00; C10K1/002; C10K1/003; C10K1/004; C10K1/005; C10K1/08; C10K1/10; C10K1/101; C10K1/12; C10K1/122; C10K1/14; C10K1/143; C10K1/16; C10K3/00; C10K3/02; C10K3/04; C10G; C10G2300/00; C10G2300/10; C10G2300/1003; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0943; C10J2300/12; C10J2300/1215; C10J2300/16; C10J2300/1603; C10J2300/1615; C10J2300/164; C10J2300/1656; C10J2300/1662; C10J2300/169; C10J2300/1696

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 135 words
In a system of synthesis gas manufacture including a gasifier wherein fluidized char is reacted with steam using a particulate heat exchange material to sustain the endothermic steam-carbon reaction to produce a synthesis gas stream which on cooling gives water contaminated with H 2 S and NH 3 and a carbonizer wherein fluidized coal is carbonized below about 700°C to provide said char and vapors which on cooling give oil and water contaminated with H 2 S and NH 3 and organic materials, the improvement which comprises steam-stripping the contaminated waters to remove the H 2 S but retaining sufficient ammonia to keep the pH between about 8.5 to 10.5 and introducing the resulting treated water into the gasifier to provide at least a portion of the steam requirement therefor while consuming the organic materials.
Claim 2
Dependent Claim 135 words
In a system of synthesis gas manufacture including a gasifier wherein fluidized char is reacted with steam using a particulate heat exchange material to sustain the endothermic steam-carbon reaction to produce a synthesis gas stream which on cooling gives water contaminated with H 2 S and NH 3 and a carbonizer wherein fluidized coal is carbonized below about 700°C to provide said char and vapors which on cooling give oil and water contaminated with H 2 S and NH 3 and organic materials, the improvement which comprises steam-stripping the contaminated waters to remove the H 2 S but retaining sufficient ammonia to keep the pH between about 8.5 to 10.5 and introducing the resulting treated water into the gasifier to provide at least a portion of the steam requirement therefor while consuming the organic materials.
Claim 3
Dependent Claim 99 words
Process as in claim 1 in which said H 2 S is stripped off at a pressure of about 75 to 125 psig, said ammonia is stripped off at a pressure of about 175 to 230 psig, the ammoniacal water remaining after said ammonia stripping has a pH of about 8.5 to 10.5 and a temperature of at least about 200°C, said stream of superheated steam has a temperature of about 300° to 600°C and a pressure of about 150 to 550 psig, and substantially all of the resulting stream of steam is fed into the gasification zone directly.

References Cited (Backward Citations)

US3375175A Cited
US3540867A Cited
US3505204A Cited
US3752771A Cited
US3759837A Cited
US3850839A Cited
US3725270A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-29 1979-12-29 1980-06-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-29 1983-12-29 1984-06-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-29 1987-12-29 1988-06-29 $7700.00 Window Closed / Lapsed

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