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US3717545A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for treating waste liquors

Assignee: Texaco Inc
•
Filing: 1970-07-17
•
Granted: 1973-02-20
•
Expires: 1990-07-17
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Abstract

Abstract Closed circuit process for treating waste liquors, such as spent sulfite liquors from wood digestion by coking the liquors in the liquid phase under pressure under turbulent flow conditions to form coke and a clear effluent of low chemical oxygen demand. In the process, a heat exchange zone, a coking zone, a steam-and flue gas-producing zone, an absorbing zone, a wood digesting zone and a kilning zone are provided and interconnected by suitable conduits. Pressurized spent liquor is sent to the heat exchange zone where it absorbs heat from the coking zone effluent before coke separation, thereby absorbing also heat content contained in the coke. The coke is discharged to the kilning zone where it is dried by hot flue gases produced by burning previously dried coke in the steam producing zone. Sulfur dioxide containing warm, flue gas from the kilning zone is contacted in an absorbing zone with cool coker effluent to produce warm ammonium bisulfite solution which is passed to a wood digestion zone as well as cool flue gas substantially free of all air pollutants. Sulfur-containing gases produced by coking and wood digestion are burned in the steamproducing zone to manufacture sulfur dioxide for recycling. Use of a closed system reduces to a minimum odors in the digestion section of a pulp plant since all the odorous sulfur compounds are burned and the sulfur dioxide is recovered.

Inventors

  • 👤 H Hess
  • 👤 E Cole

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 21:06
CPC Classifications
D; D21; D21C; D21C11/00; D21C11/02; Y; Y10; Y10S; Y10S210/00; Y10S210/928

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 137 words
Process for the treatment of a spent wood pulping liquor comprising coking same in a tubular coking zone under turbulent flow conditions characterized by a Reynolds number greater than 4000 for about 0.5 to 10 minutes at about 550*F to 650*F in the liquid phase to produce an effluent consisting of particulate coke suspended in water; bringing said effluent including said coke in heat exchange relationship with said liquor whereby the heat content of both said coke and said water is transferred to said liquor, then separating said coke from said resulting cooled effluent, drying said coke with hot flue gas containing SO2, burning said dried coke to produce process steam and SO2-rich flue gas, contacting said flue gas with said cooled effluent to recover SO2 therefrom, thereby forming additional pulping liquor and clean cool flue gas.
Claim 2
Dependent Claim 137 words
Process for the treatment of a spent wood pulping liquor comprising coking same in a tubular coking zone under turbulent flow conditions characterized by a Reynolds number greater than 4000 for about 0.5 to 10 minutes at about 550*F to 650*F in the liquid phase to produce an effluent consisting of particulate coke suspended in water; bringing said effluent including said coke in heat exchange relationship with said liquor whereby the heat content of both said coke and said water is transferred to said liquor, then separating said coke from said resulting cooled effluent, drying said coke with hot flue gas containing SO2, burning said dried coke to produce process steam and SO2-rich flue gas, contacting said flue gas with said cooled effluent to recover SO2 therefrom, thereby forming additional pulping liquor and clean cool flue gas.
Claim 3
Dependent Claim 38 words
Process as defined in claim 1 wherein said additional pulping liquor is passed on to a pulping area where wood pulp and sulfur-containing gases are produced, said gases being burned with said coke to produce additional flue gas.
Claim 4
Dependent Claim 13 words
Process as defined in claim 1, wherein said liquor is spent sulfite liquor.
Claim 5
Dependent Claim 41 words
Process as defined in claim 1, wherein said coke, upon being separated from said cooled effluent is discharged to a kilning zone for drying by hot flue gases produced by burning previously dried coke, thereby also cooling said hot flue gases.
Claim 6
Dependent Claim 22 words
Process as defined in claim 1, wherein said effluent is de-pressurized to about atmospheric pressure before being heat exchanged with said liquor.
Claim 7
Dependent Claim 19 words
Process as defined in claim 1 wherein pulping chemicals are added to said additional pulping liquor to fortify same.

References Cited (Backward Citations)

US3183145A Cited
US3331732A Cited
US3558426A Cited
US3591449A Cited
US3595742A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-02-20 1976-08-21 1977-02-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-02-20 1980-08-21 1981-02-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-02-20 1984-08-21 1985-02-20 $7700.00 Window Closed / Lapsed

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