US4067767A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Liquid phase coking of spent kraft pulping liquors
Assignee: Texaco Inc
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Filing: 1974-01-08
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Granted: 1978-01-10
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Expires: 1994-01-08
Abstract
Abstract An improved process for treating spent Kraft wood pulping liquors by coking the liquors after reducing the pH thereof with SO2 and recovering the sulfur contained in the resulting coke by contact with hydrogen preheated to temperatures in the range of 750 DEG to 2000 DEG F to produce H2S. The H2S and lime are added to the coker effluent to form new kraft cooking liquor.
Inventors
- 👤 Howard Vincent Hess
- 👤 William Francis Franz
- 👤 Edward Lawrence Cole
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 16:44
CPC Classifications
D; D21; D21C; D21C11/00; D21C11/12; D21C11/125; C; C10; C10B; C10B53/00; C10B53/02; C10L; C10L9/00; C10L9/02; C10L9/04; Y; Y02; Y02E; Y02E50/00; Y02E50/10
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
153 words
In a proceess for treating spent alkaline Kraft pulping liquors, the steps of flowing said liquor to an absorbing zone and adding SO 2 to said liquors in said zone to lower the pH thereof to below 7; coking said liquors in the liquid phase under autogenous pressure of about 1000 to about 3000 psi at 450° F to 700° F for 0.5 minutes to 6 hours in a coking zone thereby forming coke, gases, and an aqueous effluent; separating in a separating zone said coke from said effluent; burning said gas to produce said sulfur dioxide; drying said coke with flue gas; the improvement comprising preheating hydrogen to 700° to 2000° F. passing said hydrogen over said coke to reduce the sulfur content of said coke and produce H 2 S and adding lime and said H 2 S to said effluent in an absorbing zone to form new Kraft cooking liquor.
Claim 2
Dependent Claim
153 words
In a proceess for treating spent alkaline Kraft pulping liquors, the steps of flowing said liquor to an absorbing zone and adding SO 2 to said liquors in said zone to lower the pH thereof to below 7; coking said liquors in the liquid phase under autogenous pressure of about 1000 to about 3000 psi at 450° F to 700° F for 0.5 minutes to 6 hours in a coking zone thereby forming coke, gases, and an aqueous effluent; separating in a separating zone said coke from said effluent; burning said gas to produce said sulfur dioxide; drying said coke with flue gas; the improvement comprising preheating hydrogen to 700° to 2000° F. passing said hydrogen over said coke to reduce the sulfur content of said coke and produce H 2 S and adding lime and said H 2 S to said effluent in an absorbing zone to form new Kraft cooking liquor.
Claim 3
Dependent Claim
22 words
The process according to claim 1 wherein the pH of the liquor is brought down to between 2 and 5 before coking.
Claim 4
Dependent Claim
18 words
The process according to claim 1 wherein said hydrogen is preheated by passage over said hot desulfurized coke.
Claim 5
Dependent Claim
15 words
The process of claim 1 wherein said hydrogen is heated to 1000° to 1500° F.
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) | 1981-01-09 | 1981-07-11 | 1982-01-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-09 | 1985-07-11 | 1986-01-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-09 | 1989-07-11 | 1990-01-10 | $7700.00 | Window Closed / Lapsed |