Patent US5327580A successfully refreshed from Google Patents.
US4872950A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for recovering energy and chemicals from spent liquor in pulp preparation
Assignee: GENERAL PROCESS AA A JOINT-STOCK Co OF SWEDEN AB
•
Filing: 1987-11-17
•
Granted: 1989-10-10
•
Expires: 2007-11-17
Abstract
Abstract Eenrgy and process chemicals are recovered from spent liquor in pulp preparation by thermally decomposing the spent liquor to solid and gaseous products at an elevated pressure and with addition of oxygen. The supply of oxygen should be less than that stoichiometrically required for a complete combustion and the temperature at the decomposition should be below the temperature at which a melt is formed. After recovery of sulfur-containing compounds the gas formed can give off energy in a gas turbine, thereafter generate steam and finally be used for drying fuel which is subsequently gasified under pressure and provides a further contribution of energy in the form of a combustible gas. Process chemicals are recovered from the solid products in known manner.
Inventors
- 👤 Alf O. Andersson
- 👤 Bjorn S. Warnqvist
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:00
CPC Classifications
D; D21; D21C; D21C11/00; D21C11/12; D21C11/125; D21C11/04; D21C11/06; D21C11/063; D21C11/066; D21C11/08; Y; Y02; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
140 words
A process for recovering energy and chemicals from spent liquor containing organic materials in pulp preparation, said liquor being thermally decomposed after concentration, forming gaseous and solid products and energy being recovered from the gases, the process comprising: concentrating said spent liquor containing organic materials; and thermally decomposing said concentrated spent liquor, wherein said thermal decomposition is carried out in a single step at a supply of oxygen in an amount corresponding to from 5 to 75% of the stoichiometric amount required for a complete oxidation, at a pressure of from 10 to 50 bar and at a temperature of from 700° to 850° C. such that no melt is formed, wherein the formation of carbon from included organic materials is suppressed and wherein the thermal decomposition forms sulfur-containing gases which are recovered by being absorbed in an alkaline solution.
Claim 2
Dependent Claim
140 words
A process for recovering energy and chemicals from spent liquor containing organic materials in pulp preparation, said liquor being thermally decomposed after concentration, forming gaseous and solid products and energy being recovered from the gases, the process comprising: concentrating said spent liquor containing organic materials; and thermally decomposing said concentrated spent liquor, wherein said thermal decomposition is carried out in a single step at a supply of oxygen in an amount corresponding to from 5 to 75% of the stoichiometric amount required for a complete oxidation, at a pressure of from 10 to 50 bar and at a temperature of from 700° to 850° C. such that no melt is formed, wherein the formation of carbon from included organic materials is suppressed and wherein the thermal decomposition forms sulfur-containing gases which are recovered by being absorbed in an alkaline solution.
Claim 3
Dependent Claim
15 words
The process of claim 1, wherein the spent liquor originates from a sulfate pulping process.
Claim 4
Dependent Claim
44 words
The process of claim 1, further comprising the gases from the thermal decomposition are washed and then are made to perform work by being combusted in a gas turbine and subsequently said gases give off energy in a flue gas boiler which generates steam.
Claim 5
Dependent Claim
55 words
The process of claim 3, further comprising the exhaust gases from the flue gas boiler are used for drying and heating one or more fuels which are thereafter thermally decomposed with a supply of oxygen in a gas generator at a pressure above atmospheric to form combustible gases which are combined with the washed gases
Claim 6
Dependent Claim
34 words
The process of claim 4, further comprising the gas turbine drives a compressor compressing an oxygen-containing gas which is thereafter led to the thermal decomposition of the residual liquor and to the gas generator.
Claim 7
Dependent Claim
35 words
The process of claim 3, further comprising the steam from the flue gas boiler is heat exchanged against the gases from the thermal decomposition and is thereafter made to perform work in a steam turbine.
Claim 8
Dependent Claim
14 words
The process of claim 1, wherein said temperature is from 740° to 800° C.
Claim 9
Dependent Claim
14 words
The process of claim 1, wherein said pressure is from 15 to 25 bar.
Claim 10
Dependent Claim
32 words
The process of claim 1, wherein said oxygen is supplied in the thermal decomposition in an amount corresponding to from 30 to 50% of the stoichiometric amount required for a complete oxidation.
References Cited (Backward Citations)
US3183145A
Cited
US3920506A
Cited
US3873414A
Cited
US4111743A
Cited
US4299652A
Cited
US4522685A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-10-09 | 1993-04-10 | 1993-10-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-10-09 | 1997-04-10 | 1997-10-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-10-09 | 2001-04-10 | 2001-10-10 | $7700.00 | Window Closed / Lapsed |