US5201172A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for treating black liquor
Assignee: Andritz Oy
•
Filing: 1991-11-05
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Granted: 1993-04-13
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Expires: 2011-11-05
Abstract
Abstract A method and apparatus for recovering black liquor chemicals and heat in a sulphate pulp process. The black liquor is concentrated in an evaporation plant, which includes a pressure heating reactor, after which the black liquor is gasified or combusted in a reactor for producing hot gases. The hot gases formed in the reactor are introduced into gas turbine power plant. The exhaust gases from the gas turbine are introduced into a waste heat boiler, where steam is generated for a steam turbine power plant. Secondary steam is led from the pressure heating reactor as injection steam into the gas turbine, to control inlet temperature.
Inventors
- 👤 Bertel K. Hakulin
- 👤 Erkki J. Kiiskila
- 👤 Marjo Kuusio
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 17:46
CPC Classifications
F; F01; F01K; F01K23/00; F01K23/02; F01K23/06; F01K23/067; D; D21; D21C; D21C11/00; D21C11/06; D21C11/10; D21C11/103; D21C11/12; Y; Y02; Y02E; Y02E20/00; Y02E20/12; Y02E20/16; Y02E20/18; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
191 words
A method of treating black liquor from a sulphate pulp process, for recovering chemicals and heat therefrom, utilizing a gas turbine having vanes and preceded by a combustor, a waste heat boiler, and a steam turbine power plant, comprising the steps of: (a) evaporating black liquor from a sulphate pulp process to produce a concentrated black liquor having a higher dry solids content; (b) gasifying and/or combusting the concentrated black liquor to produce hot gases and molten and/or solid salts; (c) recovering sulphate cooking chemicals from the molten and/or solid salts; (d) purifying the hot gases; (e) introducing purified hot gases into the combustor for the gas turbine, and then into the gas turbine, in order to recover energy from the hot gases, the gas turbine producing exhaust gases; (f) introducing the exhaust gases into the waste heat boiler to effect generation of steam; (g) recovering energy from the waste heat boiler steam in the steam turbine power plant; (h) pressurizing secondary steam from the sulphate pulp process; and (i) introducing the pressurized secondary steam as injection steam prior to the gas turbine vanes, to regulate the gas turbine inlet temperature.
Claim 2
Independent Claim
191 words
A method of treating black liquor from a sulphate pulp process, for recovering chemicals and heat therefrom, utilizing a gas turbine having vanes and preceded by a combustor, a waste heat boiler, and a steam turbine power plant, comprising the steps of: (a) evaporating black liquor from a sulphate pulp process to produce a concentrated black liquor having a higher dry solids content; (b) gasifying and/or combusting the concentrated black liquor to produce hot gases and molten and/or solid salts; (c) recovering sulphate cooking chemicals from the molten and/or solid salts; (d) purifying the hot gases; (e) introducing purified hot gases into the combustor for the gas turbine, and then into the gas turbine, in order to recover energy from the hot gases, the gas turbine producing exhaust gases; (f) introducing the exhaust gases into the waste heat boiler to effect generation of steam; (g) recovering energy from the waste heat boiler steam in the steam turbine power plant; (h) pressurizing secondary steam from the sulphate pulp process; and (i) introducing the pressurized secondary steam as injection steam prior to the gas turbine vanes, to regulate the gas turbine inlet temperature.
Claim 3
Dependent Claim
28 words
A method as recited in claim 1 comprising the further step of purifying the secondary steam from the sulphate pulp process prior to the practice of step (i).
Claim 4
Dependent Claim
28 words
A method as recited in claim 1 wherein the secondary steam from the sulphate pulp process is obtained by pressure heating the black liquor prior to step (a).
Claim 5
Dependent Claim
30 words
A method as recited in claim 3 wherein said step of pressure heating the black liquor is practiced by passing the black liquor into heat exchanging contact with hot steam.
Claim 6
Dependent Claim
44 words
A method as recited in claim 4 wherein said step of pressure heating the black liquor by passing it in heat exchanging contact with hot steam is practiced by supplying reheat steam from the steam turbine power plant into contact with the black liquor.
Claim 7
Dependent Claim
22 words
A method as recited in claim 3 wherein said pressure heating step is practiced at a temperature of between about 180°-200° C.
Claim 8
Dependent Claim
29 words
A method as recited in claim 1 wherein step (i) is practiced by introducing the secondary steam into the gas turbine combustor into contact with the purified hot gases.
Claim 9
Dependent Claim
40 words
A method as recited in claim 1 comprising the further steps of utilizing the gas turbine to compress air, and introducing the air compressed thereby into the combustor, and utilizing the air compressed thereby in the practice of step (b).
Claim 10
Dependent Claim
27 words
A method as recited in claim 2 wherein said step of purifying the secondary steam is accomplished by removing sulfur and alkali compounds from the secondary steam.
Claim 11
Dependent Claim
34 words
A method as recited in claim 2 wherein step (d) and said step of purifying the secondary steam are practiced by passing the hot gases and secondary steam into contact with separate absorption devices.
Claim 12
Dependent Claim
36 words
A method as recited in claim 10 comprising the further step of providing the same absorption mass for the separate absorption devices so as to minimize costs and facilitate ease of regeneration of the absorption mass.
Claim 13
Dependent Claim
17 words
A method as recited in claim 1 wherein the secondary steam is provided from the cooking plant.
Claim 14
Independent Claim
194 words
A method of treating black liquor from a sulphate pulp process, for recovering chemicals and heat therefrom, utilizing a gas turbine having vanes and preceded by a combustor, a waste heat boiler, and a steam turbine power plant, comprising the steps of: (a) evaporating black liquor from a sulphate pulp process to produce a concentrated black liquor having a higher dry solids content; (b) gasifying and/or combusting the concentrated black liquor to produce hot gases and molten and/or solid salts; (c) recovering sulphate cooking chemicals from the molten and/or solid salts; (d) purifying the hot gases; (e) introducing purified hot gases into the combustor for the gas turbine, and then into the gas turbine, in order to recover energy from the hot gases, the gas turbine producing exhaust gases; (f) introducing the exhaust gases into the waste heat boiler to effect generation of steam; (g) recovering energy from the waste heat boiler steam in the steam turbine power plant; (h) purifying secondary steam from the sulphate pulp process; and (i) introducing the purified secondary steam as injection steam in the combustor prior to the gas turbine vanes, to regulate the gas turbine inlet temperature.
Claim 15
Independent Claim
194 words
A method of treating black liquor from a sulphate pulp process, for recovering chemicals and heat therefrom, utilizing a gas turbine having vanes and preceded by a combustor, a waste heat boiler, and a steam turbine power plant, comprising the steps of: (a) evaporating black liquor from a sulphate pulp process to produce a concentrated black liquor having a higher dry solids content; (b) gasifying and/or combusting the concentrated black liquor to produce hot gases and molten and/or solid salts; (c) recovering sulphate cooking chemicals from the molten and/or solid salts; (d) purifying the hot gases; (e) introducing purified hot gases into the combustor for the gas turbine, and then into the gas turbine, in order to recover energy from the hot gases, the gas turbine producing exhaust gases; (f) introducing the exhaust gases into the waste heat boiler to effect generation of steam; (g) recovering energy from the waste heat boiler steam in the steam turbine power plant; (h) purifying secondary steam from the sulphate pulp process; and (i) introducing the purified secondary steam as injection steam in the combustor prior to the gas turbine vanes, to regulate the gas turbine inlet temperature.
Claim 16
Dependent Claim
28 words
A method as recited in claim 13 wherein the secondary steam from the sulphate pulp process is obtained by pressure heating the black liquor prior to step (a).
Claim 17
Dependent Claim
30 words
A method as recited in claim 14 wherein said step of pressure heating the black liquor is practiced by passing the black liquor into heat exchanging contact with hot steam.
Claim 18
Dependent Claim
44 words
A method as recited in claim 15 wherein said step of pressure heating the black liquor by passing it in heat exchanging contact with hot steam is practiced by supplying reheat steam from the stem turbine power plant into contact with the black liquor.
Claim 19
Dependent Claim
29 words
A method as recited in claim 13 wherein step (i) is practiced by introducing the secondary steam into the gas turbine combustor into contact with the purified hot gases.
Claim 20
Dependent Claim
40 words
A method as recited in claim 13 comprising the further steps of utilizing the gas turbine to compress air, and introducing the air compressed thereby into the combustor, and utilizing the air compressed thereby in the practice of step (b).
Claim 21
Dependent Claim
28 words
A method as recited in claim 13 comprising the further step of purifying the secondary steam from the sulphate pulp process prior to the practice of step (i).
Claim 22
Dependent Claim
27 words
A method as recited in claim 14 wherein said step of purifying the secondary steam is accomplished by removing sulfur and alkali compounds from the secondary steam.
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) | 1996-04-12 | 1996-10-12 | 1997-04-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-04-12 | 2000-10-12 | 2001-04-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-04-12 | 2004-10-12 | 2005-04-13 | $7700.00 | Window Closed / Lapsed |