CA2050818A1 - Impregnation with black liquor prior to white liquor introduction - Google Patents
Impregnation with black liquor prior to white liquor introductionInfo
- Publication number
- CA2050818A1 CA2050818A1 CA002050818A CA2050818A CA2050818A1 CA 2050818 A1 CA2050818 A1 CA 2050818A1 CA 002050818 A CA002050818 A CA 002050818A CA 2050818 A CA2050818 A CA 2050818A CA 2050818 A1 CA2050818 A1 CA 2050818A1
- Authority
- CA
- Canada
- Prior art keywords
- liquor
- digester
- chips
- black liquor
- cooking
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/0021—Introduction of various effluents, e.g. waste waters, into the pulping, recovery and regeneration cycle (closed-cycle)
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/24—Continuous processes
Landscapes
- Inorganic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Paper (AREA)
- Alcoholic Beverages (AREA)
- Toys (AREA)
- Nitrogen Condensed Heterocyclic Rings (AREA)
- Bidet-Like Cleaning Device And Other Flush Toilet Accessories (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Soy Sauces And Products Related Thereto (AREA)
- Inks, Pencil-Leads, Or Crayons (AREA)
- Plural Heterocyclic Compounds (AREA)
- Reinforced Plastic Materials (AREA)
- Coloring (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Electroluminescent Light Sources (AREA)
Abstract
A method of continuously digesting comminuted cellulosic fibrous material (e.g. wood chips) is provided which simultaneously improves uniformity of the end product and has substantial energy economy.
The chips are slurried, e.g. with black liquor, and fed to the top of a vertical digester. In the digester the chips are soaked in and heated with black liquor withdrawn from near the bottom of the cooking zone, which black liquor is at cooking temperature. White liquor (kraft cooking liquor) introduced into the cooking zone is preheated by passing it in heat exchange relationship with a portion of the black liquor withdrawn from the digester, so that only a small amount of heat in the form of steam need be added to the white liquor to bring it to cooking temperature. At the top of the digester, a portion of the liquid in the slurry can be withdrawn through a screen, pressurized, and then introduced under pressure with a downward velocity component facilitating a zone of concurrent movement of the chips and liquor.
The chips are slurried, e.g. with black liquor, and fed to the top of a vertical digester. In the digester the chips are soaked in and heated with black liquor withdrawn from near the bottom of the cooking zone, which black liquor is at cooking temperature. White liquor (kraft cooking liquor) introduced into the cooking zone is preheated by passing it in heat exchange relationship with a portion of the black liquor withdrawn from the digester, so that only a small amount of heat in the form of steam need be added to the white liquor to bring it to cooking temperature. At the top of the digester, a portion of the liquid in the slurry can be withdrawn through a screen, pressurized, and then introduced under pressure with a downward velocity component facilitating a zone of concurrent movement of the chips and liquor.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US58579090A | 1990-09-20 | 1990-09-20 | |
US585,790 | 1990-09-20 |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2050818A1 true CA2050818A1 (en) | 1992-03-21 |
CA2050818C CA2050818C (en) | 2002-07-02 |
Family
ID=24342973
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002050818A Expired - Lifetime CA2050818C (en) | 1990-09-20 | 1991-09-06 | Impregnation with black liquor prior to white liquor introduction |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0477059B1 (en) |
JP (1) | JP3126763B2 (en) |
AT (1) | ATE125010T1 (en) |
BR (1) | BR9104005A (en) |
CA (1) | CA2050818C (en) |
DE (1) | DE69111165T2 (en) |
FI (1) | FI103589B1 (en) |
NO (1) | NO913628L (en) |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5536366A (en) * | 1993-05-04 | 1996-07-16 | Ahlstrom Machinery Inc. | Digester system for implementing low dissolved solids profiling |
AU704580B2 (en) * | 1993-05-04 | 1999-04-29 | Kamyr Inc. | Dissolved solids control in pulp protection |
US5489363A (en) * | 1993-05-04 | 1996-02-06 | Kamyr, Inc. | Pulping with low dissolved solids for improved pulp strength |
US5824187A (en) * | 1993-12-29 | 1998-10-20 | Kvaerner Pulping Ab | Method for the continuous cooking of pulp |
SE502039C2 (en) * | 1993-12-29 | 1995-07-24 | Kvaerner Pulping Tech | Methods and apparatus for continuous cooking of pulp |
AU2697295A (en) * | 1994-09-02 | 1996-03-27 | Kamyr Inc. | Continuous kraft cooking with black liquor pretreatment |
US5660686A (en) * | 1994-09-02 | 1997-08-26 | Ahlstrom Machinery Inc. | Cooking with spent liquor pretreatment of cellulose material |
SE9403978L (en) * | 1994-11-15 | 1995-11-06 | Kvaerner Pulping Tech | Black liquor impregnation in single boiler hydraulic boiler |
US5925216A (en) * | 1994-11-15 | 1999-07-20 | Kvaerner Pulping Ab | Method of continuous pulping in a digester with high black liquor usage in the impregnation stage |
US6248208B1 (en) | 1995-06-02 | 2001-06-19 | Andritz-Ahlstrom Inc. | Pretreatment of chips before cooking |
US5635026A (en) * | 1995-11-13 | 1997-06-03 | Ahlstrom Machinery Inc. | Cooking cellulose material with high alkali concentrations and/or high pH |
SE506458C2 (en) | 1996-02-09 | 1997-12-15 | Kvaerner Pulping Tech | Continuous boiling of cellulosic material with heat exchange between boiler extraction and circulating boiling liquid |
US6159336A (en) * | 1997-08-07 | 2000-12-12 | Kvaerner Pulping Ab | Method and device for the continuous cooking of pulp |
US20010032711A1 (en) * | 1998-10-26 | 2001-10-25 | C. Bertil Stromberg | Pulp cooking with particular alkali profiles |
SE518993E (en) * | 2002-01-24 | 2013-04-23 | Metso Paper Sweden Ab | Preparation of cellulose pulp by boiling with a boiling liquid containing evaporated black liquor |
SE527058C2 (en) * | 2004-02-09 | 2005-12-13 | Kvaerner Pulping Tech | Continuous cooking process with improved heat economy |
US7556713B2 (en) * | 2004-06-22 | 2009-07-07 | Andritz, Inc. | Method and system for feeding cellulose chips to a high pressure continuous cooking system |
SE0602675L (en) * | 2006-12-13 | 2007-09-18 | Metso Fiber Karlstad Ab | Method for energy efficient production of cellulose pulp in a continuous cookery |
FI20090079A (en) | 2009-03-05 | 2010-09-06 | Andritz Inc | Heat recovery from waste cooking liquor at a pulp mill digester |
FI20105613A (en) * | 2010-05-31 | 2011-12-01 | Chempolis Oy | Lignocellulosaprocess |
FI129440B (en) * | 2020-01-15 | 2022-02-28 | Chempolis Oy | Cooking equipment and method for treating biomass containing lignocellulose |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3303088A (en) * | 1963-04-19 | 1967-02-07 | Lummus Co | Continuous liquid-phase rapid pulping |
SE359331B (en) * | 1970-03-17 | 1973-08-27 | Kamyr Ab | |
KR0171423B1 (en) * | 1989-09-28 | 1999-05-01 | 더크 제이. 빈맨 | Substitution heating apparatus and method in continuous immersion |
-
1991
- 1991-09-03 EP EP91402350A patent/EP0477059B1/en not_active Expired - Lifetime
- 1991-09-03 DE DE69111165T patent/DE69111165T2/en not_active Expired - Fee Related
- 1991-09-03 AT AT91402350T patent/ATE125010T1/en not_active IP Right Cessation
- 1991-09-06 CA CA002050818A patent/CA2050818C/en not_active Expired - Lifetime
- 1991-09-13 NO NO91913628A patent/NO913628L/en unknown
- 1991-09-18 BR BR919104005A patent/BR9104005A/en not_active IP Right Cessation
- 1991-09-18 FI FI914378A patent/FI103589B1/en not_active IP Right Cessation
- 1991-09-20 JP JP03241805A patent/JP3126763B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH05132882A (en) | 1993-05-28 |
FI914378A0 (en) | 1991-09-18 |
NO913628L (en) | 1992-03-23 |
EP0477059A3 (en) | 1993-06-23 |
JP3126763B2 (en) | 2001-01-22 |
DE69111165T2 (en) | 1995-11-16 |
FI103589B (en) | 1999-07-30 |
ATE125010T1 (en) | 1995-07-15 |
EP0477059B1 (en) | 1995-07-12 |
DE69111165D1 (en) | 1995-08-17 |
NO913628D0 (en) | 1991-09-13 |
EP0477059A2 (en) | 1992-03-25 |
BR9104005A (en) | 1992-05-26 |
FI103589B1 (en) | 1999-07-30 |
FI914378A (en) | 1992-03-21 |
CA2050818C (en) | 2002-07-02 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |