SE0300089D0 - Continuous pulping processes and systems - Google Patents
Continuous pulping processes and systemsInfo
- Publication number
- SE0300089D0 SE0300089D0 SE0300089A SE0300089A SE0300089D0 SE 0300089 D0 SE0300089 D0 SE 0300089D0 SE 0300089 A SE0300089 A SE 0300089A SE 0300089 A SE0300089 A SE 0300089A SE 0300089 D0 SE0300089 D0 SE 0300089D0
- Authority
- SE
- Sweden
- Prior art keywords
- screen
- liquor
- digester
- screen assembly
- extracted
- Prior art date
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
- D21C7/00—Digesters
-
- 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
- D21C7/00—Digesters
- D21C7/08—Discharge devices
-
- 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
- D21C7/00—Digesters
- D21C7/14—Means for circulating the lye
Abstract
A set of spaced apart screen assemblies are provided within a continuous kraft digester. Liquor is extracted from a first screen assembly of the set without recirculation of at least a portion of the extracted liquor into the digester above the first screen. In such a manner, the need for circulation flow below the first screen assembly of the set to the second screen assembly of the set is minimized, thereby also minimizing (if not eliminating entirely) the packing problems such flow may cause. The liquor extracted from the first screen assembly in the set could be reintroduced, however, into the digester at some other location in the cooking system (e.g., at a location just above the bottom screen). By employing the present invention, the distance between the first and second screen assemblies is greater than one digester diameter (D). In addition, the liquor discharge below the first screen assembly, to which the circulated liquor from the second screen assembly (plus added dilution liquor and heat, if desired) may be at a distance of less than one-half (½) of a digester diameter (D) below the first screen. A small upflow can thus be used to displace the liquor at the first screen assembly, with a relatively short upflow zone. Multiple sets of such first and second screen assemblies may also be provided within the digester along with other conventional screen assemblies to effect desired internal liquor flows.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US34836702P | 2002-01-16 | 2002-01-16 | |
US10/304,096 US20030131956A1 (en) | 2002-01-16 | 2002-11-26 | Continuous pulping processes and systems |
Publications (2)
Publication Number | Publication Date |
---|---|
SE0300089D0 true SE0300089D0 (en) | 2003-01-16 |
SE0300089L SE0300089L (en) | 2003-07-17 |
Family
ID=26973808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE0300089A SE0300089L (en) | 2002-01-16 | 2003-01-16 | Continuous pulp preparation processes and systems |
Country Status (5)
Country | Link |
---|---|
US (1) | US20030131956A1 (en) |
JP (1) | JP2003213581A (en) |
CA (1) | CA2414070A1 (en) |
FI (1) | FI20030043A (en) |
SE (1) | SE0300089L (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7828930B2 (en) * | 2007-11-20 | 2010-11-09 | International Paper Company | Use of polysulfide in modified cooking |
SE531632C2 (en) * | 2007-12-20 | 2009-06-09 | Metso Fiber Karlstad Ab | Process of manufacture of sulphate pulp in which hemicelluloses are recycled |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5824188A (en) * | 1993-05-04 | 1998-10-20 | Ahlstrom Machinery Inc. | Method of controlling the pressure of a continuous digester using an extraction-dilution |
US6132556A (en) * | 1993-05-04 | 2000-10-17 | Andritz-Ahlstrom Inc. | Method of controlling pulp digester pressure via liquor extraction |
US5536366A (en) * | 1993-05-04 | 1996-07-16 | Ahlstrom Machinery Inc. | Digester system for implementing low dissolved solids profiling |
US5575890A (en) * | 1993-05-04 | 1996-11-19 | Kamyr, Inc. | Method for selectively increasing the sulfide ion concentration and sulfidity of kraft cooking liquor during kraft cooking of wood |
US5489363A (en) * | 1993-05-04 | 1996-02-06 | Kamyr, Inc. | Pulping with low dissolved solids for improved pulp strength |
SE502510C2 (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 |
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 |
US5958181A (en) * | 1997-08-07 | 1999-09-28 | Ahlstrom Machinery, Inc. | Continuous cooking with a two-stage cool impregnation |
US6123808A (en) * | 1997-12-09 | 2000-09-26 | Ahlstrom Machinery Inc. | Distribution of dilution liquor to the discharge of a cellulose pulp digester |
US6277240B1 (en) * | 1998-10-02 | 2001-08-21 | Andritz-Ahlstrom Inc. | Method for continuously pulping cellulosic fibrous material |
CA2318027C (en) * | 1999-09-13 | 2008-07-08 | Andritz-Ahlstrom Inc. | Treating pulp with yield or strength-enhancing additive |
SE0004049L (en) * | 2000-11-03 | 2001-11-05 | Kvaerner Pulping Tech | Continuous boiling of pulp less used cooking liquor partly from the digester and partly from a subsequent pressure diffuser |
-
2002
- 2002-11-26 US US10/304,096 patent/US20030131956A1/en not_active Abandoned
- 2002-12-12 CA CA002414070A patent/CA2414070A1/en not_active Abandoned
-
2003
- 2003-01-08 JP JP2003002026A patent/JP2003213581A/en not_active Withdrawn
- 2003-01-13 FI FI20030043A patent/FI20030043A/en unknown
- 2003-01-16 SE SE0300089A patent/SE0300089L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
SE0300089L (en) | 2003-07-17 |
FI20030043A (en) | 2003-07-17 |
US20030131956A1 (en) | 2003-07-17 |
FI20030043A0 (en) | 2003-01-13 |
JP2003213581A (en) | 2003-07-30 |
CA2414070A1 (en) | 2003-07-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
NAV | Patent application has lapsed |