BR9103650A - METHOD AND APPLIANCE FOR CONTINUOUSLY TRANSFORMING FRAGMENTED CELLULOSIC FRAGMENTED MATERIAL INTO KRAFT PULP - Google Patents
METHOD AND APPLIANCE FOR CONTINUOUSLY TRANSFORMING FRAGMENTED CELLULOSIC FRAGMENTED MATERIAL INTO KRAFT PULPInfo
- Publication number
- BR9103650A BR9103650A BR919103650A BR9103650A BR9103650A BR 9103650 A BR9103650 A BR 9103650A BR 919103650 A BR919103650 A BR 919103650A BR 9103650 A BR9103650 A BR 9103650A BR 9103650 A BR9103650 A BR 9103650A
- Authority
- BR
- Brazil
- Prior art keywords
- fragmented
- white liquor
- kraft
- digester
- cellulosic
- Prior art date
Links
- 239000002655 kraft paper Substances 0.000 title abstract 5
- 239000000463 material Substances 0.000 title abstract 2
- 230000001131 transforming effect Effects 0.000 title 1
- 229920001131 Pulp (paper) Polymers 0.000 abstract 1
- 238000010411 cooking Methods 0.000 abstract 1
- 239000002657 fibrous material Substances 0.000 abstract 1
- 238000004537 pulping Methods 0.000 abstract 1
- 239000002023 wood Substances 0.000 abstract 1
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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/147—Bleaching ; Apparatus therefor with oxygen or its allotropic modifications
-
- 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
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/24—Continuous 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
-
- 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/147—Bleaching ; Apparatus therefor with oxygen or its allotropic modifications
- D21C9/153—Bleaching ; Apparatus therefor with oxygen or its allotropic modifications with ozone
-
- 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/16—Bleaching ; Apparatus therefor with per compounds
- D21C9/163—Bleaching ; Apparatus therefor with per compounds with peroxides
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
- Cookers (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Detergent Compositions (AREA)
- Nitrogen Condensed Heterocyclic Rings (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
Abstract
In the continuous kraft pulping of comminuted cellulosic fibrous material (e.g. wood chips) to produce paper pulp, viscosity for a given Kappa Number is significantly increased (e.g. at least about 20%) by adding kraft white liquor to the wash recirculation loop (38-40) in a continuous digester (19). Optimum results are obtained when kraft white liquor is also added to a recirculation loop (28-30) at a central portion of the digester, so that the majority of the digester has countercurrent flow between white liquor and cellulosic material. About 5-20% of the total white liquor necessary to effect kraft cooking is introduced in the wash circulation, and about 10-20% is introduced into the central portion recirculation. The temperature in the wash zone is maintained at about 140-175 DEG C. <IMAGE>
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US58304390A | 1990-09-17 | 1990-09-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BR9103650A true BR9103650A (en) | 1992-05-19 |
Family
ID=24331461
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BR919103650A BR9103650A (en) | 1990-09-17 | 1991-08-26 | METHOD AND APPLIANCE FOR CONTINUOUSLY TRANSFORMING FRAGMENTED CELLULOSIC FRAGMENTED MATERIAL INTO KRAFT PULP |
Country Status (10)
| Country | Link |
|---|---|
| EP (1) | EP0476230B1 (en) |
| JP (1) | JP3029492B2 (en) |
| AT (1) | ATE146538T1 (en) |
| BR (1) | BR9103650A (en) |
| CA (1) | CA2037717C (en) |
| DE (1) | DE69123670D1 (en) |
| FI (1) | FI103815B (en) |
| NO (1) | NO179918C (en) |
| RU (1) | RU2089694C1 (en) |
| ZA (1) | ZA912117B (en) |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2089516A1 (en) * | 1992-02-21 | 1993-08-22 | Kaj Henricson | Chlorine free pulping and bleaching sequence |
| US5401361A (en) * | 1992-08-19 | 1995-03-28 | Kamyr, Inc. | Completely coutercurrent cook continuous digester |
| SE500455C2 (en) * | 1992-11-18 | 1994-06-27 | Kamyr Ab | Method of continuous cooking under elevated pressure and temperature of fiber material in a vertical digester |
| SE501848C2 (en) * | 1992-11-18 | 1995-06-06 | Kvaerner Pulping Tech | Method to cook pulp continuously at constant temperature |
| WO1994024362A1 (en) * | 1993-04-20 | 1994-10-27 | Kamyr Ab | Method of continuously cooking pulp |
| US5766413A (en) * | 1993-04-23 | 1998-06-16 | Kvaerner Pulping Ab | Process for isothermal cooking pulp in a continuous digester |
| 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 |
| 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 |
| US5489363A (en) * | 1993-05-04 | 1996-02-06 | Kamyr, Inc. | Pulping with low dissolved solids for improved pulp strength |
| SE502667C2 (en) * | 1993-07-12 | 1995-12-04 | Kvaerner Pulping Tech | Treatment of fiber material with complexing agents before cooking |
| WO1996007786A1 (en) * | 1994-09-02 | 1996-03-14 | Kamyr, Inc. | Continuous kraft cooking with black liquor pretreatment |
| 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 |
| BE1011503A3 (en) * | 1997-10-17 | 1999-10-05 | Solvay Interox | Manufacturing pulp chemicals. |
| 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 |
| SE518542C2 (en) * | 2001-03-21 | 2002-10-22 | Kvaerner Pulping Tech | Continuous boiler method for operating a continuous boiler and boiler liquid return system in a continuous boiler |
| SE517674E8 (en) * | 2001-05-02 | 2015-10-20 | Metso Paper Sweden Ab | Method of washing liquid supply to boiling process for cellulose pulp |
| GB0119237D0 (en) * | 2001-08-07 | 2001-10-03 | Bioregional Minimills Uk Ltd | Paper plant |
| RU2407768C2 (en) * | 2005-06-03 | 2010-12-27 | Андриц Аг | Method to reduce power consumption in production of thermomechanical wood pulp by means of low-temperature grinding of wood pulp of low and medium concentration |
| RU2335590C1 (en) * | 2007-01-16 | 2008-10-10 | Витаутас Валентинович Сенкус | Method of manufacture of stable railway sleeper with application of mining and smelting production wastes |
| CA2638196C (en) | 2007-08-07 | 2015-12-15 | Andritz Inc. | Method and system for semi-chemical pulping |
| US20090038767A1 (en) * | 2007-08-07 | 2009-02-12 | Andritz Inc. | Method and System for Semi-Chemical Pulping |
| US7828930B2 (en) * | 2007-11-20 | 2010-11-09 | International Paper Company | Use of polysulfide in modified cooking |
| SE539706C2 (en) * | 2014-11-07 | 2017-11-07 | Valmet Oy | Method for recovering hydrolysate |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3215588A (en) * | 1963-08-15 | 1965-11-02 | Lummus Co | Continuous impregnation, cooking, and washing of fibrous material |
| US3427218A (en) * | 1964-07-10 | 1969-02-11 | Kamyr Ab | Method of performing counter-current continuous cellulose digestion |
| US5053108A (en) * | 1989-06-28 | 1991-10-01 | Kamyr Ab | High sulfidity cook for paper pulp using black liquor sulfonization of steamed chips |
-
1991
- 1991-03-07 CA CA002037717A patent/CA2037717C/en not_active Expired - Lifetime
- 1991-03-21 ZA ZA912117A patent/ZA912117B/en unknown
- 1991-05-22 DE DE69123670T patent/DE69123670D1/en not_active Expired - Lifetime
- 1991-05-22 AT AT91108241T patent/ATE146538T1/en not_active IP Right Cessation
- 1991-05-22 EP EP91108241A patent/EP0476230B1/en not_active Expired - Lifetime
- 1991-08-26 BR BR919103650A patent/BR9103650A/en not_active IP Right Cessation
- 1991-09-10 JP JP3230501A patent/JP3029492B2/en not_active Expired - Lifetime
- 1991-09-16 RU SU915001635A patent/RU2089694C1/en active
- 1991-09-16 NO NO913639A patent/NO179918C/en not_active IP Right Cessation
- 1991-09-17 FI FI914353A patent/FI103815B/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| FI103815B1 (en) | 1999-09-30 |
| EP0476230B1 (en) | 1996-12-18 |
| AU647129B2 (en) | 1994-03-17 |
| JP3029492B2 (en) | 2000-04-04 |
| ATE146538T1 (en) | 1997-01-15 |
| NO179918B (en) | 1996-09-30 |
| JPH04300378A (en) | 1992-10-23 |
| EP0476230A3 (en) | 1993-06-09 |
| NO913639D0 (en) | 1991-09-16 |
| CA2037717A1 (en) | 1992-03-18 |
| EP0476230A2 (en) | 1992-03-25 |
| FI914353A0 (en) | 1991-09-17 |
| NO913639L (en) | 1992-03-18 |
| DE69123670D1 (en) | 1997-01-30 |
| RU2089694C1 (en) | 1997-09-10 |
| ZA912117B (en) | 1991-11-27 |
| NO179918C (en) | 1997-01-08 |
| FI914353A7 (en) | 1992-03-18 |
| AU7830591A (en) | 1992-03-19 |
| CA2037717C (en) | 1996-03-05 |
| FI103815B (en) | 1999-09-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FF | Decision: intention to grant | ||
| FG9A | Patent or certificate of addition granted | ||
| B25D | Requested change of name of applicant approved | ||
| B25D | Requested change of name of applicant approved | ||
| B25D | Requested change of name of applicant approved | ||
| B25G | Requested change of headquarter approved | ||
| B21A | Patent or certificate of addition expired [chapter 21.1 patent gazette] |
Free format text: PATENTE EXTINTE EM 26/08/2011 |