SE0502851L - Systems and process for the generation of steam in a boiler for the production of chemical cellulose pulp - Google Patents
Systems and process for the generation of steam in a boiler for the production of chemical cellulose pulpInfo
- Publication number
- SE0502851L SE0502851L SE0502851A SE0502851A SE0502851L SE 0502851 L SE0502851 L SE 0502851L SE 0502851 A SE0502851 A SE 0502851A SE 0502851 A SE0502851 A SE 0502851A SE 0502851 L SE0502851 L SE 0502851L
- Authority
- SE
- Sweden
- Prior art keywords
- steam
- black liquor
- generation
- heating
- treatment
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 3
- 229920002678 cellulose Polymers 0.000 title abstract 2
- 239000001913 cellulose Substances 0.000 title abstract 2
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 239000000126 substance Substances 0.000 title abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 4
- 238000002203 pretreatment Methods 0.000 abstract 4
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000007787 solid 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
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
-
- 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
- D21C11/06—Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds
-
- 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
- D21C11/06—Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds
- D21C11/08—Deodorisation ; Elimination of malodorous compounds, e.g. sulfur compounds such as hydrogen sulfide or mercaptans, from gas streams
-
- 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
- D21C11/10—Concentrating spent liquor by evaporation
-
- 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
- D21C11/0042—Fractionating or concentration of spent liquors by special methods
Landscapes
- Paper (AREA)
Abstract
The invention concerns a system and a method for the generation of steam in a digester plant for the production of chemical cellulose pulp. The pressure of hot, pressurised black liquor from a digester (4) is reduced in a first step (11 a/11 b) for the formation of sufficient quantities of black liquor steam (BL-ST) that is used for the steam pre-treatment of the chips in a second pre-heating step (2). Pure steam (P-ST) for the steam pre-treatment of the chips in a first pre¬ heating step (1 ) is formed in sufficient quantities through re-heating (13) the black liquor whose pressure has been reduced before a final subsequent pressure reduction, where the increased quantity of black liquor steam is led to a steam converter (14) for the generation of pure steam. This system entails an efficient use of the heat content of the black liquor with simple process equipment, with less problems from clogging, and it generates sufficient quantities of pure and more contaminated steam that is used in a first steam pre-treatment step and a second steam pre-treatment step, respectively. At the same time, an increased dry solids content of the black liquor is achieved through re-heating and repeated reduction in pressure, which reduces the load on the recovery plant.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE0502851A SE0502851L (en) | 2005-12-21 | 2005-12-21 | Systems and process for the generation of steam in a boiler for the production of chemical cellulose pulp |
PCT/SE2006/050583 WO2007073333A1 (en) | 2005-12-21 | 2006-12-15 | System and method for the generation of steam from hot black liquor in a digester plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE0502851A SE0502851L (en) | 2005-12-21 | 2005-12-21 | Systems and process for the generation of steam in a boiler for the production of chemical cellulose pulp |
Publications (2)
Publication Number | Publication Date |
---|---|
SE528574C2 SE528574C2 (en) | 2006-12-19 |
SE0502851L true SE0502851L (en) | 2006-12-19 |
Family
ID=37545610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE0502851A SE0502851L (en) | 2005-12-21 | 2005-12-21 | Systems and process for the generation of steam in a boiler for the production of chemical cellulose pulp |
Country Status (2)
Country | Link |
---|---|
SE (1) | SE0502851L (en) |
WO (1) | WO2007073333A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI122983B (en) * | 2009-02-09 | 2012-09-28 | Andritz Inc | A process for steam generation at a pulp mill digester |
US9328963B2 (en) | 2013-07-10 | 2016-05-03 | Renmatix, Inc. | Energy recovery when processing materials with reactive fluids |
SE539449C2 (en) * | 2015-11-16 | 2017-09-26 | Valmet Oy | Method for heating cellulosic material to full cooking temperature in digesters |
SE1650664A1 (en) | 2016-05-17 | 2017-10-17 | Valmet Oy | Method for generation of clean steam in a continuous digester system |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5547546A (en) * | 1994-10-04 | 1996-08-20 | Ahlstrom Machinery Inc. | Chip bin with steaming control and a gas vent containing a vacuum and pressure relief device |
BR9816065A (en) * | 1998-11-09 | 2001-08-21 | Kvaerner Pulping Tech | Process vapor production method from black liquor |
US6176971B1 (en) * | 1998-11-18 | 2001-01-23 | Andritz-Ahlstrom Inc. | Heat economy enhancements for the recovery and use of energy obtained from spent cooking liquors |
-
2005
- 2005-12-21 SE SE0502851A patent/SE0502851L/en not_active IP Right Cessation
-
2006
- 2006-12-15 WO PCT/SE2006/050583 patent/WO2007073333A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
SE528574C2 (en) | 2006-12-19 |
WO2007073333A1 (en) | 2007-06-28 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
NUG | Patent has lapsed |