CA2041536A1 - Method for treatment and recycling of pulp mill bleach plant effluents - Google Patents
Method for treatment and recycling of pulp mill bleach plant effluentsInfo
- Publication number
- CA2041536A1 CA2041536A1 CA 2041536 CA2041536A CA2041536A1 CA 2041536 A1 CA2041536 A1 CA 2041536A1 CA 2041536 CA2041536 CA 2041536 CA 2041536 A CA2041536 A CA 2041536A CA 2041536 A1 CA2041536 A1 CA 2041536A1
- Authority
- CA
- Canada
- Prior art keywords
- bleach
- pulp
- recycling
- treatment
- chlorine
- 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
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/10—Concentrating spent liquor by evaporation
Landscapes
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Extraction Or Liquid Replacement (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Abstract The invention relates to a method for treatment and recycling of pulp mill bleach plant effluents. Chlorine-containing chemicals are separated from the fluid obtained from the first bleach stage (DC) implemented with these chlorine-containing bleach chemicals on pulp (2) that has been washed (W) and partially dewatered (P1) whereby the pulp (3) from the mentioned bleach stage (DC), with chlorine-containing bleach chemicals, is dewatered (P2) up to about the same dryness of at least 25 % and at most 35 % as for the mentioned thereto incoming pulp (2) and whereby the fluid from the second dewatering (P2) is recycled to the bleach stage (DC) and the outcoming fluid (9) from the bleach stage (DC) is evaporated (EV) through indirect heating with condensing vapour obtained through recompression of vapour stripped in the evaporation. The dewatering (P1, P2) is preferably performed by pressing out the liquid from the pulp (2, 3) and the evaporation (EV) in several stages connected in parallel or in series at a temperature below 70°C.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI902261 | 1990-05-04 | ||
FI902261A FI85293C (en) | 1990-05-04 | 1990-05-04 | FOERFARANDE FOER RENING OCH AOTERFOERING AV CELLULOSAFABRIKERS BLEKERIAVATTEN. |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2041536A1 true CA2041536A1 (en) | 1991-11-05 |
CA2041536C CA2041536C (en) | 1997-12-09 |
Family
ID=8530380
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA 2041536 Expired - Fee Related CA2041536C (en) | 1990-05-04 | 1991-04-30 | Method for treatment and recycling of pulp mill bleach plant effluents |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPH089837B2 (en) |
AU (1) | AU634381B2 (en) |
BR (1) | BR9101745A (en) |
CA (1) | CA2041536C (en) |
ES (1) | ES2034879B1 (en) |
FI (1) | FI85293C (en) |
SE (1) | SE507066C2 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994003673A1 (en) * | 1992-07-30 | 1994-02-17 | Kamyr, Inc. | Zero discharge pulp mill |
US5300191A (en) * | 1992-07-30 | 1994-04-05 | Kamyr, Inc. | Chlorine dioxide generation for a zero discharge pulp mill |
WO1994020675A1 (en) * | 1993-03-02 | 1994-09-15 | Kamyr, Inc. | Zero discharge mill distillation, salt recovery, and water management |
WO1995006774A1 (en) * | 1993-08-31 | 1995-03-09 | Kamyr, Inc. | Minimum adverse environmental pulp mill with feed to chlorate manufacture |
AU671844B2 (en) * | 1992-07-20 | 1996-09-12 | Unilever Plc | Manufacture of gas hydrates |
US5628872A (en) * | 1993-10-22 | 1997-05-13 | Kanyr Ab | Method for bleaching pulp with hydrogen peroxide recovered from cellulosic spent liquor |
EP0719359B1 (en) * | 1993-08-31 | 1998-12-09 | Ahlstrom Machinery Oy | Minimum adverse environmental impact pulp mill |
WO2000043589A1 (en) * | 1999-01-22 | 2000-07-27 | Andritz-Ahlstrom Oy | Treatment of recirculated filtrates in pulp production |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10506964A (en) * | 1994-10-05 | 1998-07-07 | エカ ケミカルズ アクチェボラーグ | Method for treating process water in pulp production |
GB0301183D0 (en) | 2003-01-18 | 2003-02-19 | Rolls Royce Plc | Electrostatic sensors |
SE0300276L (en) * | 2003-01-31 | 2003-12-09 | Kvaerner Pulping Tech | Method for bleaching cellulose pulp and bleaching line for this |
FI126551B (en) * | 2009-11-25 | 2017-02-15 | Andritz Oy | A method for treating fluid flows at a pulp mill |
JP7317509B2 (en) * | 2019-01-10 | 2023-07-31 | 日本製紙株式会社 | Method for producing lignin, and lignin-based dispersant |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA973661A (en) * | 1972-09-29 | 1975-09-02 | Pulp And Paper Research Institute Of Canada | Press alkaline extraction of cellulosic pulp |
US4159682A (en) * | 1977-12-01 | 1979-07-03 | Dorr-Oliver Incorporated | Fluid bed combustion with predrying of moist feed using bed sand |
DE3043194A1 (en) * | 1980-11-15 | 1982-07-01 | Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover | DEVICE FOR MECHANICALLY SEPARATING LIQUIDS FROM LIQUIDS-SOLIDS MIXTURES IN A SCREW PRESS |
FI67894C (en) * | 1982-05-21 | 1985-06-10 | Rauma Repola Oy | FOERFARANDE OCH ANORDNING FOER BLEKNING AV FIBERMASSA |
FI77064C (en) * | 1985-04-29 | 1989-01-10 | Tampella Oy Ab | Process for boiling and bleaching cellulose |
NO159494C (en) * | 1986-10-23 | 1989-01-04 | Kvaerner Eureka As | PROCEDURE BY BLACKING CELLULOSMASS OR FRACTION THEREOF, PLANT FOR USE BY IMPLEMENTING THE PROCEDURE. |
NO882815L (en) * | 1988-06-24 | 1989-12-27 | Sigurd Fongen | PROCEDURE FOR CELLULOUS PREPARATION AND DELIGNIFICATION, WHEATING, DE-INKING AND CLEANING OF CELLULOSE FIBER AND DEVICE FOR CARRYING OUT THE PROCEDURE. |
AU619580B2 (en) * | 1988-08-23 | 1992-01-30 | Sappi Limited | Elimination of bleach effluents |
WO1990001977A1 (en) * | 1988-08-26 | 1990-03-08 | Aquamax Oy | A distillation apparatus |
-
1990
- 1990-05-04 FI FI902261A patent/FI85293C/en active IP Right Grant
-
1991
- 1991-04-26 AU AU76278/91A patent/AU634381B2/en not_active Ceased
- 1991-04-26 SE SE9101278A patent/SE507066C2/en not_active IP Right Cessation
- 1991-04-29 ES ES9101076A patent/ES2034879B1/en not_active Expired - Fee Related
- 1991-04-30 CA CA 2041536 patent/CA2041536C/en not_active Expired - Fee Related
- 1991-04-30 BR BR9101745A patent/BR9101745A/en not_active IP Right Cessation
- 1991-04-30 JP JP9857491A patent/JPH089837B2/en not_active Expired - Fee Related
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU671844B2 (en) * | 1992-07-20 | 1996-09-12 | Unilever Plc | Manufacture of gas hydrates |
US5518583A (en) * | 1992-07-30 | 1996-05-21 | A. Ahlstrom Corporation | Zero discharge mill distillation, salt recovery, and water management |
US5300191A (en) * | 1992-07-30 | 1994-04-05 | Kamyr, Inc. | Chlorine dioxide generation for a zero discharge pulp mill |
WO1994003673A1 (en) * | 1992-07-30 | 1994-02-17 | Kamyr, Inc. | Zero discharge pulp mill |
US5374333A (en) * | 1992-07-30 | 1994-12-20 | Kamyr, Inc. | Method for minimizing pulp mill effluents |
AU666204B2 (en) * | 1992-07-30 | 1996-02-01 | Kamyr Inc. | Zero discharge pulp mill |
US5439555A (en) * | 1992-07-30 | 1995-08-08 | Kamyr, Inc. | Minimum adverse environmental pulp with feed to chlorate manufacture |
US5547543A (en) * | 1992-07-30 | 1996-08-20 | Ahlstrom Machinery Inc. | Apparatus for minimizing effluent discharges and recovering chemicals in a pulp mill |
WO1994015020A1 (en) * | 1992-12-23 | 1994-07-07 | Kamyr, Inc. | Chlorine dioxide generation for a zero discharge pulp mill |
EP0728864A2 (en) * | 1993-03-02 | 1996-08-28 | Kamyr Inc. | Zero discharge pulp mill cascading water management |
WO1994020675A1 (en) * | 1993-03-02 | 1994-09-15 | Kamyr, Inc. | Zero discharge mill distillation, salt recovery, and water management |
EP0728864A3 (en) * | 1993-03-02 | 1999-07-28 | Ahlstrom Machinery Oy | Zero discharge pulp mill cascading water management |
WO1995006774A1 (en) * | 1993-08-31 | 1995-03-09 | Kamyr, Inc. | Minimum adverse environmental pulp mill with feed to chlorate manufacture |
EP0719359B1 (en) * | 1993-08-31 | 1998-12-09 | Ahlstrom Machinery Oy | Minimum adverse environmental impact pulp mill |
US5628872A (en) * | 1993-10-22 | 1997-05-13 | Kanyr Ab | Method for bleaching pulp with hydrogen peroxide recovered from cellulosic spent liquor |
WO2000043589A1 (en) * | 1999-01-22 | 2000-07-27 | Andritz-Ahlstrom Oy | Treatment of recirculated filtrates in pulp production |
Also Published As
Publication number | Publication date |
---|---|
FI85293B (en) | 1991-12-13 |
FI902261A0 (en) | 1990-05-04 |
FI85293C (en) | 1992-03-25 |
SE9101278D0 (en) | 1991-04-26 |
SE9101278L (en) | 1991-11-05 |
CA2041536C (en) | 1997-12-09 |
JPH06257088A (en) | 1994-09-13 |
ES2034879B1 (en) | 1993-11-01 |
JPH089837B2 (en) | 1996-01-31 |
AU7627891A (en) | 1991-11-07 |
ES2034879A1 (en) | 1993-04-01 |
BR9101745A (en) | 1991-12-10 |
AU634381B2 (en) | 1993-02-18 |
FI902261A (en) | 1991-11-05 |
SE507066C2 (en) | 1998-03-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |