GB1035456A - Production of pulp - Google Patents
Production of pulpInfo
- Publication number
- GB1035456A GB1035456A GB41407/63A GB4140763A GB1035456A GB 1035456 A GB1035456 A GB 1035456A GB 41407/63 A GB41407/63 A GB 41407/63A GB 4140763 A GB4140763 A GB 4140763A GB 1035456 A GB1035456 A GB 1035456A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquor
- line
- liquid
- impregnator
- pressure steam
- 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.)
- Expired
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
- D21C3/22—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
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/10—Physical methods for facilitating impregnation
Landscapes
- Paper (AREA)
Abstract
1, 035, 456. Treating wood pulp. DOMTAR Ltd. Oct. 21, 1963 [Oct. 20, 1962], No. 41407/63. Heading D2W. [Also in Division B1] Material such as wood chips or other cellulosic raw materials containing a vaporizable liquid are impregnated with an impregnant in a vaporizable liquid, such as sulphidic alkali liquor, by continuously introducing said materials into said liquid to effect impregnation, continuously removing from the system impregnated material together with vaporizable liquid, continuously evaporating an amount of the liquid left in the system equal to the difference between the total amount of liquid entering the system and the amount leaving the system and removing the so-formed vapour, to prevent accumulation of liquid in the system. As shown in Fig. 1, wood chips are passed from storage bin 10 to presteamer 11 and thence to impregnator 13, cooking tube 15, washer 19 and further washer 22 from which pulp product is obtained. The impregnating liquor is supplied through line 28 to a circulating supply to the impregnator after being preheated by black liquor formed in the process, in heat exchanger 42. The circulating impregnating liquor is heated by high pressure steam in heat exchanger 26 to a temperature such that flashing takes place in the impregnator, and released steam is vented through line 30 under the control of valve 30<SP>1</SP>, so that a constant level L is maintained in the impregnator. By this means optimum impregnation is achieved, irrespective of the amount of water in the chips. The impregnated chips then pass to the cooker 15 to which high pressure steam is admitted through line 16. Black liquor is withdrawn through line 32 and the cooked material passes to counter-current washer 19 which removes further black liquor through line 41 which is combined with that from the cooker and passed through heat exchanger 42 to flasher 43, if desired to oxidation tower 54, and then to concentrators 45, 44 arranged in multiple effect before final discharge through flash tank 58 as concentrated black liquor. High pressure steam in line 30 derived from the impregnation stage is employed to perform this concentration and the process renders hot water available for causticising, and low pressure steam. In the embodiment illustrated in Fig. 2 (not shown), flashing of the impregnating liquor is arranged to take place in a tank externally of the impregnation vessel. Fig. 3 (not shown) shows an alternative washing system in which pulp from cooker 15 passes through a pool of washing liquor and thence to a tank from which it is withdrawn for final washing and dewatering. Washing liquors are recycled.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA860584 | 1962-10-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1035456A true GB1035456A (en) | 1966-07-06 |
Family
ID=4141584
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB41407/63A Expired GB1035456A (en) | 1962-10-20 | 1963-10-21 | Production of pulp |
Country Status (5)
Country | Link |
---|---|
US (1) | US3258390A (en) |
DE (1) | DE1246384B (en) |
FI (1) | FI46087C (en) |
FR (1) | FR1372871A (en) |
GB (1) | GB1035456A (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE330819B (en) * | 1966-09-12 | 1970-11-30 | Kamyr Ab | |
US3549483A (en) * | 1967-08-04 | 1970-12-22 | Lummus Co | Impregnation and digestion of cellulosic material in a single vessel |
DE2627333A1 (en) * | 1976-06-18 | 1977-12-29 | Bayer Ag | DISPLACEMENT OF A LIQUID A BY A LIQUID B IN A SUSPENSION |
SE7802408L (en) * | 1978-03-02 | 1979-09-03 | Gloeersen Stig | WAY TO TRANSFER WITH LIQUID TRANSPORTABLE MATERIALS AS FIBER MATERIALS |
US4322184A (en) * | 1979-12-05 | 1982-03-30 | Kamyr, Inc. | Apparatus for continuously feeding solid particles into a pressurized container having an improved lifting mechanism |
SE510706C2 (en) * | 1997-10-16 | 1999-06-14 | Kvaerner Pulping Tech | Process system and process for impregnating and basing chips before pulping |
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 |
FI122841B (en) * | 2004-10-04 | 2012-07-31 | Metso Paper Inc | Method and apparatus for making cellulosic pulp |
FI120547B (en) * | 2004-10-04 | 2009-11-30 | Metso Paper Inc | Alkaline cooking process and pulp making plant |
FI126802B (en) * | 2014-09-12 | 2017-05-31 | Andritz Oy | Process and continuous hydraulic boiler system for chemical pulp production |
FI20165470A (en) | 2016-06-06 | 2017-12-07 | Andritz Oy | A process for producing chemical pulp at a pulp mill digester |
CN113299253B (en) * | 2021-05-25 | 2024-05-07 | 李成兵 | Preparation method of anti-cracking flute |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2205374A (en) * | 1936-07-02 | 1940-06-18 | Chemipulp Process Inc | Digesting process and apparatus |
US2858211A (en) * | 1956-02-13 | 1958-10-28 | Condi Engineering Corp | Apparatus for wood chip digestion |
US2809111A (en) * | 1956-02-13 | 1957-10-08 | Condi Engineering Corp | Apparatus for wood chip digestion |
-
1963
- 1963-10-14 US US316021A patent/US3258390A/en not_active Expired - Lifetime
- 1963-10-18 FI FI632036A patent/FI46087C/en active
- 1963-10-18 FR FR951131A patent/FR1372871A/en not_active Expired
- 1963-10-21 GB GB41407/63A patent/GB1035456A/en not_active Expired
- 1963-10-21 DE DED42771A patent/DE1246384B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
FR1372871A (en) | 1964-09-18 |
FI46087C (en) | 1972-12-11 |
DE1246384B (en) | 1967-08-03 |
FI46087B (en) | 1972-08-31 |
US3258390A (en) | 1966-06-28 |
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