GB418133A - Improvements in continuous bleaching processes and apparatus - Google Patents
Improvements in continuous bleaching processes and apparatusInfo
- Publication number
- GB418133A GB418133A GB4833/33A GB483333A GB418133A GB 418133 A GB418133 A GB 418133A GB 4833/33 A GB4833/33 A GB 4833/33A GB 483333 A GB483333 A GB 483333A GB 418133 A GB418133 A GB 418133A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- bleaching agent
- chambers
- connections
- driven
- 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
- 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
-
- 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
- D21C9/08—Removal of fats, resins, pitch or waxes; Chemical or physical purification, i.e. refining, of crude cellulose by removing non-cellulosic contaminants, optionally combined with bleaching
-
- 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
- D21C9/1005—Pretreatment of the pulp, e.g. degassing the pulp
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
- Treatment Of Fiber Materials (AREA)
Abstract
<PICT:0418133/III/1> Fibrous cellulosic material in a substantially dry, sub-divided form is bleached by advancing the mass through a reaction chamber, the manner of introduction and withdrawal of the material being such as to maintain a substantially air-tight seal at the inlet and outlet of the chamber, and treating the material with gaseous bleaching agent under abnormal pressure conditions within the chamber. The material may be first subjected to a vacuum in one portion of the chamber and then reacted with a gaseous bleaching agent in another portion of the chamber. A suitable apparatus comprises a reaction chamber 10 suitably lined with rubber, glass, phenolic condensation products or the like 11. The top of the chamber is provided with a tapered neck 12 in which turns a feed screw 14 driven by a motor 18. The pulp obtained from a screw-press 21, from which water drains by way of the discharge pipe 25, is fed into a pulper, disintegrator, or breaker 27 from which it is discharged into the tapered neck 12. The lower portion of the chamber converges towards a narrow discharge neck 29 fitted with a screw 30 driven by a motor 32. For removing the air from the material a vacuum pump 34 is provided which may have a plurality of connections 35. At a point further down a suitable bleaching agent such as chlorine is introduced from a vessel 36, and may be present either at, below, or above atmospheric pressure. In order to remove residual chlorine, one or more byepass connections 38 are provided. In other forms of apparatus (not shown) the screws 14 and 30 may be replaced by reciprocating pistons, and a series of chambers may be provided having means for washing and pressing the pulp between treatments in successive chambers.ALSO:<PICT:0418133/IV/1> Fibrous cellulosic material in a substantially dry subdivided form is bleached by advancing the mass through a reaction chamber, the manner of introduction and withdrawal of the material being such as to maintain a substantially air-tight seal at the inlet and outlet of the chamber, and treating the material with gaseous bleaching agent under abnormal pressure conditions within the chamber. The material may be first subjected to a vacuum in one portion of the chamber and then reacted with a gaseous bleaching agent in another portion of the chamber. If required, the material may have an alkaline substance distributed through it before it enters the chamber, and according to a modification, the material may be subjected to successive bleaching treatments in separate chambers and prior, to introducing the material into each chamber, an alkaline solution is added thereto and partly expressed. A suitable apparatus comprises a reaction chamber 10 suitably lined with rubber, glass, phenolic condensation products or the like 11. The top of the chamber is provided with a tapered neck 12 in which turns a feed screw 14 driven by a motor 18. The pulp obtained from a screwpress 21, from which water drains by way of the discharge pipe 25, is fed into a pulper, disintegrator, or breaker 27 from which it is discharged into the tapered neck 12. The lower portion of the chamber converges towards a narrow discharge neck 29 fitted with a screw 30 driven by a motor 32. For removing the air from the material a vacuum pump 34 is provided which may have a plurality of connections 35. At a point further down a suitable bleaching agent such as chlorine is introduced from a vessel 36, and may be present either at, below, or above atmospheric pressure. In order to remove residual chlorine, one or more byepass connections 38 are provided. Preferably, only a partial bleach is effected during each treatment and the material is passed through the chamber several times, the discharged material being washed and advantageously admixed with alkali such as caustic soda before being returned to the screwpress 21. In other forms of apparatus (not shown) the screws 14 and 30 may be replaced by reciprocating pistons, and a series of chambers may be provided having means for washing and pressing the pulp between treatments in successive chambers.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US598582A US2089992A (en) | 1932-03-14 | 1932-03-14 | Continuous bleaching process and apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
GB418133A true GB418133A (en) | 1934-10-16 |
Family
ID=24396138
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4833/33A Expired GB418133A (en) | 1932-03-14 | 1933-02-16 | Improvements in continuous bleaching processes and apparatus |
Country Status (4)
Country | Link |
---|---|
US (1) | US2089992A (en) |
DE (1) | DE627360C (en) |
FR (1) | FR751230A (en) |
GB (1) | GB418133A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2562882A (en) * | 1948-08-26 | 1951-08-07 | Sharples Chemicals Inc | Chlorination of cellulose |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2525973A (en) * | 1946-11-19 | 1950-10-17 | Allied Chem & Dye Corp | Apparatus for feeding solid material |
US2607680A (en) * | 1947-02-17 | 1952-08-19 | Buckeye Cotton Oil Company | Apparatus and method for processing vegetable fibers |
US2730426A (en) * | 1951-06-20 | 1956-01-10 | Cellulose Dev Corp Ltd | Treating vegetable fibrous material with chlorine gas |
US2906417A (en) * | 1951-09-22 | 1959-09-29 | Rossi Giovanni | Material conveying device |
US2863575A (en) * | 1952-12-31 | 1958-12-09 | Samuel H Vasold | Storage hoppers |
US2893909A (en) * | 1954-06-09 | 1959-07-07 | Bauer Bros Co | Combined digestion and refining of paper pulp |
US2772864A (en) * | 1954-12-08 | 1956-12-04 | John P Rich | Method and apparatus for evacuating pulp from high density storage towers |
DE1080848B (en) * | 1958-02-06 | 1960-04-28 | Escher Wyss Gmbh | Device for the continuous digestion of fibrous vegetable substances in the pulp industry |
DE1095244B (en) * | 1958-10-21 | 1960-12-22 | Walther Klatt | Packing and pressing device for dyeing loose fiber material |
US3044541A (en) * | 1959-09-26 | 1962-07-17 | Sugasawa Masao | Continuous digesting and extracting apparatus |
US3182966A (en) * | 1960-04-06 | 1965-05-11 | Carlsson Ake Simon | Method and means for equalizing quality fluctuations in manufacture of fibre mass |
DE1288900B (en) * | 1960-05-09 | 1969-02-06 | Improved Machinery Inc | Container for the treatment of crushed cellulosic solids |
US3313678A (en) * | 1962-02-14 | 1967-04-11 | Svenska Cellulose Aktiebolaget | Bleaching of cellulose pulp in towers in completely filled and closed system |
CH414514A (en) * | 1962-11-12 | 1966-06-15 | Establishment For Automation | Device for steaming loose material, especially textile fibers |
CH412766A (en) * | 1962-12-15 | 1966-05-15 | Establishment For Automation | Device for steaming, in particular textile goods |
US3293675A (en) * | 1965-02-02 | 1966-12-27 | Butte Knitting Mills | Apparatus and method for dyeing and aging textile materials |
AT271363B (en) * | 1967-03-31 | 1969-05-27 | Vyzk Ustav Zuslechtovaci | Method for treating textile fibers with an aerosol |
JPS5035154B1 (en) * | 1970-01-10 | 1975-11-13 | ||
US3729290A (en) * | 1971-10-04 | 1973-04-24 | P Dillies | Process and apparatus for the treatment of loose materials such as textile fibers |
US4869783A (en) * | 1986-07-09 | 1989-09-26 | The Mead Corporation | High-yield chemical pulping |
WO1996005365A1 (en) * | 1994-08-11 | 1996-02-22 | Beloit Technologies, Inc. | Means for gas-sealingly conveying shredded pulp |
FI112957B (en) * | 1999-07-21 | 2004-02-13 | Metso Paper Pori Oy | Method and apparatus for washing pulp |
-
1932
- 1932-03-14 US US598582A patent/US2089992A/en not_active Expired - Lifetime
-
1933
- 1933-02-16 GB GB4833/33A patent/GB418133A/en not_active Expired
- 1933-02-22 FR FR751230D patent/FR751230A/en not_active Expired
- 1933-03-11 DE DEI46730D patent/DE627360C/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2562882A (en) * | 1948-08-26 | 1951-08-07 | Sharples Chemicals Inc | Chlorination of cellulose |
Also Published As
Publication number | Publication date |
---|---|
US2089992A (en) | 1937-08-17 |
DE627360C (en) | 1936-03-13 |
FR751230A (en) | 1933-08-29 |
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