GB418133A - Improvements in continuous bleaching processes and apparatus - Google Patents

Improvements in continuous bleaching processes and apparatus

Info

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
Application number
GB4833/33A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
International Paper Co
Original Assignee
International Paper Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by International Paper Co filed Critical International Paper Co
Publication of GB418133A publication Critical patent/GB418133A/en
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-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
    • D21C9/10Bleaching ; Apparatus therefor
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-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
    • D21C9/08Removal 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
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-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
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/1005Pretreatment 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.
GB4833/33A 1932-03-14 1933-02-16 Improvements in continuous bleaching processes and apparatus Expired GB418133A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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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