GB681661A - Treatment of chemical pulp - Google Patents
Treatment of chemical pulpInfo
- Publication number
- GB681661A GB681661A GB4661/51A GB466151A GB681661A GB 681661 A GB681661 A GB 681661A GB 4661/51 A GB4661/51 A GB 4661/51A GB 466151 A GB466151 A GB 466151A GB 681661 A GB681661 A GB 681661A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- alkali
- peroxide
- pulp
- fibres
- 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
- D21C9/16—Bleaching ; Apparatus therefor with per compounds
- D21C9/163—Bleaching ; Apparatus therefor with per compounds with peroxides
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
Abstract
Sulphite pulp is bleached by adding thereto alkaline peroxide solution until the fibre density is 20-65 per cent, the peroxide content (calculated as H2O2) is 0.3-1.75 per cent and the alkali content (calculated as NaOH) is 0.75-3.25 per cent, based on dry pulp; the fibres are maintained damp at a density above 20 per cent and a temperature below 130 DEG F. until maximum brightness is obtained, e.g. 1-20 days. Typical concentrations are H2O2 0.75-1.25 per cent and NaOH 1.0-2.5 per cent, when the time needed is 2-14 days. The peroxide solution is applied to pulp crumbs or to a self-supporting lap or web by normal methods, e.g. spraying or padding. The fibres are stacked or piled in close contact during bleaching to prevent drying out. Examples are given of the process and results are compared with those obtained by prior-art methods. Graphs are given of the cuprammonium viscosity of the product when different alkali concentrations and temperatures are used in bleaching. The peroxide solution may be obtained from sodium peroxide, hydrogen peroxide or other inorganic compound which generates hydrogen peroxide (e.g. a perborate) by adding acid or alkali as necessary. A stabilizer is preferably added, e.g. sodium silicate, alkali phosphate or pyrophosphate or a soluble magnesium salt. This will contribute to the total alkali concentration of the solution. The process is applicable to soft, medium and hard cooked pulps, from soft or hard woods, whether cooked with calcium, magnesium, ammonium or mixed base liquors.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US148312A US2692181A (en) | 1950-03-08 | 1950-03-08 | Treatment of unbleached sulfite pulp |
Publications (1)
Publication Number | Publication Date |
---|---|
GB681661A true GB681661A (en) | 1952-10-29 |
Family
ID=22525223
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4661/51A Expired GB681661A (en) | 1950-03-08 | 1951-02-26 | Treatment of chemical pulp |
Country Status (4)
Country | Link |
---|---|
US (1) | US2692181A (en) |
CH (1) | CH293130A (en) |
FR (1) | FR1036726A (en) |
GB (1) | GB681661A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1043789B (en) * | 1954-11-19 | 1958-11-13 | Fmc Corp | Process to stabilize the degree of whiteness of already bleached pulp for paper manufacture |
WO2009015704A1 (en) * | 2007-07-31 | 2009-02-05 | Voith Patent Gmbh | Bleached fibrous material |
WO2017178849A1 (en) | 2016-04-15 | 2017-10-19 | MIKULIC Marinko | A continuous process for production of cellulose pulp |
WO2020160955A1 (en) | 2019-02-07 | 2020-08-13 | MIKULIC Marinko | Continuous process for production of cellulose pulp from grass-like feedstock |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE573341C (en) * | 1927-02-27 | 1933-03-31 | Max Steinschneider Dipl Ing | Process for the production of cellulose, in particular for the manufacture of rayon |
US2107297A (en) * | 1934-03-08 | 1938-02-08 | Buffalo Electro Chem Co | Bleaching fiber |
US2150926A (en) * | 1937-07-03 | 1939-03-21 | Buffalo Electro Chem Co | Process of making and bleaching paper |
US2189378A (en) * | 1938-02-05 | 1940-02-06 | Buffalo Electro Chem Co | Bleaching fibers and a composition therefor |
US2465738A (en) * | 1945-12-22 | 1949-03-29 | Buffalo Electro Chem Co | Method of bleaching mechanical wood fibers |
US2492047A (en) * | 1946-03-30 | 1949-12-20 | Du Pont | Bleaching wood pulp |
US2513344A (en) * | 1946-09-19 | 1950-07-04 | Buffalo Electro Chem Co | Method of bleaching high-density pulp |
US2510595A (en) * | 1946-09-20 | 1950-06-06 | Buffalo Electro Chem Co | Method of bleaching groundwood |
US2514503A (en) * | 1947-07-30 | 1950-07-11 | Buffalo Electro Chem Co | Method of bleaching moist felted groundwood pulp |
US2466633A (en) * | 1948-05-26 | 1949-04-05 | James M Daily | Method of bleaching cellulosic pulp |
-
1950
- 1950-03-08 US US148312A patent/US2692181A/en not_active Expired - Lifetime
-
1951
- 1951-02-26 GB GB4661/51A patent/GB681661A/en not_active Expired
- 1951-02-26 FR FR1036726D patent/FR1036726A/en not_active Expired
- 1951-03-05 CH CH293130D patent/CH293130A/en unknown
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1043789B (en) * | 1954-11-19 | 1958-11-13 | Fmc Corp | Process to stabilize the degree of whiteness of already bleached pulp for paper manufacture |
WO2009015704A1 (en) * | 2007-07-31 | 2009-02-05 | Voith Patent Gmbh | Bleached fibrous material |
WO2017178849A1 (en) | 2016-04-15 | 2017-10-19 | MIKULIC Marinko | A continuous process for production of cellulose pulp |
WO2020160955A1 (en) | 2019-02-07 | 2020-08-13 | MIKULIC Marinko | Continuous process for production of cellulose pulp from grass-like feedstock |
US11976416B2 (en) | 2019-02-07 | 2024-05-07 | Marinko Mikulic | Continuous process for production of cellulose pulp from grass-like feedstock |
Also Published As
Publication number | Publication date |
---|---|
US2692181A (en) | 1954-10-19 |
FR1036726A (en) | 1953-09-10 |
CH293130A (en) | 1953-09-15 |
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