GB733364A - An improved physico-chemical process for the extraction of celluloses from vegetablematerials in general, and a product obtained thereby - Google Patents
An improved physico-chemical process for the extraction of celluloses from vegetablematerials in general, and a product obtained therebyInfo
- Publication number
- GB733364A GB733364A GB24073/52A GB2407352A GB733364A GB 733364 A GB733364 A GB 733364A GB 24073/52 A GB24073/52 A GB 24073/52A GB 2407352 A GB2407352 A GB 2407352A GB 733364 A GB733364 A GB 733364A
- Authority
- GB
- United Kingdom
- Prior art keywords
- washed
- sodium
- treatment
- solution
- liquid
- 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
- D21C3/006—Pulping cellulose-containing materials with compounds not otherwise provided for
-
- 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
- D21C3/222—Use of compounds accelerating the pulping 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
- 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
- D21C7/00—Digesters
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Cellulose is obtained from fibrous vegetable material by crushing the material and then treating it with a dilute solution of an oxidizing agent in the presence of caustic soda, sodium carbonate or the like so that non-cellulosic constituents of the material undergo hydrolysis and are removed. The hydrolysis may be carried out at 30-50 DEG C. The oxidizing agent may be sodium, potassium or calcium hypochlorite; sodium or hydrogen peroxide; ammonium persulphate or sodium meta-perborate. Mixtures of oxidizing agents may be used if desired. Non-woody material such as straw, broom-corn, stems and cobs of maize, or genista is washed with water, ground and selected in lengths of 3-5 cm. The material is washed and then passed through crushing machines to break knots and crush the fibres, and to expel moisture and air. Small quantities of oxidizing agents may be present during the crushing. Woody material is washed and reduced to pieces of 2-5 cm. in length and then passed through crushing machines, preferably after being moistened with a dilute oxidizing solution. The crushed material may then be treated with a solution of sodium hypochlorite of specific gravity 1.15-1.18, together with caustic soda, sodium carbonate or the like to obtain an alkaline medium up to a pH of 9-12. During the reaction, chlorine is liberated. This is collected and returned to the liquid, through which it is bubbled. The heat liberated during the reaction may raise the temperature to 65 DEG C. The time of treatment may range from 1-6 hours. The treatment time may be reduced by projecting light on to the material undergoing treatment. At the end of the treatment the mass is filtered and the liquid is treated for the recovery of salts and chlorinated compounds formed during the reaction. The liquid may then be re-used for treating a subsequent quantity of the crushed vegetable material. The crude cellulose, freed from the bulk of treatment liquid, is washed with water at 40 DEG C. in a tank provided with a stirrer to dissolve salts and chlorinated compounds, and it is further washed in Hollanders. It is then subjected to an anti-chlor treatment with sodium thiosulphate solution, washed with water, treated with dilute sodium carbonate solution, washed again, filtered and dried.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT733364X | 1952-05-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB733364A true GB733364A (en) | 1955-07-13 |
Family
ID=11315279
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB24073/52A Expired GB733364A (en) | 1952-05-14 | 1952-09-25 | An improved physico-chemical process for the extraction of celluloses from vegetablematerials in general, and a product obtained thereby |
Country Status (3)
Country | Link |
---|---|
BE (1) | BE525692A (en) |
FR (3) | FR1076136A (en) |
GB (1) | GB733364A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2800102A1 (en) * | 1999-10-21 | 2001-04-27 | Haji Skander Ben | Paper production comprises washing straw, grinding, washing and contacting with Na hypochlorite and NaCl to bleach and then give cellulosic fibers and refining |
US10968283B2 (en) * | 2014-07-28 | 2021-04-06 | Anomera Inc. | Method for producing functionalized nanocrystalline cellulose and functionalized nanocrystalline cellulose thereby produced |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2560898B1 (en) * | 1984-03-06 | 1988-01-08 | Air Liquide | METHOD FOR DESTRUCTURING LIGNOCELLULOSIC MATERIALS |
FR2571757A1 (en) * | 1984-10-16 | 1986-04-18 | Rauma Repola Oy | Process for filling a noncontinuously operating chip digester and digester for this process |
SE506456C2 (en) * | 1989-06-28 | 1997-12-15 | Kvaerner Pulping Tech | Apparatus and method for continuous production of pulp, wherein the impregnation vessel is arranged in the cooking pot |
-
0
- BE BE525692D patent/BE525692A/xx unknown
- FR FR65634D patent/FR65634E/fr not_active Expired
-
1952
- 1952-09-25 GB GB24073/52A patent/GB733364A/en not_active Expired
- 1952-10-23 FR FR1076136D patent/FR1076136A/en not_active Expired
-
1953
- 1953-05-12 FR FR1079333D patent/FR1079333A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2800102A1 (en) * | 1999-10-21 | 2001-04-27 | Haji Skander Ben | Paper production comprises washing straw, grinding, washing and contacting with Na hypochlorite and NaCl to bleach and then give cellulosic fibers and refining |
US10968283B2 (en) * | 2014-07-28 | 2021-04-06 | Anomera Inc. | Method for producing functionalized nanocrystalline cellulose and functionalized nanocrystalline cellulose thereby produced |
Also Published As
Publication number | Publication date |
---|---|
BE525692A (en) | |
FR65634E (en) | 1956-02-29 |
FR1079333A (en) | 1954-11-29 |
FR1076136A (en) | 1954-10-22 |
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