GB734216A - Process for the treatment of ligno-cellulosic fibres - Google Patents
Process for the treatment of ligno-cellulosic fibresInfo
- Publication number
- GB734216A GB734216A GB2946/53A GB294653A GB734216A GB 734216 A GB734216 A GB 734216A GB 2946/53 A GB2946/53 A GB 2946/53A GB 294653 A GB294653 A GB 294653A GB 734216 A GB734216 A GB 734216A
- Authority
- GB
- United Kingdom
- Prior art keywords
- treatment
- sulphur dioxide
- materials
- mass
- acid
- 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
- D21C3/04—Pulping cellulose-containing materials with acids, acid salts or acid anhydrides
- D21C3/06—Pulping cellulose-containing materials with acids, acid salts or acid anhydrides sulfur dioxide; sulfurous acid; bisulfites sulfites
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
-
- 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
- D21C1/04—Pretreatment of the finely-divided materials before digesting with acid reacting compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Fibrous ligno-cellulosic materials such as wood chips, bagasse or straw are treated, prior to alkali digestion, with steam at atmospheric pressure and at a temperature of substantially 100 DEG C., the steam containing sulphur dioxide and the treatment being carried out under such conditions that the quantity of dilute sulphurous acid condensed on the materials is so small, in relation to the amount of the materials, that substantially no flow of such dilute sulphurous acid occurs over the surfaces of the particles of the materials. The apparatus may consist of an autoclave for discontinuous treatment or of a tall column for continuous treatment. The proportion of sulphur dioxide may be 1-3 per cent, calculated on the dry material treated. In an example 100 kg. of eucalyptus wood chips (dry weight) containing 15 per cent of water are charged into a pressure cooker provided with a heat-insulating jacket, the air therein is partially exhausted and 2.5 kg. of gaseous sulphur dioxide is injected together with sufficient steam to increase the temperature to 100 DEG C. The mass is maintained at 100 DEG C. for 2-3 hours, during which time the water content of the chips increases to 40-50 per cent but no flow of condensate occurs over the chips. The pressure cooker is exhausted to remove the residual free sulphur dioxide, and the lignosulphonic acid formed during the treatment is neutralized and dissolved by the addition of black liquor from a previous cycle of operations. The mass is heated to 100 DEG C., drained and covered with an aqueous solution of caustic soda (110 g. per litre). Part of the caustic soda may be replaced by sodium sulphide. The mass is heated to 160-170 DEG C. for 1.2 hours, drained and washed. The black liquor thereby obtained is used for the neutralization of the next batch of hydrolized cellulosic material. The treated pulp may be bleached, e.g. by two or three treatments with chlorine in an acid medium followed by hypochlorite in an alkaline medium. Examples are given of the similar treatment of bagasse and chopped straw. The sulphur dioxide may be generated in situ in the cooker, e.g. by charging the cooker with aqueous solutions of sodium bisulphite and sulphuric acid.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1005824X | 1952-02-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB734216A true GB734216A (en) | 1955-07-27 |
Family
ID=9565170
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2946/53A Expired GB734216A (en) | 1952-02-15 | 1953-02-02 | Process for the treatment of ligno-cellulosic fibres |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE1005824B (en) |
FR (1) | FR1052900A (en) |
GB (1) | GB734216A (en) |
NL (1) | NL87584C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998049390A1 (en) * | 1997-04-28 | 1998-11-05 | Almeida Oliveira Baptista Joao | A wood delignification chemical process using ammonium magnesium bisulphite as the active reagent |
WO2013164598A1 (en) * | 2012-05-02 | 2013-11-07 | Innovia Films Limited | Process |
EP3901367A1 (en) * | 2020-04-20 | 2021-10-27 | Scitech-service OY | Method for prehydrolysis of lignocellulosic material |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA766073B (en) * | 1975-10-24 | 1977-09-28 | D Econimidis | Production of pulp |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE124556C (en) * | ||||
DE237081C (en) * | 1909-12-13 | |||
DE395119C (en) * | 1923-10-11 | 1924-05-14 | Carl G Schwalbe Dr | Process for the pretreatment of vegetable raw materials to facilitate the subsequent acidic or alkaline digestion |
DE484805C (en) * | 1924-11-02 | 1929-11-11 | Leopold Enge | Process for softening wood or similar vegetable fibers |
DE744868C (en) * | 1940-03-22 | 1944-01-27 | Dr Georg Jayme | Process for the production of low-pentosan cellulose from plant matter |
BE447209A (en) * | 1941-12-22 |
-
0
- NL NL87584D patent/NL87584C/xx active
-
1952
- 1952-02-15 FR FR1052900D patent/FR1052900A/en not_active Expired
-
1953
- 1953-02-02 GB GB2946/53A patent/GB734216A/en not_active Expired
- 1953-02-13 DE DES32188A patent/DE1005824B/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998049390A1 (en) * | 1997-04-28 | 1998-11-05 | Almeida Oliveira Baptista Joao | A wood delignification chemical process using ammonium magnesium bisulphite as the active reagent |
WO2013164598A1 (en) * | 2012-05-02 | 2013-11-07 | Innovia Films Limited | Process |
CN104321347A (en) * | 2012-05-02 | 2015-01-28 | 伊诺维亚薄膜有限公司 | Process |
JP2015517582A (en) * | 2012-05-02 | 2015-06-22 | イノヴィア フィルムズ リミテッド | Method |
US9493581B2 (en) | 2012-05-02 | 2016-11-15 | Innovia Films Limited | Process for the manufacture of viscose |
EP3901367A1 (en) * | 2020-04-20 | 2021-10-27 | Scitech-service OY | Method for prehydrolysis of lignocellulosic material |
WO2021214387A1 (en) * | 2020-04-20 | 2021-10-28 | Scitech-Service Oy | Method for prehydrolysis of lignocellulosic material |
Also Published As
Publication number | Publication date |
---|---|
NL87584C (en) | |
DE1005824B (en) | 1957-04-04 |
FR1052900A (en) | 1954-01-28 |
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