GB616304A - Cellulose ethers and the process for producing the same - Google Patents

Cellulose ethers and the process for producing the same

Info

Publication number
GB616304A
GB616304A GB14935/46A GB1493546A GB616304A GB 616304 A GB616304 A GB 616304A GB 14935/46 A GB14935/46 A GB 14935/46A GB 1493546 A GB1493546 A GB 1493546A GB 616304 A GB616304 A GB 616304A
Authority
GB
United Kingdom
Prior art keywords
alkali
cellulose
acid
hydrate
product
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
GB14935/46A
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.)
Sylvania Industrial Corp
Original Assignee
Sylvania Industrial Corp
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 Sylvania Industrial Corp filed Critical Sylvania Industrial Corp
Publication of GB616304A publication Critical patent/GB616304A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B11/00Preparation of cellulose ethers

Abstract

Cellulosic material is subjected in the presence of alkali to the action of an etherifying agent so as to form a hydrophilic cellulose ether and the reaction mixture is treated with an acid which neutralizes the alkali and removes free water by forming a salt hydrate which is stable at temperatures up to 35 DEG C. The major portion of the remaining water in the product may be removed by drying at a temperature below the decomposition temperature of the hydrate or by adding to the mixture an anhydrous salt similar to the hydrate produced by the neutralization. The amount of free water is thus at all times kept below the amount which causes gelling, which is usually about 25 per cent by weight of the cellulose, and the product is obtained in the form of dry free-flowing granules. The hydrophilic cellulose ether may be water-soluble or alkali-soluble. The cellulosic starting material may be wood-pulp, cotton linters, or a cellulosic conversion product such as regenerated cellulose or cellulose hydrate. The alkali used may be caustic soda or potash. The cellulose may be first converted into alkali cellulose which is then pressed to remove excess alkali solution and then treated with etherifying agent while still wet with the alkali. After draining off the alkali, the alkali cellulose may be pressed to 2.5 to 3.0 times the weight of the air-dry cellulose. The alkali-cellulose is then shredded and it may be aged. The etherifying agent may be dimethyl sulphate, methyl sodium sulphate, ethyl chloride, benzyl chloride, ethylene oxide, propylene oxide, a glycide, or a halohydrin. The temperature during etherification should not be allowed to rise above 70 DEG C. A gaseous etherifying agent may be used. After the etherification, the neutralizing acid may be added in solid or liquid form or as a concentrated aqueous solution. The acid used may be ortho-, pyro- or meta-phosphoric acid, glycero-phosphoric acid, arsenic acid, sulphurous acid, aluminium hydrogen sulphate, metantimonic acid or molybdic acid. The mixture of cellulose ether and hydrated salt is removed from the reaction vessel, spread in a thin layer and dried. The major portion of the remaining free water may be driven out while heating to a temperature lower than the decomposition of the hydrate, and the drying may be completed by allowing the temperature to rise gradually to 100 DEG C. If desired, the salt may be removed from the dried product by dissolving the product and dialyzing.
GB14935/46A 1945-05-19 1946-05-17 Cellulose ethers and the process for producing the same Expired GB616304A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US616304XA 1945-05-19 1945-05-19

Publications (1)

Publication Number Publication Date
GB616304A true GB616304A (en) 1949-01-19

Family

ID=22037052

Family Applications (1)

Application Number Title Priority Date Filing Date
GB14935/46A Expired GB616304A (en) 1945-05-19 1946-05-17 Cellulose ethers and the process for producing the same

Country Status (1)

Country Link
GB (1) GB616304A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2221419A1 (en) * 1973-03-14 1974-10-11 Modokemi Ab
EP1342733A1 (en) * 2002-03-04 2003-09-10 Shin-Etsu Chemical Co., Ltd. Low-substituted cellulose ether powder and production process thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2221419A1 (en) * 1973-03-14 1974-10-11 Modokemi Ab
EP1342733A1 (en) * 2002-03-04 2003-09-10 Shin-Etsu Chemical Co., Ltd. Low-substituted cellulose ether powder and production process thereof
US6849729B2 (en) 2002-03-04 2005-02-01 Shin-Etsu Chemical Co., Ltd. Low-substituted cellulose ether powder and production process thereof

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