GB735481A - Improved cellulose products - Google Patents

Improved cellulose products

Info

Publication number
GB735481A
GB735481A GB8913/53A GB891353A GB735481A GB 735481 A GB735481 A GB 735481A GB 8913/53 A GB8913/53 A GB 8913/53A GB 891353 A GB891353 A GB 891353A GB 735481 A GB735481 A GB 735481A
Authority
GB
United Kingdom
Prior art keywords
pulp
polymer
cellulose
oxide
polyethylene oxide
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
GB8913/53A
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.)
Rayonier Inc
Original Assignee
Rayonier Inc
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 Rayonier Inc filed Critical Rayonier Inc
Publication of GB735481A publication Critical patent/GB735481A/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
    • C08B1/00Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
    • C08B1/08Alkali cellulose

Abstract

Cellulose pulp of high alpha-cellulose content is rendered more suitable for the production of cellulose derivatives, particularly cellulose acetate and cellulose xanthate, and for the subsequent production of rayon and allied products, by incorporating in it not more than 0.5 per cent, based on the dry weight of the pulp, of a non-ionic water-soluble polypropylene oxidepolyethylene oxide polymerization product containing at least one lipophilic polypropylene oxide radical derived from a water-insoluble polypropylene oxide and at least one hydrophilic polyethylene oxide radical. Refined pulp which still contains up to 0.15 per cent of residual natural resins may be treated. The presence of the polymerization product inhibits the adverse effect of the resins on the resistance to fatigue of tyre cord filaments made from viscose derived from such pulp. The presence of the polymer in the viscose also minimizes clogging and cratering of the spinnerets. Preferably the polymer is introduced into the cellulose pulp prior to the drying of the pulp sheets. Inactivation of the cellulose due to drying, particularly towards acetylating and other esterifying agents, is thereby minimized. The polymer may be incorporated in the wet pulp before sheet formation or in the sheet at any stage prior to completion of the drying. It may be applied as an aqueous solution to refined wood pulp on the sheet-forming machine by means of sprays or a rotating roll. An aqueous solution of the polymer may be applied to already dried wood-pulp sheets in order to improve their reactivity. The non-ionic polymer may be a bis-polyethenoxy polypropylene oxide and it may be derived from a polypropylene oxide which has a specific viscosity of at least 0.129 in a 4 g./100 ml. benzene solution at 25 DEG C., which is water-insoluble and contains at least 13 propenoxy groups and has two terminal hydroxyl groups. The hydrogen atoms in these hydroxyl groups are substituted by polyethylene oxide chains of about equal length in order to render the final compound water-soluble. A proportion of 40-90 per cent of ethylene oxide in the final compound may be required in order that the compound may be water-soluble. The polymer may also be a halopolypropenoxy polyethylene oxide derived from a long chain polypropylene oxide having a specific viscosity of at least 0.129 and having one terminal halogen atom and one terminal hydroxyl group, by substitution of the hydrogen in the hydroxyl by a polyethylene oxide chain. The polymer may also be an alkoxy (or phenoxy) polypropenoxy polyethylene oxide or it may be a bis-polypropenoxy polyethylene oxide. In an example purified cellulose pulp containing 0.1 per cent of ether-extractable resin is impregnated with 0.1 per cent of a polypropylene oxide-polyethylene oxide polymerization product and converted into alkali cellulose and then into viscose. The viscose is extruded into dilute sulphuric acid containing sodium and zinc sulphates, without cratering of the spinnerets. Tyre cords made from the filaments so produced have an improved fatigue life compared with that of cords made from filaments which have been produced in the absence of the polymerization product. If desired, a polymer may be used which contains more than one polyalkenoxy chain, each of which contains as component parts one polypropenoxy chain and one polyethenoxy chain. A polypropylene oxide may be polymerized in presence of a small proportion of a polyhydric alcohol of relatively small molecular weight to provide terminal groups, and the product may then be converted into a multi-chain polypropylene oxide-polyethylene oxide polymerization product.
GB8913/53A 1952-05-24 1953-03-31 Improved cellulose products Expired GB735481A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US735481XA 1952-05-24 1952-05-24

Publications (1)

Publication Number Publication Date
GB735481A true GB735481A (en) 1955-08-24

Family

ID=22114354

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8913/53A Expired GB735481A (en) 1952-05-24 1953-03-31 Improved cellulose products

Country Status (1)

Country Link
GB (1) GB735481A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1110511B (en) * 1957-03-25 1961-07-06 Buckeye Cellulose Corp Wood pulp obtained by the pre-hydrolysis sulphate process for the production of cellulose esters or regenerated cellulose
DE1176989B (en) * 1957-05-16 1964-08-27 Buckeye Cellulose Corp Use of a surface-active agent as an additive to wood pulp
WO2007144824A2 (en) * 2006-06-14 2007-12-21 Sappi Manufacturing (Pty) Ltd Pulp reactivity enhancement
CN104451932A (en) * 2014-12-16 2015-03-25 广东中烟工业有限责任公司 Cellulose acetate fiber silk yarn and preparation method thereof
CN104532378A (en) * 2014-12-16 2015-04-22 广东中烟工业有限责任公司 Method for improving spinnability of acetate fibers
CN104831395A (en) * 2014-12-16 2015-08-12 广东中烟工业有限责任公司 Application of PEO-PPO-PEO segmented ternary copolymer in preparation of cellulose acetate tow
CN113840960A (en) * 2018-11-30 2021-12-24 索理思科技开曼公司 Pulp mixture

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1110511B (en) * 1957-03-25 1961-07-06 Buckeye Cellulose Corp Wood pulp obtained by the pre-hydrolysis sulphate process for the production of cellulose esters or regenerated cellulose
DE1176989B (en) * 1957-05-16 1964-08-27 Buckeye Cellulose Corp Use of a surface-active agent as an additive to wood pulp
WO2007144824A2 (en) * 2006-06-14 2007-12-21 Sappi Manufacturing (Pty) Ltd Pulp reactivity enhancement
WO2007144824A3 (en) * 2006-06-14 2008-04-10 Sappi Mfg Pty Ltd Pulp reactivity enhancement
CN104292342A (en) * 2006-06-14 2015-01-21 塞皮制造(Pty)有限公司 Method for preparing alkali cellulose
CN104451932A (en) * 2014-12-16 2015-03-25 广东中烟工业有限责任公司 Cellulose acetate fiber silk yarn and preparation method thereof
CN104532378A (en) * 2014-12-16 2015-04-22 广东中烟工业有限责任公司 Method for improving spinnability of acetate fibers
CN104831395A (en) * 2014-12-16 2015-08-12 广东中烟工业有限责任公司 Application of PEO-PPO-PEO segmented ternary copolymer in preparation of cellulose acetate tow
CN104451932B (en) * 2014-12-16 2017-02-22 广东中烟工业有限责任公司 Cellulose acetate fiber silk yarn and preparation method thereof
CN113840960A (en) * 2018-11-30 2021-12-24 索理思科技开曼公司 Pulp mixture
CN113840960B (en) * 2018-11-30 2023-09-12 索理思科技开曼公司 pulp mixture

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