GB274814A - Process and apparatus for the continuous manufacture of cellulose acetate - Google Patents

Process and apparatus for the continuous manufacture of cellulose acetate

Info

Publication number
GB274814A
GB274814A GB9500/27A GB950027A GB274814A GB 274814 A GB274814 A GB 274814A GB 9500/27 A GB9500/27 A GB 9500/27A GB 950027 A GB950027 A GB 950027A GB 274814 A GB274814 A GB 274814A
Authority
GB
United Kingdom
Prior art keywords
reagents
wall
carried
paddles
stirring
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
GB9500/27A
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.)
Chimique des Usines du Rhone
Original Assignee
Chimique des Usines du Rhone
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 Chimique des Usines du Rhone filed Critical Chimique des Usines du Rhone
Publication of GB274814A publication Critical patent/GB274814A/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
    • C08B17/00Apparatus for esterification or etherification of cellulose
    • C08B17/02Apparatus for esterification or etherification of cellulose for making organic esters of cellulose

Abstract

274,814. Soc. Chimique des Usines du Rh¶ne. July 26, 1926, [Convention date]. Continuous-discharge apparatus with moving containers.-Cellulose acetate is made by passing the reagents continuously through apparatus of small diameter compared with its length and rotating about an inclined axis. The temperature at different zones may be regulated by sprinkling the outside of the apparatus with hot or cold water. The diameter of the apparatus may be variable so as to modify the speed of the travel of the reagents at different parts of the apparatus, and material may be caused to accumulate at desired points by arranging perforated discs or continuous or discontinuous helicoidal partitions in the apparatus, and near these points, energetic stirring may be affected by means of straight or bent rods arranged radially or at some distance from the wall and carried by the wall near the inlet end, and in the second part of the apparatus where the mass is of a pasty consistency paddles may be employed. Baffles may be provided independent of the wall and carried by a central shaft, and these may be inclined to the axis of the apparatus to assist in causing the reagents to travel. The rods and paddles may be carried by a central shaft instead of by the wall and a heating or cooling fluid may be circulated through the stirring devices. Several of the inclined rotary apparatus may be arranged in conjunction, part of the process being carried out in each; their inclinations and rates of rotation may be different, and fresh reagents may be added at the various stages of the operation. The apparatus may consist of a tapered cylinder 1 Fig. 1, rotating about a slightly inclined axis, with sprays 8 directed upon its outer surface. Reagents are admitted at 5, 6, and 7 and the finished product is withdrawn at 9. In a modification, Fig. 2, stirring rods 10, paddles 11 and 13 and helicoidal paddles 12 are carried by the wall of the reaction chamber, and a disc 16 with a central opening causes an accumulation of material at one point. Baffles 14 and 15 inside the shell are provided for ensuring a regular advance. of the reaction mass. Specifications 231,837, [Class 2 (ii), Cellulose &c.], and 270,656 are referred to.
GB9500/27A 1926-07-26 1927-04-06 Process and apparatus for the continuous manufacture of cellulose acetate Expired GB274814A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR274814X 1926-07-26

Publications (1)

Publication Number Publication Date
GB274814A true GB274814A (en) 1928-07-05

Family

ID=8886243

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9500/27A Expired GB274814A (en) 1926-07-26 1927-04-06 Process and apparatus for the continuous manufacture of cellulose acetate

Country Status (1)

Country Link
GB (1) GB274814A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113550150A (en) * 2021-09-02 2021-10-26 浙江宝时美化工有限公司 Preparation method of compound organic silicon softening agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113550150A (en) * 2021-09-02 2021-10-26 浙江宝时美化工有限公司 Preparation method of compound organic silicon softening agent
CN113550150B (en) * 2021-09-02 2023-07-18 浙江宝时美化工有限公司 Preparation method of compound organic silicon softener

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