US2622273A - Method and means for precipitating cellulose acetate - Google Patents

Method and means for precipitating cellulose acetate Download PDF

Info

Publication number
US2622273A
US2622273A US37030A US3703048A US2622273A US 2622273 A US2622273 A US 2622273A US 37030 A US37030 A US 37030A US 3703048 A US3703048 A US 3703048A US 2622273 A US2622273 A US 2622273A
Authority
US
United States
Prior art keywords
nozzle
dope
precipitating
cellulose acetate
slot
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 - Lifetime
Application number
US37030A
Inventor
George T Detwiler
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.)
Akzo Nobel UK PLC
Original Assignee
American Viscose 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 American Viscose Corp filed Critical American Viscose Corp
Priority to US37030A priority Critical patent/US2622273A/en
Application granted granted Critical
Publication of US2622273A publication Critical patent/US2622273A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B3/00Preparation of cellulose esters of organic acids
    • C08B3/22Post-esterification treatments, including purification
    • C08B3/26Isolation of the cellulose ester
    • C08B3/28Isolation of the cellulose ester by precipitation

Definitions

  • This invention relates to a method and apparatus for precipitating cellulose acetate .in the form of thirusubstantially fiat, porous particles.
  • the acetylation of cellulose by one method results in a viscous solution of cellulose acetate in acetic acid.
  • cellulose acetate is further processed to produce films, filaments, and otherpmducts, it is usually separated from the acetic acid solvent by precipitation and washing. This precipitation is brought about by diluting the solvent with water, in one case by adding water slowly to the so-called acid dope; in another case by running the dope into a bath of water or very dilute acid.
  • This and other objects of the invention are accomplished by extruding the cellulose acetate into the precipitating bath through an elongated slot, in the form of a substantially flat stream and contacting the fiat stream with a cutting means so positioned that the cutting edge thereof strikes against the face of the extruding stream to separate it into flat sections.
  • Fig. 1 is an inverted plan of the elongated extrusion slot and knife employed to separate the stream;
  • Fig. 2 is a vertical section through apparatus for precipitating cellulose acetate using an elongated extrusion slot in accordance with the present invention.
  • the precipitating bath is contained in a precipitating chamber 5 and the cellulose acetate dope is supplied thereto from a supply tank 4, preferably supported by a bracket 6 on the chamber 5.
  • the supply tank 4 has a removable cover (not shown) to permit charging thereof and an air pipe (not shown) to supply compressed air thereto after charging.
  • From the tank 4 the supply pipe 1 extends down int chamber 5.
  • the lower end of pipe 1 receives a cap 8 containing an extrusion elongated slot 9 and forming an ex- 'trusion nozzle.
  • Cooperating with the nozzle is a knife 10 keyed to the lower end of avertical shaft "H journaled in bearing brackets 12 on the tank 4 and pipe I.
  • the upper end of the shaft M carries-a pulley l3 connected by a pulley H "to a pulley 1'5 on the shaft 16 journaled in a "bearing 11 ina bridge 8 supported by the chamleer-5.
  • the knife I0 is rotated at a predetermined rate so that its cutting edge intermittently strikes against the face of the fiat stream of dope leaving the slot 9 at regular intervals and cuts it into flat sections.
  • the knife striking against the face of the flat stream tends to attenuate and draw out the individual sections to produce thin, substantially flat particles 20 of irregular contour.
  • the rotation of the blade [9 agitates the precipitating bath and carries away the particles as they are formed, and also carries away the acid or other products of the precipitating reaction preventing local concentration of these around the nozzle and knife.
  • the precipitating bath is maintained at a level well above the slot 9.
  • the rate at which the shaft H is driven to give the size of particle desired may be readily calculated from the dimensions of the blade I!) and the extrusion flow rate, in turn dependent upon the air pressure, viscosity of the dope, and the area of the slot.
  • the elongated slot may have a length of from to 1 and a width of from to A".
  • a slot having the dimensions .065" x .750" (area equals .0489 sq. in.) is entirely satisfactory.
  • the attenuated sections of dope are set in the form of thin, substantially flat cellulose acetate particles which are characterized by a rough, crepeover a period of forty minutes, and the bath was. then tested for acetic acid, the bath was foundv to contain 25.92% acetic acid and, after four washings with plain water, the particles con- 2,c22,27s 'i 1 j tained only 0.04% acetic acid. This contrasts with the results obtained when a cellulose acetate dope of the same concentration was extruded into a precipitating liquid of the same composition through an orifice of circular cross-section having an area of 0.0487 sq. in.
  • the precipitating liquid was found to contain only 20.32% acetic acid and, after four washings, the smooth, dense pellets thus obtained still contained 0.11% acetic acid.
  • the thin, substantially flat particles obtained by extruding through the elongated slot are fluffier and of very low density as compared to the pellets obtained using a round extrusion orifice. It required only 25.3 grams of such cellulose acetate particles to fill a 4 ounce container, whereas it required 36.8 grams of cellulose acetate pellets produced by extruding the dope through an oriflce of circular cross-section to fill a container of the same capacity.
  • Apparatus for precipitating cellulose acetate in the form of thin, substantially flat porous particles having rough crepe-like surfaces from acid dope formed by acetylation of cellulose comprising, in combination, a nozzle, an elongated extrusion slot having a length of from one-half to one and one-half inches, and a width of from one-eighth to one-fourth inch in the nozzle, a chamber containing a bath of dilute aqueous precipitating liquid, means for supporting the nozzle below the surface of the bath, means for forcing dope through the elongated slot in the nozzle into the liquid, a cutting means rotatably supported adjacent the nozzle and positioned so that when it is rotated the cutting edge thereof strikes against the face of the flat stream of dope extruded through the slot, and means for continuously agitating the precipitating liquid.
  • Method of precipitating cellulose acetate in the form of thin, substantially fiat porous particles having rough crepe-like surfaces from acid dope formed by acetylation of cellulose which comprises extruding a stream of the acid dope of substantially flat cross-section below the surface of a bath of dilute aqueous precipitating liquid, and simultaneously contacting the face of the stream of dope with a cutting means to cut it into substantially flat sections and agitating the liquid, said extrusion and cutting rates being in timed relation to produce sections of substantially uniform length, and the agitating rate also being in timed relation to carry away the sections and the acid formed by'the precipitation and prevent local concentration of the products of the precipitation.

Description

Dec. 23, 1952 e. T. DETWILER METHOD AND MEANS FOR PRECIPITATING CELLULOSE ACETATE Filed July 5, 1948 INVENTOR. GEORGE r DETW'I-LER Patented Dec. 23, 1952 UNITED STATES PATENT OFFICE 'METHODANI) FOR PRECIPITATING CELLUEOSE ACETATE George T. Detwiler, Chester, 'Pa., "assignor to American Viscose Corporation, Wilmington, Del., a corporation of Delaware Application July 3, 1948;"S'erialNo. 37,030
2 Claims.
1 This invention relates to a method and apparatus for precipitating cellulose acetate .in the form of thirusubstantially fiat, porous particles.
The acetylation of cellulose by one method results ina viscous solution of cellulose acetate in acetic acid. Before this cellulose acetateis further processed to produce films, filaments, and otherpmducts, it is usually separated from the acetic acid solvent by precipitation and washing. This precipitation is brought about by diluting the solvent with water, in one case by adding water slowly to the so-called acid dope; in another case by running the dope into a bath of water or very dilute acid.
It has been proposed to extrude the acid dope into the precipitating bath through an orifice of circular cross-section and shear the rod-like stream of extruding dope into segments of uniform'size. That procedure'results in the production of aprecipitate in th'e form of comparatively lthick, smooth, dense pellets which are not readily penetrated by fluids and require a considerable time for washing, drying and dissolving in the spinning or casting solvent.
It is a primary object of the present invention to produce a cellulose acetate precipitate in a faster washing, faster drying and faster dissolving form. This and other objects of the invention are accomplished by extruding the cellulose acetate into the precipitating bath through an elongated slot, in the form of a substantially flat stream and contacting the fiat stream with a cutting means so positioned that the cutting edge thereof strikes against the face of the extruding stream to separate it into flat sections.
The invention will be readily understood when read in the light of the following description having reference to the drawing, in which,
Fig. 1 is an inverted plan of the elongated extrusion slot and knife employed to separate the stream; and
Fig. 2 is a vertical section through apparatus for precipitating cellulose acetate using an elongated extrusion slot in accordance with the present invention.
The precipitating bath is contained in a precipitating chamber 5 and the cellulose acetate dope is supplied thereto from a supply tank 4, preferably supported by a bracket 6 on the chamber 5. The supply tank 4 has a removable cover (not shown) to permit charging thereof and an air pipe (not shown) to supply compressed air thereto after charging. From the tank 4 the supply pipe 1 extends down int chamber 5. The lower end of pipe 1 receives a cap 8 containing an extrusion elongated slot 9 and forming an ex- 'trusion nozzle. Cooperating with the nozzle is a knife 10 keyed to the lower end of avertical shaft "H journaled in bearing brackets 12 on the tank 4 and pipe I. The upper end of the shaft M carries-a pulley l3 connected by a pulley H "to a pulley 1'5 on the shaft 16 journaled in a "bearing 11 ina bridge 8 supported by the chamleer-5. The'upper end of the shaft I6 issuitably journaled and driven by any desired source of power while -thelower end is k eyed to an'agitat'or In operation, water or diluteacid is-supp'lied to the chamber 5 while cellulose acetate acid dope is charged into the tank 4. Compressed air is introduced into chamberl, and forces thedope through the pipe '1 and out=thr0ugh the extrusion slot 9.
It is obvious that a pump could be used for transferring the acid dope from the chamber 4 to the'pipe land slot'9 without changing the-nature of this invention.
' The precipitating liquid in the chamber 5 contacts the flat stream of acid dope leaving the slot 9 and'precipitates the-cellulose acetate.
At the same time, i. e. simultaneously with extrusion of the dope, the knife I0 is rotated at a predetermined rate so that its cutting edge intermittently strikes against the face of the fiat stream of dope leaving the slot 9 at regular intervals and cuts it into flat sections. The knife striking against the face of the flat stream tends to attenuate and draw out the individual sections to produce thin, substantially flat particles 20 of irregular contour. The rotation of the blade [9 agitates the precipitating bath and carries away the particles as they are formed, and also carries away the acid or other products of the precipitating reaction preventing local concentration of these around the nozzle and knife. The precipitating bath is maintained at a level well above the slot 9.
Obviously the rate at which the shaft H is driven to give the size of particle desired may be readily calculated from the dimensions of the blade I!) and the extrusion flow rate, in turn dependent upon the air pressure, viscosity of the dope, and the area of the slot. The elongated slot may have a length of from to 1 and a width of from to A". A slot having the dimensions .065" x .750" (area equals .0489 sq. in.) is entirely satisfactory.
By the action of the precipitating liquid, the attenuated sections of dope are set in the form of thin, substantially flat cellulose acetate particles which are characterized by a rough, crepeover a period of forty minutes, and the bath was. then tested for acetic acid, the bath was foundv to contain 25.92% acetic acid and, after four washings with plain water, the particles con- 2,c22,27s 'i 1 j tained only 0.04% acetic acid. This contrasts with the results obtained when a cellulose acetate dope of the same concentration was extruded into a precipitating liquid of the same composition through an orifice of circular cross-section having an area of 0.0487 sq. in. In the latterv case, the precipitating liquid was found to contain only 20.32% acetic acid and, after four washings, the smooth, dense pellets thus obtained still contained 0.11% acetic acid. The thin, substantially flat particles obtained by extruding through the elongated slot are fluffier and of very low density as compared to the pellets obtained using a round extrusion orifice. It required only 25.3 grams of such cellulose acetate particles to fill a 4 ounce container, whereas it required 36.8 grams of cellulose acetate pellets produced by extruding the dope through an oriflce of circular cross-section to fill a container of the same capacity.
some variations and modifications may be made in practicing the invention without departing from the spirit and scope thereof, and the invention is not to be limited therefor except as defined in the appended claims.
I claim:
1. Apparatus for precipitating cellulose acetate in the form of thin, substantially flat porous particles having rough crepe-like surfaces from acid dope formed by acetylation of cellulose comprising, in combination, a nozzle, an elongated extrusion slot having a length of from one-half to one and one-half inches, and a width of from one-eighth to one-fourth inch in the nozzle, a chamber containing a bath of dilute aqueous precipitating liquid, means for supporting the nozzle below the surface of the bath, means for forcing dope through the elongated slot in the nozzle into the liquid, a cutting means rotatably supported adjacent the nozzle and positioned so that when it is rotated the cutting edge thereof strikes against the face of the flat stream of dope extruded through the slot, and means for continuously agitating the precipitating liquid.
'2. Method of precipitating cellulose acetate in the form of thin, substantially fiat porous particles having rough crepe-like surfaces from acid dope formed by acetylation of cellulose which comprises extruding a stream of the acid dope of substantially flat cross-section below the surface of a bath of dilute aqueous precipitating liquid, and simultaneously contacting the face of the stream of dope with a cutting means to cut it into substantially flat sections and agitating the liquid, said extrusion and cutting rates being in timed relation to produce sections of substantially uniform length, and the agitating rate also being in timed relation to carry away the sections and the acid formed by'the precipitation and prevent local concentration of the products of the precipitation.
' GEORGE T. DETWILER.
REFERENCES CITED The following references are of record in th file of this patent:
UNITED STATES PATENTS 9

Claims (1)

1. APPARATUS FOR PRECIPITATING CELLULOSE ACETATE IN THE FORM OF THIN, SUBSTANTIALLY FLAT POROUS PARTICLES HAVING ROUGH CREPE-LIKE SURFACES FROM ACID DOPE FORMED BY ACETYLATION OF CELLULOSE COMPRISING, IN COMBINATION, A NOZZLE, AN ELONGATED EXTRUSION SLOT HAVING A LENGTH OF FROM ONE-HALF TO ONE AND ONE-HALF INCHES, AND A WIDTH OF FROM ONE-EIGHT TO ONE-FOURTH INCH IN THE NOZZLE, A CHAMBER CONTAINING A BATH OF DILUTE AQUEOUS PRECIPITATING LIQUID, MEANS FOR SUPPORTING THE NOZZLE BELOW THE SURFACE OF THE BATH, MEANS FOR FORCING DOPE THROUGH THE ELONGATED SLOT IN THE NOZZLE INTO THE LIQUID, A CUTTING MEANS ROTATABLY SUPPORTED ADJACENT THE NOZZLE AND POSITIONED SO THAT WHEN IT IS ROTATED THE CUTTING EDGE THEREOF STRIKES AGAINST THE FACE OF THE FLAT STREAM OF DOPE EXTRUDED THROUGH THE SLOT, AND MEANS FOR CONTINUOUSLY AGITATING THE PRECIPITATING LIQUID.
US37030A 1948-07-03 1948-07-03 Method and means for precipitating cellulose acetate Expired - Lifetime US2622273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US37030A US2622273A (en) 1948-07-03 1948-07-03 Method and means for precipitating cellulose acetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US37030A US2622273A (en) 1948-07-03 1948-07-03 Method and means for precipitating cellulose acetate

Publications (1)

Publication Number Publication Date
US2622273A true US2622273A (en) 1952-12-23

Family

ID=21892063

Family Applications (1)

Application Number Title Priority Date Filing Date
US37030A Expired - Lifetime US2622273A (en) 1948-07-03 1948-07-03 Method and means for precipitating cellulose acetate

Country Status (1)

Country Link
US (1) US2622273A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2925413A (en) * 1954-03-02 1960-02-16 British Celanese Manufacture of organic substances of very high molecular weight
US2925414A (en) * 1954-03-11 1960-02-16 British Celanese Manufacture of very high molecular weight organic substances
US2925412A (en) * 1953-03-24 1960-02-16 British Celanese Manufacture of organic substances of very high molecular weight
US3143918A (en) * 1961-06-28 1964-08-11 Makay Nicolas De Powder forming apparatus
US3393425A (en) * 1965-06-16 1968-07-23 Baker Perkins Inc Apparatus for forming and cooling pellets
US3464086A (en) * 1966-11-25 1969-09-02 Gen Mills Inc Fxtrusion apparatus
US3493992A (en) * 1965-02-18 1970-02-10 Rhodiatoce Spa Apparatus for the precipitation of cellulose esters
US3723035A (en) * 1970-10-29 1973-03-27 Fuller Co H Apparatus for forming hot melt adhesives into a readily packageable form
US3961007A (en) * 1973-10-23 1976-06-01 E & J Gallo Winery Continuous process for making fibrous cellulose acetate filter material
US4737407A (en) * 1986-03-10 1988-04-12 Essex Composite Systems Thermoset plastic pellets and method and apparatus for making such pellets
US4853270A (en) * 1988-06-27 1989-08-01 Essex Specialty Products, Inc. Knee blocker for automotive application
US5488104A (en) * 1994-06-30 1996-01-30 The Dow Chemical Company Process for comminuting cellulose ethers

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1350722A (en) * 1920-08-24 Daniel e
US1979762A (en) * 1930-02-12 1934-11-06 Fiberloid Corp Method of finishing sheet pyroxylin
US2021837A (en) * 1933-10-31 1935-11-19 Viscose Co Method and apparatus for precipitating cellulose acetate
US2408627A (en) * 1943-10-11 1946-10-01 Lee B Green Apparatus for extruding

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1350722A (en) * 1920-08-24 Daniel e
US1979762A (en) * 1930-02-12 1934-11-06 Fiberloid Corp Method of finishing sheet pyroxylin
US2021837A (en) * 1933-10-31 1935-11-19 Viscose Co Method and apparatus for precipitating cellulose acetate
US2408627A (en) * 1943-10-11 1946-10-01 Lee B Green Apparatus for extruding

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2925412A (en) * 1953-03-24 1960-02-16 British Celanese Manufacture of organic substances of very high molecular weight
US2925413A (en) * 1954-03-02 1960-02-16 British Celanese Manufacture of organic substances of very high molecular weight
US2925414A (en) * 1954-03-11 1960-02-16 British Celanese Manufacture of very high molecular weight organic substances
US3143918A (en) * 1961-06-28 1964-08-11 Makay Nicolas De Powder forming apparatus
US3493992A (en) * 1965-02-18 1970-02-10 Rhodiatoce Spa Apparatus for the precipitation of cellulose esters
US3393425A (en) * 1965-06-16 1968-07-23 Baker Perkins Inc Apparatus for forming and cooling pellets
US3464086A (en) * 1966-11-25 1969-09-02 Gen Mills Inc Fxtrusion apparatus
US3723035A (en) * 1970-10-29 1973-03-27 Fuller Co H Apparatus for forming hot melt adhesives into a readily packageable form
US3961007A (en) * 1973-10-23 1976-06-01 E & J Gallo Winery Continuous process for making fibrous cellulose acetate filter material
US4737407A (en) * 1986-03-10 1988-04-12 Essex Composite Systems Thermoset plastic pellets and method and apparatus for making such pellets
US4853270A (en) * 1988-06-27 1989-08-01 Essex Specialty Products, Inc. Knee blocker for automotive application
US5488104A (en) * 1994-06-30 1996-01-30 The Dow Chemical Company Process for comminuting cellulose ethers

Similar Documents

Publication Publication Date Title
US2622273A (en) Method and means for precipitating cellulose acetate
US2021837A (en) Method and apparatus for precipitating cellulose acetate
SE425089B (en) PROCEDURE FOR PREPARING WATER SOLUTIONS OF POLYMERS
US2814851A (en) Keratin treating process and products thereof
US2224355A (en) Process of dissolving solid substances in liquids
US2573949A (en) Dissolving of polymers
US3961007A (en) Continuous process for making fibrous cellulose acetate filter material
US2210116A (en) Manufacture of artificial materials
US2875473A (en) Process of forming solid particulate hydroxyethoxycellulose
JP2666137B2 (en) Sheet forming method
US3136644A (en) Regenerated cellulose shaped articles and process
US2114275A (en) Process for producing foam from aqueous dispersions of rubber
US2558037A (en) Viscose production
US2962766A (en) Process of producing cellulose film using a flowing coagulating bath
US2239753A (en) Precipitation of cellulose compounds
US2359749A (en) Manufacture of synthetic yarns and the like
US2925412A (en) Manufacture of organic substances of very high molecular weight
US2536094A (en) Process for spinning artificial fibers
US2790698A (en) Process of removing impurities from fresh spun polyacrylonitrile gel filaments by directing inert gas bubbles against the filaments
US2939177A (en) Process of cutting partially coagulated esters of cellulose into short lengths
US2647114A (en) Method for making readily filterable viscose
US2403251A (en) Production of fibers from proteins
US2079313A (en) Method for making alkali-cellulose and products therefrom
US2287897A (en) Manufacture of organic derivatives of cellulose materials
US2814550A (en) High viscosity saline coagulants for latexes