US1937225A - Mechanism for and method of producing cellulose tubing - Google Patents

Mechanism for and method of producing cellulose tubing Download PDF

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Publication number
US1937225A
US1937225A US498497A US49849730A US1937225A US 1937225 A US1937225 A US 1937225A US 498497 A US498497 A US 498497A US 49849730 A US49849730 A US 49849730A US 1937225 A US1937225 A US 1937225A
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tubing
bath
rollers
gas
regenerating
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US498497A
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Alfred G Hewitt
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Visking Corp
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Visking Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/919Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils

Definitions

  • Theinvention relates to mechanism for and a method of producing cellulose tubing, and a primary object of the invention is to provide apparatus for and a method of producing such tubing efficiently so that there will be a loss thereof due to punctures, etc., made in it to permit the escape of gas evolved during the chemical reactions which take place.
  • Cellulose tubing is formed from cellulose which may be obtained by practicing the method briefly described in U. S. Letters Patent granted to 1 William F. Henderson and Harold E. Dietrich, December 28, 1926, No. 1,612,508.
  • the viscose is extruded through an annular orifice and is subjected to coagulating and regenerating baths, after which the tubing is washed in water.
  • the washed tubing is then treated with a hygroscopic agent and dried.
  • present invention comprises a tank holding aregenerating bath, the tubing being trained over a plurality of rollers, both above and in the bath.
  • the rollers above the bath are spaced a conr 5 0 siderable distance therefrom'so that long leads of the tubing reach from the bath to these rollers.
  • These leads of tubing accommodate a relatively large quantity of gas and, therefore, it becomes unnecessary to puncture the tubingat frequent .55 intervals.
  • the tubing so that gas will accumulate in all of the leads thereof extending from the regenerating bath to the rollers mounted above it, the acid content of the bath is reduced below that, which has heretofore been the general practice.
  • the bath is acidified to such an extent that the conversion-from viscose into cellulose takes place at a rate which causes the gas to collect in the leads above the bath in substantially equal quantities. Then it only becomes necessary to puncture the tubing at relatively long intervals.
  • Figure 1 is a central vertical section taken through apparatus which embodies the invention.
  • Fig. 2 is an enlarged central vertical section through extruding apparatus which forms part of theapparatus shown in Fig. 1.
  • the reference character 10 designates generally apparatus for extruding viscose. through an annular orifice 11 (see Fig. 2). Briefly, the viscose is introduced into an annular chamber 12 and is extruded through the annular orifice 11 into a coagulating bath 13 and thence over rollers 14 and 15 into a regenerating bath 16. From the bath 16, the tubing is led through a series of tanks 17, 18, 19 and 20.
  • the tank 17 contains a water which is acidified by the acid car rledover from the bath 16 to the tubing.
  • Thetanks 18 and 19 preferably contain running water in which the tubing is thoroughly washed.
  • the tank 20 contains. an aqueous solution of some softening agent, preferably glycerine. tubing has been treated with the softening agent, it is dried in suitable apparatus (not shown) after which the tubing is ready for use.
  • the tubing which is indicated by the reference character 22, is trained around a plurality of idler rollers 23 in the bottom of the bath l6 and is also trained around a plurality of rollers 24 mounted above the bath 16, the arrangement being such that relatively long leads of the tub- After the ing extend from the surface of the bath to the or longer'than the lengths of tubing extending from the surface of the bath to the rollers 23 so that relatively large quantities of gaseous byproducts may accumulate in, the leads of tubing above the bath.
  • the tubing passing through the regenerating bath has been distended to an undesirable degree by the evolved gases resulting from the regenerating operation,
  • the tubing may be slit before it passes into the- It has been common practice heretofore to employ a regenerating bath which consisted of an aqueous solution comprising 4 to 6% of sulfuric acid and a percentage of sodium sulfate which accumulated in the bath.
  • the acid content of the bath is preferably reduced to such an extent that the conversion'of viscose into cellulose is retarded, the conversion being preferably at a rate which permits'the gas to accumulate in substantially equal quantities in the several leads of tubing extending from the surface of the bath 16 to the rollers 24.
  • gas also accumulate s in those portions of the tubing submerged in the regenerating bath.
  • the lengths of tubing extending between the rollers 23 and 24 can hold large quantities of gas and if this gas is evenly distributed through these lengths all the lengths will hold a maximum quantity of the gas before it becomes necessary to puncture the tubing. Then when the tubing is punctured the puncture passes over the rollers 23 and 24 so that the gas in each length may escape.
  • the regeneratlng bath is about three feet deep and if the rollers 24 are spaced about seven feet above the bath, the tubing may be punctured only at infrequent intervals.
  • the rollers 24 may be placed higher above the bath if it is so desired, but this distance is determined largely by the accessibility of the rollers to the operator when the tubing is being threaded through the apparatus.
  • the rollers should be at least two feet abovethe surfene or the bath.
  • a method of forming cellulose tubing which method comprises extruding viscose through an annular orifice to form seamless tubing thereof, and passing said seamless tubing through a rel atively weal; regenerating bath a plurality of times in such manner that the gas evolved during can the regenerating operation will collect in substan- .tially equal quantities in a plurality of long lengths of the tubing extending above the bath.
  • a method of forming cellulose tubing which method comprises extruding viscose through an annular orifice to form seamless tubing thereof, and passing said seamless tubing through a regenerating bath a plurality of times in such manner that the gas evolved during the regenerating operation will collect in approximately equal quantities in a plurality of long lengths 1 of the tubing extending above the bath.

Description

Nov. 28, 1933-. A, H 1,937,225
MECHANISM FOR AND METHOD OF PRODUCING CELLULQSE TUBING Filed Nov. 26, 1930 Patented Nov. 28, 1933 UNITED STATES MECHANISM FOR AND METHOD or PRO- DUCINGCELLULOSE 'ruame Alfred G. Hewitt, Chicago, Ill.,- assignor to 'l he Visking' Corporation, Chicago, Ill., a. corporation of Virginia Application November 26, 1930 Serial No. 498,497
3 Claims. (01. 18-8) Theinvention relates to mechanism for and a method of producing cellulose tubing, and a primary object of the invention is to provide apparatus for and a method of producing such tubing efficiently so that there will be a loss thereof due to punctures, etc., made in it to permit the escape of gas evolved during the chemical reactions which take place.
Cellulose tubing is formed from cellulose which may be obtained by practicing the method briefly described in U. S. Letters Patent granted to 1 William F. Henderson and Harold E. Dietrich, December 28, 1926, No. 1,612,508. The viscose is extruded through an annular orifice and is subjected to coagulating and regenerating baths, after which the tubing is washed in water. The washed tubing is then treated with a hygroscopic agent and dried.
In the conversion of viscose back into cellulose a considerable quantity of gaseous by-products is evolved. In the'formation of thread and film from viscose, this becomes a difliculty only in so far as bubbles of gas are entrapped within the walls of the product and is ordinarily avoided by retarding the conversion in such manner that the gaseous by-products will escape as rapidly as they are evolved. This same difliculty is experiencedin the formation of seamless tubing from viscose and, to some extent, is overcome in so a like manner. However, another difllculty from these gaseous by-products is experienced. The evolved gas is released to the inside-of the tubing and cannot escape without breaking the wall of the tube. Each such rupture or puncture in the wall of the tube causes a loss of tubing, and for this reason it is highly desnable that these punctures be made as infrequently as is possible.
It has been the practice to puncture the tubing above the regenerating bath to permit the escape -01 evolved gas from the interior of the tubing. This method would be'quite satisfactory but for the fact that the time between punctures or ruptures is too short, or, in other words, the loss is entirely too great.
present invention comprises a tank holding aregenerating bath, the tubing being trained over a plurality of rollers, both above and in the bath. The rollers above the bath are spaced a conr 5 0 siderable distance therefrom'so that long leads of the tubing reach from the bath to these rollers. These leads of tubing accommodate a relatively large quantity of gas and, therefore, it becomes unnecessary to puncture the tubingat frequent .55 intervals. To retard the formation of gas in Apparatus embodying a preferred form of the rollers 24.
the tubing so that gas will accumulate in all of the leads thereof extending from the regenerating bath to the rollers mounted above it, the acid content of the bath is reduced below that, which has heretofore been the general practice. The bath is acidified to such an extent that the conversion-from viscose into cellulose takes place at a rate which causes the gas to collect in the leads above the bath in substantially equal quantities. Then it only becomes necessary to puncture the tubing at relatively long intervals.
Other objects and advantages of the invention will become apparent as the following detailed description progresses, reference being had to the accompanying drawing, wherein:--
Figure 1 is a central vertical section taken through apparatus which embodies the invention, and
Fig. 2 is an enlarged central vertical section through extruding apparatus which forms part of theapparatus shown in Fig. 1.
Referring to the drawing wherein a preferred embodiment of the invention is illustrated, the reference character 10 designates generally apparatus for extruding viscose. through an annular orifice 11 (see Fig. 2). Briefly, the viscose is introduced into an annular chamber 12 and is extruded through the annular orifice 11 into a coagulating bath 13 and thence over rollers 14 and 15 into a regenerating bath 16. From the bath 16, the tubing is led through a series of tanks 17, 18, 19 and 20. The tank 17 contains a water which is acidified by the acid car rledover from the bath 16 to the tubing. Thetanks 18 and 19 preferably contain running water in which the tubing is thoroughly washed. The tank 20 contains. an aqueous solution of some softening agent, preferably glycerine. tubing has been treated with the softening agent, it is dried in suitable apparatus (not shown) after which the tubing is ready for use.
The tubing, which is indicated by the reference character 22, is trained around a plurality of idler rollers 23 in the bottom of the bath l6 and is also trained around a plurality of rollers 24 mounted above the bath 16, the arrangement being such that relatively long leads of the tub- After the ing extend from the surface of the bath to the or longer'than the lengths of tubing extending from the surface of the bath to the rollers 23 so that relatively large quantities of gaseous byproducts may accumulate in, the leads of tubing above the bath. Obviously, when the tubing passing through the regenerating bath has been distended to an undesirable degree by the evolved gases resulting from the regenerating operation,
the tubing may be slit before it passes into the- It has been common practice heretofore to employ a regenerating bath which consisted of an aqueous solution comprising 4 to 6% of sulfuric acid and a percentage of sodium sulfate which accumulated in the bath. In practicing the present invention, the acid content of the bath is preferably reduced to such an extent that the conversion'of viscose into cellulose is retarded, the conversion being preferably at a rate which permits'the gas to accumulate in substantially equal quantities in the several leads of tubing extending from the surface of the bath 16 to the rollers 24. Of course, gas also accumulate s in those portions of the tubing submerged in the regenerating bath. It is readily understood that the lengths of tubing extending between the rollers 23 and 24 can hold large quantities of gas and if this gas is evenly distributed through these lengths all the lengths will hold a maximum quantity of the gas before it becomes necessary to puncture the tubing. Then when the tubing is punctured the puncture passes over the rollers 23 and 24 so that the gas in each length may escape.
In practice I have found that if the regeneratlng bath is about three feet deep and if the rollers 24 are spaced about seven feet above the bath, the tubing may be punctured only at infrequent intervals. Of course, the rollers 24 may be placed higher above the bath if it is so desired, but this distance is determined largely by the accessibility of the rollers to the operator when the tubing is being threaded through the apparatus. To obtain goed results, the rollers should be at least two feet abovethe surfene or the bath.
While I have shown and described certain enerbodiments of my invention, it is to be under= stood that it is capable of many modifications. Changes, therefore, in the construction and an rangement may be made without departing from the spirit and scope of the invention as disclosed in the appended claims, in which it is my intention to claim all novelty inherent in my invention as broadly as possible, in view of the prior What I regard new, and desire to secure by Letters Patent, is:
during the regenerating operation collects in substantially equal quantities in the lengths of'tub ing extending between the upper and lower rollers.
2. A method of forming cellulose tubing, which method comprises extruding viscose through an annular orifice to form seamless tubing thereof, and passing said seamless tubing through a rel atively weal; regenerating bath a plurality of times in such manner that the gas evolved during can the regenerating operation will collect in substan- .tially equal quantities in a plurality of long lengths of the tubing extending above the bath.
3. A method of forming cellulose tubing, which method comprises extruding viscose through an annular orifice to form seamless tubing thereof, and passing said seamless tubing through a regenerating bath a plurality of times in such manner that the gas evolved during the regenerating operation will collect in approximately equal quantities in a plurality of long lengths 1 of the tubing extending above the bath.
ALFRED G; HEJVI'lI.
Mill
US498497A 1930-11-26 1930-11-26 Mechanism for and method of producing cellulose tubing Expired - Lifetime US1937225A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2586046A (en) * 1949-01-28 1952-02-19 William C Huebner Filament forming apparatus
US3872196A (en) * 1972-12-04 1975-03-18 Tee Pak Inc Process for plasticizing and partially drying tubular film casings for edible products
US4195054A (en) * 1978-04-21 1980-03-25 Teepak, Inc. Method and apparatus for the manufacture of fibrous casing
WO1998004140A1 (en) * 1996-07-31 1998-02-05 Alfacel S.A. Adjustable reaction tubs for cellulose
US5773035A (en) * 1996-07-01 1998-06-30 Alfacel S.A. Tubular cellulosic casing die
US5776398A (en) * 1997-01-15 1998-07-07 Alfacel S.A. Method of regenerating sausage casing
US5783131A (en) * 1996-08-27 1998-07-21 Alfacel S.A. Method to slowly regenerate cellulosic sausage casing
US5795523A (en) * 1996-10-30 1998-08-18 Alfacel S.A. Method for treatment of CS2 and H2 S emissions during viscose regeneration

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2586046A (en) * 1949-01-28 1952-02-19 William C Huebner Filament forming apparatus
US3872196A (en) * 1972-12-04 1975-03-18 Tee Pak Inc Process for plasticizing and partially drying tubular film casings for edible products
US4195054A (en) * 1978-04-21 1980-03-25 Teepak, Inc. Method and apparatus for the manufacture of fibrous casing
US5773035A (en) * 1996-07-01 1998-06-30 Alfacel S.A. Tubular cellulosic casing die
WO1998004140A1 (en) * 1996-07-31 1998-02-05 Alfacel S.A. Adjustable reaction tubs for cellulose
US5741529A (en) * 1996-07-31 1998-04-21 Alfacel S.A. Adjustable reaction tubs for cellulose
EP0935422A1 (en) * 1996-07-31 1999-08-18 Alfacel S.A. Adjustable reaction tubs for cellulose
EP0935422A4 (en) * 1996-07-31 2003-01-02 Alfacel S A Adjustable reaction tubs for cellulose
US5783131A (en) * 1996-08-27 1998-07-21 Alfacel S.A. Method to slowly regenerate cellulosic sausage casing
US5795523A (en) * 1996-10-30 1998-08-18 Alfacel S.A. Method for treatment of CS2 and H2 S emissions during viscose regeneration
US5776398A (en) * 1997-01-15 1998-07-07 Alfacel S.A. Method of regenerating sausage casing

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