US2910380A - Method of making seamless viscoseregenerated cellulose tubing - Google Patents

Method of making seamless viscoseregenerated cellulose tubing Download PDF

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Publication number
US2910380A
US2910380A US540351A US54035155A US2910380A US 2910380 A US2910380 A US 2910380A US 540351 A US540351 A US 540351A US 54035155 A US54035155 A US 54035155A US 2910380 A US2910380 A US 2910380A
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United States
Prior art keywords
viscose
tubing
cellulose
fibrous
temperature
Prior art date
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Expired - Lifetime
Application number
US540351A
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English (en)
Inventor
Edward A Shiner
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Union Carbide Corp
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Union Carbide Corp
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Filing date
Publication date
Priority to BE551624D priority Critical patent/BE551624A/xx
Application filed by Union Carbide Corp filed Critical Union Carbide Corp
Priority to US540351A priority patent/US2910380A/en
Priority to GB29098/56A priority patent/GB803193A/en
Priority to DEV11323A priority patent/DE1107928B/de
Application granted granted Critical
Publication of US2910380A publication Critical patent/US2910380A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A22BUTCHERING; MEAT TREATMENT; PROCESSING POULTRY OR FISH
    • A22CPROCESSING MEAT, POULTRY, OR FISH
    • A22C13/00Sausage casings
    • A22C13/0013Chemical composition of synthetic sausage casings

Definitions

  • the invention relates to the manufacture of regenerated cellulose tubing. More particularly it relates to the manufacturing of seamless regenerated cellulose tubing reinforced with fibers embedded therein.
  • Casings of seamless regenerated cellulose tubing reinforced with fibers are used extensively for the packaging of meat food products and other applications.
  • such tubing was produced by applying viscose, at room temperature, to one or both sides of a tube formed by curving a thin long-fibered paper strip in which the fibers were bonded with viscoseregenerated cellulose and/ or resins about its longitudinal axis with overlapping longitudinal margins and after permitting the viscose to penetrate into paper subjecting the resultant tubing to a treatment for coagulating the viscose and regenerating the cellulose therefrom whereby the regenerated cellulose constituted a matrix in the form of a seamless tubing in which a coextensive paper tube was embedded.
  • the aforementioned process was carried out continuously by a machine in which the steps were consecutively performed.
  • the viscose should penetrate the base tubing prior to coagulation and regeneration and this was obtained by permitting a time lapse between the application of the viscose and the coagulating and regenerating steps.
  • To secure complete penetration of the viscose would require such a period of time as to make the process uneconomical. Accordingly, as a compromise, a viscose penetration time was used as would make the process commercially practical and give a satisfactory commercial product. Manifestly, the viscose penetration time limited the speed of the machine.
  • An object of this invention is to substantially reduce the viscose penetration time in the method of producing seamless regenerated cellulose tubing having a coextensive tubing formed of a fibrous web embedded therein.
  • Another object of this invention' is to cause the viscose to more effectively penetrate the tubing formed of a fibrous web and the individual fibers thereof in the method of producing seamless regenerated cellulose tubing having a tubing formed of a fibrous web embedded therein.
  • the above objects are accomplished in general by lowering the viscosity of a viscose composition of the kind normally used in the process of embedding a base paper tube in a seamless tubing of regenerated cellulose, at a stage in the process prior to the regeneration of the cellulose in situ on the paper base tube, such as either before or after application to the base paper tubing, by means of heat.
  • viscose at room temperature is passed through a heat exchanger and thence through pipes to the apply ing device. If the distance between the heat exchanger and the applying device is such that the viscose in traveling through it will appreciably drop in temperature below that desired at the point of application, precautions such as insulating the pipes to prevent such drop in temperature, must be taken.
  • the applying device' may also be insulated.
  • any temperature of the viscose above room temperature and below that at which the viscose will increase in viscosity during passage through the heatexchanger and the applying device can be used.
  • the temperature should be employed which will yield a viscose of minimum viscosity.
  • the maximum viscose temperature to be employed will be governed by the point in the process at which the viscose is heated, Whether prior to or after application to the paper.
  • the maximum viscose temperature When the viscose is heated after application to the paper the maximum viscose temperature will be governed by the rate of evaporation of Water from the viscose which will tend to increase viscosity and counter the lowering effect of the temperature on viscosity. Unless it is desired to heat coagulate the viscose in the same operation, which can be accomplished at higher temperatures, for optimum rate of penetration of viscose into paper the viscose temperature when heated after application to the paper should not exceed 65 to 75 C.
  • composition of the viscose may be similar to those employed in-the art for making seamless regenerated cellulose tubing reinforced with fibrous webs such as paper.
  • a viscose of the following composition is particularly suitable:
  • Any appropriate coagulating and regenerating bath may be used.
  • An aqueous bath containing 3 /2%-12% sulphuric acid and l0%l5% sodium sulphate (or 10%- 20% ammonium sulphate) has given satisfactory results.
  • a paper formed of hemp fibers bonded together by viscose regenerated cellulose is the preferred fibrous base tubing.
  • Tubings formed of other fibrous webs such as non-woven fabrics formed of fibers such as, for example, those employed in the production of yoshino paper, rice paper and the like, hemp, rayon, cotton, nylon, polyethylene terephthalate, acrylonitrile and the like and appropriately bonded, as well as woven fabrics such as cheese cloth, muslin, marquisette, organdy, voile and the like can be used.
  • the invention can be used in conjunction with the methods and apparatus set out in U.S. Patent Nos. 2,105,273 and 2,144,900 and the viscose can be applied to outer or inner or both the outer and inner surfaces of the base tubing.
  • Regenerated cellulose tubinghaving a tube of a fibrous web embedded therein when produced in accordance with this invention is more transparent than similar tubing prepared with viscose at room temperature and same viscose penetration time. This indicates that in the product ofthis invention there are less unpenetrated fibers and/or the individual fibers are more effectively penetrated than in the products resulting from processes utilizing viscose at room temperature with same penetration time.
  • the product resulting from this invention has a greater strength than similar products prepared by the prior art method. This will become apparent from the following table setting out a comparison of the Burst pressures of tubings prepared with viscose at room temperature (20 C.) and similar viscose but of reducedviscosity obtained by heating to 55 C.
  • Table II illustrates the effect on strength ,of the product by the improved penetration due to lower 1 Method described in U.S. Patent No. 1,978,134.
  • Example 1 A strip of paper consisting of manila hemp fibers bonded together with regenerated cellulose is formed into a tube by curving it along its longitudinal axis with overlapping margins and then viscose of the following composition and maintained at a temperature of 55 C., is applied to the inner margin and entire outer surface of the wall of the paper tubing:
  • Example 2 Cellulose contentpercent 6-8 Caustic soda do -7 'Index 28-35 Cellulose degree of polymerization 300-800
  • the viscose was permittedto penetrate the paper tubing for 40 seconds and thereafter the coated and impreg- Example 2 Same as Example 1 except that the viscose is applied at room temperature and the fibrous tubing coated and impregnated with viscose is subjected to a temperature of 65 75 C. for 20-30 seconds prior to coagulation and regeneration in an aqueous bath as set out in Example 1.
  • Example 3 Same as Example 2 except that regeneration is affected by heating to 95-110 C.
  • the product of the foregoing example consisted o seamless regenerated cellulose tubing having a coextensive paper tubing formed of manila hemp fibers embedded and incorporated therein.
  • the viscose was at room temperature, it had improved transparency and greater strength as previously indicated.
  • Casings produced in accordance with this invention withstand the processing conditions employed in the production of sausage and accordingly are admirably suited for such use as well as for storage of such items.
  • the casings can also be used for encasing and storing of preprocessed meat, foods, cheese, and like applications.
  • the invention permits reducing the viscose penetration time and thus the machine on which the product is produced can be operated at higher speeds than heretofore. In the event the machines are operated at the same speeds as heretofore, a more transparent product is obtained. In either case, the product has improved properties.
  • the viscose contains 6-8% cellulose and 58% caustic soda and is heated to a temperature not above C. prior to application to the fibrous tubing.
  • the viscose contains 6-8% cellulose and 5-7% caustic soda and is heated to a temperature of 55 C. prior to application to the fibrous tubing.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Food Science & Technology (AREA)
  • Processing Of Meat And Fish (AREA)
  • Artificial Filaments (AREA)
  • Laminated Bodies (AREA)
  • Reinforced Plastic Materials (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
US540351A 1955-10-13 1955-10-13 Method of making seamless viscoseregenerated cellulose tubing Expired - Lifetime US2910380A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
BE551624D BE551624A (de) 1955-10-13
US540351A US2910380A (en) 1955-10-13 1955-10-13 Method of making seamless viscoseregenerated cellulose tubing
GB29098/56A GB803193A (en) 1955-10-13 1956-09-24 Method of making tubing
DEV11323A DE1107928B (de) 1955-10-13 1956-10-05 Verfahren zur Herstellung von nahtlosen Schlaeuchen aus viskose-regenerierter Cellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US540351A US2910380A (en) 1955-10-13 1955-10-13 Method of making seamless viscoseregenerated cellulose tubing

Publications (1)

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US2910380A true US2910380A (en) 1959-10-27

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US540351A Expired - Lifetime US2910380A (en) 1955-10-13 1955-10-13 Method of making seamless viscoseregenerated cellulose tubing

Country Status (4)

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US (1) US2910380A (de)
BE (1) BE551624A (de)
DE (1) DE1107928B (de)
GB (1) GB803193A (de)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3135613A (en) * 1959-08-17 1964-06-02 Union Carbide Corp Impregnated paper web and method of making sausage casings therefrom
US3291789A (en) * 1962-06-07 1966-12-13 Tee Pak Inc Decausticization of polysaccharide xanthates
US3433663A (en) * 1964-05-04 1969-03-18 Union Carbide Corp Impregnated porous paper webs and method of obtaining same
US3450555A (en) * 1962-06-07 1969-06-17 Tee Pak Inc Treatment of textile fibers with soluble polymeric alcohol derivatives
US3497584A (en) * 1963-04-22 1970-02-24 Tee Pak Inc Method of preparing polysaccharide films and fiber- of paper-reinforced polysaccharide films
US3661621A (en) * 1968-06-08 1972-05-09 Wolff & Co Ag Process for producing tubular structures coated on both sides
DE2338418A1 (de) * 1972-08-01 1974-02-21 Union Carbide Corp Geraffte und zusammengepresste schlauchfoermige huelle
US3956539A (en) * 1974-09-09 1976-05-11 Tee-Pak, Inc. Imidazolines in preparing fibrous artificial sausage casings
US4317794A (en) * 1978-07-03 1982-03-02 Hoechst Aktiengesellschaft Process for the continuous manufacture of fiber-reinforced cellulose hydrate tubing and equipment for carrying out the processes
US4390490A (en) * 1980-04-07 1983-06-28 Teepak, Inc. Fibrous casing extrusion
US4409251A (en) * 1982-03-25 1983-10-11 Union Carbide Corporation Controllably moisturized mold resistant cellulosic food casings
WO1996014752A1 (de) * 1994-11-14 1996-05-23 Wolff Walsrode Ag Fällverfahren für viskoseschläuche

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3104682A (en) * 1959-07-13 1963-09-24 Union Carbide Corp Fibrous web reinforced cellulosic casings
JPS5822178B2 (ja) * 1979-05-16 1983-05-07 東和化工株式会社 糸入りフアイブラスケ−シングおよびその製造方法
BR9403440A (pt) * 1994-09-05 1996-09-03 Hoechst Do Brasil Quimica E Fa Processos para fabricar um invólucro tubular flexivel à base de celulose regenerada para uso na indústria de carnes principalmente na fabricaçao de salsichas
DE102005043149A1 (de) 2005-09-10 2007-03-15 Kalle Gmbh Verpackungsfolie auf Basis von regenerierter Cellulose mit Mikrofasern und/oder mikrokristalliner Cellulose

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1036282A (en) * 1911-11-10 1912-08-20 Leon Lilienfeld Process of finishing, filling, loading, or dressing textile fabrics and spun goods.
US1729681A (en) * 1926-06-25 1929-10-01 Gen Electric Waterproof wrapping cloth
US2016719A (en) * 1930-06-27 1935-10-08 Sayles Finishing Plants Inc Viscose coating and filling
US2031854A (en) * 1931-09-11 1936-02-25 Brown Co Surface-finished paper
US2045349A (en) * 1931-02-04 1936-06-23 Visking Corp Reenforced hydrated cellulose container
US2109591A (en) * 1928-06-18 1938-03-01 Lilienfeld Leon Process for coagulating or precipitating viscose
US2460480A (en) * 1939-01-10 1949-02-01 Wolff Julius Method of and apparatus for producing artificial sausage skins

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT126128B (de) * 1929-07-02 1932-01-11 Wolff & Co Verfahren zur Herstellung von Folien und anderen nichtfadenförmigen, flächenhaften Gebilden aus wässerigen Celluloselösungen.

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1036282A (en) * 1911-11-10 1912-08-20 Leon Lilienfeld Process of finishing, filling, loading, or dressing textile fabrics and spun goods.
US1729681A (en) * 1926-06-25 1929-10-01 Gen Electric Waterproof wrapping cloth
US2109591A (en) * 1928-06-18 1938-03-01 Lilienfeld Leon Process for coagulating or precipitating viscose
US2016719A (en) * 1930-06-27 1935-10-08 Sayles Finishing Plants Inc Viscose coating and filling
US2045349A (en) * 1931-02-04 1936-06-23 Visking Corp Reenforced hydrated cellulose container
US2031854A (en) * 1931-09-11 1936-02-25 Brown Co Surface-finished paper
US2460480A (en) * 1939-01-10 1949-02-01 Wolff Julius Method of and apparatus for producing artificial sausage skins

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3135613A (en) * 1959-08-17 1964-06-02 Union Carbide Corp Impregnated paper web and method of making sausage casings therefrom
US3291789A (en) * 1962-06-07 1966-12-13 Tee Pak Inc Decausticization of polysaccharide xanthates
US3450555A (en) * 1962-06-07 1969-06-17 Tee Pak Inc Treatment of textile fibers with soluble polymeric alcohol derivatives
US3497584A (en) * 1963-04-22 1970-02-24 Tee Pak Inc Method of preparing polysaccharide films and fiber- of paper-reinforced polysaccharide films
US3433663A (en) * 1964-05-04 1969-03-18 Union Carbide Corp Impregnated porous paper webs and method of obtaining same
US3661621A (en) * 1968-06-08 1972-05-09 Wolff & Co Ag Process for producing tubular structures coated on both sides
DE2338418A1 (de) * 1972-08-01 1974-02-21 Union Carbide Corp Geraffte und zusammengepresste schlauchfoermige huelle
US3956539A (en) * 1974-09-09 1976-05-11 Tee-Pak, Inc. Imidazolines in preparing fibrous artificial sausage casings
US4317794A (en) * 1978-07-03 1982-03-02 Hoechst Aktiengesellschaft Process for the continuous manufacture of fiber-reinforced cellulose hydrate tubing and equipment for carrying out the processes
US4390490A (en) * 1980-04-07 1983-06-28 Teepak, Inc. Fibrous casing extrusion
US4409251A (en) * 1982-03-25 1983-10-11 Union Carbide Corporation Controllably moisturized mold resistant cellulosic food casings
WO1996014752A1 (de) * 1994-11-14 1996-05-23 Wolff Walsrode Ag Fällverfahren für viskoseschläuche

Also Published As

Publication number Publication date
DE1107928B (de) 1961-05-31
GB803193A (en) 1958-10-22
BE551624A (de)

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