US1683199A - Artificial thread and process for making same - Google Patents

Artificial thread and process for making same Download PDF

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US1683199A
US1683199A US156751A US15675126A US1683199A US 1683199 A US1683199 A US 1683199A US 156751 A US156751 A US 156751A US 15675126 A US15675126 A US 15675126A US 1683199 A US1683199 A US 1683199A
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viscose
sulphuric acid
thread
per cent
acid
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Lilienfeld Leon
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00—Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
    • D01F2/08—Composition of the spinning solution or the bath
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/07—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with halogens; with halogen acids or salts thereof; with oxides or oxyacids of halogens or salts thereof
    • D06M11/11—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with halogens; with halogen acids or salts thereof; with oxides or oxyacids of halogens or salts thereof with halogen acids or salts thereof
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/07—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with halogens; with halogen acids or salts thereof; with oxides or oxyacids of halogens or salts thereof
    • D06M11/11—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with halogens; with halogen acids or salts thereof; with oxides or oxyacids of halogens or salts thereof with halogen acids or salts thereof
    • D06M11/22—Halides of elements of Groups 5 or 15 of the Periodic System
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/32—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/36—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond with oxides, hydroxides or mixed oxides; with salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/38—Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic System
    • D06M11/40—Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic System combined with, or in absence of, mechanical tension, e.g. slack mercerising
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/51—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with sulfur, selenium, tellurium, polonium or compounds thereof
    • D06M11/53—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with sulfur, selenium, tellurium, polonium or compounds thereof with hydrogen sulfide or its salts; with polysulfides
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/51—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with sulfur, selenium, tellurium, polonium or compounds thereof
    • D06M11/55—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with sulfur, selenium, tellurium, polonium or compounds thereof with sulfur trioxide; with sulfuric acid or thiosulfuric acid or their salts
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/58—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with nitrogen or compounds thereof, e.g. with nitrides
    • D06M11/64—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with nitrogen or compounds thereof, e.g. with nitrides with nitrogen oxides; with oxyacids of nitrogen or their salts
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/73—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with carbon or compounds thereof
    • D06M11/75—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with carbon or compounds thereof with phosgene; with compounds containing both carbon and sulfur, e.g. thiophosgene
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M59/00—Pumps specially adapted for fuel-injection and not provided for in groups F02M39/00 -F02M57/00, e.g. rotary cylinder-block type of pumps
    • F02M59/20—Varying fuel delivery in quantity or timing
    • F02M59/24—Varying fuel delivery in quantity or timing with constant-length-stroke pistons having variable effective portion of stroke
    • F02M59/26—Varying fuel delivery in quantity or timing with constant-length-stroke pistons having variable effective portion of stroke caused by movements of pistons relative to their cylinders
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00—Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/02—Natural fibres, other than mineral fibres
    • D06M2101/04—Vegetal fibres
    • D06M2101/06—Vegetal fibres cellulosic
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00—Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/02—Natural fibres, other than mineral fibres
    • D06M2101/04—Vegetal fibres
    • D06M2101/06—Vegetal fibres cellulosic
    • D06M2101/08—Esters or ethers of cellulose
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M2700/00—Supplying, feeding or preparing air, fuel, fuel air mixtures or auxiliary fluids for a combustion engine; Use of exhaust gas; Compressors for piston engines
    • F02M2700/13—Special devices for making an explosive mixture; Fuel pumps
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M2700/00—Supplying, feeding or preparing air, fuel, fuel air mixtures or auxiliary fluids for a combustion engine; Use of exhaust gas; Compressors for piston engines
    • F02M2700/13—Special devices for making an explosive mixture; Fuel pumps
    • F02M2700/1317—Fuel pumpo for internal combustion engines
    • F02M2700/1388—Fuel pump with control of the piston relative to a fixed cylinder

Definitions

  • the invention is'based upon the observation that artificial threads, for example artificial silk of high dry tenacity, are obtained by bringing viscose into the form of a thread and causing to act upon the formed thread one or more agents which have upon viscose the two following cficcts:
  • exceeding 2 grammes per denier can be made for example by bringing the viscose into the form of a thread and causing to act upon the formed thread sulphuric acid containing not less than about per cent, for example about per cent of H,SO,, ano preferably sulphuric acid containing more than 55 per cent, for example to 86 per cent of H,SO,.
  • a further advantage of I the artificial threads manufactured according to the presout process over ordinary viscose silk is their higher resistance to aqueous alkalies and to soap.
  • the process is carried out by bringing viscose into the form of an artificial thread and coagulating it by means of sulphuric acid, containing atleast about 50, preferably about 55 per cent of H SO for example sulphuric acid containing 55 to 85 per cent of monohydrate. In most cases this can be effected in such a manner that the viscose is caused to pass through suitably formed openings into sulphuric acid, containing 55 to 98 per cent of H 80 for instance acid of 65 to 85 per cent strength (calculated as H SOJ, or into a bath containing 55 to 98 per cent, for instance 65 to 85 per cent of monohydrate.
  • the strong sulphuric acid may be employed by itself or, so far as is compatible with the conditions under which it is used, in admixture with a suitable quantity of one or more suitable inorganic substances, for example with another strong mineral acid, such as hydrochloric acid, nitric acid or phos )horic acid, or with a neutral or acid salt, suc as sodium sulphate, sodium bisulphate, ammonium sulphate, magnesium sulphate, zinc sulphate, sodium bisul hite, sodium sulphite, sodium nitrite or bone acid.
  • another strong mineral acid such as hydrochloric acid, nitric acid or phos )horic acid
  • a neutral or acid salt suc as sodium sulphate, sodium bisulphate, ammonium sulphate, magnesium sulphate, zinc sulphate, sodium bisul hite, sodium sulphite, sodium nitrite or bone acid.
  • the strong sulphuric acid or its mixture with another strong acid or with one or more of the inor anic substances mentioned 1 above there may be added a suitable quantity of one or more organic bodies, such as glycerol or asugar, for example glucose, or alcohol or a salt of an organic base, for example of aniline; or an organic acid, such as acetic acid or formic acid or lactic acid or oxalic acid.
  • organic bodies such as glycerol or asugar, for example glucose, or alcohol or a salt of an organic base, for example of aniline
  • an organic acid such as acetic acid or formic acid or lactic acid or oxalic acid.
  • the coagulating bath contains free sulphuric acid of the desired strength, but at any rate not less than about 50, preferably about 55 parts by weight of monohydrate in 100 parts by weight of the precipitating bath.
  • the process may also be carried out in such a manner that the formed thread is first coagulated by means of a setting bath known from the vlscose artificial silk art regardless whether such bath coagulates the viscose in a form soluble or insoluble in water, whereupon the thread is treated with a liquid that consists of, or contains one or more stronger mineral acids, preferably strong sulphuric acid for example such of 50 to 94 per cent or more strength (calculated on monohydrate)
  • a liquid that consists of, or contains one or more stronger mineral acids, preferably strong sulphuric acid for example such of 50 to 94 per cent or more strength (calculated on monohydrate) This can be done, for example so, that the viscose is forced to pass through suitably formed alpertures into a coagulating bath known from t 1
  • the strength of the sulphuric acid depends, ceteris paribus, partly on the time of maturing given the alkali cellulose, partly on the time of ripening given the finished viscose and partly on the viscosity or amount of cellulose contained in the viscose.
  • viscoses which have matured for several days and viscoses that have been prepared from alkali cellulose that has been allowed to mature for a relatively long time, for example 2 to 3 days and viscoses that are poor 1n cellulose or little visin cellulose or highly viscous.
  • the 7 best viscoses for use in this invention are such as have a viscosity of 2 or more, as compared with glycerine, the viscosity of which is taken as unity.
  • the strength of the sulphuric acid is further, to a certaindegree, dependent on the length of immersion in the coagulating bath and thetension given the coagulated mate rial in the acid or outside it, for example between the coagulatin bath and the collecting device, for example bobbin.
  • the precipitating bath may be kept at room temperature or at a temperature exceeding room temperature, for example at 25 to 50 C. but asa rule I prefer to employ a temperature lower than room temperature, for example at 0 to 10 C.', or even below 03 (1, for example at from 1 to -10 C.
  • the length of thethread or filament immersed in the strong sulphuric acid or in the bath containing it may be varied within wide present process.
  • the thread may be stretched either immediately after its formation, that is in the coagulating bath containing, or consisting of, strong sulphuric acid, or subsequently, that is bet-ween the coagulating bath and the collecting device, such as bobbin or centrifuge, or both in the coagulating bath and between the coagulating bath and the collecting device.
  • the thread, after washing, may be heated or steamed before or after drying.
  • any suitable viscose may be used in the The process gives good results with viscoses that are prepared from alkali cellulose that has been allowed to mature for such a time as is commonly allowed for maturing alkali cellulose in the artificial silk art, but generally speaking more satisfactory results are obtained with viscoses in the manufacture of which alkali cellulose is used which has not been allowed to mature at all, or has been allowed to mature for a shorter time than is usual in the artificial silk art, that is, not longer than for example about 36 hours, for example 1 to 24 hours.
  • viscoses as are prepared from alkali cellulose that has not been matured or has been matured for a shorter time than is usual in the artificial silk art, i. e. not longer than about 36 to 48 hours, for example 1 to 24 hours, yield strong threads if spun into sulphuric acld containing about 50 per cent of I-I SO,,whilst the lower limit of the concentration of the sulphuric acid for obtaining strong threads from viscoses prepared from alkali cellulose that has been matured for a longer time than 36 to 48 hours (according to the quality of the starting cellulose and to the temperature of maturing the alkali cellulose) 1s about per cent of H 30
  • the present 1nvent1on gives good results with such viscoses also as are prepared by directly mixing the ingredients.
  • viscose there may be added to the viscose one or more suitable substances known in the viscose-silk art, for example g1 ycerine or glucose or sodium sulphate or sodium sulphite or sodium bisulphite or ammonium sulphate 'or an alkali silicate or an alkali aluminate or ammonia.
  • suitable substances for example g1 ycerine or glucose or sodium sulphate or sodium sulphite or sodium bisulphite or ammonium sulphate 'or an alkali silicate or an alkali aluminate or ammonia.
  • the thread thus produced is made up of filaments of about 3 to 4 deniers each.
  • three glass rods are situated over which the thread runs and which create an loo cial silk.
  • the mode of operation is as 1n (a), except that the temperature of the coagulating bath is 25 C. and that the length of immersion is 20 to' 30. centimetres only.
  • the mode of operation is as in (a) or (b), with the exception that the temperature of the coagulating bath is 40 to (J. and that the length of immersion is 20 to 30 centimetres only.
  • the mode of operation is as-in (a), or (b) with the difierenc'e that the bath contains to per cent sulphuric acid.
  • the mode of operation is as in (a), or (b), or (e), or (f) with the exception that the viscose is allowed to age for 144 to'200 hours at 13 to 15 C. before spinning.
  • the comminuted soda cellulose is then kept for '60 to 7 2 hours at room temperature, whereafter 30 to 60 parts of carbon bisulphide are added, and the mixture preferabl while stirring (for example m a closed eading machine) or agirtating (for exam le in a sulphidizing drum),
  • Example I is kept for sever lf gr example 4 to 8) hours at 16 to 20 C. ereafter the excem of the carbon bisulphide is removed by driving off or cvacuatin and then the sulphidized mass is dissolve in water or dilute caustic soda solution in such a manner that the vlscose'co'ntains about 8 to 12 per centof cellulose (determined in the known manner itating with acid, washing and dry manner through cotton wool or a dense cotton fabric or thron -h both and freed from gas bubbles. Immediately after, or after it has been allowed to ripen at 16-18 C. for a shorter (for example, 12 hours to two days). or a longer (for example, four days to seven days) time, the viscose is spun as in Example I into one of the following precipitating baths:
  • the temperature of the coagulating bath I is kept at O to 16 C. for instance at 8 CL, or at -4 to 8. C.
  • the length of the threads immersed in the coagulating bath inwhich -th ey-are being formed ma be short',"for example 10 centimetres, or ong, for instance from 30 to ,100 centimetres and more. They are then collected on a bobbin or in a spinnin centrifuge which may be placed either close by the precipitating bath'or in a distance from 20 to centimetres from the bath, whilst the sulphuric acid is quenched or diluted as in Example I. The threads are then further washed anddried.
  • the threads may be stretched in any known manner whilst they are in the coagulating bath, or after they have been removed from the bath, that is, between the coagulating bath and the collecting device. This may be done, for example, either by choosing a more or less long distance between the bath and, 125
  • the collecting device or by leading the threads over rods or hooks arranged in the bath or between the bath and the collecting device, or in the bath and between the bath and the collecting device.
  • the speed of spinning may be varied with in wide limits.
  • the upper limit of speed possible is dependent partly upon the temperature of the coagulating bath, partly upon the length of immersion, partly upon the distance between the coagulating bath and the collecting device, partly upon the degree of stretchlng given the thread durin spinning, and partly upon the quantity o viscose delivered by the pump.
  • the following examples, to which, however, the process is not intended to be limited, may be adduced for the purpose of illustration:
  • the coagulating bath is used at a temperature below C., for example at 0., and if the length of thread immersed is 60 to 120, for example 80 centimetres, and if the distance between the coagulating bath and the collecting device, for example bobbin, is 60 to 1.50 centimetres, for instance 120 centimetres, and if the stretching given the thread between the coagulating bath and the collecting device is comparatively high, and if the pump delivers about 2 to 3 cubic centimetres of viscose a minute, then excellent results are obtained with a speed of 18 to 26 metres a minute, or of metres a min ute, but also, a higher speed may be used if desired.
  • a speed up to to 60 metres a minute may be used.
  • the threads may be treated in any known manner with a coagulating bath known in the viscose-silk art,
  • the washed threads may, before or after drying, be heated (for example, at 100-110 C.) or steamed.
  • Example III (a), or III (6), or III (0) Mode of operation as in Example III (a), or III (6), or III (0), with the difference- (1) That the sulphidized mass is dissolved in water or dilute caustic soda solution so as to yield a viscose that contains 5 to 8 per cent of cellulose, for instance, 6 to 7 per cent of cellulose (determined in the known manner by precipitating with acid, washing and drylng (2) That as coagulating bath one of the following baths is used (l) Sulphuric acid of 55 to 60 B., or
  • Example III (a), or III (7)), or III (a), or as in Example IV with the exception that the viscose is not allowed to mature at all, or to mature for 12 to 48 hours only, and that as coagulating bath sulphuric acid of 60 to 64 B., for instance sulphuric acid of 62 B., at 6 to 10 C. is used.
  • sulphuric acid 60 to 64 B., for instance sulphuric acid of 62 B., at 6 to 10 C.
  • the spinning In using so strong an acid it is preferable to run the spinning at a high speed, for example 40 to 60 metres a minute.
  • the temperature of the coagulating bath iskept at 0 to 16 (3., for instance at 8 C. or at' *4 to 8". C.
  • the threads are spun and treated during and after spinning in the same manner as described in the foregoing examples.
  • the mode of operation is as in (a), or (b) except that 75 or more parts of carbon bisulphide are used for sulphidizing the sodacellulose.
  • the mode of o ration is as in (a), or (b), or (0), with t e difference that the soda-cellulose is pressed to 200 parts.
  • the mode of operation is as in (a), or (b), or (c), or (d), with the diflerence that sulphuric acid of 62 to 64 B. at 8 C. is used as coagulating bath, the viscose being 12 to 48 hours old and the speed of spinning about 45 to 60 metres a minute.
  • mass may be equal to those used in Example VI or somewhat lower, for example so as to produce a 10 to 12 per cent viscose (calculated on the parent cellulose).
  • the viscose is worked up into threads as in VI (a) to (e).
  • the temperature of the coagulatingbath is kept at 0 to 16 C., for instance at 8 C. or at t to 8 C.
  • the threads are spun and treated as in the foregoing examples. 4
  • a catalyzer is a ded to the mixture of the cellulosic body with the caustic alkali solution, for example 0.2 to 1 part of a soluble chromic salt or nickel salt or iron salt.
  • the final viscose contains 8 per cent of parent cellulose.
  • This viscose is filtered and spun and the threads are treated as in the foregoing examples.
  • the formed thread is introduced directly from one of the foregoing baths into one of the following baths:
  • the temperature of the second-bath may be kept below room temperature, for instance at 0 to 10 0., or at room temperature, or even above room temperature, for example at 25 to 45 C.
  • the length of immersion given the thread in the second bath may be short, for instance 20 centimetres, or long, for example 30 to 100 centimeters or more.
  • the threads are then collected whilst the sulphuric acid is quenched or diluted as described above, and the threads are finally washed, dried and treated as in Example I.
  • the arresting of the action of the acid may be also .done by subjecting the thread leaving the coagulating bath consisting of, or containing the strong acid to a loW temperature, for instance to 5 to 15 C. before washing.
  • artificial silk or staple fibre which has a considerably greater. dry or wet tenacity than silk spun under the same spinning conditions, but by means of chemicals customary in the viscose silk art, for fixample by using a known precipitating bat
  • strong sulphuric acid there may be used in the foregoing examples a strong halogen hydracid, such as hydrochloric acid, for exampde of 35 to 40 per cent strength, or nitric acid, for example such as contains to 90 per cent of I-INO,, or phosphoric acid, for example of 1.5 to 1.86 specific gravity, or arsenic acid, for example such as contains from 60 to 90 per cent of I-I,As(),.
  • strong mineral acid means in the description and in the claims: sulphuric acid of at least 50 per cent I-I SO and the other mineral acids equivalent in strength, i. e. hydrochloric acid of at least 35 per cent strength, nitric acid of at least 60 per cent strength, phosphoric acid of at least 1.5 specific gravity and arsenic least 60 per cent of H AsO
  • strong sulphuric acid or sulphuric acid containing at least 50 per cent of sulphuric acid monohydrate means in the description and claims: sulphuric acid of 50 to 98 or 100 per cent strength.
  • cellulose used in the. product claims is intended to mean: cellulose or cellulose hydrate, as the body regenerated acid of at' from viscose is regarded by some cellulose.
  • the artificial threads produced accordin to the present process may be distinguishe from artificial threads consistingof, or containing cellulose or cellulose hydrate, particularly from viscose silk produced after methods known hitherto, or from cuprammonia silk by means of a very dilute solution of iodine in an aqueous solution of potassium iodide or by a solution of zinc chloride to which a very small 'quantity of a solution of iodine in an aqueous solution of potassium iodide has been added.
  • viscose silk produced by a method known hitherto and copper silk are colored blue, while silk produced according to the present process remains either perfectly colorless or is tinted a grayish blue.
  • Solution 1 contains 28 grams of zinc chloride in 30 c. c. of solution.
  • Solution 2 1 gram iodine and 20 grams of potassium iodide dissolved in 100 c. c. of water.
  • Viscose silk produced according to t e present invention colorless, or a greylsh blue tint
  • I claim: 1' Process for manufacturing artificial threads of high-dry tenacity, exceeding 2 grammes per denier, from viscose, which comprises causing a viscose to pass through suitably formed openings into contact with a liquid which contains not less than about 65 per cent of sulphuric acid monohydrate.
  • Process for manufacturing artificial threads of high dry tenacity, exceeding 2 grammes per denier, from viscose which comprises causing a viscose to pass through suitably formed openings into contact" with a liquid which contains not less than about 65 per cent of sulphuric acid monohydrate, and checking the action of the strong sulphuric acid not later than the thread arrives at the collecting device.
  • Process for manufacturing artificial threads 'of high dry tenacity, exceeding 2 grammes per denier, from viscose which comprises causing a vis ose to pass through suitably formed openinigs into a bath containing not less than about 55 per cent of sulphuric acid monohydrate and applying 'to the coagulated thread additional stretch in the course of its passage after it enters the bath and before it is washed.
  • grammes per denier from viscose, which comprises causing a viscose to pass through suitably formed openings into a bath containing not less than about 55 per cent of sulphuric acid monohydrate, and applying to the coagulated thread additional stretch in the course of its passage after it enters the bath and before it is washed, and checking the action of the strong sulphuric acid not later than the thread arrives at the collecting device.
  • the process of manufacturing artificial thread of high dry tenacity which comprises contacting athreadlike stream of a viscose with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
  • the process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains at least about 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
  • the process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains at least about 50 per cent sulphuric acidmonohydrate and diluting the strong acid adhering to the thread by washing the thread before it is injured by the strong acid.
  • the process for manufacturing artificialthread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it. with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid nionohydrate.
  • the process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains at least about 50 per cent of sulphuric acid monohydrate.
  • the process for manufacturing artificialthread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains not less than about 55 per cent of sulphuric acid monohydrate.
  • the process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains at least 50 per cent of sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
  • the process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains not less than about 55 per cent of sulphuric acid monohydrate, and

Description

Patented Sept. 4, 1928.
UNITED STATES PATENT OFFICE.
ARTIFICIAL THREAD AND PROCESS FOR MAKING SAME.
No Drawing. Application filed December 23, 1926, Serial No. 156,751, and in Austria June 20, 1925.
The invention is'based upon the observation that artificial threads, for example artificial silk of high dry tenacity, are obtained by bringing viscose into the form of a thread and causing to act upon the formed thread one or more agents which have upon viscose the two following cficcts:
1. A coagulating elfect upon the formed but not yet coagulated thread, and
2. A dissolving or swelling up or plasticizing action upon the coagulated thread. Observations made under the microscope indicate that the combination of the two actions described above results in a high dry tenacity, because the coagulation combined with either a plasticization of the thread or with a filling out of the interstices by the swollen or dissolved parts of the thread or both, imparts to the thread a much higher continuity than the coagulation by itself. In addition to this, the plasticization which takes place simultaneously with, or subsequently to the coagulation, makes the coagulated thread capable of being stretched during spinning to a degree unattainable if an agent is used which has a coagulating action only and no or very little plasticizing effect.
According to the invention, the dissolving or swelling or plasticizing action of the set .0 ting bath must not be prolonged until the cellulose thread is attacked by the destroying or depolymcrizing action the bath may have on the thread during its passage through the bath itself or during the air passage between =5 the bath and the collecting device.
In other words: The time during which the thread is in contact with the coagulating liquid must be so chosen that no destruction or depolymerization and no'considerable loss .0 in weight (calculated on the content of cellulose of the original viscose on the one hand and the weight of the thread produced on the other) takes place, and the action of the liquid must be checked before it has an injurious ef- =5 fect upon the thread.
I have further observed that strong mineral acids, particularly strong sulphuric acid, are specially suitable for the carrying out of the inventive idea underlying the present prociu ess: The combination of a coagulating action on the one hand and of a plasticizing action on the other, on formed viscose.
In carrying outmy invention, artificial threads or viscose silk of high dry tenacity,
exceeding 2 grammes per denier, can be made for example by bringing the viscose into the form of a thread and causing to act upon the formed thread sulphuric acid containing not less than about per cent, for example about per cent of H,SO,, ano preferably sulphuric acid containing more than 55 per cent, for example to 86 per cent of H,SO,.
My discovery that such strong sulphuric acid can be used as coagulating bath in the manufacture of artificial threads from viscose is surprising, it having been stated that with thread known hitherto and in some cases approaches, in some cases equals, and in some cases even surpasses that of natural fibres, such as cotton or real silk. For example, I am able to produce according to the present process artificial silk or staple fibre that has a dry tenacity of considerably more than 2 grammes and even more than 3 grammes per denier, for example 3 or even 3.5 to 4 grammes per denier, and in some cases even more than 4, or in some cases even 5 grammes per denier or more, and a wet tenacity of 1.5 to 2.5 grammes per denier and more.
A further advantage of I the artificial threads manufactured according to the presout process over ordinary viscose silk is their higher resistance to aqueous alkalies and to soap.
I have further found that it is advantageous to the tensile strength of the artificial threads, manufactured according to-the present process, to apply additional stretch to the threads either in the coagulating bath or between the coagulating bath and the collecting device or in both places. The process yields however quite good results also when only such stretch is applied as is usual in the viscose artificial silk art, particularly when spinning machines with a long air passage or high spinning speed or both are employed.
The process is carried out by bringing viscose into the form of an artificial thread and coagulating it by means of sulphuric acid, containing atleast about 50, preferably about 55 per cent of H SO for example sulphuric acid containing 55 to 85 per cent of monohydrate. In most cases this can be effected in such a manner that the viscose is caused to pass through suitably formed openings into sulphuric acid, containing 55 to 98 per cent of H 80 for instance acid of 65 to 85 per cent strength (calculated as H SOJ, or into a bath containing 55 to 98 per cent, for instance 65 to 85 per cent of monohydrate. The strong sulphuric acid may be employed by itself or, so far as is compatible with the conditions under which it is used, in admixture with a suitable quantity of one or more suitable inorganic substances, for example with another strong mineral acid, such as hydrochloric acid, nitric acid or phos )horic acid, or with a neutral or acid salt, suc as sodium sulphate, sodium bisulphate, ammonium sulphate, magnesium sulphate, zinc sulphate, sodium bisul hite, sodium sulphite, sodium nitrite or bone acid. Again, so far as is compatible with the conditions under which it is used, to the strong sulphuric acid or its mixture with another strong acid or with one or more of the inor anic substances mentioned 1 above, there may be added a suitable quantity of one or more organic bodies, such as glycerol or asugar, for example glucose, or alcohol or a salt of an organic base, for example of aniline; or an organic acid, such as acetic acid or formic acid or lactic acid or oxalic acid. If a salt is added which is capable of reacting with g the strong sulphuric acid with formation of an acid sulphate, or which mutually interacts with the sulphuric acid, the strength of the sulphuric acid should be so chosen that,
7 after the amount required for the formation of the acid sulphate or for the mutual interaction-is used up, the coagulating bath contains free sulphuric acid of the desired strength, but at any rate not less than about 50, preferably about 55 parts by weight of monohydrate in 100 parts by weight of the precipitating bath.
The process may also be carried out in such a manner that the formed thread is first coagulated by means of a setting bath known from the vlscose artificial silk art regardless whether such bath coagulates the viscose in a form soluble or insoluble in water, whereupon the thread is treated with a liquid that consists of, or contains one or more stronger mineral acids, preferably strong sulphuric acid for example such of 50 to 94 per cent or more strength (calculated on monohydrate) This can be done, for example so, that the viscose is forced to pass through suitably formed alpertures into a coagulating bath known from t 1e viscose artificial silk art, for instance into a solution of ammonium sulphate or sodium bisulphate or into dilute sulphuric acid, for instance such of 10 per cent strength, or into a liquid containing sodium sulphate or sodium bisulphate and dilute sulphuric acid, or into a li uid containing ammonium sulphate and sulp uric acid, and that the thread, after having been immersed in said bath for a longer or shorter time or distance, is introduced into a second bath which consists of, or contains one or more strong mineral acids, rcferabl y strong sulphuric acid, for example such of 50 to per cent of H,SO,.
.The strength of the sulphuric acid depends, ceteris paribus, partly on the time of maturing given the alkali cellulose, partly on the time of ripening given the finished viscose and partly on the viscosity or amount of cellulose contained in the viscose. As a rule, to which, however, the invention is not confined, it may be stated that viscoses which have matured for several days and viscoses that have been prepared from alkali cellulose that has been allowed to mature for a relatively long time, for example 2 to 3 days, and viscoses that are poor 1n cellulose or little visin cellulose or highly viscous. In fact, the 7 best viscoses for use in this invention are such as have a viscosity of 2 or more, as compared with glycerine, the viscosity of which is taken as unity.
There is in some cases also advantage in' using a viscose in the reparation of which there has been used carbon bisulphide amounting to over 40 per cent. of the weight of the cellulose used in making the Viscose. As a rule, when using the larger proportion of carbon bisulphide in the production of the viscose, longer aging of the viscose is desirable.
The strength of the sulphuric acid is further, to a certaindegree, dependent on the length of immersion in the coagulating bath and thetension given the coagulated mate rial in the acid or outside it, for example between the coagulatin bath and the collecting device, for example bobbin.
The precipitating bath may be kept at room temperature or at a temperature exceeding room temperature, for example at 25 to 50 C. but asa rule I prefer to employ a temperature lower than room temperature, for example at 0 to 10 C.', or even below 03 (1, for example at from 1 to -10 C.
The length of thethread or filament immersed in the strong sulphuric acid or in the bath containing it, may be varied within wide present process.
limits, for example from 3 to 60 centimetres and even more, for instance 1 to 2 metres, de pending generally on the age of the viscose and the temperature and concentration of the spinning bath.
If desired the thread may be stretched either immediately after its formation, that is in the coagulating bath containing, or consisting of, strong sulphuric acid, or subsequently, that is bet-ween the coagulating bath and the collecting device, such as bobbin or centrifuge, or both in the coagulating bath and between the coagulating bath and the collecting device.
Since, during prolonged contact with sulphuric acids of the strengths used in my process, cellulose is attacked and ultimately destroyed, it is essential .to check the action of the acid on the filament or the like formed, by washing or other means, for instance subjecting the formed thread to a low temperature, and this is preferably carried out before or during the deposition of the thread upon the bobbin or in the centrifugal box or similar device. This immediate checking of the action of the acid is of less importance if the thread or the like is collected in thin layers, in which case a somewhat delayed washing is possible; such collection 1n thin .layers, however, is not the best practice, for
reasons well-known to those skilled in the art.
The thread, after washing, may be heated or steamed before or after drying.
Any suitable viscose may be used in the The process gives good results with viscoses that are prepared from alkali cellulose that has been allowed to mature for such a time as is commonly allowed for maturing alkali cellulose in the artificial silk art, but generally speaking more satisfactory results are obtained with viscoses in the manufacture of which alkali cellulose is used which has not been allowed to mature at all, or has been allowed to mature for a shorter time than is usual in the artificial silk art, that is, not longer than for example about 36 hours, for example 1 to 24 hours.
As a further rule it may be stated that such viscoses as are prepared from alkali cellulose that has not been matured or has been matured for a shorter time than is usual in the artificial silk art, i. e. not longer than about 36 to 48 hours, for example 1 to 24 hours, yield strong threads if spun into sulphuric acld containing about 50 per cent of I-I SO,,whilst the lower limit of the concentration of the sulphuric acid for obtaining strong threads from viscoses prepared from alkali cellulose that has been matured for a longer time than 36 to 48 hours (according to the quality of the starting cellulose and to the temperature of maturing the alkali cellulose) 1s about per cent of H 30 The present 1nvent1on gives good results with such viscoses also as are prepared by directly mixing the ingredients.
If desired, there may be added to the viscose one or more suitable substances known in the viscose-silk art, for example g1 ycerine or glucose or sodium sulphate or sodium sulphite or sodium bisulphite or ammonium sulphate 'or an alkali silicate or an alkali aluminate or ammonia.
It will be seen from the foregoing statements that success in obtaining threads of dry tenacity, exceeding 2 grammes per denier by the use of sulphuric acid of about 55 per cent strength or more, depends upon many factors which vary with the particular strength of acid selected. It is impossible to indicate every condition for success in every particular case and it is to be understood that experiment cannot be avoided to find what are the conditions necessary for success when using a particular cellulose, a particular form of viscose and particular details of the spinning operation. I give the following examples of carrying out the process without confining the invention to these particular examples.
I. (a) to (I (a) Place 100 parts of wood pulp containing from 910 per cent of moisture, or 100 parts of linters containing 7-8 per cent of moisture, in 2,000 parts of 18% caustic soda solution at 15 C. and allow to steep for three hours, then press the pul until its total weight is 300 parts, or in t e case of liii'ters 340 parts, then grind it in a milling machine for 2% to 3 hours at 11 (1, then, without allowing the alkali cellulose to ripen for any further length of time, add 40 to parts of carbon bisulphide and allow to react for 8 hours at 15 to 18 0., then blow off any excess carbon bisulphide for 10-15 minutes, and dissolve the cellulose xanthate so obtained us ing so much water and caustic soda that the final solution on analysis contains about 6.5 per cent of cellulose and 8 per cent NaOH. Filter the viscose three timethrough cotton wool, two filtrations being carried out soon after its preparation and the other just before spinning. Allow the viscose to age for 90-96 hours at 1315 C. for spinning. Force the viscose at a rate of about 3 c.-c. per minute through a platinum jet containing 24 holes, each of 0.12 mm. diameter into a bath containing per cent sulphuric acid at 8 0., giving the thread alength of immersion in the sulphuric acid for 80 cms. and then leading the thread through a passage in free air of at least 120 cms. and winding on a bobbin which rotates at such a speed that the thread is drawn at about 80 metres per minute. The thread thus produced is made up of filaments of about 3 to 4 deniers each. In the aforesaid air passage three glass rods are situated over which the thread runs and which create an loo cial silk. For instance, I am able by-inyr process to obtain threads pos'esssing. a dry tenacity of more than 2 grammes per denler and 1n some cases the dry tenacity has beenas large as or more than 4 grammes and even 5 grammes, while the wet "tenacity; is .correspondingly high and may be, for instance, 1.5
to 2.5 grammes per denier or-more.
(b) The mode of'operation is'as in (a), except that the viscose is forced at a rate of about 0.9 to 1.2 c. e. per minute through the platinum jet, and that the bobbin rotates at.
such a speed that the thread is drawn at about 18 metres er minute. so that the thread obtained is ma e up of filaments of about 1.5 to 3 deniers each.
(a) The mode of operation is as in (a) or (1)), except that the temperature of the coagulating bath is 25 C.
(d) The mode of operation is as 1n (a), except that the temperature of the coagulating bath is 25 C. and that the length of immersion is 20 to' 30. centimetres only.
(e) The mode of operation is as in (a) or (b), with the exception that the temperature of the coagulating bath is 40 to (J. and that the length of immersion is 20 to 30 centimetres only.
(f) The mode of operation is as-in (a), or (b) with the difierenc'e that the bath contains to per cent sulphuric acid.
(g) The mode of operation is as in (a),
or (6), except that the temperature of the coagulating bath is 5 C. (h) The mode of operation is as in (a), or (b), or (e), or (f) with the exception that the viscose is allowed to age for 144 to'200 hours at 13 to 15 C. before spinning.
- as coagulating bath."
111; (a) we (a) 100 parts of a sulphite-pulp or linters are impregnated with 900 to 2,000 parts of a causticsoda. solution of 18 per cent. strength at 15 to 18 0., and the mixture is allowed to stand for 3 to'24' hours. Then the mass is ressed to 300 to 400 parts and comminuted by hand or in a suitable apparatus, for instance in a cooled shredder. The comminuted soda cellulose is then kept for '60 to 7 2 hours at room temperature, whereafter 30 to 60 parts of carbon bisulphide are added, and the mixture preferabl while stirring (for example m a closed eading machine) or agirtating (for exam le in a sulphidizing drum),
is kept for sever lf gr example 4 to 8) hours at 16 to 20 C. ereafter the excem of the carbon bisulphide is removed by driving off or cvacuatin and then the sulphidized mass is dissolve in water or dilute caustic soda solution in such a manner that the vlscose'co'ntains about 8 to 12 per centof cellulose (determined in the known manner itating with acid, washing and dry manner through cotton wool or a dense cotton fabric or thron -h both and freed from gas bubbles. Immediately after, or after it has been allowed to ripen at 16-18 C. for a shorter (for example, 12 hours to two days). or a longer (for example, four days to seven days) time, the viscose is spun as in Example I into one of the following precipitating baths:
$1; Sulphuric acid of 50 to 55 B., or 2 Sulphuric acid of 45 to 50 B., or (3) A solution of 13.3 parts of ammonium sulphate in 120 .parts of sulphuric acid of 50 to 55 B. to which 7 to 9 parts of sulphuric acid of 66 B. have been added, or
(4) A. solution of 10 to 15 arts of hicosein 190 to 185 parts by weig t of sulphuric acid of 45 to55 B.
Inc
The temperature of the coagulating bath I is kept at O to 16 C. for instance at 8 CL, or at -4 to 8. C.
The length of the threads immersed in the coagulating bath inwhich -th ey-are being formed ma be short',"for example 10 centimetres, or ong, for instance from 30 to ,100 centimetres and more. They are then collected on a bobbin or in a spinnin centrifuge which may be placed either close by the precipitating bath'or in a distance from 20 to centimetres from the bath, whilst the sulphuric acid is quenched or diluted as in Example I. The threads are then further washed anddried.
The threads may be stretched in any known manner whilst they are in the coagulating bath, or after they have been removed from the bath, that is, between the coagulating bath and the collecting device. This may be done, for example, either by choosing a more or less long distance between the bath and, 125
the collecting device, or by leading the threads over rods or hooks arranged in the bath or between the bath and the collecting device, or in the bath and between the bath and the collecting device.
The speed of spinning may be varied with in wide limits. As a rule, to which, however, the invention is not intended to be confined, it may be assumed that the upper limit of speed possible is dependent partly upon the temperature of the coagulating bath, partly upon the length of immersion, partly upon the distance between the coagulating bath and the collecting device, partly upon the degree of stretchlng given the thread durin spinning, and partly upon the quantity o viscose delivered by the pump. The following examples, to which, however, the process is not intended to be limited, may be adduced for the purpose of illustration:
(1) If the coagulating bath is used at a temperature below C., for example at 0., and if the length of thread immersed is 60 to 120, for example 80 centimetres, and if the distance between the coagulating bath and the collecting device, for example bobbin, is 60 to 1.50 centimetres, for instance 120 centimetres, and if the stretching given the thread between the coagulating bath and the collecting device is comparatively high, and if the pump delivers about 2 to 3 cubic centimetres of viscose a minute, then excellent results are obtained with a speed of 18 to 26 metres a minute, or of metres a min ute, but also, a higher speed may be used if desired.
(2) If all spinning conditions remain the same as in (1), except that the pump delivers 4 to 5 cubic centimetres of viscosea minute,
- then, if desired, a speed up to to 60 metres a minute may be used.
(3) If the spinning conditions are exactly as in (1), except that the temperature of the coagulating bath is 4 to 25 (1., for example 8 (1, if desired the speed may be up to to metres a minute.
If in 1) the length immersed or the dis tance between the coagulating bath and the collecting device or both are shortened, it is recommended not to use too low a speed.
If no additional stretch to the thread is applied during spinning, it is recommendable to employ high speed.
' Before the final washing, the threads may be treated in any known manner with a coagulating bath known in the viscose-silk art,
for example a solution of sodium bisulphate or sodium bisulphite or with dilute sulphuric acid or the like.
The washed threads may, before or after drying, be heated (for example, at 100-110 C.) or steamed.
They may also be treated with any desulphurizing or bleaching agent known in the viscose art.
(b) The mode of operation is as in (a), except that 75 or more parts of carbon bisulphide are used for the sulphidizing of the soda-cellulose.
(c) The mode of operation is as in (a) or (b), with the difl'erence that the soda-cellulose is pressed to 200 parts.
Mode of operation as in Example III (a), or III (6), or III (0), with the difference- (1) That the sulphidized mass is dissolved in water or dilute caustic soda solution so as to yield a viscose that contains 5 to 8 per cent of cellulose, for instance, 6 to 7 per cent of cellulose (determined in the known manner by precipitating with acid, washing and drylng (2) That as coagulating bath one of the following baths is used (l) Sulphuric acid of 55 to 60 B., or
(2) Sulphuric acid of 50 to 55 B., or
( 3) A solution of 13.3 parts of ammonium sulphate in 120 parts of sulphuric acid of 50 to 60 B. to which 7 to 9 parts of sulphuric acid of 66 B. have been added, or
(4 A solution of 10 to 15 parts of glucose in 190 to 185 parts of sulphuric acid of 55 to 60 B.
Mode of operation as in Example III (a), or III (7)), or III (a), or as in Example IV, with the exception that the viscose is not allowed to mature at all, or to mature for 12 to 48 hours only, and that as coagulating bath sulphuric acid of 60 to 64 B., for instance sulphuric acid of 62 B., at 6 to 10 C. is used.
In using so strong an acid it is preferable to run the spinning at a high speed, for example 40 to 60 metres a minute.
VI. (a) to (e).
(a) 100 parts of sulphite-pulp or linters are impregnated with 900 to 2,000 parts of a caustic soda solution of 18 per cent strength at 15 to 18 (1, and the mixture allowed to stand for 3 to 24 hours. Then the mass is pressed to 300 parts in the case of sulphite pulp and to 340 parts in the case of linters and comminuted by hand or in a suitable apparatus, for instance, in a cooled shredder.
Immediately or soon after (for example 1 hour) the comminution, 40 to 60 parts of carbon bisulphide are added, and the mixture, preferably while stirring (for example in a closed kneading machine) or agitating (for example in a sulphidizing drum) is kept for several hours (for example 4 to 12) at 16 to 20 C. Thereafter the excess of the carbon bisulphide is removed by driving off or evacuating, and the sulphidized mass, the weight of which generally amounts to from about 330 to 400 parts, is dissolved in 650 to 900 and in the case of linters even up to 1050 parts of a caustic soda solution of 6.5 to 10 per cent strength. The viscose solution thus or through both and freed from gas bubbles. Immediately after, or after it has been allowed to ripen at 1518 C. for a shorter (for example 12 hours to two days) or a .sulphate in 120 parts of sulphuric acid of 55 to 60 B., to which 9 to 10 parts of sulphuric acid of 66 B. have been added, or
Asolution of 15 parts of ammonium sulphate in 120 parts of sulphuric acld of 40 to 45? B., to which 9 to parts of sulphuric acid of 66 B. have been added.
(6) A solution of 10 to parts of glucose in 190485 parts of sulphuric acid of 55 to 60 B.
The temperature of the coagulating bath iskept at 0 to 16 (3., for instance at 8 C. or at' *4 to 8". C.
The threads are spun and treated during and after spinning in the same manner as described in the foregoing examples.
(6) The mode of operation is as in (a), with the difference that a caustic soda solution of 3 to 5 per cent strength is used for dissolving the sulphidized soda cellulose. Accordingly, the viscose is somewhat more viscous.
(c) The mode of operation is as in (a), or (b) except that 75 or more parts of carbon bisulphide are used for sulphidizing the sodacellulose.
(d) The mode of o ration is as in (a), or (b), or (0), with t e difference that the soda-cellulose is pressed to 200 parts.
(a) The mode of operation is as in (a), or (b), or (c), or (d), with the diflerence that sulphuric acid of 62 to 64 B. at 8 C. is used as coagulating bath, the viscose being 12 to 48 hours old and the speed of spinning about 45 to 60 metres a minute.
VII.
, mass may be equal to those used in Example VI or somewhat lower, for example so as to produce a 10 to 12 per cent viscose (calculated on the parent cellulose).
The viscose is worked up into threads as in VI (a) to (e).
VIII. (a) to (d). (a) 80-100 parts of finely divided sulphitepulp or bleached cotton are mixed with 920- 900 parts of a caustic soda solution of 8 to 10 per cent strength. To this mixture 40 to 150 parts of carbon bisulphide are added and the mixture kept at room temperature for 12 to 7 2 hours, preferably under continual or temporary stirring or kneading. .The viscose solution thus obtained is filtered in a known manner through cotton wool or a dense cotton fabric or through both and freed from "as bubbles, if any. Immediately after, or after it has been allowed to ripen at'1618 C. for a shorter (for example 12 hours to two days) or a longer (for example four days or seven days) time, the viscose is spun as in Example I into one of the following coagulating baths (1) Sulphuric acid of 55 to 60 B., or
(2) Sulphuric acid of to B.,or
(3) A solution of 13.3 parts of ammonium sulphate in 120 parts of sulphuric acid of 45 to B. to which 7 to 9 parts of sulphuric acid of 66 B. have been added, or Y (4) A solution of 10 to 15 parts of glucose in 190 to 185 parts of sulphuric acid of 45 t0'60 B.
The temperature of the coagulatingbath is kept at 0 to 16 C., for instance at 8 C. or at t to 8 C.
The threads are spun and treated as in the foregoing examples. 4
(6) Mode of operation as in (a), with the exception that the viscose is prepared according to the method 3 in the British specification No. 212,865, for example according to the following examples of t at specification. I (a) to (e), or II (a) to (c), or III (a) to (c),orIV (a) to (e), orV (a) to b), 'orVI (a) or (a), or VII to VIII, or I to X, or XII, or XIII.
(0) Mode of operation asin (a), or (b), with the exception that, before or after the addition of carbon bisul hide, a small quantity of a catalyzer is a ded to the mixture of the cellulosic body with the caustic alkali solution, for example 0.2 to 1 part of a soluble chromic salt or nickel salt or iron salt.
(d) Mode of operation as in (a), or (b), with the difference that, before or afterthe addition of carbon bisulphide, a small quantity of a soluble peroxide, such as 5 to 20 parts of sodium peroxide to 100 parts of parent cellulose is added.
of 6.15 per cent strength, the weight of the sulphidized mass being 330 parts. The final viscose contains 8 per cent of parent cellulose.
This viscose is filtered and spun and the threads are treated as in the foregoing examples.
X. (a) and (b).
(a) A viscose prepared according to one of the formulas given above is spun in a wellknown manner into:
1) A solution of ammonium sulphate of to per cent strength, or
(2) In a bath consisting of 500 parts of sodium bisulphate, 76 parts of sulphuric acid of 66 B6. and 587 parts of water, which bath may be kept at room temperature or at a raised temperature, for instance 50 C., or
(3) In a bath consisting of 990 parts of water,'180 parts of ammonium sulphate, 15 parts of zinc sulphate, 135 parts of glucose and 255 parts of sulphuric acid of 66 Be.
The formed thread is introduced directly from one of the foregoing baths into one of the following baths:
(1) Sulphuric acid of 55 B., or (2 Sulphuric acid of B., or
(3) A solution of 13.3 parts of ammonium sulphate in 120 parts of sulphuric acid of to B. towhich 9 to 10 parts of sulphuric acid of 66 B. are added.
The temperature of the second-bath may be kept below room temperature, for instance at 0 to 10 0., or at room temperature, or even above room temperature, for example at 25 to 45 C.
The length of immersion given the thread in the second bath may be short, for instance 20 centimetres, or long, for example 30 to 100 centimeters or more.
The threads are then collected whilst the sulphuric acid is quenched or diluted as described above, and the threads are finally washed, dried and treated as in Example I.
(6) Mode of operation as in (a), with the difference that as second bath hydrochloric acid of 40 per cent is used.-
In all foregoing examples the arresting of the action of the acid may be also .done by subjecting the thread leaving the coagulating bath consisting of, or containing the strong acid to a loW temperature, for instance to 5 to 15 C. before washing.
Examples for producing staple fibre follow automatically from the foregoing examples.
According to the foregoing examples, it is possible to obtain artificial silk or staple fibre which has a considerably greater. dry or wet tenacity than silk spun under the same spinning conditions, but by means of chemicals customary in the viscose silk art, for fixample by using a known precipitating bat For example, it is not diflicult to produce by the present invention artificial silk having a dry tenacity of more than 2 grammes per denier, even more than 3 grammes per denier, for example 3 to 4 grammes per denier and more and a wet tenacity of 1.5 to 2.5 grammes per denier and more.
Instead of strong sulphuric acid there may be used in the foregoing examples a strong halogen hydracid, such as hydrochloric acid, for exampde of 35 to 40 per cent strength, or nitric acid, for example such as contains to 90 per cent of I-INO,,, or phosphoric acid, for example of 1.5 to 1.86 specific gravity, or arsenic acid, for example such as contains from 60 to 90 per cent of I-I,As(),. p
In the foregoing examples, in the preparation of viscose, instead of wood-pulp, there may be used bleached or' unbleached cotton, or cellulose treated in the cold or in the heat with dilute acids, for example hydrochloric been. shortly matured means either-an alkali cellulose made from standard commercial cellulose of the type commonly provided for viscose manufacture, which alkali cellulose has been matured in the mercerization stage for a shorter period than is common in viscose manufacture (say, less than 36 hours at a temperature of 1522 6.), or alkali cellulose in which the modification of the cellulose that characterises the effect of maturing has been kept below that of the practice normal in making silk by means equivalent to a short period of maturing, such as by restriction of a catalytic action, a diminished temperature or the selection of a special type of cellulose. These means are Well-known in the art.
The expression strong mineral acid means in the description and in the claims: sulphuric acid of at least 50 per cent I-I SO and the other mineral acids equivalent in strength, i. e. hydrochloric acid of at least 35 per cent strength, nitric acid of at least 60 per cent strength, phosphoric acid of at least 1.5 specific gravity and arsenic least 60 per cent of H AsO The expression strong sulphuric acid or sulphuric acid containing at least 50 per cent of sulphuric acid monohydrate means in the description and claims: sulphuric acid of 50 to 98 or 100 per cent strength.
The expression cellulose used in the. product claims is intended to mean: cellulose or cellulose hydrate, as the body regenerated acid of at' from viscose is regarded by some cellulose.
The statements in the description and claims regarding percentages relate to percentages by weight.
The artificial threads produced accordin to the present process may be distinguishe from artificial threads consistingof, or containing cellulose or cellulose hydrate, particularly from viscose silk produced after methods known hitherto, or from cuprammonia silk by means of a very dilute solution of iodine in an aqueous solution of potassium iodide or by a solution of zinc chloride to which a very small 'quantity of a solution of iodine in an aqueous solution of potassium iodide has been added.
While with the first solution viscose silk produced according to processes known hitherto is colored a deep reddish brown, copper silk a brownish black or reddish brown, denitrated nitrate silk a brownish reddish-black, silk produced according to the present process is colored a very light olive gray.
When using the second solution, viscose silk produced by a method known hitherto and copper silk are colored blue, while silk produced according to the present process remains either perfectly colorless or is tinted a grayish blue. I
It is essential that the quantity of iodine in both solutions, particularly in the zinc chloride solution must be very minute.
These reactions may be executed for exam- Second reaction.
Solution 1: contains 28 grams of zinc chloride in 30 c. c. of solution.
Solution 2: 1 gram iodine and 20 grams of potassium iodide dissolved in 100 c. c. of water.
Immediatelybefore using, from 0.4 to 0.6 c. c. of solution 2, are added to 100 c. c. of solution 1. The samples of silk are then immersed in the solution, when, after a short a deep reddish time, the following colorations will appear:
Ordinary viscose silk: a deep blue, which does not disappear when the silk remains in the solution-for 1 to 2 hours and lon er.
Viscose silk produced according to t e present invention: colorless, or a greylsh blue tint,
Itshould be pointed out that, if there is an excess of iodine present in the solution, all the various silks will be colored.
The presentapplication is a part continuation of my copending application Serial No. 113,582 filed June 3, 192
I claim: 1'. Process for manufacturing artificial threads of high-dry tenacity, exceeding 2 grammes per denier, from viscose, which comprises causing a viscose to pass through suitably formed openings into contact with a liquid which contains not less than about 65 per cent of sulphuric acid monohydrate.
2. Process for manufacturing artificial threads of high dry tenacity, exceeding 2 grammes per denier, from viscose, which comprises causing a viscose to pass through suitably formed openings into contact" with a liquid which contains not less than about 65 per cent of sulphuric acid monohydrate, and checking the action of the strong sulphuric acid not later than the thread arrives at the collecting device.
3. Process for manufacturing artificial threads 'of high dry tenacity, exceeding 2 grammes per denier, from viscose, which comprises causing a vis ose to pass through suitably formed openinigs into a bath containing not less than about 55 per cent of sulphuric acid monohydrate and applying 'to the coagulated thread additional stretch in the course of its passage after it enters the bath and before it is washed.
4. Process for manufacturing artificial threads of high dry tenacity, exceeding 2;
grammes per denier, from viscose, which comprises causing a viscose to pass through suitably formed openings into a bath containing not less than about 55 per cent of sulphuric acid monohydrate, and applying to the coagulated thread additional stretch in the course of its passage after it enters the bath and before it is washed, and checking the action of the strong sulphuric acid not later than the thread arrives at the collecting device. 1
5. The process of coagulating a viscose which comprises cont-acting it with at least one strong mineral acid of a strength equiva lent to at last 50 per cent sulphuric acid monohydrate.
I mpe es with at least one strong mineral acid of a strength equivalent to at least per cent sulphuric acid monohydrate.
9. The process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains at least about 50 per cent sulphuric acid monohydrate.
10. The process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains not less than about per cent sulphuric acid monohydrate.
11. The process of coagulating a viscose which comprises contacting it with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the coagulated viscose occur.
12. The process of coagulating a viscose which comprises contacting it with a liquid which contains at least about 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon thecoagulated viscose occur.
13. The process of coagulating a viscose which comprises contacting it with a liquid which contains not less than 55 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the coagulated viscose occur.
14. The process of manufacturing artificial thread of high dry tenacity which comprises contacting athreadlike stream of a viscose with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
15. The process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains at least about 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
16. The process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains not less than about 55 per cent sulphuric acid monohydrate and checking the. action of the acid before injurious effects upon the thread occur.
0 17. The process of manufacturing artificial thread of high dry tenacity which comprises contacting a threadlike stream of a viscose with a liquid which contains at least about 50 per cent sulphuric acidmonohydrate and diluting the strong acid adhering to the thread by washing the thread before it is injured by the strong acid.
18. The process for manufacturing artificial bodies from a viscose which comprises bringing a viscose into the form'o-f an artificial body and contacting said body with at least one strong mineral acid of a strength equivalent to at least 55 per cent sulphuric acid monohydrate.
19. The process for manufacturing artificialthread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it. with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid nionohydrate.
20. The process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains at least about 50 per cent of sulphuric acid monohydrate.
21-. The process for manufacturing artificialthread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains not less than about 55 per cent of sulphuric acid monohydrate.
22. The process for manufacturing art-ificial thread of high dry tenacity which comprises bringing a Viscose into the form of an artificial thread and contacting it with at least one strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur. x
23. The process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains at least 50 per cent of sulphuric acid monohydrate and checking the action of the acid before injurious effects upon the thread occur.
24. The process for manufacturing artificial thread of high dry tenacity which comprises bringing a viscose into the form of an artificial thread and contacting it with a liquid which contains not less than about 55 per cent of sulphuric acid monohydrate, and
phuric acid monohydrate and diluting the strong acid adhering to the thread by washing the thread before it is injured by the strong acid.
26. As a new product, artificial thread of the type as obtained by coagulating viscose in a bath containing a strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate, consisting substantially of regenerated cellulose and having a dry tenacity of considerably more than 2 grams per denier.
27. As a new product, artificial thread of the type as obtained by coagulating viscose in a bath containing a strong mineral acid 0 a strength equivalent to at least 50 per cent sulphuric acid monohydrate, consisting substantially of regenerated cellulose and having a dry tenacity of more than 3 grams per denier.
28. As a new product, artificial thread of the type as obtained by coagulating viscose in a bath containing a strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate, consisting substantially of regenerated cellulose and having a dry tenacity of more than 4.- grams per denier.
29. As a new product, artificial thread of the type as obtained by coagulating viscose in a bath containing a strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate, consisting substantially of regenerated cellulose and having a wet tenacity of more than 1.5 grams per denier.
30. As a new product, artificial thread of the type as obtained by coagulatingviscose in a bath containing a strong mineral acid of a strength equivalent to at least 50 per cent sulphuric acid monohydrate, consisting substantially of regenerated cellulose and having a wet tenacity of more than 2 grams per denier.
31. The process of coagulating a viscose which comprises contacting it with a liquid ,Which contains at least 65 per cent sulphuricacid monohydrate.
32. The process of manufacturing artificial bodies from a viscose which comprises bringing a viscose into the form of an artificial body and contacting said body with a liquid which contains at least 65 per cent sulphuric acid inonoliydrate.
In testimony whereof I afiix my signature.
DR. LEON LILIENFELD.
all
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US186575A Expired - Lifetime US1989098A (en) 1925-06-20 1927-04-25 Manufacture of artificial threads
US367148A Expired - Lifetime US1989099A (en) 1925-06-20 1929-05-29 Process of improving artificial threads
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US2439039A (en) * 1944-09-26 1948-04-06 American Viscose Corp Process of producing medullated artificial filaments
US2457350A (en) * 1943-07-07 1948-12-28 American Viscose Corp Method and apparatus for spinning artificial filamentous products
US2467541A (en) * 1943-07-03 1949-04-19 American Viscose Corp Method and apparatus for spinning artificial filamentous products
US2515834A (en) * 1942-11-13 1950-07-18 Du Pont Cellulose filaments and method of producing same
US2517694A (en) * 1943-09-14 1950-08-08 American Viscose Corp Crimped artificial filament
US2518753A (en) * 1949-07-14 1950-08-15 Du Pont Crimped yarn production
US2535045A (en) * 1947-04-26 1950-12-26 Du Pont Spinning of viscose
US2536014A (en) * 1946-12-14 1950-12-26 Du Pont Spinning of viscose
US2581835A (en) * 1946-03-22 1952-01-08 Du Pont Method of spinning viscose
US2946650A (en) * 1958-02-17 1960-07-26 Tatsuji Tachikawa Process for the manufacture of viscose rayon staple
US20100291823A1 (en) * 2008-01-11 2010-11-18 Lenzing Ag Microfiber

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DE749264C (en) * 1938-11-09 1944-11-21 Ig Farbenindustrie Ag Process for the production of synthetic fibers or threads from viscose
DE749501C (en) * 1941-05-25 1952-04-17 Spinnfaser A G Process for the production of rayon from viscose
DE903208C (en) * 1943-01-23 1954-02-04 Schachenmayr Mann & Cie Process for curling cellulose hydrate cellulose wool or rayon
US2509549A (en) * 1943-11-06 1950-05-30 Du Pont Process of producing highly extensible regenerated cellulose yarn
NL61100C (en) * 1944-02-15
US2531513A (en) * 1944-04-20 1950-11-28 Celanese Corp Process for the production of textile materials
US2479218A (en) * 1944-12-12 1949-08-16 Int Paper Canada Process for making rayon filaments
GB605536A (en) * 1944-12-30 1948-07-26 Christian Bener Process for refining textiles made of regenerated cellulose
BE471098A (en) * 1946-04-24
US2647036A (en) * 1946-08-17 1953-07-28 Hogg & Mitchell Ltd Curving cellulose collar blanks by differential shrinking with chemical shrinking agents
US2497519A (en) * 1946-12-04 1950-02-14 Alrose Chemical Company Art of stabilizing rayon type fabric
BE480557A (en) * 1947-04-14
NL71391C (en) * 1947-05-28
US2512951A (en) * 1947-06-16 1950-06-27 Dixie Mercerizing Company Mercerization
BE488949A (en) * 1948-05-11
US2586795A (en) * 1948-05-11 1952-02-26 Textile & Chem Res Co Ltd Pneumatic tire
US2536094A (en) * 1949-09-17 1951-01-02 American Viscose Corp Process for spinning artificial fibers
GB709700A (en) * 1950-08-11 1954-06-02 Textile & Chem Res Co Ltd Improvements in or relating to the production of cellulose xanthogenate compositions
BE510207A (en) * 1951-04-25
US2935372A (en) * 1955-02-21 1960-05-03 Du Pont Process of producing shaped bodies by combining reactive intermediates, at least one of which intermediates is in the vapor phase
US3084020A (en) * 1956-05-30 1963-04-02 Rene Ruegg Method of treating knitted superpoly-amide textile fabric with an aqueous phenol bath subjected to ultra-sonic waves and fabric produced thereby
US3511591A (en) * 1965-04-09 1970-05-12 Deering Milliken Res Corp Process and product of rendering cellulosic fabrics amenable to molding operations
US3689613A (en) * 1970-11-02 1972-09-05 Anselm Talalay Glove making
FR2175582B1 (en) * 1972-03-14 1974-08-02 Omnium De Prospective Ind Sa
US4196559A (en) * 1973-03-28 1980-04-08 Ljungbo Sven O B Swellable fabrics for ceiling structures
DE2720087A1 (en) * 1976-05-07 1977-11-24 Centre Tech Ind Papier PROCESS FOR MANUFACTURING VISCOSE FEMES AND FEMES PRODUCED BY THE PROCESS
FR2377462A2 (en) * 1977-01-13 1978-08-11 Centre Tech Ind Papier Viscose fibre prepn. - by spinning, coagulating in a volatile gas, partially regenerating and then completely regenerating
FR2372251A1 (en) * 1976-11-26 1978-06-23 Rhone Poulenc Textile NEW PROCESS FOR SPINNING OR SHAPING CELLULOSE SOLUTIONS AND ARTICLES THUS OBTAINED
JPS6027496B2 (en) * 1977-10-19 1985-06-29 南国パルプ工業株式会社 Manufacturing method of cellophane for casing
US5849818A (en) * 1993-06-03 1998-12-15 Walles; Wilhelm E. Skin sulfonated particles in matrices

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2515834A (en) * 1942-11-13 1950-07-18 Du Pont Cellulose filaments and method of producing same
US2467541A (en) * 1943-07-03 1949-04-19 American Viscose Corp Method and apparatus for spinning artificial filamentous products
US2457350A (en) * 1943-07-07 1948-12-28 American Viscose Corp Method and apparatus for spinning artificial filamentous products
US2517694A (en) * 1943-09-14 1950-08-08 American Viscose Corp Crimped artificial filament
US2439039A (en) * 1944-09-26 1948-04-06 American Viscose Corp Process of producing medullated artificial filaments
US2581835A (en) * 1946-03-22 1952-01-08 Du Pont Method of spinning viscose
US2536014A (en) * 1946-12-14 1950-12-26 Du Pont Spinning of viscose
US2535045A (en) * 1947-04-26 1950-12-26 Du Pont Spinning of viscose
US2518753A (en) * 1949-07-14 1950-08-15 Du Pont Crimped yarn production
US2946650A (en) * 1958-02-17 1960-07-26 Tatsuji Tachikawa Process for the manufacture of viscose rayon staple
US20100291823A1 (en) * 2008-01-11 2010-11-18 Lenzing Ag Microfiber
US11932969B2 (en) 2008-01-11 2024-03-19 Lenzing Aktiengesellschaft Microfiber

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US1989099A (en) 1935-01-29
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US1820811A (en) 1931-08-25
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US2112499A (en) 1938-03-29
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NL23113C (en)
FR37344E (en) 1930-11-15
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FR666178A (en) 1929-09-27
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US1683200A (en) 1928-09-04
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