US3114592A - Process for the production of elements made of hydrated cellulose - Google Patents

Process for the production of elements made of hydrated cellulose Download PDF

Info

Publication number
US3114592A
US3114592A US123116A US12311661A US3114592A US 3114592 A US3114592 A US 3114592A US 123116 A US123116 A US 123116A US 12311661 A US12311661 A US 12311661A US 3114592 A US3114592 A US 3114592A
Authority
US
United States
Prior art keywords
viscose
production
oxide
hydrated cellulose
dimethyl
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US123116A
Inventor
Barthell Eduard
Schmidt-Neuba Hermann-Dietrich
Hilgers Friedrich
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Stockhausen GmbH and Co KG
Original Assignee
Chemische Fabrik Stockhausen GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chemische Fabrik Stockhausen GmbH filed Critical Chemische Fabrik Stockhausen GmbH
Application granted granted Critical
Publication of US3114592A publication Critical patent/US3114592A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • D01F2/06Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
    • D01F2/08Composition of the spinning solution or the bath
    • D01F2/10Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either

Definitions

  • One modification which is frequently employed consists in using substances which facilitate the production of the viscose, for example, at the time of xanthation, by shortening the time required for xanthate formation by emulsifying the carbon disulphide and/ or dispersing impurities in extremely fine form in the viscose, so that, for example, satisfactory filtration is guaranteed.
  • An improvement in the filament-drawing capacity is apparent with these additives.
  • the disadvantageous deposition of impurities from the viscose and/or from the spinning bath at the spinnerets is avoided. On account of the products added to the spinning baths or products reaching the baths from the viscose, the said baths remain free from clouding substances which otherwise usually sediment.
  • amine oxides of the general formula cording to the invention are, for example dimethyl lauryl, diethyloctyl, tributyl, dimethyl butyl, triisopropyl, triiso- 3,114,592 Patented Dec. 17, 1963 octyl, methoxyethylmethyl lauryl, dimethyl stearyl, diethyl oleyl, dimethyl cyclohexyl, dicyclohexyl methyl and dimethyl phenyl amine oxides.
  • Example 0.2 g. of dimethyl laurylamine oxide are added per litre to a viscose normally used for the production of textile filaments.
  • the eflfect of the additive is that the viscose becomes completely transparent, can easily be filtered and shows excellent filament-drawing capacity. Its surface tension is also reduced by at least 50% and, on spinning into a conventional Miiller bath, it does not cause any incrustation of the spinnerets. Impurities in the precipitation bath are also avoided.
  • Example 2 If an unripe viscose is processed, as in Example 1, using 0.8 g./l. of diethyloctylamine oxide, the effects mentioned in Example 1 are also produced. In addition, the milkiness which always occurs when processing unripe viscose is avoided.
  • Example 3 0.5 g./l. of dimethyl laurylamine oxide are added to a normal viscose to which a matting agent or a spinning dye-stuff has been added.
  • the amine oxide can also be added by first of all being mixed with the pigment, the mixture then being incorporated in the viscose. If this viscose is spun in the usual manner, more intensive matting or dyeing effects are produced than those obtained when amine oxide is not used. It is obvious that the amine oxide produces an improved dispersion of the pigment in the viscose, whereby a better utilisation of the pigment is obtained.
  • Example 4 If 2 g./l. of tributylamine oxide are added to a viscose normally used for the production of cord filaments, the stretchability is improved to a surprising degree and thereby a cord rayon with a high strength value is produced.
  • amine oxide selected from the group consisting of Dimethyl laurylamine oxide
  • Dimethyl cyclohexylamine oxide Dicyclohexyl methylamine oxide, and Dimethyl phenylamine oxide.
  • a process for the production of spun hydrated cellulose which comprises the steps of adding to viscose 0.2 g./l. referred to the viscose of an amine oxide of the formula Ra wherein R R R are selected from the group consisting of alkyl, cycloalkyl, alkoxyalkyl, and phenyl, the sum of the C atoms of the R substituents being from 6 to 24, introducing the viscose through spinnerets into a spinning bath and recovering the spun hydrated cellulose therefrom.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Description

United States Patent 3,114,592 PROCESS FOR THE PRODUCTION OF ELEMENTS MADE OF HYDRATED CELLULOSE Eduard Barthel], Hermann-Dietrich Schmidt-Neuhaus,
and Friedrich Hilgers, all of Krefeld, Germany, assignors to Chemische Fabrik Stockhausen & Cie, Krefeld, Germany, a corporation No Drawing. Filed July 11, 1961,, Ser. No. 123,116 Claims priority, application Germany July 15, 1960 6 Claims. (Cl. 18-54) This invention is concerned with a process for the production of elements made of hydrated cellulose.
It is known to manufacture fibres and films from hydrated cellulose by forcing viscose through nozzles or slots into baths which advantageously contain acid salts, the aforesaid elements being formed by decomposition of the cellulose xanthate contained in the viscose. The process may be modified in a number of ways. These modifications serve mainly to facilitate the carrying out of the process and/ or the improving of the quality of the elements produced in accordance with the process. One modification which is frequently employed consists in using substances which facilitate the production of the viscose, for example, at the time of xanthation, by shortening the time required for xanthate formation by emulsifying the carbon disulphide and/ or dispersing impurities in extremely fine form in the viscose, so that, for example, satisfactory filtration is guaranteed. An improvement in the filament-drawing capacity is apparent with these additives. Furthermore, the disadvantageous deposition of impurities from the viscose and/or from the spinning bath at the spinnerets is avoided. On account of the products added to the spinning baths or products reaching the baths from the viscose, the said baths remain free from clouding substances which otherwise usually sediment. This effect is only shown to its best effect in the spinning bath if the additive has been added directly to spinning bath. Ethoxylated amines and pyridinium compounds have inter alia been used as such additives as well as sulphonated and sulphated oils.
Rayons which in use show particularly good properties are obtained by spinning viscoses which contain cellulose with a relatively high average degree of polymerisation. However, such viscoses have a higher viscosity. In order to be able to spin such viscoses, they must be brought to a higher temperature so that the viscosity becomes lower.
With the prior known viscose additives which are active at boundary surfaces and which contain basic nitrogen, however, the disadvantage arises that at temperatures above 40 C. they no longer remain clearly soluble in the viscose or in the spinning bath. With this undesirable change in their solubility they lose their efficacy during the spinning operation.
It has been found that amine oxides of the general Formula I below do not show these disadvantages and can best be used as additives to the viscose and also to the spinning bath.
According to the invention therefore, there is provided a process for the production of elements of hydrated cellulose from viscose in which there is added to the viscose or to a bath in which the viscose is to be precipitated one or more amine oxides of the general formula cording to the invention are, for example dimethyl lauryl, diethyloctyl, tributyl, dimethyl butyl, triisopropyl, triiso- 3,114,592 Patented Dec. 17, 1963 octyl, methoxyethylmethyl lauryl, dimethyl stearyl, diethyl oleyl, dimethyl cyclohexyl, dicyclohexyl methyl and dimethyl phenyl amine oxides.
The addition of the compounds according to the invention to the viscose results in substantially all the improvements indicated above, these compounds when added to the viscose being substantially as effective in the precipitation bath as if they had been directly added thereto.
In order that the invention may be well understood, the following examples are given, by way of illustration only:
Example 0.2 g. of dimethyl laurylamine oxide are added per litre to a viscose normally used for the production of textile filaments. The eflfect of the additive is that the viscose becomes completely transparent, can easily be filtered and shows excellent filament-drawing capacity. Its surface tension is also reduced by at least 50% and, on spinning into a conventional Miiller bath, it does not cause any incrustation of the spinnerets. Impurities in the precipitation bath are also avoided.
Example 2 If an unripe viscose is processed, as in Example 1, using 0.8 g./l. of diethyloctylamine oxide, the effects mentioned in Example 1 are also produced. In addition, the milkiness which always occurs when processing unripe viscose is avoided.
Example 3 0.5 g./l. of dimethyl laurylamine oxide are added to a normal viscose to which a matting agent or a spinning dye-stuff has been added. The amine oxide can also be added by first of all being mixed with the pigment, the mixture then being incorporated in the viscose. If this viscose is spun in the usual manner, more intensive matting or dyeing effects are produced than those obtained when amine oxide is not used. It is obvious that the amine oxide produces an improved dispersion of the pigment in the viscose, whereby a better utilisation of the pigment is obtained.
Example 4 If 2 g./l. of tributylamine oxide are added to a viscose normally used for the production of cord filaments, the stretchability is improved to a surprising degree and thereby a cord rayon with a high strength value is produced.
We claim:
1. In a process for the production of elements of hydrated cellulose by precipitation of viscose in a precipitation bath the step of adding to the viscose at least 0.2 g./l. referred to the viscose of an amine oxide of the general formula wherein R R and R are selected from the group consisting of aliphatic hydrocarbon radicals, cycloaliphatic hydrocarbon radicals, and phenyl, the sum of the C atoms of the R substituents being from 6 to 24.
2. In the process of claim 1, the step of adding said amine oxide to the precipitation bath instead of to the viscose.
3. In the process for the production of elements of hydrated cellulose by precipitation of viscose in a precipitation bath the step of adding to the viscose 0.2 g./l.
referred to the viscose of an amine oxide selected from the group consisting of Dimethyl laurylamine oxide,
Diethyl octylamine oxide, Tributylamine oxide,
Dimethyl butylamine oxide, Triisopropylamine oxide, Methoxyethyl methyl laurylamine oxide, Dimethyl stearylamine oxide,
Diethyl oleylamine oxide,
Dimethyl cyclohexylamine oxide, Dicyclohexyl methylamine oxide, and Dimethyl phenylamine oxide.
4. In the process of claim 3, the step of adding said amine oxide to the precipitation bath instead of to the viscose.
5.A process for the production of elements of hydrated cellulose from viscose which comprises the step of adding to the viscose 0.2 g./l. referred to the viscose of an amine oxide of the general formula R1 R2 N=O Ra wherein R R and R are selected from the group con- 4 sisting of alkyl, cycloalkyl, alkoxyalkyl, and phenyl, the sum of the C atoms of the R substituents being from 6 to 24, precipitating the viscose by introduction thereof into a precipitating bath and recovering the precipitated hydrated cellulose.
6. A process for the production of spun hydrated cellulose which comprises the steps of adding to viscose 0.2 g./l. referred to the viscose of an amine oxide of the formula Ra wherein R R R are selected from the group consisting of alkyl, cycloalkyl, alkoxyalkyl, and phenyl, the sum of the C atoms of the R substituents being from 6 to 24, introducing the viscose through spinnerets into a spinning bath and recovering the spun hydrated cellulose therefrom.
References Cited in the file of this patent UNITED STATES PATENTS 2,179,195 Polak et al. Nov. 7, 1939 2,422,021 Kline et a1. June 10, 1947 2,519,227 Collins Aug. 15, 1950

Claims (1)

1. IN A PROCESS FOR THE PRODUCTION OF ELEMENTS OF HYDRATED CELLULOSE BY PRECIPITATION OF VISCOSE IN A PRECIPITATION BATH THE STEP OF ADDING TO THE VISCOSE AT LEAST 0.2 G./1. REFERRED TO THE VISCOSE OF AN AMINE OXIDE OF THE GENERAL FORMULA
US123116A 1960-07-15 1961-07-11 Process for the production of elements made of hydrated cellulose Expired - Lifetime US3114592A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEC21918A DE1217544B (en) 1960-07-15 1960-07-15 Process for the production of fibers from hydrate cellulose
DEC0027744 1962-08-18

Publications (1)

Publication Number Publication Date
US3114592A true US3114592A (en) 1963-12-17

Family

ID=25969320

Family Applications (1)

Application Number Title Priority Date Filing Date
US123116A Expired - Lifetime US3114592A (en) 1960-07-15 1961-07-11 Process for the production of elements made of hydrated cellulose

Country Status (5)

Country Link
US (1) US3114592A (en)
BE (2) BE635885A (en)
DE (1) DE1217544B (en)
GB (2) GB947115A (en)
NL (2) NL296702A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2179195A (en) * 1935-02-16 1939-11-07 American Enka Corp Manufacture of artificial silk
US2422021A (en) * 1940-07-29 1947-06-10 Ind Rayon Corp Manufacture of thread or the like
US2519227A (en) * 1941-04-19 1950-08-15 American Viscose Corp Manufacture of yarns and the like

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2179195A (en) * 1935-02-16 1939-11-07 American Enka Corp Manufacture of artificial silk
US2422021A (en) * 1940-07-29 1947-06-10 Ind Rayon Corp Manufacture of thread or the like
US2519227A (en) * 1941-04-19 1950-08-15 American Viscose Corp Manufacture of yarns and the like

Also Published As

Publication number Publication date
NL266943A (en)
DE1217544B (en) 1966-05-26
BE605928A (en)
NL296702A (en)
GB947115A (en) 1964-01-22
BE635885A (en)
GB998293A (en) 1965-07-14

Similar Documents

Publication Publication Date Title
US2179196A (en) Manufacture of artificial silk
US2852333A (en) Viscose spinning process
US3266918A (en) Viscose solutions for making flame retardant rayon
GB1087045A (en) Elastic polypropylene yarn and process for the production thereof
US3114592A (en) Process for the production of elements made of hydrated cellulose
US3066032A (en) Method of making fibers of regenerated cellulose of improved dyeing properties
US3385814A (en) Linear polycarbonate-containing spinning solutions
US3419653A (en) Prevention of filament twinning in dry spinning
US2937922A (en) Viscose process
US3018158A (en) Viscose process
US2993811A (en) Textile yarn finish
US3381075A (en) Process for preparation of viscose regenerated cellulose fibers
US3112981A (en) Process for improving dyeability of synthetic materials obtained by polymerizing monoolefinic hydrocarbons
US2983572A (en) Manufacture of viscose rayon
US3082057A (en) Manufacture of rayon
US2231890A (en) Process for improving the dyeing properties of artificial fibers, foils, films, ribbons, and the like, and products obtained therefrom
US3026171A (en) Manufacture of rayon
US3194861A (en) Viscose spinning process and bath
US2875079A (en) Spinning solution
US3031320A (en) Spinning of viscose
US2307864A (en) Method of spinning artificial filaments
US3087903A (en) Aqueous dispersion containing viscose and a polymer of acrylonitrile and process of preparing same
US3284428A (en) Dyeable polyolefins
KR0167001B1 (en) Process for preparing full-dull polyester resin
US3041132A (en) Spinning of viscose