Classifications

• • 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
  • D01F2/10—Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either

Definitions

• the present application relates to the use of end-capped alkoxylated amines as auxiliaries in the production of cellulose fibers by the viscose process and to a process for the production of cellulose fibers by the viscose process.
• the large-scale production of cellulose fibers is mainly carried out using the viscose process.
• the pulp is first converted into cellulose exanthate, the so-called viscose, and this is pressed into an acidic precipitation bath.
• Contact with the acidic solution precipitates the xanthate and saponification releases the cellulose in the form of a filament.
• modifiers e.g. B. quaternary ammonium bases, N-substituted dithiocarboxylic acids, polyethylene glycols and aliphatic monoamines and especially oxyethylated amines and amides or their derivatives.
• DE 28 37 766 describes, for example, alkoxylation products of a polyhydric alcohol and / or a dibasic amine as modifiers.
• DE 29 21 314 describes a process for the production of crimped cellulose fibers, wherein, among other things, ethoxylated fatty acid amines with 8 to 20 carbon atoms are used as modifiers.
• alkyl amine glycol ethers are often used as modifiers in viscose production. These compounds are prepared by reacting alkoxylated amines with alkyl halides, preferably alkyl chlorides, in the sense of a Williamson ether synthesis. This inevitably releases significant amounts of salts, the disposal of which is expensive and causes environmental problems. In some cases, residues of the alkyl chlorides remain in the reaction product, which may have to be removed by a complex and expensive cleaning process.
• the present application relates to the use of reaction products of the nucleophilic ring opening of epoxides of the formula (I)
• R 1 represents a linear or branched aliphatic alkyl radical having 1 to 22 carbon atoms with compounds of the formula (II)
• the ring opening products are known compounds that can be synthesized by the usual methods of organic chemistry. Such compounds are usually synthesized by reacting the epoxides of the formula (I) with compounds of the formula (II) in the presence of suitable, preferably alkaline, catalysts, e.g. Potassium or lithium hydroxide. Potassium hydroxide is preferably used.
• suitable, preferably alkaline, catalysts e.g. Potassium or lithium hydroxide. Potassium hydroxide is preferably used.
• the ring is opened by a nucleophilic attack of the oxygen atom of the compounds of the formula (II) on one of the epoxy C atoms and an ⁇ -hydroxy ether is formed. Details of this reaction can be found, for example, in the article by W. Stein in Fette, Seifen, Anstrichstoff, No. 2, 84th year 1992, page 51 and the literature cited therein.
• the ring opening reaction preferably takes place under anhydrous conditions at normal pressure. Depending on the type of starting materials used, reaction temperatures between 100 and 180 ° C are required. It is preferred to carry out the reaction in the temperature range from 140 to 160 ° C.
• the epoxides of the formula (I) are known compounds which are prepared by epoxidizing alpha-olefins which are obtained, for example, by the shop process. Typical examples are the epoxides of Octen-1, Decen-1, Dodecen-1, Tetradecen-1, Octadecen-1 or Octadecen-9. Epoxides of the formula (I) in which R 1 is a linear aliphatic alkyl radical having 8 to 14 carbon atoms are preferred.
• the compounds of the formula (II) are also known. These are ethanol or propanol amines and their alkoxylation products. These can be achieved, for example, by alkoxylation of mono-, di- or trialkanolamines using customary methods be preserved. Ethylene oxide (EO) or propylene oxide (PO) or mixtures of these alkoxides can be used as alkoxides.
• Preferred compounds of the formula (II) are those in which m is a number between 10 and 20 and preferably 12 to 18. Compounds which contain only ethylene oxide groups are particularly preferred. Preferably ring opening products are used, in the production of which ethoxylated trialkanolamines, preferably triethanolamine, are used.
• suitable compounds can be obtained by alkoxylation of other alkanolamines, for example 2- (dibutylamino) ethanol, 2- (diethylamino) ethanol, 2- (methylamino) ethanol, 2-ethylaminoethanol, 2-dimethylaminoethanol, ethanolamine or diethanolamine.
• the molar ratio between the epoxide (I) and the compound of the formula (II) in the ring opening reaction is preferably between 1: 2 and 1: 1.
• the ring opening products typically have hydroxide numbers of at least 160, preferably at least 180.
• the ring opening products are manufactured without the addition of chlorine chemicals. There is also no salt load when opening the ring, e.g. at Williamson 'see ether synthesis occurs.
• the products obtained by ring opening can be added as modifiers both to the viscose solution and to the acidic precipitation bath into which the viscose is pressed.
• the ring opening products are preferably added in amounts of between 1 and 5% by weight, based on the cellulose contained in the viscose or in the precipitation bath.
• ring opening products as modifiers in the viscose solution makes spinning easier, and a reduced blockage of the spinnerets is also observed. If the ring opening products are used as modifiers in the acidic precipitation bath, a more uniform decomposition of the xanthate cellulose and the slowing down of the thread formation are observed. This leads to threads with higher mechanical resilience. At the same time, the precipitation of inorganic salts is prevented.
• the modifiers according to the invention are suitable for use in all processes known to the person skilled in the art for the production of cellulose fibers by the viscose process.
• Another object of the present application relates to a process for the production of cellulose fibers by the viscose process, comprising the steps
• reaction products of the xanthate solution and / or the precipitation bath are added in effective amounts as modifiers.
• viscose processes are understood to mean the process of cellulose fiber production used industrially, as described, for example, in Z.A. Rogowin, chemical fibers, Georg Thieme Verlag, Stuttgart, 1982, pages 67 to 152.
• cellulose for example in the form of pressed plates, rolled goods, flakes or pressed, undried pulp
• alkali an alkali
• Any basic systems can be used as bases, in particular aqueous alkali bases, such as potassium or Caustic soda.
• concentration usually amounts to 15 to 30% by weight of base, based on the total weight of the alkali.
• Process step b) follows, which comprises the individual steps of pre-ripening, xanthation with carbon disulphide, dissolving the xanthate in alkali metal hydroxide solution, ripening and deaeration and leading to the spinnable viscose solution. Details of this process are e.g. in the above-mentioned publication by Z.A. Rogowin, pages 97 to 119.
• the modifiers described above are added to the xanthate solution during the dissolution of the cellulose xanthate in alkali metal hydroxide solution and / or during the maturation.
• the amount of the modifiers is preferably between 1 and 5% by weight, based on the cellulose contained in the solution.
• the ripened xanthate solution, process step c), is then spun by pressing the solution, which has been filtered and tempered beforehand, through a spinneret with essentially round nozzle bores into the precipitation bath. Examples of this are spinnerets with 250 to 30,000 holes and a single diameter of 35 to 100 ⁇ m.
• the xanthate coagulates into threads in the precipitation bath and is hydrolyzed to regenerated cellulose, salt and carbon disulphide using a protonic acid.
• the carbon disulfide is returned to the process.
• Organic acids such as acetic acid or mineral acids such as salt, nitric or sulfuric acid can be used as protonic acid. Concentrated sulfuric acid is preferably used.
• the precipitation bath also contains certain metal salts which can slow down the xanthate coagulation.
• metal salts are magnesium, aluminum, iron and in particular zinc salts.
• the salts are usually used as chlorides, nitrates or sulfates.
• the concentration of the salts is usually between 2 to 10 g / 1.
• the modifiers described above are added to the precipitation bath, preferably in amounts of 1 to 5% by weight, based on the cellulose contained.
• the precipitation bath can contain, in addition to the modifiers described above, the acid and the metal salts, further auxiliaries known to the person skilled in the art, for example formaldehyde or other modifiers.
• the cellulose filaments thus obtained are then spun, cleaned and further treated in a manner known per se.
• the process according to the invention is characterized in that modifiers of the type described above are used in at least one of the two process steps b) or c).
• the process is preferably carried out in such a way that the modifiers are only added to the viscose solution before spinning, that is to say in step b).

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

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• 1997
  • 1997-12-08 DE DE19754314A patent/DE19754314A1/de not_active Withdrawn
• 1998
  • 1998-11-28 US US09/581,031 patent/US6475419B1/en not_active Expired - Fee Related
  • 1998-11-28 AT AT98963528T patent/ATE233837T1/de not_active IP Right Cessation
  • 1998-11-28 EP EP98963528A patent/EP1040214B1/fr not_active Expired - Lifetime
  • 1998-11-28 WO PCT/EP1998/007700 patent/WO1999029937A1/fr active IP Right Grant

Non-Patent Citations (1)

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