SE181468C1 - - Google Patents
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- SE181468C1 SE181468C1 SE134159A SE134159A SE181468C1 SE 181468 C1 SE181468 C1 SE 181468C1 SE 134159 A SE134159 A SE 134159A SE 134159 A SE134159 A SE 134159A SE 181468 C1 SE181468 C1 SE 181468C1
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- cellulose
- titanium
- cellulosic
- cellulosic material
- polymer
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/24—Formation of filaments, threads, or the like with a hollow structure; Spinnerette packs therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
- B01D67/003—Organic membrane manufacture by inducing porosity into non porous precursor membranes by selective elimination of components, e.g. by leaching
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B15/00—Preparation of other cellulose derivatives or modified cellulose, e.g. complexes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F251/00—Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof
- C08F251/02—Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof on to cellulose or derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/26—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/24—Formation of filaments, threads, or the like with a hollow structure; Spinnerette packs therefor
- D01D5/247—Discontinuous hollow structure or microporous structure
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- 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
- D06M14/00—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials
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- 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
- D06M14/00—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials
- D06M14/02—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin
- D06M14/04—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin of vegetal origin, e.g. cellulose or derivatives thereof
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- 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
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
- D06M15/21—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D06M15/227—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of hydrocarbons, or reaction products thereof, e.g. afterhalogenated or sulfochlorinated
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Textile Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Uppfinnare: J A Orsino, D F Herman och J J Brancato Prioritet begard frdn den 11 febrnari 1958 (USA) Fdreliggande uppfinning avser ett formbart material, bestaende av ett cellulosamaterial med ett yttre skikt av en polymer, samt ett forfarande for framstfillning harav. Inventors: J A Orsino, D F Herman and J J Brancato Priority as of February 11, 1958 (USA) The present invention relates to a moldable material, consisting of a cellulosic material having an outer layer of a polymer, and a process for producing the same.
Manga fOrfaranden ha foreslagits f8r kemisk behandling av cellulosamaterial for forandring av deras egenskaper pa olika satt, t. ex. for Wining av deras flambestfindighet, fir modifiering av greppet hos darav framstallda textilier, for astadkommande av vattenfranstotande egenskaper, etc. Foreliggande uppfinning avser speciellt ett nytt och forbattrat fOrfarande for modifiering av cellulosamaterialen, sa att en ny cellulosa-kolvatekomposition framstalles, som av nathrea ar hydrofob. Artiklar framstallda av en sfidan komposition aro vattenfranstotande eller vattentata beroende pa graden av modifiering och av artikelns fysikaliska struktur. Many methods have been proposed for the chemical treatment of cellulosic materials to alter their properties in various ways, e.g. The present invention relates in particular to a new and improved process for modifying the cellulosic materials so as to produce a new cellulose-carbonate composition which is made from nathrea ares for the purpose of modifying the grip of their flame-retardant fabrics, for providing water-repellent properties, etc. hydrophobic. Articles made from a soft composition are water repellent or water resistant depending on the degree of modification and the physical structure of the article.
Pet vanliga forfarandet for att gra cellulosamaterial vattenfranstotande har hittills varit att impregnera dem med olika substanser, valda med hansyn till den ffirdiga produktens anvandning. En typ av +antigen anvant impregneringsmedel är paraffinvax efler liknande material, som ger en anvandbar grad av vattenfranstotande egenskaper hos papper och som i viss man aven ay anvandbart for att gora talt och liknande' vattentata. Sadana material lida av den olagenheten, att de ha en tendens att falla av i flagor, nOr materialet bOjes upprepade ganger, varvid den vattenfranstotande egenskapen for-stores utefter bojningen. De tEa dessutom icke kemisk tvatt eller sa.dana hogre temperaturer, som vanligtvis uppsta vid strykning och vid kontakt med varma vatskor, t. ex. vid pappersbagare for kaffe. The usual procedure for making cellulosic materials water-repellent has hitherto been to impregnate them with various substances, selected with regard to the use of the finished product. One type of + antigen used impregnating agent is paraffin wax or similar materials, which provide a usable degree of water repellent properties of paper and which to some extent are also useful for making spoken and similar 'water resistant'. Such materials suffer from the disadvantage that they have a tendency to fall off in flakes when the material is bent repeatedly, the water-repellent property being increased along the bend. They also do not require chemical washing or such higher temperatures, which usually occur during ironing and in contact with hot water shoes, e.g. at paper bakeries for coffee.
En annan grupp inapregneringsmedel, som vanligen anvandas, da olagenheten med vaximpregneringsmedel gra dem oanyandbara, Or konsthartserna. Behandlingen med denna typ av material utf Ores i allmanhet genom doppning av det material, som skall behandlas, i en losning av ett lampligt konstharts i ett losningsmedel eller genom sprutning av en sadan losning pa materialet antingen under sista framstallningssteget eller darefter. Bland de konsthartser, som anvants i f8rfaranden av denna typ, ma namnas karbamidformaldehydharts, vinylplast, cellulosaderivat och liknande. Metoder grundade pa impregnering med sadana konsthartser som dessa undanrojer i viss man nagra av olagenheterna med vaximpregneringen. A andra sidan lida de av vissa andra olagenheter, speciellt den att konsthartserna maste paforas i form av en losning och att det for avsattning av konsthartset pa fibern dr nedvandigt att foranga losningsmedlet, vilket Or ett dyrbart och till och med farligt forfarande. For att Ora forfarandet ekonomiskt anvandbart är det dessutom nodvandigt att samla och atervirma det fOrangade losningsmedlet, vilket medfiir ytterligare dyra och besvarliga steg i farfarandet. Another group of impregnating agents, which are commonly used, as the inadequacy of wax impregnating agents makes them inadvertent, or the synthetic resins. The treatment with this type of material is generally carried out by dipping the material to be treated in a solution of a suitable synthetic resin in a solvent or by spraying such a solution on the material either during the final manufacturing step or thereafter. Among the synthetic resins used in processes of this type, mention may be made of urea formaldehyde resin, vinyl plastic, cellulose derivatives and the like. Methods based on impregnation with such synthetic resins as these eliminate to some extent some of the disadvantages of wax impregnation. On the other hand, they suffer from certain other disadvantages, in particular the fact that the synthetic resins must be applied in the form of a solution and that the deposition of the synthetic resin on the fiber makes it difficult to evaporate the solvent, which is an expensive and even dangerous process. In order for the process to be economically feasible, it is also necessary to collect and recycle the preferred solvent, which entails further expensive and cumbersome steps in the process.
De konsthartsimpregnerade produkterna Wilma dessutom mycket ovrigt att onska, ehuru de undanroj a nagra av olagenheterna hos vaximpregnerade material. De firo mycket bestandigare mot verkningarna av mattlig uppvarmning, men bli Iiksom de vaximpregnerade materialen fOrstorda vid hogre temperaturer. Impregneringen Or dessutom fortfarande borttagbar med vanliga losningsmedel f8r kemisk tvatt, ehuru mindre snabbt an vaximpregneringen. The synthetic resin impregnated products Wilma also have a lot to wish for, although they eliminate some of the illegality of wax impregnated materials. They are much more resistant to the effects of moderate heating, but like the wax-impregnated materials become enlarged at higher temperatures. The impregnation is also still removable with ordinary solvents for chemical washing, although less fast than the wax impregnation.
Foreliggande formbara material kannetecknas (Wray, att de enskilda cellulosafibrerna aro helt eller delvis belagda med polyeten, polypropen, polybutadien eller polyisopren. Cellulosamaterialet fOreligger harvid lampliaen i form av partiklar, fibrer eller tradar. The present moldable materials can be characterized (Wray, that the individual cellulose fibers are completely or partially coated with polyethylene, polypropylene, polybutadiene or polyisoprene. The cellulosic material is present in the lamplia in the form of particles, fibers or threads.
Forfarandet enligt uppfinningen kanneteck- 2— — nas darav, att ett cellulosamaterial bringas att reagera med en titan- eller zirkoniumforening och ett organometalliskt alkyleringseller aryleringsmedel, varefter det pa sá satt behandlade cellulosamaterialet Mlles i kontakt med eten, propen, butadien eller isopren under tillrackligt lang tid for bildning av en polymer pa cellulosamaterialet. Titan- eller zirkoniumforeningen utgores lampligen av en tetraklorid eller en ester. Sasom organometalliskt alkyleringsmedel kan man anvanda ett grignardreagens eller en aluminiumalkyl. The process according to the invention is characterized in that a cellulosic material is reacted with a titanium or zirconium compound and an organometallic alkylating or arylating agent, after which the cellulosic material thus treated is in contact with ethylene, propylene, butadiene or isoprene for a sufficiently long time. time for the formation of a polymer on the cellulosic material. The titanium or zirconium compound is suitably composed of a tetrachloride or an ester. As the organometallic alkylating agent, a Grignard reagent or an aluminum alkyl can be used.
Foreliggande formbara cellulosamaterial har forbattrade vattenfra.nstotande egenskaper och ar bestandigt mot normala losningsmedel for kemisk tvatt. The present moldable cellulosic materials have improved water repellent properties and are resistant to normal chemical wash solvents.
Cellulosamaterial, som aro anvandbara enligt uppfinningen, innefatta tyg, t. ex. av bomull, lin, regenererad cellulosa, sasom viskossilke, kopparsilke och acetatsilke, forutom naturliga fibrer, sasom hampa, tra och traprodukter, byggnadsplattor, papper, tramjiil, sagspan och liknande. Dessutom kunna anvandas substituerade cellulosamaterial, sasom cellulosaacetat, etylcellulosa, cellulosanitrat etc. Cellulosic materials useful in the invention include fabrics, e.g. of cotton, flax, regenerated cellulose, such as viscose silk, copper silk and acetate silk, in addition to natural fibers, such as hemp, wood and wood products, building boards, paper, tramjiil, sawdust and the like. In addition, substituted cellulosic materials can be used, such as cellulose acetate, ethylcellulose, cellulose nitrate, etc.
De enligt foreliggande forfarande framstallda nya kompositionerna aro cellulosamaterial, som aro modifierade, genom att de i intim forbindelse innehalla partiklar av kolvatepolymerer. Den angivna forbindelsen ar icke en sadan enkel mekanisk blandning, som kan erhallas genom mekanisk blandning av cellulosamaterial med polymeren. Den utmarkes snarare av narvaron av polymerparlor eller -knappar, fordelade pa cellulosafibrernas yta. Dessa polymerpartiklar, som kunna vara fullstandigt skilda eller i viss utstrackning sammansmalta, hafta sa fast vid cellulosafibrernas yta, som om de hallas med kemiska bindningar eller motsvarande starka forbindningskrafter. De mest aktiva omradena i cellulosamolekylen aro hydroxylgrupperna och det antages, att atminstone fran borjan de reaktioner, som slutligen leda till bildningen av polymerparlor, aga rum vid cellulosans hydroxylgrupper. Enligt f5religgande forfarande behandlas cellulosan antingen fore polymerisationssteget eller samtidigt med detta med en titan- eller zirkoniumforening. Det antages, att metallatomen (titan eller zirkonium) ersitter vateatomen i en hydroxylgrupp i cellulosan, vilket leder till en modifierad eellulosastruktur, som har katalytiskt aktiva omraden, i vilka hydroxylgrupperna ha reagerat pa detta satt. The novel compositions prepared according to the present process are cellulosic materials which are modified in that they contain, in intimate connection, particles of carbonate polymers. The indicated compound is not such a simple mechanical mixture which can be obtained by mechanical mixing of cellulosic material with the polymer. Rather, it is marked by the presence of polymer beads or buttons, distributed on the surface of the cellulosic fibers. These polymer particles, which may be completely separated or to some extent fused together, adhere to the surface of the cellulosic fibers as if they are held by chemical bonds or correspondingly strong bonding forces. The most active regions in the cellulose molecule are the hydroxyl groups and it is believed that at least initially the reactions which ultimately lead to the formation of polymer beads take place at the hydroxyl groups of the cellulose. According to the present process, the cellulose is treated either before the polymerization step or simultaneously with a titanium or zirconium compound. It is believed that the metal atom (titanium or zirconium) replaces the hydrogen atom in a hydroxyl group in the cellulose, leading to a modified cellulose structure having catalytically active regions in which the hydroxyl groups have reacted in this way.
Polymerisationen ager darefter rum vid de katalytiskt aktiva omradena langs cellulosakedjan, sá att den framstallda polymeren ãr intimt inflatad i cellulosan. Nfir polymerisationen ar fullstandig, forkvaves katalysatorn pa vanligt satt, t. ex. genom tillsats av alkohol till systemet med foljande tvattning med ytterligare alkohol eller liknande for bortta gande av katalysatorrester. Detta forfarande kan leda till spjalkning av bindningen melIan cellulosamolekyl oak katalytiskt aktiv grupp, sa att det icke aterstar flagon direkt kovalent kemisk bindning i vanlig mening mellan cellulosan och den polyolefiniska de-lea av komposifionen. Icke desto mindre forblir polyolefinen oextraherbar med vanliga losningsmedel, vilket tyder pa att kompositionen icke ar en enkel blandning av cellulosa och polyolefin. Detta beteende synes visa, att cellulosan och polyetenmolekylerna arc sa inflatade i varandra, att de uppfora sig, som om de arc kemiskt bundna, aven am detta i verkligheten eventuellt icke fir fallet. The polymerization then takes place at the catalytically active areas along the cellulose chain, so that the polymer produced is intimately flattened in the cellulose. Before the polymerization is complete, the catalyst is cooled in the usual way, e.g. by adding alcohol to the system with subsequent washing with additional alcohol or the like to remove catalyst residues. This process can lead to the cleavage of the bond between the cellulose molecule and the catalytically active group, so that it does not restore direct direct covalent chemical bonding between the cellulose and the polyolefinic part of the composition. Nevertheless, the polyolefin remains unextractable with common solvents, indicating that the composition is not a simple mixture of cellulose and polyolefin. This behavior seems to show that the cellulose and the polyethylene molecules are so intertwined that they behave as if they were chemically bound, although in reality this may not be the case.
Dot exakta schernat for de reaktioner, som aga rum, och den exakta strukturen hos det enligt fOreliggande forfarande framstallda, modifierade cellulosamaterialet aro annu icke faststallda, och ovanstaende beskrivning av kompositionens struktur ma darfor icke betraktas som nagon begransning av uppfinningen, utan endast som ett forsok att askadliggora den. Pa detta satt forklaras emellertid de iakttagna fakta, att nar en. olefiniskt omattad kolvatemonomer polymeriseras i narvaro av en med titan- eller zirkoniumforening behandlad cellulosafiber eller tillsammans med en cellulosafiber under betingelser, som beframj a en samtidig behandling med en titan- eller zirkoniumforening darav, den erhallna fibern utefter hela sin langd f5rbundits med partiklar av polymeren, som uppfor sig, som am den var kemiskt bunden vid cellulosafibern. Nar daremot en. kolvatemonomer polymeriseras i narvaro av omodifierad cellulosa eller under betingelser, som icke beframja behandlingen med titan- eller zirkoniumforening av cellulosahydroxylgrupperna, ar produkten en enkel blandning av cellulosa och polymerpartiklar. The exact scheme of the reactions which take place and the exact structure of the modified cellulosic material prepared according to the present process have not yet been determined, and the above description of the structure of the composition is therefore not to be construed as limiting the invention, but merely as an experiment. to ash it. In this way, however, the observed facts are explained, that when one. olefinically unsaturated hydrocarbon monomer is polymerized in the presence of a cellulosic fiber treated with titanium or zirconium compound or together with a cellulosic fiber under conditions which promote simultaneous treatment with a titanium or zirconium compound thereof, the obtained fiber being bonded along its entire length to particles of the polymer, which behaves as if it were chemically bound to the cellulosic fiber. Nar daremot en. hydrocarbon monomer is polymerized in the presence of unmodified cellulose or under conditions which do not promote the treatment with titanium or zirconium compound of the cellulose hydroxyl groups, the product is a simple mixture of cellulose and polymer particles.
Talrika metoder arc sjalvklara far behandlingen med titan- eller zirkoniumforeningen av cellulosa under samtidig eller foljande polymerisering av en ovannamnd olefiniskt omattad kolvatemonomer i narvaro av cellulosan. En av de lampligaste metoderna ar emellertid att behandla cellulosan med titaneller zirkoniumforening pa kant satt, t. ex. genom att behandla den med titan- eller zirkoniumtetraklorid eller med en lamplig ester, sasom tetrabutyltitanat, tetrabutylzirkonat etc., och genom att darefter overfora metallatomen i den behandlade cellulosan till en form, som innehaller en metall-kolbildfling. Detta kan ske med hjalp av kanda organometalliska alkylerings- eller aryleringsmedel, sasom grignardreagenser eller alkyloch arylforeningar av litium, natrium, kadmium, zink, aluminium etc. Nar denna OverfOring skett, kommer cellulosan att innehalla katalytiskt aktiva contra pa de stallen, i vilka metallatomen ursprungligen infordes av titan.- eller zirkoniumforeningen. — 181 968 —3 Reaktionsbetingelserna aro milda. Titaneller zirkoniuminfOrandet kan snabbt genomforas vid rumstemperatur. Be betingelser, som anyandas vid polymerisationen, kunna variera i stor utstrackning, men i allmanhet an det lampligt att utfora polymerisationen vid tern.- peraturer mellan cirka 20 och 80° C och vid tryck fran atmosfarstryck upp till cirka 7 kp/cm2. Numerous methods are obvious from the treatment with the titanium or zirconium compound of cellulose during simultaneous or subsequent polymerization of an above-mentioned olefinically unsaturated hydrocarbon monomer in the presence of the cellulose. However, one of the most suitable methods is to treat the cellulose with titanium or zirconium compound by edge, e.g. by treating it with titanium or zirconium tetrachloride or with a suitable ester, such as tetrabutyl titanate, tetrabutyl zirconate, etc., and by subsequently transferring the metal atom of the treated cellulose to a form containing a metal-carbon image flake. This can be done with the aid of known organometallic alkylating or arylating agents, such as grignard reagents or alkyl and aryl compounds of lithium, sodium, cadmium, zinc, aluminum, etc. When this transfer has taken place, the cellulose will contain catalytically active contra on the stalls in which introduced by the titanium or zirconium compound. - 181 968 —3 The reaction conditions are mild. Titanium or zirconium introduction can be carried out quickly at room temperature. Conditions, which are different from the polymerization, can vary widely, but in general it is convenient to carry out the polymerization at temperatures between about 20 and 80 ° C and at pressures from atmospheric pressure up to about 7 kp / cm 2.
Polymerisationen sker snabbt, och en reaktionstid av 2-12 timmar är i allmanhet tillracklig for att ge en betydande avsattning av polymer pa cellulosaytan. Kortare eller hingre kontakttider kunna anvandas beroende pa den onskade modifieringsgraden. The polymerization takes place rapidly, and a reaction time of 2-12 hours is generally sufficient to give a significant deposition of polymer on the cellulose surface. Shorter or longer contact times can be used depending on the desired degree of modification.
Forfarandet enligt uppfinningen askadliggores i foljande exempel. The process of the invention is illustrated in the following examples.
Exempel 1. 24 g vadd av mekanisk massa dispergerades i torrt tillstand i 1400 ml toluen. Luften i karlet fortrangdes med kvave och 0,0316 mol TiC14 sattes till dispersionen. Blandningen reagerade i 0,5 timmar vid rumstemperatur for astadkommande av titaninf 5-ring i cellulosan, varefter 0,075 mol metylmagnesiumbromid tillsattes. Temperaturen hi5jdes till och halls vid 50-60° C, medan en strOm av etengas leddes genom blandningen. Fargen forandrades fran orange Over markt grOn till nastan svart. Etengasstrommen fortsattes 6 timmar, tills absorptionshastigheten blev obetydlig. Den mangd eten, som absorberades, var ungefar lika med mangden cellulosavadd i reaktionskarlet. Example 1. 24 g wad of mechanical pulp was dispersed in the dry state in 1400 ml of toluene. The air in the vessel was displaced with nitrogen and 0.0316 moles of TiCl 4 was added to the dispersion. The mixture reacted for 0.5 hours at room temperature to produce titanium inf 5-ring in the cellulose, after which 0.075 mol of methylmagnesium bromide was added. The temperature was raised and maintained at 50-60 ° C, while a stream of ethylene gas was passed through the mixture. The color changed from orange Over markt grOn to almost black. The ethylene gas flow was continued for 6 hours, until the rate of absorption became negligible. The amount of ethylene absorbed was approximately equal to the amount of cellulose wadding in the reaction vessel.
Losningen kyldes och spaddes genom tillsats av en lika stor volym metanol, varefter den kylda losningen filtrerades och tvattades med ytterligare metanol. Filterkakan bestod efter torkning av en pulverformig cellulosa-polyetenkomposition, som inneholl cirka 50 % polyeten. The solution was cooled and spatulated by adding an equal volume of methanol, after which the cooled solution was filtered and washed with additional methanol. After drying, the filter cake consisted of a powdered cellulose-polyethylene composition containing about 50% polyethylene.
Ett mikrofotografi ay den framstallda kompositionen visar ett fibrost natverk av cellulosafibrer med cirka 20-30 it genomsnittlig diameter och miirkare flacks" av polyeten, som Tar narvarande som en fastsittande belaggning ph cellulosafibrernas yta, medan icke na.gon eller en ringa mangd polyeten fanns de oppna omradena mellan cellulosafibrerna. A photomicrograph of the composition produced shows a fibrous network of cellulosic fibers having an average diameter of about 20-30 .mu.m and more flakes "of polyethylene, which presently present as a sticky coating on the surface of the cellulosic fibers, while no open the areas between the cellulose fibers.
Produkten anvandes for framstallning av ackumulatorseparatorer, genom att den Overfordes till arkform i en pappersmaskin och darefter pressades latt samman i en uppvarmd form. Separatorn var poros och latt genomtranglig f Or vatten och f5r utspadd svavelsyra, men den var mycket bestandig gentemot syra. Den fardiga separatorn. talde Over 2 timmar neddoppning i konc. svavelsyra (spec. vikt 1,84) vid rumstemperatur utan synlig forkolning. The product was used to make accumulator separators by transferring it to sheet form in a paper machine and then pressing it lightly together in a heated mold. The separator was porous and slightly permeable to water and to dilute sulfuric acid, but it was very resistant to acid. The finished separator. spoke Over 2 hours immersion in conc. sulfuric acid (spec. weight 1.84) at room temperature without visible charring.
Exempel 2. 40 g cellulosavadd dispergerades i 1400 ml toluen. Luften i karlet fortrangdes med kvavgas och 0,0158 mol titantetraklorid tillsattes. Efter 0,5 timmar staende for att titan skulle infOras i cellulosan, tillsattes 0,0474 mol triiaobutylaluminium. Temperaturen hojdes darefter och h011s Yid 50-60° C, medan etengas leddes genom blandningen, tills absorptionen av gas blev obetydlig. Blandningen avkyldes darefter och spaddes med metanol, filtrerades, tvattades och torkades, sasom beskrivits i exempel 1. Produkten, som erholls i gott utbyte, var en cellulosa-polyetenkomposition, som inneholl cirka 35 % polyeten. 1/id mikroskopisk undersokning uppvisade produkten det typiska utseendet f Or kompositioner, framstallda enligt foreliggande fOrfarande, dvs. den bestod av langa cellulosafibrer och pa vane fiber fanns det parlor eller knappar av polymeriserat kolvate, fast vid olika punkter utefter fibrernas langd. Ett elektronmikroskopfotografi visade forutom de stOrre parlor, som voro synliga i mikroskopet for vanligt ljus, ett stort antal sma parlor, varav en del voro sammansmalta till ett sammanhangande skikt pa varje fibers yta. Fa, om ens flagon polymerpartikel fanns i mellanrummet mellan cellulosafibrerna vid undersokningen i ljusmikroskop och i elektronmikroskop. Example 2. 40 g of cellulose wadding was dispersed in 1400 ml of toluene. The air in the vessel was displaced with nitrogen and 0.0158 moles of titanium tetrachloride was added. After 0.5 hours standing for titanium to be introduced into the cellulose, 0.0474 moles of triobutylaluminum was added. The temperature was then raised and kept at 50-60 ° C, while ethylene gas was passed through the mixture until the absorption of gas became insignificant. The mixture was then cooled and diluted with methanol, filtered, washed and dried as described in Example 1. The product obtained in good yield was a cellulose-polyethylene composition containing about 35% polyethylene. On microscopic examination, the product showed the typical appearance of compositions prepared according to the present process, i.e. it consisted of long cellulose fibers and on ordinary fibers there were beads or buttons of polymerized carbonate, fixed at different points along the length of the fibers. An electron microscope photograph showed, in addition to the larger beads visible in the microscope for ordinary light, a large number of small beads, some of which were fused together into a coherent layer on the surface of each fiber. Fa, if even flake polymer particle was present in the space between the cellulose fibers at the examination in light microscope and in electron microscope.
Exempel 3. 24 g cellulosaacetat suspenderades 11400 ml toluen i ett slutet karl, och luften spolades ut med kvavgas, varefter 0,023 mol titantetraklorid tillsattes. Blandningen stod 0,5 timmar fOr att medge inforing av titan, varefter 0,055 mol metylmagnesiumbromid tillsattes. Temperaturen hojdes till 50(300 C och holls mom detta intervall, medan etengas inleddes i losningen, tills icke mer absorberades. Blandningen kyldes och spaddes med metanol, sasom i foregaende exempel, tvattades och torkades. Example 3. 24 g of cellulose acetate were suspended in 11400 ml of toluene in a closed vessel, and the air was purged with nitrogen gas, after which 0.023 mol of titanium tetrachloride was added. The mixture was allowed to stand for 0.5 hours to allow the introduction of titanium, after which 0.055 mol of methylmagnesium bromide was added. The temperature was raised to 50 DEG C. (300 DEG C. and kept at this range while ethylene gas was started in the solution until no more was absorbed. The mixture was cooled and diluted with methanol, as in the previous example, washed and dried.
Produkten inneholl 20 % polyeten och fuktades icke av vatten °eh var mycket bestandig mot angrepp av kone. svavelsyra. Obehandlat cellulosaacetat fuktas daremot latt av vat-ten och loses i konc. svavelsyra. The product contained 20% polyethylene and was not wetted by water and was very resistant to cone infestation. sulfuric acid. Untreated cellulose acetate, on the other hand, is slightly moistened by the water and dissolved in conc. sulfuric acid.
Exempel 4. Forfarandet i exempel 1 upprepades med den andringen att 0,0316 mol tetrabutylzirkonat anvandes i stallet f Or titantetrakloriden. Produkten var en cellulosapolyetenkomposition, som var mycket lik den som framstalldes enligt exempel 1. Example 4. The procedure of Example 1 was repeated with the change that 0.0316 moles of tetrabutyl zirconate was used in place of the titanium tetrachloride. The product was a cellulose polyethylene composition very similar to that prepared according to Example 1.
Exempel 5. Forfarandet i exempel 2 upprepades med den andringen att propengas anvandes i stallet for etengas. Produkten var en cellulosa-polypropenkomposition, som inneholl icke extraherbar polypropen. Example 5. The procedure of Example 2 was repeated with the change that propylene gas was used instead of ethylene gas. The product was a cellulosic polypropylene composition containing non-extractable polypropylene.
Exempel 6. Forfarandet i exempel 1 upprepades med den fOrandringen att i stallet for maid mekanisk massa anvandes ett latt cel-. lulosagarn (bomullsgarn). Det behandlade garnet vavdes till tyg, vans utseende och grepp liknade obehandlat bomullstygs, men det var mycket vattenfranstotande och syrabestandigt och lampligt for regnskydd, skyddande laboratorieklader och liknande. Example 6. The procedure of Example 1 was repeated with the change that a light cell was used instead of mechanical pulp. lulosagarn (cotton yarn). The treated yarn was woven into fabric, the appearance and grip of the vans resembled untreated cotton fabric, but it was very water-repellent and acid-resistant and suitable for rain protection, protective laboratory clothes and the like.
Exempel 7. 25 g maid, renad sulfitpappers- — — massa dispergerades i 450 ml bensen under torra betingelser. Luften i behallaren ersattes med kvavgas och 0,0054 mol titantetraklorid i 50 ml torr bensen sattes till dispersionen. Blandningen fick reagera0,5 timmar vid rumstemperatur f6r astadkommande av en titanering av cellulosan, varefter 0,0054 mol trietylaluminium i heptan och darefter 50 g isopren tillsattes. PoIymerisationen borjade spontant, nagot som framgick darav, att temperaturen steg fran 26° C till 37° C mom loppet av 0,5 timmar. Da temperaturen hade faint en grad till 36° C under loppet av ytterligare 40 minuter, uppvarmdes blandningen forsiktigt till 74° C under loppet av 1,5 timmar och holls vid denna temperatur i en timme. Example 7. 25 g of maid, purified sulphite paper pulp was dispersed in 450 ml of benzene under dry conditions. The air in the container was replaced with nitrogen gas and 0.0054 moles of titanium tetrachloride in 50 ml of dry benzene was added to the dispersion. The mixture was allowed to react for 0.5 hours at room temperature to effect a titanation of the cellulose, after which 0.0054 moles of triethylaluminum in heptane and then 50 g of isoprene were added. The polymerization began spontaneously, as evidenced by the fact that the temperature rose from 26 ° C to 37 ° C over the course of 0.5 hours. When the temperature reached a temperature of 36 ° C over a further 40 minutes, the mixture was gently warmed to 74 ° C over 1.5 hours and kept at this temperature for one hour.
Katalysatorn hejdades eller spjalkades genom tillsats av 25 ml metanol. Den fasta substansen utvanns genom centrifugering, tvattning, tvâ ganger med bensen, filtrering och torkning. Den fasta substansen var efter torkning en pulverformad cellulosa-polyisoprenkomposition, som inneholl cirka 13 viktprocent polyisopren. The catalyst was stopped or cleaved by the addition of 25 ml of methanol. The solid was recovered by centrifugation, washing, twice with benzene, filtration and drying. The solid, after drying, was a powdered cellulose-polyisoprene composition containing about 13% by weight of polyisoprene.
Kompositioner framstallda enligt foreliggande forfarande aro anvandbara for manga andamal pa grand av sina kemiska och fysikaliska egenskaper. De aro hydrofoba, orga- nofila cellulosamaterial och kunna bearbetas till olika formade, pressade och gjutna foresasom ror, behallare, teitilfibrer, skyddande belaggningar och liknande, speciellt dar bestandighet mot fuktning av vatten, be- standighet mot losning i organiska losningsmedel och bestandighet mot koncentrerade mineralsyror är onskvard. De kunna anvandas till sa olika foremal som blyackumulatorseparatorer, ackumulatorbehfillare, filterme- dia, behallare for varma och kalla drycker, vattenfranstotande skyddande tyg, strandklader etc. Compositions prepared according to the present process are useful for many purposes due to their chemical and physical properties. They are hydrophobic, organophilic cellulosic materials and can be processed into various shaped, pressed and cast foresums, containers, tea fibers, protective coatings and the like, in particular where resistance to water wetting, resistance to dissolution in organic solvents and resistance to concentrated mineral acids are desirable. They can be used for such different objects as lead-acid battery separators, accumulator fillers, filter media, containers for hot and cold drinks, water-repellent protective fabric, beachwear, etc.
Claims (5)
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US71456958A | 1958-02-11 | 1958-02-11 |
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1959
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