CS232636B1 - Polyethylene oxide concentrates for modifying the properties of polypropylene fiber products - Google Patents
Polyethylene oxide concentrates for modifying the properties of polypropylene fiber products Download PDFInfo
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Abstract
Koncentráty polyetylénoxidov pre zlepšenie absorpčmých vlastností vlákien, zníženie Youngovho modulu a zvýšenie účinkov modifikátorov pre povrchové farbenie polypropylénových vlákien pozostávajú z 80 až 98 percent hmot. polypropylénu s rel. mol. hmot. 30 000 až 200 000 a 2 až 20 % polyetylénoxidu s rel. hmot. 600 až 35 000, připadne zo zmesi polyetylénoxidov róznych rel. mol. hmotností.Concentrates of polyethylene oxides for improving the absorption properties of fibers, reducing Young's modulus and increasing the effects of modifiers for surface dyeing of polypropylene fibers consist of 80 to 98 percent by mass. polypropylene with rel. moth. mass 30,000 to 200,000 and 2 to 20% polyethylene oxide with rel. mass 600 to 35,000, or from a mixture of polyethylene oxides of various rel. moth. weight.
Description
Vynález sa týká koncentrátov polyetylénoxidov pre výrobu polypropylénových vlákien, ktorých prídavok do vlákno-tvorného polypropylénu upravuje a zlepšuje niektoré užitková vlastnosti vyrobených vlákien.The present invention relates to polyethylene oxide concentrates for the production of polypropylene fibers, the addition of which to the fiber-forming polypropylene modifies and improves some of the useful properties of the fibers produced.
Příprava vlákien s upravovanými vlastnosťami si vyžaduje zabudovanie roznych přísad do hmoty vlákna. Pridávanie přísad v požadovanej koncentrácii priamo do polyméru pri jeho výrobě na velkokapacitmých zarladeniach s relativné malým miešacím účinkom je spojené so- zvýšením odpadu při čistění zariadení pri přechode na bežnú výrobu, připadne so zhoršeným rozdělením pridávanej přísady v hmotě vyrobeného polyméru.The preparation of fibers with modified properties requires the incorporation of various additives into the fiber mass. The addition of additives at the desired concentration directly to the polymer during its manufacture on large-capacity devices with relatively low mixing effect is associated with an increase in waste during cleaning of the apparatus when switching to conventional production, possibly with impaired distribution of the additive in the mass of polymer produced.
Uvedené nedostatky rieši vynález, podlá ktorého- pridávanie polyetylénoxidov do filmo- alebo vláknotvorného polypropylénu sa výhodnejšie prevádza pomocou koncentrátu polyetylénoxidov, podlá tohoto vynálezu, pozostávajúceho z 80 až 98 % hmot. polypropylénu s rel. mol. hmotnostou 30 000 až 200 000, 2 až 20 % hmot. polyetylénoxidu s relativnou mol. hmot. 600 až 35 000, připadne ich zmesi, ako aj připadne 0,05 až 5 % hmot. stabilizátorov.These drawbacks are solved by the invention according to which the addition of polyethylene oxides to the film- or fiber-forming polypropylene is preferably carried out by means of a polyethylene oxide concentrate according to the invention consisting of 80 to 98% by weight. polypropylene with rel. mol. by weight 30,000 to 200,000, 2 to 20 wt. of polyethylene oxide with a relative mol. wt. % 600 to 35,000, or mixtures thereof, as well as 0.05 to 5 wt. stabilizers.
Sposob výrohy koncentrátu podlá vynálezu spočívá v tom, že násada práškového polypropylénu a kvapalného, alebo- pevného práškového polyetylénoxidu podlá rel. mol. hmotnosti a príadne aj stabilizátora sa mieša v rýchlobežnej miešačke, připravená zmes sa vedie do taviaceho zariadenia, kde sa taví, mieša a hnetie pri teplote 120 až 280° Celsia, připadne odplyňuje, alebo vákuuje a nakoniec sa vytvaruje na pozdížny útvar, ktorý sa prevedie na granulát.The process according to the invention is characterized in that the feed of polypropylene powder and liquid or solid polyethylene powder according to rel. mol. the weight and optionally also the stabilizer are mixed in a high-speed mixer, the prepared mixture is fed to a melter, where it is melted, stirred and kneaded at a temperature of 120 to 280 ° C, optionally degassed or vacuumed and finally formed into a longitudinal formation. to granulate.
Zistili sme, že prídavok polyetylénoxidov do hmoty polypropylénových vlákien v priebehu ich zvlákňovania z taveniny vedie k úpravě niektorých ich vlastností čo kladné ovplyvňuje ich vhodnost pre zvolené aplikácie. Prídavok polyetylénoxidu do hmoty polypropylénového vlákna sposobuje rozvolnenie jeho, fibrilárnej štruktúry, čím sa ufahčuje napr. difúzia íarbív do vlákna a tým zvyšuje účinok modifikácie pre povrchové farbenie pomocou Ni-zlúčenín podlá čs. AO 185 006, alebo pomocou aminického dusíkatého modifikátora podlá čs. AO 219 176. Prídavok polyetylénoxidu svojim účinkom zlepšuje adsorpčné i absorpčně vlastnosti POP vlákna a tým ho umožňuje výhodné použiť napr. ako náplň cigaretových filtrov, podlá čs. AO 196 654.We have found that the addition of polyethylene oxides to the mass of polypropylene fibers during their melt spinning results in a modification of some of their properties which positively affects their suitability for the selected applications. The addition of polyethylene oxide to the mass of the polypropylene fiber causes disintegration of its fibrillar structure, thereby facilitating e.g. diffusion of dyes into the fiber thereby increasing the effect of the surface dye modification by Ni-compounds according to U.S. Pat. AO 185 006, or by means of an amine nitrogen modifier according to U.S. Pat. AO 219 176. The addition of polyethylene oxide improves the adsorption and absorption properties of the POP fiber by its action and thus makes it advantageous to use e.g. as a filling of cigarette filters, according to MS. AO 196 654
Prídavok polyetylénoxidu do hmoty POP vlákna dalej ovplyvňuje Youngov modul inedížených vlákien a sposobuje nárast maximálneho dížiacieho poměru, čím umožňuje ovplyvňovať spracovatelínosť týchto vlákien hlavně v operácii díženia.The addition of polyethylene oxide to the POP fiber mass further affects the Young's modulus of the ingested fibers and causes an increase in the maximum grain ratio, thereby allowing the fiber to be processed, particularly in the gravity operation.
Příklad 1Example 1
Na rýchlomiešačke sa miešaním po dobu 5 minút připraví homogenná zmes práškovitého polypropylénu o ITT 10,7 g/10 min. s 15 percenty hmot. práškovitého polyetylémoxidu o rel. molekulovej hmotnosti 6000. Zmes z rýchlomiešačky sa previedla do šesťzónového dvojvretenového hnetaco-taviaceho zariadenia s nasledujúcim teplotným režimom na ohrievacích zónách počínajúc od vstupu: 240, 240, 150, 150, 220, 220 °C. Tavenina sa na výstupe zo zariadenia vytláča do vody vo formě strún, ktoré sa po ochladení sekali na drvimu.A homogeneous mixture of powdered polypropylene of ITT 10.7 g / 10 min is prepared by stirring for 5 minutes on a rapid mixer. with 15 percent by weight. powdered polyethylene oxide of rel. The mixture from the rapid mixer was transferred to a six-zone two-spindle kneading melter with the following temperature regime on the heating zones starting from the inlet: 240, 240, 150, 150, 220, 220 ° C. At the outlet of the apparatus, the melt is extruded into water in the form of strings, which, after cooling, are chopped on a crushed mill.
Připravený granulovaný koncentrát polyetylénoxidu bol použitý na úpravu vlastností polypropylénových komjugovaných vlákien pre náplň cigaretových filtrov podl'a čs. AO 196 654. Cigaretové filtre vyrobené z vlákna upraveného prídavkom 1 % hmotnostně polyetylémoxidu vykazujú v porovnaní s neupravenými vláknami výrazné zvýšenú schopnost zachytávat dechtovité látky z predchádzajúceho cigaretového dýmu.The prepared granulated polyethylene oxide concentrate was used to modify the properties of polypropylene conjugated fibers for the cigarette filter filling according to U.S. Pat. AO 196 654. Cigarette filters made from a fiber treated with 1% by weight of polyethylene oxide exhibit a markedly increased ability to catch tars from the previous cigarette smoke compared to untreated fibers.
Přiklad 2Example 2
Za technologických podmienok podta příkladu 1 bol připravený koncentrát pojyetylénoxidu o rel. mol. hmotnosti 20 000 s obsahom polyetylénoxidu v koncentráte 20 % hmotnostných.Under the technological conditions of Example 1, a methylene oxide concentrate of rel. mol. 20% by weight with a polyethylene oxide content of 20% by weight.
Na zvlákňovacom zariadení bolo připravené vlákno s prídavkom koncentrátu polyetylénoxidu na obsah 1 °/o hmotnostně polyetylénoxidu v hmotě připraveného vlákna. Pri porovnaní z vláknom bez přídavku polyetylénoxidu došlo k zvýšeniu maximálneho' dížiaceho poměru u nedíženého vlákna o 12 percent a k zníženiu Youngovho modulu o· 14 % u vlákna upravovaného prídavkom polyetylénoxidu.A fiber was prepared on the spinner with the addition of a polyethylene oxide concentrate to a content of 1% by weight of polyethylene oxide in the mass of the prepared fiber. When compared to fibers without the addition of polyethylene oxide, the maximum weight ratio of the undiluted fiber increased by 12 percent and the Young's modulus decreased by 14% for the fiber treated with the addition of polyethylene oxide.
Pri k1 a d 3At k1 and d 3
Práškový izotaktický polypropylén s rel. mol. hmotnosťou 100 000 sa na rýchlomiešačke mieša na homogénnu zmes s prídavkom 5 % hmotnostných zmesi polyetylénoxidov, v ktorej polyetylénoxidy o rel. mol. hmotnosti 600 a 30 000 sú zastúpené v hmotnostnom pomere 1:1. Připravená zmes sa vedie do taviaco-hnetacieho zariadenia s piatimi ohrevnými zónami, kde sa vypracovává pri nasledovnom teplotnom režime na ohrie-vacích zónách počínajúc od vstupu: 270, 240, 120, 120, 230 °C. Tavenina sa na výstupe zariadenia vytláča do vody vo formě strún, ktoré sa po ochladení sekajú na drvinu.Isotactic polypropylene powder with rel. mol. with a weight of 100,000, it is mixed on a rapid mixer to a homogeneous mixture with the addition of 5% by weight of a mixture of polyethylene oxides in which the polyethylene oxides of rel. mol. weights of 600 and 30,000 are represented in a 1: 1 weight ratio. The prepared mixture is fed to a melting-kneading machine with five heating zones, where it is worked up at the following temperature regime on the heating zones starting from the inlet: 270, 240, 120, 120, 230 ° C. At the outlet of the apparatus, the melt is extruded into water in the form of strings, which, after cooling, are cut into crushed material.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS834385A CS232636B1 (en) | 1983-06-16 | 1983-06-16 | Polyethylene oxide concentrates for modifying the properties of polypropylene fiber products |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS834385A CS232636B1 (en) | 1983-06-16 | 1983-06-16 | Polyethylene oxide concentrates for modifying the properties of polypropylene fiber products |
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| Publication Number | Publication Date |
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| CS438583A1 CS438583A1 (en) | 1984-05-14 |
| CS232636B1 true CS232636B1 (en) | 1985-02-14 |
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| CS834385A CS232636B1 (en) | 1983-06-16 | 1983-06-16 | Polyethylene oxide concentrates for modifying the properties of polypropylene fiber products |
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1983
- 1983-06-16 CS CS834385A patent/CS232636B1/en unknown
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| CS438583A1 (en) | 1984-05-14 |
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