CS233205B1 - Device for continuous filtration of polymer melts - Google Patents
Device for continuous filtration of polymer melts Download PDFInfo
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- CS233205B1 CS233205B1 CS823902A CS390282A CS233205B1 CS 233205 B1 CS233205 B1 CS 233205B1 CS 823902 A CS823902 A CS 823902A CS 390282 A CS390282 A CS 390282A CS 233205 B1 CS233205 B1 CS 233205B1
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Abstract
Zariadenie pre nepretržitu filtráciu taveniny polymérov, najma pri výrobě syntetických vláken pozostáva z telesa filtra s filtrařnou komorou, zo vstupnej a výstupnej Strbiny pre přechod-'pásu filtračného šita z oboch stráň zovretého medzi dvorná perforovanými platniSkami.The device for continuous filtration of polymer melts, especially in the production of synthetic fibers, consists of a filter body with a filter chamber, an inlet and outlet slot for the passage of the filter seam from both sides, clamped between two perforated plates.
Description
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Vynález sa týlca zariadenia na nepretržitu filtráciu tavenin, najma vláknotvornýchpolymérov, pozostávajáce z telesa filtra s filtračnou komorou opatřenou vstupnou a výstup-nou chladenou Strbinou a posávajáceho sa filtračného šita filtračnou komorou, ktoré zni-žuje nároky na konBtrukoiu filtračného šita.BACKGROUND OF THE INVENTION The present invention relates to a continuous melt filtration apparatus, in particular fiber-forming polymers, comprising a filter body having a filter chamber provided with an inlet and outlet chute and a filtering sewage filtering chamber which reduces the need for filter filtration.
Pre kontinuálnu filtráciu sa používáju doteraz obdobné kontinuálně filtre, u ktorýohposuv filtračného šita filtraCnou komorou sa robí ťahom filtraCného šita na výstupnejstrana pomocou posuvných íelustí zvierajúeieh filtraCné šito ako je to uvedené v Ss. AO 196876, Cs. AO 196877, Cs. AO 196878, Cs. AO 203595. V tohto zariadenia sa mechanickýťaha filtraCné šito v závislosti od snímaného tlaku filtrované;) taveniny před jej vstupomdo filtračnej komory. Pri posuve filtračného šita filtraCným zariadením je potřebnáznaCna sila, ktoré je limitujícím požiadavkom na kvalitu a konStrukciu filtračního šita,kým kvalitná filtráeia by vyžadovala tenSie a menej pevné a hlavně menej nákladné kon-Strukcie filtračných sit. Tým sa zvyáuju náklady na filtračný materiál a celu filtráciu.For continuous filtration, a filter similar to the one used so far has been used, in which the filtering sieve is moved by pulling the filter suture to the outlet side by means of sliding filter sieves as shown in Ss. AO 196876, Cs. AO 196877, Cs. AO 196878, Cs. AO 203595. In this apparatus, the mechanical pulling filter is sewn depending on the sensed pressure of the filtered melt prior to its entry into the filter chamber. When moving the filter sieve through a filtering device, there is a need for a force which is a limiting requirement for the quality and design of the filter sieve, whereas a high quality filtration would require a thinner and less rigid, and especially less expensive, filter screen. This increases the cost of the filter material and the cell filtration.
Ekonomiku filtrácie a navazujuceho tvarovania taveniny najma na vlékna určuje kva-lita filtrácie a jej bezporuchový priebeh. Pri náběhu filtrácie aj pri dnes používanýchvysokokvalitných a najma pevných filtračných sitach dochádza k prietrhom týchto síta v dčsledku toho k poruchám, vypadom vo výrobě a zvýSeniu odpadu.The economy of filtration and the subsequent melt molding of the melt is determined by the quality of the filtration and its trouble-free performance. During the filtration start-up, even with the high-quality and especially solid filter sieves used today, these sieves break out due to failures, production looks and waste increases.
Uvedené nedostatky odstraňuje zariadenie na nepretržitu filtráciu tavenin polymérovpodl’a tohto vynálezu, ktoré pozostáva z telesa filtra s filtračnou komorou zo vstupnoua výstupnou chladenou Strbinou pre přechod filtračného šita, u ktorého je filtraCné šitozovreté medzi svoma posúvanými perforovanými platničkami prechédzajúcimi spolu s filtreč-ným sitom cez filtračnou komoru uzavretu chladenou vstupnou a výstupnou Strbinou,The above drawbacks are eliminated by the continuous melt filtration device of the polymer of the present invention, which consists of a filter body with a filter chamber of an inlet and outlet chute for the passage of a filter screen in which the filter sewn between its displaced perforated plates passing through the filter screen through filter chamber closed by chilled inlet and outlet chute
Na pripojenom obrázku je v pozdTžnom řeze schematicky znázorněné zariadenie přenepřetržitá filtráciu tavenin polymérov podl’a tohto vynálezu pozostávajáce z dutého te-lesa filtra i s ohrevom 12 privádzacím kanálom 9a a k němu protilehlým kanálom 9b přeodvod taveniny polyméru. Filtračna komora 6 v telese filtra 2 je prehradená posávajácimsa filtračným sitom 2 zovretym medzi vrchnou opornou perforovanou platničkou 14a aspodnou opornou perforovanou platničkou 14b posuvajúcou sa po podložke 4. FiltraCné šito2 spolu s oboma opornými perforovanými platničkami 14a. 14b prechádza filtrom cez vstupnáchladená Strbinu 1a a výstupná chladená štrbinu 1b s kanalmi 2, pre chladiace médium.In the accompanying drawing, a device for continuous filtration of the polymer melts of the present invention is shown schematically in the following section, consisting of a hollow filter material with heating 12 supply channel 9a and a channel 9b for transferring the polymer melt therebetween. The filter chamber 6 in the filter body 2 is blocked by a filter screen 2 squeezed between the upper support perforated plate 14a and the bottom support perforated plate 14b sliding over the support 4. Filter sieve 2 together with both support perforated plates 14a. 14b, the filter passes through the inlet tuned slot 1a and the outlet chilled slot 1b with the channels 2 for cooling medium.
Posuv filtračného šita 2 vykonává mechanický posuv 2 s pohonom g, ktorého rýchlosťje odvodená od ádajov tlakového čidla 10 na přívode tavenin polyméru 9a cez ovládačia regulačny člen 11 posuvu perforovaných platniček 14a. 14b. Za výstupnou chladenouStrbinou 2 je ohrevná zóna 13 pre uvoTnenie přilepených oporných perforovaných platni-ček 14a. 14b od znečistěného šita 2·The feed of the filter sieve 2 is performed by a mechanical feed 2 with a drive g, the speed of which is derived from the demands of the pressure sensor 10 on the polymer melt inlet 9a via the actuation control member 11 of the perforated plates 14a. 14b. Behind the outlet chill 2 is a heating zone 13 for releasing the glued abutment plates 14a. 14b from dirty shita 2 ·
Zariadenie pre nepretržitu filtráciu taveniny vláknotvorného polyméru pracujenasledujucím spdsobom.A device for continuously filtering the melt-forming polymer of the fiber-forming polymer in a conventional manner.
Oporné perforované platničky, ktoré do seba presne zapadajá sá vtlačené SeTustmimechanického posuvu do otvoru vstupnej vodou chladenej štrbiny telesa filtra s prietočnýmpotrubím taveniny, roštom a ohrevmi následné do výstupnej chladiacej Strbiny. Medzidvorná perforovanými opornými platničkami prenašajácimi silu potřebná na ich přechod cezcelý filter, je umiestnené filtračně šito, ktoré vytvára žiadané filtračně médium. Pásfiltračného šita je možné podTa potřeby aj měnit, ako například pri náběhu výroby asilnom znečistění. Po opuštění výstupnej Strbiny prichédza zostava pásu filtračného šitaa oporných perforovaných platničiek do ohrevnej zóny kde sa jédnorázovo natavi polymérpo celej dl’žke perforovanéj platničky, čím sa umožní jej oddelenie od znečistěnéhofiltračného šita.Supporting perforated plates that fit precisely into each other through a forced mechanical movement into the inlet of the water-cooled inlet of the filter housing with the melt flow pipe, grate, and heating subsequent to the outlet cooling slot. The intermediate sieve perforated support plates transfer the force required to pass them through the full filter, a filter sieve is placed which produces the desired filter medium. It is also possible to change the filter sewn strip as needed, for example, in the production of asymmetric contamination. Upon leaving the outlet web, the filter belt assembly of the support perforated plates comes into the heating zone where the polymer is dispersed throughout the entire length of the perforated plate, thereby allowing it to be separated from the soiled filter cloth.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS823902A CS233205B1 (en) | 1982-05-27 | 1982-05-27 | Device for continuous filtration of polymer melts |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS823902A CS233205B1 (en) | 1982-05-27 | 1982-05-27 | Device for continuous filtration of polymer melts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS390282A1 CS390282A1 (en) | 1984-03-20 |
| CS233205B1 true CS233205B1 (en) | 1985-02-14 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS823902A CS233205B1 (en) | 1982-05-27 | 1982-05-27 | Device for continuous filtration of polymer melts |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS233205B1 (en) |
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1982
- 1982-05-27 CS CS823902A patent/CS233205B1/en unknown
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| Publication number | Publication date |
|---|---|
| CS390282A1 (en) | 1984-03-20 |
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