CS259586B1 - A method of preparing pure xylene - Google Patents

A method of preparing pure xylene Download PDF

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CS259586B1
CS259586B1 CS87268A CS26887A CS259586B1 CS 259586 B1 CS259586 B1 CS 259586B1 CS 87268 A CS87268 A CS 87268A CS 26887 A CS26887 A CS 26887A CS 259586 B1 CS259586 B1 CS 259586B1
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Czechoslovakia
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ppm
xylene
working pressure
distillate
pressure
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CS87268A
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Czech (cs)
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CS26887A1 (en
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Juraj Cech
Iva Fabusova
Peter Skrovina
Pavel Fried
Michal Singliar
Emil Vojtech
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Juraj Cech
Iva Fabusova
Peter Skrovina
Pavel Fried
Michal Singliar
Emil Vojtech
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Priority to CS87268A priority Critical patent/CS259586B1/en
Publication of CS26887A1 publication Critical patent/CS26887A1/en
Publication of CS259586B1 publication Critical patent/CS259586B1/en

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Xylen sa diskontínuálne alebo kontinuálně rektifikuje za atmosférického tlaku alebo vákua, bez přístupu vzduchu. Odoberá sa frakcia pri vymezenej strednej teplote, ktorá je rovnovážnou teplotou vzhfadom na pracovný tlak. Pracovný tlak je z intervalu tlakov 8 až 101,32 kPa. Destilát sa priamo vedie cez sústavu mikrofiltrov s pórovitosťou 0,8 μία, 0,4 μΐη a 0,2 μία.Xylene is discontinuously or continuously rectified under atmospheric pressure or vacuum, without access to air. A fraction is taken at a defined mean temperature, which is the equilibrium temperature with respect to the working pressure. The working pressure is from a pressure interval of 8 to 101.32 kPa. The distillate is directly passed through a system of microfilters with a porosity of 0.8 µm, 0.4 µm and 0.2 µm.

Description

259536259536

Vynález sa týká přípravy zvlášť čistéhoxylénu použitím fyzikálno-chemických me-tod čistenia.BACKGROUND OF THE INVENTION The present invention relates to the preparation of especially pure oxylene using physico-chemical purification methods.

Xylén sa používá ako oplachovadlo pri vý-robě integrovaných obvodov pre mikroelek-troniku. Pre tento účel používaný xylén mu-sí vyhovovať přísným kritériám čistoty, kto-ré výrobky bežnej komerčnej čistoty nespí-ňajú. Nečistoty, ktoré sa v týchto výrobkochnachádzajú, možno zařadit do dvoch sku-pin: I. skupina — nečistoty organického cha-rakteru, ktoré predstavujú zvyšky vstup-ných surovin, nečistoty vstupných surovina tiež produkty vedlejších reakcií. II. skupina — nečistoty anorganickéhocharakteru, napr. ióny kovov uvolněné ko-róziou výrobného zariadenia, prachové čás-tice pri styku s okolitým vzduchom.Xylene is used as a rinse aid in the manufacture of integrated microelectronic circuits. The xylene used for this purpose must comply with the stringent purity criteria that conventional commercial purity products do not. The impurities found in these products can be classified in two groups: I. Group - impurities of organic character, which represent residues of feedstock, impurities of feedstock as well as products of side reactions. II. a group - impurities of an inorganic character, e.g., metal ions released by the corrosion of a manufacturing apparatus, dust particles in contact with ambient air.

Vyššie uvedené nedostatky nemá spósobpřípravy zvlášť čistého xylénu, ktorého pod-stata tkvie v tom, že vyrábaný xylén čistoty„čistý“, alebo p. a., alebo „polymerizačný“sa kontinuálně alebo diskontinuálne desti-luje za zníženého alebo atmosférického tla-ku v aparatuře, ktorej materiál je odolnýkoróznym vplyvom xylénu, pričom sa odo-berá frakcia pri teplote U ± 1 °C danej vzťa-hom to = ___1472,733__ 6,14049 — log p — 217,808 kde to je teplota varu zodpovedajúca pracov-nému tlaku vo °C a p je pracovný tlak v destilačnej aparatu-ře v kPa.The aforementioned drawbacks are not due to the preparation of particularly pure xylene, the essence of which is that the pure xylene produced, or pure, or "polymerized" is continuously or discontinuously distilled under reduced or atmospheric pressure in an apparatus of which the material is resistant to corrosion by xylene, taking off the fraction at a temperature of ± 1 ° C given that it is 1472,733, 6,14049 log p - 217,808 where the boiling point corresponds to the working pressure in ° C and is the working pressure in the distillation apparatus in kPa.

Destilát sa následné vedie cez sústavumikrofiltrov, ktoré zabezpečujú dosiahnutiekvality produktu z hradiska množstva a dis-tribuce heterogénnych nečistót takto: velkost častíc1 až 5 μτα5 až 25 μίαnad 25 μία ipočet v 1 dm'max. 20 000max. 3 000max. 500 4 troníku sa připraví z komerčných druhovxylénu takto:The distillate is subsequently passed through a system of microfilters which ensure that the product from the hillfort of the quantity and dispersion of the heterogeneous impurities is obtained as follows: particle size 1 to 5 μτα5 to 25 μίαnad 25 μία per 1 dm'max. 20 000max. 3 000max. 500 4 of the trikone shall be prepared from commercial species of oxylene as follows:

Xylén komerčnej čistoty sa přečerpá dozásobníka a odtial sa nastrekuje dávkova-cím čerpadlom do rektifikačného zariade-nia. Rektifikáciu je možné viesť kontinuál-ně, alebo diskontinuálne. Tlakovo-teplotnépodmienky, v priestore destilačného zariade-nia sú rovnovážnehoi charakteru, pričompracovný tlak sa nastaví v oblasti od 8 kPado 101,32 kPa. Teplota odběru produktu jeto = 1 °C, pričom t0 je rovnovážná teplotavaru xylénu pri danom ipracovnom tlaku zvyššie uvedeného rozsahu pracovných tla-kov.Xylene of commercial purity is pumped through the feeder and sprayed with a metering pump into the rectification device. Rectification can be conducted continuously or discontinuously. The pressure-temperature conditions in the distillation plant space are equilibrium, the working pressure being adjusted in the range from 8 kPa to 101.32 kPa. The product withdrawal temperature is = 1 ° C, with t0 equilibrating the xylene temperature at a given working pressure of the aforementioned working pressure range.

Destilát sa zachytává do předlohy tak, žeje zamedzené přístupu vzduchu do předlo-hy. Destilát sa z destilačnej předlohy násled-né vedie do stupňa filtrácie. Filtrácia sauskutočňuje viacstupňovým spósobom tak,že filtre sú umiestnené za sebou a veíkosťpórov membrán klesá v smere toku filtro-vaného média. Produkt po rektifikácii a filt-rácii sa analyzuje na obsah chemických iheterogénnych nečistót. Filtračně i destilač-né zariadenie musí byť z materiálov odol-ných pósobeniu xylénu a jeho sprievodnýchpříměsí. PříkladThe distillate is trapped in the master by preventing air from entering the master. The distillate is subsequently passed to the filtration stage from the distillation master. The filtration is carried out in a multistage manner such that the filters are placed one behind the other and the size of the membranes decreases in the direction of the flow of the filter medium. The product after rectification and filtration is analyzed for chemical heterogeneous impurities. The filter and distillation apparatus must be made of materials resistant to the action of xylene and its accompanying additives. Example

Xylén kvality „polymerizačný“ sa v množ-stve 100 litrov načerpal do zásobníka a od-tial postupné dávkoval skleněným čerpad-lom rýchlosťou 18 litrov/h do varáka skle-nenej destilačnej odparky SIMAX s krátkourektifikačnou náplňovou kolonou. Pracovnýtlak v· kolóne bol 101,32 kPa. Odoberal saprodukt so začiatkom destilácie t0 = 137,5stupňov Celzia a koncom destilácie pri t0 == 139,5 °C. Produkt sa z destilácie viedolpomocou skleněného čerpadla do trojstup-ňovej filtrácie. Telesá filtrov boli z oceletriedy 17. Filtračně membrány použité naodstránenie heterogénnych častíc destilátumali velkosti pórov: 1. stupeň 0,8 μϊη 2. stupeň 0,4 μϊη 3. stupeň 0,2 μϊηThe "polymerization" xylene was pumped into the reservoir at 100 liters and was subsequently fed through the glass pump at a rate of 18 liters / h into a SIMAX glass-bottom cooker with a short-refill packed column. The working pressure in the column was 101.32 kPa. The product was collected with distillation beginning t0 = 137.5 degrees Celsius and the end of distillation at t = 139.5 ° C. The product is distilled from the glass pump by three-stage filtration. Filter housings were made of steel grade 17. Filter membranes used to remove heterogeneous particles destilate pore sizes: 1st degree 0.8 μϊη 2nd degree 0.4 μϊη 3rd degree 0.2 μϊη

IAND

Analýza produktu potvrdila porovnáním so surovinou, že produkt vyhovuje kvalitě ipre mikroelektroniku:Product analysis confirmed by comparison with raw material that the product conforms to ipre microelectronics:

Veíkosť otvorov pórov membrán v jednot-livých filtračných stupňoch je klesajúca vsmere toku filtrovaného média.The size of the pores of the pores of the membranes in the individual filtration stages is decreasing in proportion to the flow of the filtered medium.

Vysokočistý xylén kvality pre mikroelek-High-purity xylene quality for microelements

Claims (1)

259586 Tabulka Vstup Xylen podlá Xylen podlá surovina spůsobu vynálezu požiadaviek kvality pře mikroelektro-niku Obsah hlavnej zložky— celkový obsah izomérov 99,1 % 99,8 % 99 % odparok ppm 12,0 2,5 5,0 obsah vody ppm 20,0 14,0 100,0 kyslosť (ako HCI) ppm 6,5 1,3 5,0 olovo ppm 0,15 0,02 0,05 arzén ppm 0,15 0,01 0,01 sodík ppm 0,5 0,19 0,5 vápnik ppm 0,7 0,23 0,5 litium ppm 0,02 0,01 0,02 draslík ippm 0,2 0,1 0,1 obsah heterogénnych častíc 24 670 990 20 000 1 až 5 μτα 22 560 969 3 000 496 215 500 PREDMET VYNALEZU Spósob přípravy čistého xylenu vyznaču-júci sa tým, že sa xylén destiluje za atmo-sférického tlaku alebo vakua v destilačnomzariadení z materiálu odolného voči koróz-nym vplyvom destilovaného média, bez pří-stupu vzduchu, pričom středná teplota od-běru destilátu t0 + 1 °C závislá na zvolenompracovnom tlaku je daná vzťahom1472,733 0 6,14049 — log p 217,808 kde t0 je teplota varu zodpovedajúca pracov-nému tlaku vo °C a p je pracovný tlak v destilačnej aparatú-re v kPa, a takto odobratý destilát sa následné filtru-je na sústave mikrofiltrov s pórovitosťoumembrán 0,8 μτα, 0,4 <um a 0,2 ,um.259586 Table Input Xylene by Xylene by Raw Material Method of Invention Microelectric Quality Requirements Main Ingredient Content - Total Isomers 99.1% 99.8% 99% Evaporation ppm 12.0 2.5 5.0 Water Content ppm 20.0 14.0 100.0 acidity (as HCl) ppm 6.5 1.3 5.0 lead ppm 0.15 0.02 0.05 arsenic ppm 0.15 0.01 0.01 sodium ppm 0.5 0, 19 0.5 calcium ppm 0.7 0.23 0.5 liters ppm 0.02 0.01 0.02 potassium ippm 0.2 0.1 0.1 content of heterogeneous particles 24 670 990 20 000 1 to 5 μτα 22 SUMMARY OF THE INVENTION A method for the preparation of pure xylene, characterized in that xylene is distilled at atmospheric pressure or vacuum in a distillation apparatus made of a material resistant to the corrosive effects of the distilled medium without air the mean temperature of the distillate withdrawal t0 + 1 ° C, depending on the chosen working pressure, is given by 1472.733 0 6.14049 - log p 217,808 where t0 is the boiling temperature corresponding to the working pressure in ° C and the working pressure in the distillation apparatus is in kPa, and the distillate thus collected is followed by a filter on a microfilter system with membrane porosity of 0.8 µm, 0.4 µm and 0.2 µm.
CS87268A 1987-01-15 1987-01-15 A method of preparing pure xylene CS259586B1 (en)

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