CS232175B1 - to reduce the build up of deposits in the preheaters of the vinyl acetate synthesis mixture - Google Patents

to reduce the build up of deposits in the preheaters of the vinyl acetate synthesis mixture Download PDF

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Publication number
CS232175B1
CS232175B1 CS833820A CS382083A CS232175B1 CS 232175 B1 CS232175 B1 CS 232175B1 CS 833820 A CS833820 A CS 833820A CS 382083 A CS382083 A CS 382083A CS 232175 B1 CS232175 B1 CS 232175B1
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CS
Czechoslovakia
Prior art keywords
vinyl acetate
acid
preheaters
deposits
evaporators
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CS833820A
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Czech (cs)
Slovak (sk)
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CS382083A1 (en
Inventor
Mikulas Buday
Stefan Sikorai
Walter Waradzin
Jozef Barta
Frantisek Spacek
Stefan Bartos
Imrich Volek
Dusan Skrada
Original Assignee
Mikulas Buday
Stefan Sikorai
Walter Waradzin
Jozef Barta
Frantisek Spacek
Stefan Bartos
Imrich Volek
Dusan Skrada
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Application filed by Mikulas Buday, Stefan Sikorai, Walter Waradzin, Jozef Barta, Frantisek Spacek, Stefan Bartos, Imrich Volek, Dusan Skrada filed Critical Mikulas Buday
Priority to CS833820A priority Critical patent/CS232175B1/en
Publication of CS382083A1 publication Critical patent/CS382083A1/en
Publication of CS232175B1 publication Critical patent/CS232175B1/en

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Abstract

Vynález sa týká zvýšenia výrobnosti zariadenia na výrobu vinylacetátu a rieši sposob znlženia tvorby nánosov v predohrievačoch syntéznej zmesi výroby vinylacetátu z acetylénu a kyseliny octovej parofáznym sposobom. Podstata předmětného vynálezu spočívá v odúšlaní časti kyseliny octovej nastrekovanej do odparovačov, prostředníctvom čoho sa priebežne odstraňďjú vzniklé vyššievrúce látky a zabráni sa ich možnému prieniku únosom kvapiek do predohrievačov syntéznej zmesi. Prieniku kvapiek ako příčiny tvorby zvýšeného množstva nánosov sa zabráni reguláciou hladiny kvapalnej kyseliny v odparovačoch, ktorá sa udržuje pod úrovňou horného čela trubkovnice. Sposobom podlá vynálezu sa zabráni hromadeniu vyššievrúcich látok v kyselině octovej v odparovačoch a dosahuje sa významného zvýšenia využitelného fondu výrobného zariadenia.The invention relates to increasing the productivity of the equipment for the production of vinyl acetate and solves the method of reducing the formation of deposits in the preheaters of the synthetic mixture of the production of vinyl acetate from acetylene and acetic acid by the vapor phase method. The essence of the present invention consists in draining off part of the acetic acid injected into the evaporators, by means of which the high-boiling substances formed are continuously removed and their possible penetration by abduction of drops into the preheaters of the synthesis mixture is prevented. The penetration of droplets as the cause of the formation of an increased amount of deposits is prevented by the regulation of the level of liquid acid in the evaporators, which is kept below the level of the upper face of the tube sheet. The method according to the invention prevents the accumulation of high-boiling substances in acetic acid in the evaporators and a significant increase in the usable pool of production equipment is achieved.

Description

232 175232 175

Vynález sa týká spósobu zníženia tvorby nános ov v predo-hrievačoch syntéznej směsi výroby vinylaoetátu u acetylénua kyseliny ootovej parofáznym spósobom*BACKGROUND OF THE INVENTION The present invention relates to a method for reducing the formation of deposits in the pre-heaters of a synthetic mixture of the production of vinyl acetate in acetylene and ootic acid by a phasic process.

Ha vyhrlevamie syntéznej zmesi pozostávajúoej z aoetylénua pár kyseliny ootovej u parofázneho spósobu výroby vinylaoe-tátu sa používaná trubkové výmenníky tepla» Zdrojom tepla jevysokotlaková para vedená do medzitrubkového priestoru. Syntéz-na zmes sa vedle v trubkách* Po čase v nich doohádza k tvorbětuhých nánosov a preto zariadenle je nutné čistit’* Intenzitaioh tvorby je rózna a všeobeone závisí od koncentráoie a dru-hu nečištét naohádzajúoioh sa v surovinách, od spdsobu přípra-vy parnéj zmesi a od čistoty recyklované j kyseliny ootovej* Jeznáme, Se aoetylén získaný z karbidu vápnika obsahuje menšípočet znečisttojúoioh látok a v nižšej konoentrácii než aoety-lén vyrábaný štiepením zemného plynu* Návazné na to tvorba ná-nosov u technologií opracovávájúcioh karbid!oký aoetylén d®významné nižšia* Ro z dlely sá niekedy takého rozsahu, že častéČistenie predohrievačov významné znižuje výkon výrobného za-riadenia spraoovávajůoeho aoetylén na báze zemného plynu* Čis-tenie predohrievačov je časovo náročná operácia, skraouje využitelný fond pracovnej doby zariadenia*The heating of the synthesis mixture consisting of an ethylene and ootic acid vapor in the vapor phase process for the production of vinyl acetate used tubular heat exchangers »The source of heat is the high pressure steam conducted to the inter-tube space. The synthesis of the mixture is next to the tubes in the tubes * Over time, there is a build-up of solid deposits and, therefore, the device needs to be cleaned. The intensity of the formation is rude and depends on the concentration and the nature of the non-purifying material in the raw materials. blends and from the purity of recycled ootic acid * We know, Acetylene recovered from calcium carbide contains a smaller number of contaminants and, in a lower concentration, produced by the cleavage of natural gas * Following the formation of tungsten carbide coating technologies. Significantly Lower * Sometimes such an extent that frequent preheating of the heaters significantly reduces the performance of the production equipment of the natural gas-based ethylene * Pre-heater cleaning is a time-consuming operation;

Uvedené nedostatky odstraňuje spósob zníženia tvorby náno-sov V predohrievačoch syn té znej zmesi výroby vinylaoetátu z aoetylénu a kyseliny octovéj parofáznym spósobom prl teplotách150 až 200°C], ktorý spočívá v tom, že z dna odparovača kyselinyoctovéj sa nepřetržíte alebo přerušované odoberá 0,001 až 0,1hmotnostného dielu celkového hodinového množstva dávkovanéj ky-seliny do odparovača. Hladina kvapalnej kyseliny v odparovači 232 175 meraná v odlučovači kvapiek sa udržuje najvyššie na úrovni hor-ného čela trubkovnice výmennika tepla a odobraná část* kyselinysa spraouje znéraymi spčsobmi# Podstata předkládaného vynálezuvyohádza zo sledovania a analýzy procesu tvorby nánosov» Bolozistené, že v odparovačoch kyseliny octovej z přítomných nečis-tit sa vytvárajú neprohavé látky· Ďalej sa zistilo, že tietolátky sú rozpuštěné v kyselino octovej za podmienok panujúoiohv odparovačoch# Najdčležitejšírn poznatkem je zistená skutočnosť,že k tvorbě nadměrného množstva nánosov doohádza len v prípa-dooh únosu kvapiek, ktoré obsahujú neprohavé látky z odparova-čov do predohrievačov# Reguláoiou hladiny kyseliny ootovejv odparovačoch na optimálnej teplote sa zabráni prieniku kva-piek do pár odvádzaných do predohrievačov# Neprohavé látky,ktoré v procese odparovania objektivně vznikajú, zostávajúrozpuštěné v kyselině ootovej a sa vo formě roztoku kontinuál-ně alebo preruáovane odvádzajú z dna odperovačov do zásobníka#Kyselina ootová zo zásobníka sa spraouje na regenerovaná kyse-linu ootovú známými ep6sobini#The above drawbacks are overcome by the method of reducing the formation of molds in the preheaters of the same mixture of vinyl acetate and acetic acid production by a parasic process at temperatures ranging from 150 to 200 ° C, wherein 0.001 to 0 is removed from the bottom of the acetic acid evaporator. 1 part by weight of the total hourly amount of acid feed into the evaporator. The liquid acid level in the evaporator 232 175 measured in the droplet separator is maintained at the top level of the heat exchanger tube sheet and the acidic portion removed by the methods # The principle of the present invention is based on the monitoring and analysis of the deposit formation process. Non-impurities are present in the non-impurities present. Further, it has been found that tietools are dissolved in acetic acid under the conditions of evaporators # The most important finding is the fact that it only finds the abduction of droplets that contain impermeable substances from evaporators to preheaters # By controlling the level of ootic acid in the evaporators at optimum temperature, the penetration of kva-peaks into the vapor to the preheaters is prevented # The non-volatile substances that are objectively formed in the evaporation process remain dissolved ootovej acid and was added as a solution by continuous preruáovane them or discharged from the bottom into the container odperovačov # of acetic acid from the container to be regenerated spraouje KYSE-proline methyl ester of acetic known ep6sobini #

Vyááieho účinku v porovnaní so súčasným stavom poznaniasa dosahuje v podstatnom znížení tvorby nánosov v predohrie-vačoch# Výhody předkládaného vynálezu spočívá jú predovSetkýmv jednoduchosti jeho uSkutočnenia, s využitím jestvujúoiohvýrobnýoh zariadení s mlnimálnou úpravou potrubnóho prepoje-nia# Jeho využitím doohádza k zníženiu spotřeby vyhrievaoe jpáry v predohrievačoch, k zníženiu pracnosti pri čistění za-riadenia a tým k zvýšeniu využívania fondu pracovněj doby# Sp6-eob podl’a předloženého vynálezu bol úspěšně overený na výrob-nom zariadení, ako je to zřejmé z nasledujúoeho příkladu# Příklad 1The advantage of the present invention lies in the simplicity of its implementation, with the use of existing manufacturing equipment with a fine adjustment of the pipeline connection. pre-heaters, to reduce the laboriousness of cleaning equipment, and thus to increase the use of the Sp6-eob Working Time Fund of the present invention has been successfully verified on a manufacturing facility, as shown in the following example # Example 1

Na spodnú časť potrubia, ktoré spojuje dná odlučovačaa odparovača bolo napojené odvádzaoie potrubie opatřené venti—lom a priezornikom na vizuálnu kontrolu prietoku# V priebehupraoovného oyklu syntézy sa týmto potrubím odoberala kyselinaootová v množstváoh 50 až 70 kg/hadt pri celkovom nástreku700 kg/hfdé kyseliny na jeden odparovač# Hladina kyseliny octo-On the lower part of the pipe connecting the bottom of the evaporator separator, a drain line provided with a valve and a visor to visually inspect the flow was connected. In the course of the synthesis cycle, the acidoot was withdrawn by this line in a quantity of 50 to 70 kg / hect. one vaporizer #

Claims (1)

nej zmesi výroby vinylacetátu z acetylónu a kyseliny ootovej parofáznym spósobom pri teplotách 150 až 220°C vyznačený tým, že z dna odparovača kyseliny ootovej sa nepretržite alebo přerušované odoberá 0,001 až 0,1 hmotnostného dielu celkového hodinového množstva dávkovanéj kyseliny do odparovača, pričom hladina kvapalnéj kyseliny v odparovači meraná v odlučovači kvapiek sa udržuje najvyššie na úrovni horného Čela trubkovnice výmenníka tepla a odobraná časť kyseliny sa spraouje známými, spósobmi*A mixture of the production of vinyl acetate from acetyl and ootic acid by a parophasic process at temperatures of 150 to 220 ° C, characterized in that 0.001 to 0.1 part by weight of the total hourly amount of acid metered into the evaporator is continuously or intermittently withdrawn from the bottom of the ootic acid evaporator. of the acid in the evaporator measured in the droplet separator is maintained at the highest level of the upper face of the heat exchanger tube sheet and the removed part of the acid is sprayed by known methods *
CS833820A 1983-05-30 1983-05-30 to reduce the build up of deposits in the preheaters of the vinyl acetate synthesis mixture CS232175B1 (en)

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CS232175B1 true CS232175B1 (en) 1985-01-16

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