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US3714237A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing vinyl acetate

Assignee: Societa Italiana Resine SpA SIR
•
Filing: 1969-12-10
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Granted: 1973-01-30
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Expires: 1989-12-10
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Abstract

Abstract In the catalytic production of vinyl acetate from ethylene and acetic acid in the presence of oxygen, the improvement consisting in absorbing by-products, from the gases leaving the reaction vessel, in acetic acid with subsequent recovery of gases absorbed in the acetic acid and separation of ethylene therefrom.

Inventors

  • 👤 B Calcagno
  • 👤 C Divo
  • 👤 M Ghirga

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 10:27
CPC Classifications
C; C07; C07C; C07C67/00; C07C67/04; C07C67/05; C07C67/055

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 232 words
In a method of producing vinyl acetate in the liquid phase by feeding ethylene and oxygen or an oxygen-containing gas, at a temperature and pressure sufficient for reaction, into an acetic acid suspension of catalytic salts consisting essentially of suspended in acetic acid, a palladium salt, a copper salt and an acetate selected from the group consisting of alkali metal acetates and alkaline earth metal acetates, to obtain a gaseous reaction product containing vinyl acetate, condensing the normally liquid substances in the gaseous reaction product and recycling the non-condensed gaseous reaction product to the reaction whereby reaction by-products accumulate in the recycle gas, the improvement comprising avoiding the accumulation of by-products in the recycle gas by a process which comprises a. absorbing vinyl acetate and the by-products contained in the recycle non-condensed gaseous reaction products in a solution consisting essentially of the condensed portion of the gaseous reaction product and additional acetic acid sufficient to provide an acetic acid content in said solution of at least 40 percent by weight and directly recycling the non-absorbed gas to the reaction whereby the CO2 content in the recycle gas is less than 20 percent by volume; b. separating from said solution, after the absorption, the gases dissolved therein and recovering ethylene from the separated gases; c. recovering from the solution the vinyl acetate contained therein, and d. recycling the remaining solution to the reaction.
Claim 2
Dependent Claim 232 words
In a method of producing vinyl acetate in the liquid phase by feeding ethylene and oxygen or an oxygen-containing gas, at a temperature and pressure sufficient for reaction, into an acetic acid suspension of catalytic salts consisting essentially of suspended in acetic acid, a palladium salt, a copper salt and an acetate selected from the group consisting of alkali metal acetates and alkaline earth metal acetates, to obtain a gaseous reaction product containing vinyl acetate, condensing the normally liquid substances in the gaseous reaction product and recycling the non-condensed gaseous reaction product to the reaction whereby reaction by-products accumulate in the recycle gas, the improvement comprising avoiding the accumulation of by-products in the recycle gas by a process which comprises a. absorbing vinyl acetate and the by-products contained in the recycle non-condensed gaseous reaction products in a solution consisting essentially of the condensed portion of the gaseous reaction product and additional acetic acid sufficient to provide an acetic acid content in said solution of at least 40 percent by weight and directly recycling the non-absorbed gas to the reaction whereby the CO2 content in the recycle gas is less than 20 percent by volume; b. separating from said solution, after the absorption, the gases dissolved therein and recovering ethylene from the separated gases; c. recovering from the solution the vinyl acetate contained therein, and d. recycling the remaining solution to the reaction.
Claim 3
Dependent Claim 17 words
The method in claim 1 wherein the acetic acid content is at least 50 percent by weight.
Claim 4
Dependent Claim 39 words
The method in claim 1 wherein the substances condensed from the gases from the reaction vessel in which the vinyl acetate is being produced receive an addition of acetic acid sufficienT to offset the acid consumed by the reaction.
Claim 5
Dependent Claim 53 words
The method in claim 1 wherein the amount of absorptive solution used is such that the weight ratio of solution to the carbon dioxide contained in the gases subjected to purification is between 30 and 150:1, the temperature being between 20* C and 50* C and the pressure between 1 and 80 atmospheres.
Claim 6
Dependent Claim 30 words
The method in claim 4 wherein the weight ratio is between 50 and 100:1, the temperature being between 25*C and 35+ C and the pressure between 20 and 70 atmospheres.
Claim 7
Dependent Claim 70 words
The method of claim 1 wherein the palladium salt is present in a concentration of 0.001 to 0.05 moles per liter, the copper salt is present in a concentration of 0.10 to 0.75 moles per liter, the acetate is present in a concentration of between 0.6 and 1.8 moles per liter and the reaction temperature is between 50* C and 200* C at a pressure between 1 and 80 atmospheres.
Claim 8
Dependent Claim 20 words
The method in claim 1 wherein the ethylene recovered from said separated gases is recycled back to the reaction vessel.

References Cited (Backward Citations)

CA771193A Cited
GB1117595A Cited
US3461157A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-01-30 1976-07-31 1977-01-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-01-30 1980-07-31 1981-01-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-01-30 1984-07-31 1985-01-30 $7700.00 Window Closed / Lapsed

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