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US3715389A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing glycol esters from olefinically unsaturated compounds

Assignee: Halcon Research and Development Corp
•
Filing: 1971-03-01
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Granted: 1973-02-06
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Expires: 1991-03-01
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Abstract

Abstract Esters of vicinal glycols are prepared by reacting olefinically unsaturated compounds with molecular oxygen and monobasic carboxylic acids in the presence of a liquid phase reaction medium within an oxidation zone. The reaction is conducted in the presence of a variable valence metal cation and bromine, chlorine, a bromine-containing compound or a chlorine-containing compound. In this process a vapor stream comprising unreacted oxygen and unreacted olefinically unsaturated compound is withdrawn from the oxidation zone and recycled at least in part to the oxidation zone. Rate of formation of the desired glycol esters can be increased by maintaining specified amounts of a third component or mixture of components in the vapor recycled to the reaction system while concurrently maintaining oxygen partial pressure within a specified range.

Inventors

  • 👤 R Hoch
  • 👤 J Kollar

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 19:53
CPC Classifications
C; C07; C07C; C07C69/00; C07C69/02; C07C69/22; C07C69/28; C07C67/00; C07C67/04; C07C67/05

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 310 words
In a process for the production of monobasic carboxylic acid diesters of C2-C5 vicinal glycols by the oxidation with molecular oxygen of a C2-C5 olefinically unsaturated compound in the presence of a monobasic carboxylic acid and a variable valence metal cation selected from at least one member of the group consisting of tellurium, antimony, vanadium, gallium, arsenic, selenium and silver and at least one of bromine, chlorine, a bromine-containing compound yielding bromide ions during reaction or a chlorine-containing compound yielding chloride ions during reaction, said oxidation being conducted within an oxidation zone in the presence of a liquid phase reaction medium comprising the carboxylic acid, wherein oxygen and the olefinically unsaturated compound are introduced to the oxidation zone and are contacted with the liquid phase reaction medium therewithin and wherein a vapor stream comprising unreacted oxygen and unreacted olefinically unsaturated compound is withdrawn from the oxidation zone and recycled at least in part to the oxidation zone, the improvement which comprises: maintaining at least 55 mole percent of a third component in the vapor stream recycled to the oxidation zone, said third component being selected from at least one member of the group consisting of ethAne, propane, and carbon dioxide and concurrently maintaining the oxygen partial pressure in the vapor stream recycled to the oxidation zone at a level of at least 5 p.s.i.a. and not greater than R where: where R is the oxygen partial pressure in psia P is the total pressure of the recycled vapor stream y1 is the mole fraction of ethane in the recycled vapor stream y2 is the mole fraction of nitrogen in the recycled vapor stream y3 is the mole fraction of carbon dioxide in the recycled vapor stream y4 is the mole fraction of methane in the recycled vapor stream y5 is the mole fraction of propane in the recycled vapor stream
Claim 2
Dependent Claim 310 words
In a process for the production of monobasic carboxylic acid diesters of C2-C5 vicinal glycols by the oxidation with molecular oxygen of a C2-C5 olefinically unsaturated compound in the presence of a monobasic carboxylic acid and a variable valence metal cation selected from at least one member of the group consisting of tellurium, antimony, vanadium, gallium, arsenic, selenium and silver and at least one of bromine, chlorine, a bromine-containing compound yielding bromide ions during reaction or a chlorine-containing compound yielding chloride ions during reaction, said oxidation being conducted within an oxidation zone in the presence of a liquid phase reaction medium comprising the carboxylic acid, wherein oxygen and the olefinically unsaturated compound are introduced to the oxidation zone and are contacted with the liquid phase reaction medium therewithin and wherein a vapor stream comprising unreacted oxygen and unreacted olefinically unsaturated compound is withdrawn from the oxidation zone and recycled at least in part to the oxidation zone, the improvement which comprises: maintaining at least 55 mole percent of a third component in the vapor stream recycled to the oxidation zone, said third component being selected from at least one member of the group consisting of ethAne, propane, and carbon dioxide and concurrently maintaining the oxygen partial pressure in the vapor stream recycled to the oxidation zone at a level of at least 5 p.s.i.a. and not greater than R where: where R is the oxygen partial pressure in psia P is the total pressure of the recycled vapor stream y1 is the mole fraction of ethane in the recycled vapor stream y2 is the mole fraction of nitrogen in the recycled vapor stream y3 is the mole fraction of carbon dioxide in the recycled vapor stream y4 is the mole fraction of methane in the recycled vapor stream y5 is the mole fraction of propane in the recycled vapor stream
Claim 3
Dependent Claim 34 words
A process in accordance with claim 1 wherein the concentration of olefinically unsaturated compound in the vapor stream recycled to the oxidation zone is maintained at a level of at least 1.0 mole percent.
Claim 4
Dependent Claim 14 words
A process in accordance with claim 1 wherein the olefinically unsaturated compound is ethylene.
Claim 5
Dependent Claim 19 words
A process in accordance with claim 3 wherein reaction pressure is between about 200 p.s.i.a. and about 600 p.s.i.a.
Claim 6
Dependent Claim 17 words
A process in accordance with claim 3 wherein the oxygen partial pressure is at least 15 p.s.i.a.
Claim 7
Dependent Claim 14 words
A process in accordance with claim 1 wherein the olefinically unsaturated compound is propylene.
Claim 8
Dependent Claim 19 words
A process in accordance with claim 4 wherein the reaction pressure is between about 200 p.s.i.a. and 600 p.s.i.a.
Claim 9
Dependent Claim 17 words
A process in accordance with claim 1 wherein the oxygen partial pressure does not exceed 0.95 R.
Claim 10
Dependent Claim 19 words
A process in accordance with claim 1 wherein the third component is a mixture of ethane and carbon dioxide.
Claim 11
Dependent Claim 19 words
A process in accordance with claim 1 wherein the third component is a mixture of propane and carbon dioxide.
Claim 12
Dependent Claim 17 words
A process in accordance with claim 1 wherein the oxygen partial pressure is at least 10 p.s.i.a.
Claim 13
Dependent Claim 19 words
A process in accordance with claim 1 wherein the carboxylic acid is acetic acid and the olefin is ethylene.
Claim 14
Dependent Claim 19 words
A process in accordance with claim 1 wherein the carboxylic acid is acetic acid and the olefin is propylene.
Claim 15
Dependent Claim 26 words
A process in accordance with claim 1 wherein the cation is tellurium and the halogen is selected from the group consisting of bromine and bromine-containing compounds.
Claim 16
Dependent Claim 17 words
A process in accordance with claim 14 wherein the oxygen partial pressure is at least 10 p.s.i.a.
Claim 17
Dependent Claim 16 words
A process in accordance with claim 14 wherein the oxygen partial pressure does not exceed 0.95R.
Claim 18
Dependent Claim 12 words
A process in accordance with claim 14 wherein the olefin is ethylene.
Claim 19
Dependent Claim 14 words
A process in accordance with claim 17 wherein the carboxylic acid is acetic acid.
Claim 20
Dependent Claim 12 words
A process in accordance with claim 14 wherein the olefin is propylene.

References Cited (Backward Citations)

GB904304A Cited
US3427348A Cited
US3479395A Cited
US3542857A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-02-06 1976-08-07 1977-02-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-02-06 1980-08-07 1981-02-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-02-06 1984-08-07 1985-02-06 $7700.00 Window Closed / Lapsed

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