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US3715388A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing glycol esters from ethylene and propylene

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 Vicinal esters of ethylene glycol and propylene glycol are prepared by continuously reacting ethylene or propylene with molecular oxygen and monobasic carboxylic acids within an oxidation zone containing a liquid phase reaction medium. Selectivity of this liquid phase reaction is improved, without adverse effect upon reaction rate, by maintaining the concentration of the olefin within the liquid phase reaction medium at a level less than about 0.8 wt. percent.

Inventors

  • 👤 J Valbert

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 22:21
CPC Classifications
C; C07; C07C; C07C69/00; C07C69/02; C07C69/22; C07C69/28; C07C67/00; C07C67/04; C07C67/05

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 125 words
In a process for the continuous production of monobasic carboxylic acid diesters of a C2 vicinal glycol by the continuous oxidation with molecular oxygen of ethylene in the presence of 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 of 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 and dissolved ethylene, the improvement which comprises: maintaining the concentration of ethylene in the liquid phase reaction medium at a level less than 0.8 wt. percent.
Claim 2
Dependent Claim 125 words
In a process for the continuous production of monobasic carboxylic acid diesters of a C2 vicinal glycol by the continuous oxidation with molecular oxygen of ethylene in the presence of 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 of 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 and dissolved ethylene, the improvement which comprises: maintaining the concentration of ethylene in the liquid phase reaction medium at a level less than 0.8 wt. percent.
Claim 3
Dependent Claim 13 words
A process in accordance with claim 1 wherein the acid is acetic acid.
Claim 4
Dependent Claim 21 words
A process in accordance with claim 1 wherein the olefin concentration is maintained at a level less than 0.6 wt. percent.
Claim 5
Dependent Claim 20 words
A process in accordance with claim 1 wherein the olefin concentration is maintained at a level below 0.4 wt. percent.
Claim 6
Dependent Claim 25 words
A process in accordance with claim 1 wherein the olefin concentration is maintained at a level between 0.01 wt. percent and about 0.8 wt. percent.
Claim 7
Dependent Claim 29 words
A process in accordance with claim 1 carried out in the presence of tellurium as the variable valence cation and in the presence of bromine or a bromine-containing compound.
Claim 8
Dependent Claim 13 words
A process in accordance with claim 6 wherein the acid is acetic acid.
Claim 9
Dependent Claim 125 words
In a process for the continuous production of monobasic carboxylic acid diesters of a C3 vicinal glycol by the continuous oxidation with molecular oxygen of propylene in the presence of 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 and dissolved propylene, the improvement which comprises: maintaining the concentration of propylene in the liquid phase reaction medium at a level less than 0.6 wt. percent.
Claim 10
Dependent Claim 125 words
In a process for the continuous production of monobasic carboxylic acid diesters of a C3 vicinal glycol by the continuous oxidation with molecular oxygen of propylene in the presence of 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 and dissolved propylene, the improvement which comprises: maintaining the concentration of propylene in the liquid phase reaction medium at a level less than 0.6 wt. percent.
Claim 11
Dependent Claim 13 words
A process in accordance with claim 8 wherein the acid is acetic acid.
Claim 12
Dependent Claim 20 words
A process in accordance with claim 8 wherein the olefin concentration is maintained at a level below 0.4 wt. percent.
Claim 13
Dependent Claim 25 words
A process in accordance with claim 10 wherein the olefin concentration is maintained at a level between 0.01 wt. percent and about 0.4 wt. percent.
Claim 14
Dependent Claim 29 words
A process in accordance with claim 8 carried out in the presence of tellurium as the variable valence cation and in the presence of bromine or a bromine-containing compound.

References Cited (Backward Citations)

GB904304A 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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