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therewithin and wherein a vapor stream comprising unreacted oxygen and unreacted olefinically unsaturated compound is withdrawn from the oxidation zone and recycled at least in part to the oxidation zone, the improvement which comprises: maintaining at least 55 mole percent of a third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.