Process for the generation of .alpha., .beta.-unsaturated carboxylic acids and esters using niobium catalyst
Patent
·
OSTI ID:872735
- Durham, NC
- Cary, NC
- Kingsport, TN
A process using a niobium catalyst includes the step of reacting an ester or carboxylic acid with oxygen and an alcohol in the presence a niobium catalyst to respectively produce an .alpha.,.beta.-unsaturated ester or carboxylic acid. Methanol may be used as the alcohol, and the ester or carboxylic acid may be passed over the niobium catalyst in a vapor stream containing oxygen and methanol. Alternatively, the process using a niobium catalyst may involve the step of reacting an ester and oxygen in the presence the niobium catalyst to produce an .alpha.,.beta.-unsaturated carboxylic acid. In this case the ester may be a methyl ester. In either case, niobium oxide may be used as the niobium catalyst with the niobium oxide being present on a support. The support may be an oxide selected from the group consisting of silicon oxide, aluminum oxide, titanium oxide and mixtures thereof. The catalyst may be formed by reacting niobium fluoride with the oxide serving as the support. The niobium catalyst may contain elemental niobium within the range of 1 wt % to 70 wt %, and more preferably within the range of 10 wt % to 30 wt %. The process may be operated at a temperature from 150 to 450.degree. C. and preferably from 250 to 350.degree. C. The process may be operated at a pressure from 0.1 to 15 atm. absolute and preferably from 0.5-5 atm. absolute. The flow rate of reactants may be from 10 to 10,000 L/kg.sub.(cat) /h, and preferably from 100 to 1,000 L/kg.sub.(cat) /h.
- Research Organization:
- RESEARCH TRIANGLE INSTITUTE
- DOE Contract Number:
- AC22-94PC94065
- Assignee:
- Eastman Chemical Company (Kingsport, TN)
- Patent Number(s):
- US 5998657
- OSTI ID:
- 872735
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
-unsaturated
-unsaturated carboxylic
/999/
000
10
100
15
150
250
30
350
450
5-5
70
absolute
acid
acids
alcohol
alpha
alternatively
aluminum
aluminum oxide
atm
beta
carboxylic
carboxylic acid
carboxylic acids
cat
catalyst
consisting
contain
containing
containing oxygen
degree
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fluoride
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involve
kg
methanol
methyl
methyl ester
mixtures
niobium
niobium catalyst
niobium oxide
operated
oxide
oxide selected
oxygen
passed
preferably
presence
pressure
process
produce
range
rate
reactants
reacting
respectively
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serving
silicon
silicon oxide
step
stream
stream containing
support
temperature
titanium
titanium oxide
vapor
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wt
-unsaturated carboxylic
/999/
000
10
100
15
150
250
30
350
450
5-5
70
absolute
acid
acids
alcohol
alpha
alternatively
aluminum
aluminum oxide
atm
beta
carboxylic
carboxylic acid
carboxylic acids
cat
catalyst
consisting
contain
containing
containing oxygen
degree
elemental
ester
esters
ethyl ester
flow
flow rate
fluoride
formed
generation
involve
kg
methanol
methyl
methyl ester
mixtures
niobium
niobium catalyst
niobium oxide
operated
oxide
oxide selected
oxygen
passed
preferably
presence
pressure
process
produce
range
rate
reactants
reacting
respectively
selected
serving
silicon
silicon oxide
step
stream
stream containing
support
temperature
titanium
titanium oxide
vapor
vapor stream
wt