Development of a catalyst for conversion of syngas-derived materials to isobutylene
The CO conversion and isobutylene yield for Runs 11 to 20 (except run 12) at the conditions of 450[degree]C, 1,200 psig, and 1,920 gas hourly space velocity (GHSV), Is given in Table 2. These conditions generally provide the maximum CO conversion for each run. Runs 5 to 10 is also provided in Table 2 for a comparison. The description of the catalysts also given in Table 2 includes the composition, method of preparation, and calcination temperature for each catalyst tested. Data for Runs 12 and 21 are at different conditions, as discussed later in this report. The conversion and yield data were obtained at relatively short times on-stream ([approximately]11 hours). The extent of catalyst deactivation has not been determined. The freshly precipitated CeO[sub 2] catalyst, IS-9, is by far the most active but is poorly selective to Isobutene. The catalyst primarily produces saturated by-products. The commercial CeO[sub 2,] IS-8, had low surface area and little activity. Earlier tests show that lowering the calcination temperature of precipitated catalysts produced higher surface areas, higher tetragonal content, higher activity and higher yields. The ZrO[sub 2] sol-gel catalysts show a similar relationship. A comparison of Run 9 (ZrO[sub 2] calcined at 600[degree]C) and Run 16 (ZrO[sub 2] calcined at 500[degree]C) shows that with the decrease in temperature: the surface area almost doubles (81 m[sup 2]/g vs. 45 m[sup 2]/g); the tetragonal phase increased from 10 to 55%; and CO conversion increases (23.9 vs. 30.2%). However, the isobutylene yield remained essentially the same (2.23 vs 2.21%).
- Research Organization:
- UOP, Inc., Des Plaines, IL (United States)
- Sponsoring Organization:
- DOE; USDOE, Washington, DC (United States)
- DOE Contract Number:
- AC22-91PC90042
- OSTI ID:
- 6669055
- Report Number(s):
- DOE/PC/90042-T3; ON: DE93007602
- Country of Publication:
- United States
- Language:
- English
Similar Records
Development of a catalyst for conversion of syngas-derived materials to isobutylene. Quarterly report No. 3, September 30, 1991--December 30, 1991
Development of a catalyst for conversion of syngas-derived materials to isobutylene
Development of a catalyst for conversion of syngas-derived materials to isobutylene. Quarterly report No. 7, October 1, 1992--December 31, 1992
Technical Report
·
Thu Apr 02 23:00:00 EST 1992
·
OSTI ID:10127180
Development of a catalyst for conversion of syngas-derived materials to isobutylene
Technical Report
·
Tue Oct 01 00:00:00 EDT 1996
·
OSTI ID:567432
Development of a catalyst for conversion of syngas-derived materials to isobutylene. Quarterly report No. 7, October 1, 1992--December 31, 1992
Technical Report
·
Wed Sep 08 00:00:00 EDT 1993
·
OSTI ID:101316
Related Subjects
01 COAL, LIGNITE, AND PEAT
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37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400201* -- Chemical & Physicochemical Properties
ALKENES
CATALYSTS
CATALYTIC EFFECTS
CERIUM COMPOUNDS
CERIUM OXIDES
CHALCOGENIDES
CHEMICAL PREPARATION
CONVERSION
DOCUMENT TYPES
FLUIDS
GASES
HYDROCARBONS
ORGANIC COMPOUNDS
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OXYGEN COMPOUNDS
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PROPYLENE
RARE EARTH COMPOUNDS
SPECIFICITY
SYNTHESIS
SYNTHESIS GAS
TRANSITION ELEMENT COMPOUNDS
YIELDS
ZIRCONIUM COMPOUNDS
ZIRCONIUM OXIDES
010408 -- Coal
Lignite
& Peat-- C1 Processes-- (1987-)
37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400201* -- Chemical & Physicochemical Properties
ALKENES
CATALYSTS
CATALYTIC EFFECTS
CERIUM COMPOUNDS
CERIUM OXIDES
CHALCOGENIDES
CHEMICAL PREPARATION
CONVERSION
DOCUMENT TYPES
FLUIDS
GASES
HYDROCARBONS
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
PROGRESS REPORT
PROPYLENE
RARE EARTH COMPOUNDS
SPECIFICITY
SYNTHESIS
SYNTHESIS GAS
TRANSITION ELEMENT COMPOUNDS
YIELDS
ZIRCONIUM COMPOUNDS
ZIRCONIUM OXIDES