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U.S. Department of Energy
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Development of a catalyst for conversion of syngas-derived materials to isobutylene

Technical Report ·
DOI:https://doi.org/10.2172/6669055· OSTI ID:6669055
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