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U.S. Department of Energy
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Trifunctional catalysts for conversion to syngas to alcohols. Fourth quarterly report, June 1-August 31, 1985

Technical Report ·
OSTI ID:5246590
A number of significant catalysts were prepared and tested for CO hydrogenation at 225 to 275/sup 0/C and 450 to 750 psi in the flow reactor system. Rh-Al/sub 2/O/sub 3/-Na. The dependence of selectivity on conversion level was confirmed and further clarified using catalysts of 0 and 2% Na content. Conversion was generally varied by operating at different space rates. Promotion of activity of Rh-Al/sub 2/O/sub 3/ was observed for addition of ions of titanium or of molybdenum, but not for manganese which decreased activity. Rh-TiO/sub 2/ catalysts were found to be very active and gave relatively high selectivity to oxygenates. The addition of lanthanum increased selectivity further. Silica containing catalysts were prepared and tested. One, using a silicated alumina and containing Mo and Mn in addition to Rh, gave good activity and selectivity. A bimetallic Rh-Pd/silica catalyst did not perform well. Analytical. Using the present GC system, a previously unidentified peak was found to correspond to butane in what appears to be amounts unexpectedly high (much larger than predicted by Anderson- Shultz-Flory equation). This is being further clarified. Run data are now being computerized using Lotus 1,2,3, IBM PC. This should assist in data interpretation. XRD is being used to check metal and support character. In one instance no rhodium metal peak was observed on fresly reduced samples but appeared after extensive catalyst use. Infrared. The FTIR system is now operational and initial spectra are being obtained at elevated temperature and pressure. 2 figs.
Research Organization:
Delaware Univ., Newark (USA). Dept. of Chemical Engineering
DOE Contract Number:
AC22-79ET14880
OSTI ID:
5246590
Report Number(s):
DOE/ET/14880-T8; ON: DE850180595
Country of Publication:
United States
Language:
English