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Control of catalyst deactivation with ammonia. Quarterly report, March 1, 1986-May 31, 1986. [o-cyclohexylphenol]

Technical Report ·
OSTI ID:5723940
In the last Quarterly Report we presented data on the hyydro-deoxygenation (HDO) of dibenzofuran on a presulfided NiMo/Al/sub 2/O/sub 3/ catalyst at 360/sup 0/C and 7.0 MPa. We showed that, after the catalyst had reached steady state, a remarkable increase in catalyst activity could be achieved by replacing the H/sub 2/ stream with a 50:50 mixture of NH/sub 3/ and H/sub 2/ for 1 hour. During the one-hour treatment the HDO rate dropped, but after NH/sub 3/ was removed and the system returned to pure H/sub 2/, catalyst activity more than doubled over that before the NH/sub 3/ treatment. Although activity then slowly dropped, it was significantly greater than before NH/sub 3/ treatment, even 122 hours later. Having shown that NH/sub 3/ indeed has a marked effect on catalyst activity for the HDO of dibenzofuran (DBF), we are now turning to a more detailed examination of the reaction network of DBF to see if we can identify possible causes. We have had considerable experience with DBF in conjunction with studies under another grant, ''Catalytic Hydrotreatment Studies with Model Compounds,'' DE-FG22-83PC60798. Prior to our work the most detailed study of DBF was that of Krishnamurthy, et al. (1981). They reported that an important intermediate was o-cyclohexylphenol which decomposed thermally. We suspected that this then might be a source of carbonaceous deposits. However in an apparatus studying o-cyclohexylphenol as such, thermal reaction was essentially negligible relative to catalytic reaction. 1 fig., 2 tabs.
Research Organization:
Massachusetts Inst. of Tech., Cambridge (USA)
DOE Contract Number:
FG22-85PC80516
OSTI ID:
5723940
Report Number(s):
DOE/PC/80516-3; ON: DE86011588
Country of Publication:
United States
Language:
English