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Title: Catalytic hydroprocessing of chloropyridinols

Conference · · Industrial and Engineering Chemistry Research; (United States)
OSTI ID:6610944
;  [1]
  1. Univ. of California, Los Angeles, CA (United States). Dept. of Chemical Engineering

The hydrodechlorination and hydrodeoxygenation of 2-chloro-3-pyridinol, 5-chloro-3-pyridinol, and 6-chloro-2-pyridinol were examined using a packed bed microreactor operating at 1,500 psi and at temperatures between 275 and 325 C. A commercial NiMo catalyst was used. Dechlorination to pyridinols was the dominant pathway with some subsequent deoxygenation. The overall rates and activation energies (18--35 kcal/mol) of dechlorination were comparable to the dechlorination rate parameters observed for chlorinated benzenes and chlorinated phenols, indicating that the pyridinic nitrogen has only a minor effect on dechlorination rates. Differences in dechlorination rates between the chloropyridinols were qualitatively explained based on the electron donating properties of the hydroxyl group and steric effects. Such studies are critical for evaluating the utility of catalytic hydroprocessing in waste management since waste streams are likely to contain a variety of contaminants and some chlorinated organics are multifunctional (e.g., chlorophenol).

OSTI ID:
6610944
Report Number(s):
CONF-940301-; CODEN: IECRED
Journal Information:
Industrial and Engineering Chemistry Research; (United States), Vol. 33:12; Conference: 207. spring national meeting of the American Chemical Society (ACS), San Diego, CA (United States), 13-18 Mar 1994; ISSN 0888-5885
Country of Publication:
United States
Language:
English