Fast catalytic oxidation of phenol in supercritical water

Xiang Zhang, Phillip E. Savage

Research output: Contribution to journalArticle

52 Scopus citations

Abstract

The catalytic oxidation of phenol in water over a commercial oxidation catalyst, CARULITE 150, was investigated in a fixed bed flow reactor at 250 atm and temperatures from 380°C to 430°C. The phenol and oxygen concentrations at the reactor entrance varied between 0.070 and 1.24 mmol/l, and 9.60 and 39.6 mmol/l, respectively. The reaction conditions produced phenol conversions and selectivities to CO2 much higher than those produced by non-catalytic oxidation. The kinetics of phenol disappearance and of CO2 formation were both roughly first-order, and the activation energies were 31 and 47 kcal/ mol, respectively. The catalyst did not undergo continuous deactivation during the catalytic oxidation, but rather maintained a high activity even after several days of continuous operation.

Original languageEnglish (US)
Pages (from-to)333-342
Number of pages10
JournalCatalysis Today
Volume40
Issue number4
DOIs
StatePublished - May 14 1998

All Science Journal Classification (ASJC) codes

  • Catalysis
  • Chemistry(all)

Fingerprint Dive into the research topics of 'Fast catalytic oxidation of phenol in supercritical water'. Together they form a unique fingerprint.

  • Cite this