SUPERCRITICAL WATER OXIDATION KINETICS AND MECHANISM OF ETHANOL WASTEWATER
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SUPERCRITICAL WATER OXIDATION KINETICS AND MECHANISM OF ETHANOL WASTEWATER
CIESC JournalIssue 1, Pages: 80-85(2003)
作者机构:
清华大学化学工程系
作者简介:
基金信息:
DOI:
CLC:
Online First:25 January 2003,
Published:25 January 2003
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XIANG Botao, WANG Tao, SHEN Zhongyao. SUPERCRITICAL WATER OXIDATION KINETICS AND MECHANISM OF ETHANOL WASTEWATER[J]. CIESC Journal, 2003, (1): 80-85.
DOI:
XIANG Botao, WANG Tao, SHEN Zhongyao. SUPERCRITICAL WATER OXIDATION KINETICS AND MECHANISM OF ETHANOL WASTEWATER[J]. CIESC Journal, 2003, (1): 80-85.DOI:
SUPERCRITICAL WATER OXIDATION KINETICS AND MECHANISM OF ETHANOL WASTEWATER
Supercritical water oxidation(SCWO) of ethanol was performed in an isothermal
plug-flow reactor at temperatures from 475 to 550℃
pressures from 22 to 30 MPa
reactor residence times from 0.6 to 63.7s
and oxygen/ethanol molar feed ratios from 4.56 to 9.09.The experimental results showed that carbon monoxide and carbon dioxide were the major intermediate and the final product respectively.The ethanol conversion increased with increasing residence time and temperature and did not obviously change with varying pressure or oxygen concentration.The global kinetics for ethanol disappearance was described by a rate law that was first order in ethanol and zero order in oxygen
and the deviation between calculated and experimental results was approximately within 10%.Furthermore
SCWO processes of ethanol with different oxidant——oxygen and hydrogen peroxide were studied and compared.The same behaviors were observed under supercritical conditions
while under subcritical condition the oxidative rate with hydrogen peroxide was faster than that with oxygen.Based on the observed phenomena
a new viewpoint on SCWO reaction mechanism was proposed that under supercritical condition with oxidant of either hydrogen peroxide or oxygen
a very fast equilibrium distribution between these oxidants would be reached through a series of free radical reaction regardless of their initial concentrations
and the oxidation was proceeded under the condition of equilibrium distribution of oxidants.