TY - JOUR
T1 - Kinetics of hydrogen peroxide reduction by hydrogen in a microreactor
AU - Voloshin, Yury
AU - Lawal, Adeniyi
PY - 2009/1/31
Y1 - 2009/1/31
N2 - An overall rate expression for the formation of hydrogen peroxide by direct combination (DC) of H2 and O2 is required for a rational design of a microreactor and for the determination of the optimum operating conditions for this process. Since the formation of H2O2 by the DC process involves four simultaneous reactions (synthesis of H2O2, synthesis of water, decomposition of H2O2, and reduction of H2O2 by H2), the overall rate expression must take into account the rate expressions of these reactions. In this work, we investigate the mechanism and the rate expression for reduction of H2O2 by H2. Kinetic experiments were carried out to measure the effects of H2O2 concentration and H2 partial pressure on the rate of reaction. The reaction was shown to be free of mass transfer limitations at the conditions of the kinetic experiments. A Langmuir-Hinshelwood mechanism for the reduction of H2O2 over Pd/SiO2 catalyst was adopted since the simple power-law expression could not explain the obtained kinetic data. A rate expression based on this mechanism was shown to accurately correlate experimental data over a wide range of H2O2 concentration, H2 partial pressure, and temperature.
AB - An overall rate expression for the formation of hydrogen peroxide by direct combination (DC) of H2 and O2 is required for a rational design of a microreactor and for the determination of the optimum operating conditions for this process. Since the formation of H2O2 by the DC process involves four simultaneous reactions (synthesis of H2O2, synthesis of water, decomposition of H2O2, and reduction of H2O2 by H2), the overall rate expression must take into account the rate expressions of these reactions. In this work, we investigate the mechanism and the rate expression for reduction of H2O2 by H2. Kinetic experiments were carried out to measure the effects of H2O2 concentration and H2 partial pressure on the rate of reaction. The reaction was shown to be free of mass transfer limitations at the conditions of the kinetic experiments. A Langmuir-Hinshelwood mechanism for the reduction of H2O2 over Pd/SiO2 catalyst was adopted since the simple power-law expression could not explain the obtained kinetic data. A rate expression based on this mechanism was shown to accurately correlate experimental data over a wide range of H2O2 concentration, H2 partial pressure, and temperature.
KW - Catalysis
KW - Direct synthesis
KW - Hydrogen peroxide
KW - Kinetics
KW - Microreactor
KW - Multiphase reactors
KW - Palladium catalyst
KW - Reduction
KW - Sulfuric acid
UR - http://www.scopus.com/inward/record.url?scp=57649202242&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=57649202242&partnerID=8YFLogxK
U2 - 10.1016/j.apcata.2008.10.019
DO - 10.1016/j.apcata.2008.10.019
M3 - Article
AN - SCOPUS:57649202242
SN - 0926-860X
VL - 353
SP - 9
EP - 16
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
IS - 1
ER -