TY - JOUR
T1 - Energy efficiency improvement on in situ generating H2O2 in a double-compartment ceramic membrane flow reactor using cerium oxide modified graphite felt cathode
AU - Cui, Lele
AU - Ding, Peipei
AU - Zhou, Ming
AU - Jing, Wenheng
N1 - Publisher Copyright:
© 2017 Elsevier B.V.
PY - 2017/12/15
Y1 - 2017/12/15
N2 - Electrochemical technology offers the possibility of in situ hydrogen peroxide generation whose productivity greatly depends on the cathode properties and the reactor configuration. Herein, cerium oxide modified graphite felt is prepared and used as cathode. Ceramic membrane is integrated dividing the cell to two compartments and preventing decomposition of cathode-generated H2O2 at the anode. H2O2 is found almost impermeable through the membrane as concentration difference <0.5 M. The double-cell reactor performs higher energy efficiency than the conventional electrolytic cell. And H2O2 accumulation rate has been enhanced in the double-cell in comparison with the undivided one, no matter using either bared or modified cathode. Operation parameters including flow rate of O2 (FO2), flow rate of electrolyte solution (Fsolution), applied current (I) and pH were optimized. Accumulated concentration of H2O2 on the modified cathode reached 260.7 mg/L with the current efficiency up to 75.7% (working conditions CNa2SO4 = 0.05 M, pH = 2, I = 50 mA, FO2 = 0.2 L/min and Fsolution = 800 μL/min). The yield was 3.8 times higher than using the unmodified cathode. Energy consumption was reduced to 4.8 kWh/kg in the double-cell system (22.1 kWh/kg in the single-cell). In a conclusion, the double-compartment flow reactor is an improved configuration for energy effectiveness and increased productivity of H2O2 for E-Fenton process.
AB - Electrochemical technology offers the possibility of in situ hydrogen peroxide generation whose productivity greatly depends on the cathode properties and the reactor configuration. Herein, cerium oxide modified graphite felt is prepared and used as cathode. Ceramic membrane is integrated dividing the cell to two compartments and preventing decomposition of cathode-generated H2O2 at the anode. H2O2 is found almost impermeable through the membrane as concentration difference <0.5 M. The double-cell reactor performs higher energy efficiency than the conventional electrolytic cell. And H2O2 accumulation rate has been enhanced in the double-cell in comparison with the undivided one, no matter using either bared or modified cathode. Operation parameters including flow rate of O2 (FO2), flow rate of electrolyte solution (Fsolution), applied current (I) and pH were optimized. Accumulated concentration of H2O2 on the modified cathode reached 260.7 mg/L with the current efficiency up to 75.7% (working conditions CNa2SO4 = 0.05 M, pH = 2, I = 50 mA, FO2 = 0.2 L/min and Fsolution = 800 μL/min). The yield was 3.8 times higher than using the unmodified cathode. Energy consumption was reduced to 4.8 kWh/kg in the double-cell system (22.1 kWh/kg in the single-cell). In a conclusion, the double-compartment flow reactor is an improved configuration for energy effectiveness and increased productivity of H2O2 for E-Fenton process.
KW - Ceramic membrane
KW - Double-compartment flow reactor
KW - Energy consumption
KW - Graphite felt modification
KW - Hydrogen peroxide
UR - http://www.scopus.com/inward/record.url?scp=85034021485&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2017.08.092
DO - 10.1016/j.cej.2017.08.092
M3 - 文章
AN - SCOPUS:85034021485
SN - 1385-8947
VL - 330
SP - 1316
EP - 1325
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -