Photoelectrocatalytic hydrogen production from oilfield-produced wastewater in a filter-press reactor using TiO2-based photoanodes

被引:31
作者
Jaramillo-Gutierrez, M. I. [1 ]
Rivero, E. P. [2 ]
Cruz-Diaz, M. R. [2 ]
Nino-Gomez, M. E. [3 ]
Pedraza-Avella, J. A. [1 ]
机构
[1] UIS, GIMBA, Calle 8N 3W-60, Piedecuesta 681011, Santander, Colombia
[2] Univ Nacl Autonoma Mexico, Fac Estudios Super Cuautitlan, Dept Ingn & Tecnol, Ave 1 Mayo S-N, Cuautitlan 54740, Edo De Mexico, Mexico
[3] UIS, Ctr Invest Catalisis CICAT, Calle 8N 3W-60, Piedecuesta 681011, Santander, Colombia
关键词
Photoelectrochemical reactor; Expanded mesh electrodes; Water splitting; Phenol degradation; Wastewater treatment; Flow rate dependence; ELECTROCHEMICAL OXIDATION; MOLECULAR-HYDROGEN; STAINLESS-STEEL; FM01-LC REACTOR; PHENOL; DEGRADATION; ELECTRICITY; ELECTRODES; TIO2; PHOTOFUELCELL;
D O I
10.1016/j.cattod.2015.12.008
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Photoelectrocatalytic hydrogen production and simultaneous oxidation of organic pollutants from oilfield-produced wastewater were evaluated in a continuous filter-press reactor at bench scale using TiO2-based photoanodes under visible-light illumination. TiO2 films were prepared on AISI/SAE 304 stainless steel expanded meshes by sol-gel dip-coating. Nickeled AISI/SAE 304 stainless steel expanded meshes were used as cathode. Initially, the experiments were carried out using synthetic produced wastewater with a salinity equivalent to that of oilfield-produced wastewater and containing phenol at the same concentration as the refractory organic pollutants in this effluent. Cathodic and anodic potential ranges were established by micro-electrolysis studies using voltammetric techniques. Appropriate cathode/anode area ratios for different flow rates were estimated by macro-electrolysis studies using chronoamperometric measurements, in order to establish the cell currents required to obtain the adequate electrode potentials. After 2 h, the highest hydrogen production rate (12.36 mu mol/h) was achieved at a flow rate of 0.76 L/min applying a cell current of 32.44 mA and the lowest hydrogen production rate (5.98 mu mol/h) was achieved at a flow rate of 2.00 L/min applying a cell current of 17.90 mA. Using oilfield-produced wastewater, the hydrogen production rate was 9.11 mu mol/h at the most appropriate operating conditions (0.76 L/min, 32.44 mA). (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:17 / 26
页数:10
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