scholarly journals PERFORMANCE ASSESSMENT OF A POLYMER ELECTROLYTE MEMBRANE ELECTROCHEMICAL REACTOR UNDER ALKALINE CONDITIONS − A CASE STUDY WITH THE ELECTROOXIDATION OF ALCOHOLS

2016 ◽  
Vol 206 ◽  
pp. 165-175 ◽  
Author(s):  
Leticia García-Cruz ◽  
Clara Casado-Coterillo ◽  
Ángel Irabien ◽  
Vicente Montiel ◽  
Jesus Iniesta
2013 ◽  
Vol 91 ◽  
pp. 69-74 ◽  
Author(s):  
Alfonso Sáez ◽  
Vicente García-García ◽  
José Solla-Gullón ◽  
Antonio Aldaz ◽  
Vicente Montiel

2018 ◽  
Vol 14 ◽  
pp. 537-546
Author(s):  
Cristina Mozo Mulero ◽  
Alfonso Sáez ◽  
Jesús Iniesta ◽  
Vicente Montiel

The electrocatalytic hydrogenation of benzophenone was performed at room temperature and atmospheric pressure using a polymer electrolyte membrane electrochemical reactor (PEMER). Palladium (Pd) nanoparticles were synthesised and supported on a carbonaceous matrix (Pd/C) with a 28 wt % of Pd with respect to carbon material. Pd/C was characterised by transmission electron microscopy (TEM), and thermogravimetric analysis (TGA). Cathodes were prepared using Pd electrocatalytic loadings (LPd) of 0.2 and 0.02 mg cm−2. The anode consisted of hydrogen gas diffusion for the electrooxidation of hydrogen gas, and a 117 Nafion exchange membrane acted as a cationic polymer electrolyte membrane. Benzophenone solution was electrochemically hydrogenated in EtOH/water (90/10 v/v) plus 0.1 M H2SO4. Current densities of 10, 15 and 20 mA cm−2were analysed for the preparative electrochemical hydrogenation of benzophenone and such results led to the highest fractional conversion (XR) of around 30% and a selectivity over 90% for the synthesis of diphenylmethanol upon the lowest current density. With regards to an increase by ten times the Pd electrocatalytic loading the electrocatalytic hydrogenation led neither to an increase in fractional conversion nor to a change in selectivity.


Energies ◽  
2018 ◽  
Vol 11 (10) ◽  
pp. 2691 ◽  
Author(s):  
Chen Li ◽  
Ashanti Sallee ◽  
Xiaoyu Zhang ◽  
Sandeep Kumar

Electrochemical hydrogenation (ECH) of acetone is a relatively new method to produce isopropanol. It provides an alternative way of upgrading bio-fuels with less energy consumption and chemical waste as compared to conventional methods. In this paper, Polymer Electrolyte Membrane Fuel Cell (PEMFC) hardware was used as an electrochemical reactor to hydrogenate acetone to produce isopropanol and diisopropyl ether as a byproduct. High current efficiency (59.7%) and selectivity (>90%) were achieved, while ECH was carried out in mild conditions (65 °C and atmospheric pressure). Various operating parameters were evaluated to determine their effects on the yield of acetone and the overall efficiency of ECH. The results show that an increase in humidity increased the yield of propanol and the efficiency of ECH. The operating temperature and power supply, however, have less effect. The degradation of membranes due to contamination of PEMFC and the mitigation methods were also investigated.


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