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The electrocatalytic hydrogenation of glucose; 2: Raney nickel powder flow-through reactor model

Journal Article · · Journal of the Electrochemical Society; (United States)
DOI:https://doi.org/10.1149/1.2059198· OSTI ID:6897692
;  [1]
  1. Tulane Univ., New Orleans, LA (United States). Dept. of Chemical Engineering
A computer model which simulates the operation of a flow-through Raney nickel powder electrocatalytic hydrogenation reactor for the synthesis of sorbitol from glucose with simultaneous H[sub 2] evolution has been developed. The model utilizes porous electrode theory, considers both mass-transfer and surface kinetics effects, and contains no adjustable parameters. Hydrogen evolution on Raney nickel is described by a Volmer-Heyrovsky rate expression. The rate equation for glucose hydrogenation is identical to that for the chemical catalytic synthesis of sorbitol with pressurized H[sub 2] gas. For constant-current reactor operation, computed sorbitol current efficiencies match well with experimental data for a range of current densities (0.0053 to 0.021 A/cm[sup 2]) and glucose feed concentrations (0.4 to 1.6M), with an average error of 8.8%. Calculations show that a large fraction of adsorbed hydrogen on the nickel cathode surface is produced by the oxidation of electrogenerated H[sub 2] via the backward Heyrovsky reaction. According to the model, significantly higher sorbitol current efficiencies can be achieved by pulsing the current to the reactor.
OSTI ID:
6897692
Journal Information:
Journal of the Electrochemical Society; (United States), Journal Name: Journal of the Electrochemical Society; (United States) Vol. 141:10; ISSN JESOAN; ISSN 0013-4651
Country of Publication:
United States
Language:
English