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Continuous organic electrochemical synthesis

Technical Report ·
OSTI ID:6517210
The electrochemical oxidation of glucose to gluconic acid and reduction of glucose to sorbitol has been successfully paired in an undivided packed bed electrode flow cell. The use of a Raney nickel powder catalytic cathode significantly improved the current efficiency for sorbitol production, as compared to a high hydrogen overpotential Zn(Hg) cathode. The optimum operating conditions for the paired synthesis are: activity W-2 Raney nickel powder cathode, graphite chip anode, a 1.6 M glucose and 0.4 M CaBr/sub 2/ initial solution composition, pH 6-7, 60/sup 0/C solution temperature, a current density of 250 to 500 mA and a solution volumetric flow rate of 100 ml min/sup -1/. Under these conditions the sorbitol current efficiencies are at least 80%, the glucose acid current efficiencies are 100% and the product yields are quantitative. A separation scheme for the paired synthesis has also been devised. It consists of the precipitation of the oxidation product (calcium gluconate) and the ethanol extraction of glucose and CaBr/sub 2/ from sorbitol. Based on a preliminary economic analysis of the cost of raw materials, energy and the electrochemical cell and separation equipment the cost of producing 1 lb calcium gluconate and 0.68 lb sorbitol in a paired synthesis was estimated to be $0.896. The cost of producing the same amount of sorbitol and calcium gluconate in separate electrochemical cells was calculated to be $1.20. Thus, the paired synthesis appears to be an economically viable process.
Research Organization:
California Univ., Los Angeles (USA)
DOE Contract Number:
AC03-76SF00098
OSTI ID:
6517210
Report Number(s):
LBL-18133; ON: DE85001400
Country of Publication:
United States
Language:
English