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Ramdin, M. (author), Morrison, A.R.T. (author), de Groen, M. (author), van Haperen, M.C.H. (author), De Kler, Robert (author), Irtem, Erdem (author), Laitinen, Antero T. (author), van den Broeke, L.J.P. (author), Breugelmans, Tom (author), Trusler, J. P.Martin (author), de Jong, W. (author), Vlugt, T.J.H. (author)
We use a high-pressure semicontinuous batch electrochemical reactor with a tin-based cathode to demonstrate that it is possible to efficiently convert CO<sub>2</sub> to formic acid (FA) in low-pH (i.e., pH &lt; pK<sub>a</sub>) electrolyte solutions. The effects of CO<sub>2</sub> pressure (up to 50 bar), bipolar membranes, and electrolyte (K...
journal article 2019
document
Ramdin, M. (author), Morrison, A.R.T. (author), de Groen, M. (author), van Haperen, M.C.H. (author), De Kler, Robert (author), van den Broeke, L.J.P. (author), Trusler, J. P.Martin (author), de Jong, W. (author), Vlugt, T.J.H. (author)
A high pressure semicontinuous batch electrolyzer is used to convert CO<sub>2</sub> to formic acid/formate on a tin-based cathode using bipolar membranes (BPMs) and cation exchange membranes (CEMs). The effects of CO<sub>2</sub> pressure up to 50 bar, electrolyte concentration, flow rate, cell potential, and the two types of membranes on the...
journal article 2019