As part of a program to identify and develop techniques for operating feasible electrogenerative processes (1-3), we describe here electrogenerative bromination in which bromine and an olefin are reacted with the aid of suitable electrodes and electrolyte to give dibromoethane and bromohydrin. (We define "electrogenerative processes" as those in which two or more materials react at electrodes so that favorable thermodynamic factors drive the reaction to give a useful chemical product with the generation of byproduct electricity.) Bromine is reduced at the cathode to bromide ions which are transported through the electrolyte to the anode where they combine with olefin, while electrons are conducted through an external circuit to the cathode. Bromine vapor in a nitrogen gas stream and the olefin are introduced to cathode and anode chambers, respectively. The chambers are bounded by gas-permeable, liquid-impermeable electrodes separated by a free electrolyte phase. In contrast to earlier work on other electrogenerative systems (1-3), a diaphragm was needed to separate catholyte and anolyte. This limited the transport of free bromine, probably as Br3-and Brs-(4-6), which would give some direct chemical halogenation of olefin at the anode. Both electrodes operate at positive potentials relative to the standard hydrogen electrode. The rate of bromination and the potential of the cell are controlled by the electrical resistance of the external circuit.Electrode reactions, based on product analyses, with bromide electrolyte appear to be Cathode Br2 -b 2e---# 2Br-[1] Anode RCH=CHR' -{-2Br---> RCH--CHR' -{-2e-[2] L I Br Br or RCH=CHR' -t-2Br-~ H20 --> RCH--CHR' -{-HBr -{-2e-[3]
I I
Br OHNo significant amount of glycol is formed in the electrolyte. Electrogenerative bromination requires no external power source. Furthermore, we have also used chlorine gas instead of bromine vapor at the cathode where reaction isBr2r "4-2e-~ 2Br-Chlorine gas sometimes can be used advantageously at the cathode because of ease of handling and convenience.
ExperimentalA free electrolyte cell similar to that of Landi et al. (7) was used for all runs. It typically can be represented as Olefin I Br-(aq.) ] Membrane ] Br-(aq.) I Br~ Anode Cathode * Electrochemical Society Active Member.where the total free electrolyte chamber thickness varied from 0.25-0.5 in. The cell was constructed so that only the anode, Kel-F, and Teflon came in contact with the olefin. The free electrolyte chamber could be subdivided with diaphragms into two or three compartments. Kel-F inserts were used in the electrolyte chamber to thicken it and were sometimes fitted with inlet and outlet ports to permit electrolyte flow during operation.The electrodes used were gas-permeable, liquidimpermeable commercial American Cyanamid Type LAA-1 (7). They have a platinum black loading of 9 mg/cm 2 on a 50 mesh tantalum screen and are wet proofed with Teflon. In later experiments, carbontetrafluoroethylene film electrodes (8), American Cyanamid LSE, were used on the halogen side of the...