PDF Publication Title:
Text from PDF Page: 203
(IN) Cl2 BACK TO SYSTEM 01) MIXED GASES CONTAINING Cl2 Cl2 DEPLETED GASES TO VENT (I) CHLORINE "WINNING" CELLS Figure 36-7. Schematic of an Electrochemical Cell System Estimates for the parasitic power required are given in Table 36-2 for various operating voltages. They are based upon the expected purge rates for maintenance of an average 1% CO^ concentration in the battery system. The coulombic efficiency for this type of device will closely approach 100%. It may be concluded from the foregoing that the parasitic powers will not be excessive. Accurate sizing of the device, from estimates of projected electrode area, requires information relating current density, over-potential, and chlorine activity. Best estimates would be predicated upon experience with electrodes from battery testing. Based on battery operating data, the over-potential on the charge side would be small and predictable. Estimates of current densities for the portion of the cell operating in discharge, however, could not be considered reliable except for order of magnitude. 36-11 J___ (I) CHLORINE "WINNING” CELLS — ELECTRICALLY IN PARALLEL (II) MIXED GAS INLET—CELLS IN SERIES (III) CHLORINE RETURN TO BATTERY — CELLS IN PARALLELPDF Image | Development of the Zinc-Chlorine Battery for Utility
PDF Search Title:
Development of the Zinc-Chlorine Battery for UtilityOriginal File Name Searched:
6302789.pdfDIY PDF Search: Google It | Yahoo | Bing
Salgenx Redox Flow Battery Technology: Power up your energy storage game with Salgenx Salt Water Battery. With its advanced technology, the flow battery provides reliable, scalable, and sustainable energy storage for utility-scale projects. Upgrade to a Salgenx flow battery today and take control of your energy future.
| CONTACT TEL: 608-238-6001 Email: greg@salgenx.com | RSS | AMP |