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Electrolyte performance

The modification of electrolytes via additives is attractive to industry as an economical approach however, its impact on electrolyte performance is mainly restricted to tuning interfacial-related properties because of their small concentration in the electrolyte, while other challenges for the state-of-the-art electrolytes such as temperature limits, ion conductivity, and Inflammability are still determined by the physical properties of the bulk components. Improvements in these bulk-related properties can only be realized by replacing the bulk components of the electrolytes with new solvents and salts, but such efforts have been met with difficulty, since more often than not the improvement in the individually targeted properties is achieved at the expense of other properties that are also of vital importance to the performance of electrolytes. Such collateral damage undermines the significance of the improvements achieved and, in some cases, even renders the entire effort unworthy. [Pg.139]

Figure 8 shows the discharge profile of a cell with different gas flow rates heated to a furnace set temperature of 606°C. A maximum power density of about 0.66 W/cm2 (corresponding to 0.44 V) was obtained at a cell temperature of 744°C using a porous electrolyte. Performance of the cell increased with increasing gas flow rate however, this could usually be attributed to an increase in temperature [4],... [Pg.132]

Proton exchange membrane (PEM) fuel cells are the primary choice for transportation systems, but they can also be useful for stationary power production or local hydrogen production. Most of the challenges of PEM fuel cell commercialization center around cost and materials performance in an integrated system. Some specific issues are the cost of catalyst materials, electrolyte performance, i.e., transport rates, and water collection in the gas diffusion layer (GDL). [Pg.345]

The Krebscosmo Bipolar Cell Electrolyzer BMZ 7.5 which is basically made from steel and titanium. The partition wall of the bipolar electrode is a PTFE foil. Anodes are expanded titanium sheet with noble metal coatings and the cathode structure is a perforated steel sheet. The cell units can be arranged in parallel groups of bipolar elements. Each cell element has 2.5 m of membrane area that operate at a nominal amperage of 7.5 KA. The cell block of the BMZ 7.5/64 electrolyzer consists of 64 elements with 16 series elements with 4 current paths with a nominal block amperage of 30 KA. Electrolytic performance is not disclosed (74). [Pg.351]

The Flemion membrane was applied for the use in the electrolysis of sodium chloride solution. In Fig. 20, electrolytic performance of the membranes having different ion exchange capacity (AR, meq/g) of 1.44 and 1.23 are shown against the concentration of caustic soda produced in the cathod chamber. [Pg.439]

Figure 20. Electrolytic performance of membrane. Conditions brine concentration, 3.5 N current density, 20 A/dm2 and 90° C. Figure 20. Electrolytic performance of membrane. Conditions brine concentration, 3.5 N current density, 20 A/dm2 and 90° C.
Such a structure of the membrane leads to high current efficiency with a catholyte of 20% caustic soda and low ohmic drop of the membrane. The electrolytic performance of Flemion 430 is shown in Fig. 21, along with that of Standard Flemion. Flemion 430 can consume lesser energy than Standard Flemion 230. [Pg.443]

Figure 22. Relationship between ion exchange capacity of Flemion and electrolytic performance. Conditions concentration of KOH, 35 wt% current density, 20... Figure 22. Relationship between ion exchange capacity of Flemion and electrolytic performance. Conditions concentration of KOH, 35 wt% current density, 20...
Indeed, even nonequilibrium systems do not necessarily show measurable excess noise and, thus, deviate from relation 1. An appropriate example that is relevant to the subject is a capillary channel that contains a stream of electrolyte maintained by an external pressure difference. Measurements on several aqueous polymer solutions with added electrolytes performed at up to 5000 dyn/cm2 shear stresses and zero external voltage showed that measurable excess noise can be observed only for non-Newtonian solutions exhibiting elasticity (19, 20). Similar results were obtained for colloid suspensions... [Pg.374]

Besides the considerations on the parameters of the semiconductor and the redox electrolyte, performance of the counterelectrode also matters for designing an efficient PEC cell. The counter-electrode in a PEC cell is a charge carrier collecting material, and catalyzes the electron transfer, but is not chemically involved in the electrochemical reaction. [Pg.306]

A Electrolyte Performance Validation Using Electrochemical Supercapacitor Cells... [Pg.275]

Effect ofimpurities and moisture on lithium bisoxalatoborate (LiBOB) electrolyte performance in lithium-ion cells. [Pg.79]

Fig. 2.27 Trade-off between low flammability and electrolyte performance. Capacity utilization of first cycle and retention at hundredth (for TMP, TEP) or fiftieth cycle (HMPN)... Fig. 2.27 Trade-off between low flammability and electrolyte performance. Capacity utilization of first cycle and retention at hundredth (for TMP, TEP) or fiftieth cycle (HMPN)...

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See also in sourсe #XX -- [ Pg.604 ]




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