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General current efficiency

The General Current Efficiency for the anodic oxidation is calculated from the COD values, using the following relationship (Martinez-Huitle et al. 2004b) ... [Pg.26]

In general, current efficiency [tj in (8.3)] has to be determined by laboratory experiments. However, for such compounds as phenol which are susceptible of a fast reaction with OH radicals, the model proposed by Iniesta et al. (2001) may be used. Following this model, when the galvanostatic electrolysis is performed in a batch reactor and the process is only limited by the mass transfer of the reactant to the electrode surface, r] is equal to 1 when the applied current density is lower than the initial limiting current density for mineralization of the reactant ... [Pg.220]

The oxygen contribution from these reactions is dependent on the nature of the anode material and the pH of the medium. The current efficiency for oxygen is generally 1—3% using commercial metal anodes. If graphite anodes are used, another overall reaction leading to inefficiency is the oxidation of... [Pg.482]

Current efficiency depends on operating characteristics, eg, pH, temperature, and cell design, and is generally in the 90—98% range. The cell voltage is a function of electrode characteristics and electrolyte conductivity and can be expressed as... [Pg.497]

For a profitable electrochemical process some general factors for success might be Hsted as high product yield and selectivity current efficiency >50%, electrolysis energy <8 kWh/kg product electrode, and membrane ia divided cells, lifetime >1000 hours simple recycle of electrolyte having >10% concentration of product simple isolation of end product and the product should be a key material and/or the company should be comfortable with the electroorganic method. [Pg.86]

Restructuring will promote the introduction of other advanced technologies and practices as well. For example, the use of combined-cycle, gas turbine power plants are expected to proliferate under restructuring. These plants are generally more efficient and more environmentally benign than many fossil fuel plants currently in use. [Pg.1005]

Although the electrolysis of molten salts does not in principle differ from that of aqueous solutions, additional complications are encountered here owing to the problems related to the higher temperatures of operation, the resultant high reactivities of the components, the thermoelectric forces, and the stability of the deposited metals in the molten electrolyte. As a result of this, processes taking place in the melts and at the electrodes cannot be controlled to the same extent as in aqueous or other types of solutions. Considerations pertaining to Faraday s laws have indicated that it would be difficult to prove their applicability to the electrolysis of molten salts, since the current efficiencies obtained are generally too small in such cases. [Pg.694]

The current efficiency may range from 25-30% to as high as 90-100%. The loss in efficiency may be due to several factors which influence the chemical and the electrochemical reactions at the electrodes. For example, factors such as the occurrence of side reactions, the passage of current by electronic conduction, and the dislodging of the deposited product from the electrode may substantially reduce the value of T. In general, the current... [Pg.699]

The current efficiency also depends on the nature of the electrode and of the electrodeposit. Generally the current efficiency is high with electrodes which do not specifically polarize with respect to the desired reaction. The current efficiency is observed to be low when a powdery or a dendritic type of deposit is formed on the electrode. This is because of the relatively poor adherence of such deposits which results in mechanical loss and also because of the possibility of electrical short-circuiting between the electrodes, resulting in flow of an electrical current which does not contribute to the electrochemical reaction. [Pg.701]

Electrogravimetry is one of the oldest electroanalytical methods and generally consists in the selective cathodic deposition of the analyte metal on an electrode (usually platinum), followed by weighing. Although preferably high, the current efficiency does not need to be 100%, provided that the electrodeposition is complete, i.e., exhaustive electrolysis of the metal of interest this contrasts with coulometry, which in addition to exhaustive electrolysis requires 100% current efficiency. [Pg.228]

Electrolysis of water contained within a perfluorinated sulphonic acid membrane (Membrel water electrolysis) developed by ABB [133,201-205] and Sasakura [200]. Current efficiencies reach 14-15% at current densities of 10000 A m2 and more. The cells are generally immersed directly in the water so that ozone is introduced directly into the water to be treated, Fig. 18. [Pg.174]

In general, the efficiency of the columns used in ion chromatography is limited by the large-sized particles and broad particle size distributions of the resin packings. Resin beads are currently available in the ranges of 20-30, 37-74, and 44—57 pm. [Pg.527]

By understanding the boundary layers and the general operating condition limits, plant operators can optimise performance. Small incremental adjustments to the dependent variables, current density and electrolyte concentrations will provide linear plots of the independent variables, voltage and current efficiency, in the safe operating zone. Non-linearity will occur when a limit is reached. [Pg.99]

Asahi s investigations showed that a Na+ concentration of 1.1 N was necessary in compartment II to maintain a current efficiency of 96% in the carboxylic membrane during operation with 3.5 N brine in compartment I and 32% caustic soda in compartment III. The Na+ concentration in compartment II was generally far lower than that in compartment I, and clearly indicates the tendency for depression of the Na+ concentration at the interface of the sulphonic and carboxylic layers in the normal... [Pg.231]

Technetium metal can be electrodeposited from an acidic solution of pertechnetate using a platimun, nickel or copper cathode. Electrolysis of neutral, unbuffered solutions, alkaline solutions, and sulfuric acid solutions lower than 2 N yield a black deposit of hydrated TcOj The current efficiencies are generally poor but the deposition is reasonably quantitative. The deposition requires the application of relatively negative cathode potentials and is therefore non-selective. Polaro-graphy indicates that the overpotentials for the evolution of hydrogen on technetium are rather low hence, electrolysis from acidic media will always include concurrent discharge of hydrogen . ... [Pg.130]

This overview has presented an introduction to the subject of antibiotics in animal agriculture and provides a general view of the extent of antibiotic use. The manuscripts to follow will offer more details and provide additional food for thought. Certainly the current efficient production of meat and dairy products is dependent on a wide variety of antibiotics and this will continue to be true in most Western countries in which livestock production is an important part of the economy. [Pg.7]

Exploration of the scope of NPS in electrochemical science and engineering has so far been rather limited. The estimation of confidence intervals of population mean and median, permutation-based approaches and elementary explorations of trends and association involving metal deposition, corrosion inhibition, transition time in electrolytic metal deposition processes, current efficiency, etc.[8] provides a general framework for basic applications. Two-by-two contingency tables [9], and the analysis of variance via the NPS approach [10] illustrate two specific areas of potential interest to electrochemical process analysts. [Pg.94]

More complex reductions of CO2 by enzyme cascades have also been achieved. A combination of an electron mediator and two enzymes, formate dehydrogenase and methanol dehydrogenase, was used to reduce CO2 to methanol. This system operates with current efficiencies as high as 90% and low overpotentials (approximately —0.8 V vs. SCE at pH 7) [125]. The high selectivity and energy efficiency of this system indicate the potential of enzyme cascades. There are also drawbacks to these systems. In general, enzymes are... [Pg.221]


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See also in sourсe #XX -- [ Pg.26 ]




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