Titlebook: Electrochemical Cell Design; Ralph E. White Book 1984 Plenum Press, New York 1984 Chlor.chemical engineering.extraction.water

Chandelier

暗指

A Simple Model of a Diaphragm-Type Chlorine Cell, ratio of the electrolyte filled diaphragm relative to the electrolyte (1). It is shown theoretically that the product of N.t and the diaphragm thickness (the “effective” diaphragm thickness, N.t) is actually the important diaphragm characterizing parameter and not N. or the diaphragm thickness separately.

愛得痛了

Electrolysis Cell Design For Ion Exchange Membrane Chlor-Alkali Process,mbranes, cells, anodes, activated cathodes, and heat recovery evaporators (3–6). It has recently begun independent sale of the ion exchange membrane, in addition to the sale of its ion exchange membrane process.

名字的誤用

縫紉

Shunt Current Control in Electrochemical Systems Theoretical Analysis, to development of electrical methods for elimination of the shuntage effects. Passage of appropriate currents through the common electrolyte will null the voltage gradients which normally would produce shuntage.

angiography

狂亂

https://doi.org/10.1007/978-0-387-73186-5roduction in various fields, including effluent treatment, hydrometallurgy, photographic processing and precious metals recovery. The existing and potential uses of the RCE reactor in fields other than metal extraction and production are also briefly considered.

Lime石灰

Flooding Phenomenon of Cryogenic Liquids, sulfosuccinate and zinc electrodes. If, now, both ions react at the electrodes, the potential difference should increase with time in most cases. When it decreases, the decrease is not pronounced. Moreover, then the potential difference decreases only up to a certain time after which it increases with time.

Fulsome

cunning