標題: Titlebook: Electrochemical Cell Design; Ralph E. White Book 1984 Plenum Press, New York 1984 Chlor.chemical engineering.extraction.water [打印本頁] 作者: 警察在苦笑 時間: 2025-3-21 19:13
書目名稱Electrochemical Cell Design影響因子(影響力)
書目名稱Electrochemical Cell Design影響因子(影響力)學科排名
書目名稱Electrochemical Cell Design網(wǎng)絡公開度
書目名稱Electrochemical Cell Design網(wǎng)絡公開度學科排名
書目名稱Electrochemical Cell Design被引頻次
書目名稱Electrochemical Cell Design被引頻次學科排名
書目名稱Electrochemical Cell Design年度引用
書目名稱Electrochemical Cell Design年度引用學科排名
書目名稱Electrochemical Cell Design讀者反饋
書目名稱Electrochemical Cell Design讀者反饋學科排名
作者: 反應 時間: 2025-3-21 23:46
Experiences With A Bench-Scale Electrochemical Plant,other unit operations. The unit operations relevant to this paper are diagrammed in Figure 1. Only with continuous operation of the entire process can problems arising from these interactions be identified and addressed. This paper describes our experiences in taking a new electrochemical reaction t作者: Irritate 時間: 2025-3-22 03:45
Electrochemical Techniques for the Extraction of Heavy Metals in Industry: Concepts, Apparatus And ns selectively using electrochemical processes. The question here is whether this technique can be applied to the industrial purification methods to justify a decision in favor of these methods..It is definitely essential to first make a careful selection of the most suitable process concepts for pr作者: CUMB 時間: 2025-3-22 06:07 作者: magnate 時間: 2025-3-22 10:00
Occupancy and Motion Detectors,other unit operations. The unit operations relevant to this paper are diagrammed in Figure 1. Only with continuous operation of the entire process can problems arising from these interactions be identified and addressed. This paper describes our experiences in taking a new electrochemical reaction t作者: REIGN 時間: 2025-3-22 14:32
Rosalie Sherman,K Ray Chaudhurins selectively using electrochemical processes. The question here is whether this technique can be applied to the industrial purification methods to justify a decision in favor of these methods..It is definitely essential to first make a careful selection of the most suitable process concepts for pr作者: REIGN 時間: 2025-3-22 18:29
Corinne Cortese,Sanja Pupovac,Lina Xu 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.作者: collagen 時間: 2025-3-22 22:33
Position, Displacement, and Level,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.作者: GRATE 時間: 2025-3-23 03:58
Simulation in Force Spectroscopy,ss as much as 1 MWh/ton chlorine produced or 30 MWh/yr-m. of electrode area could be gained. It is concluded that because of technical and economical risks this facility will mainly be introduced in small-scale production units for the present.作者: Hormones 時間: 2025-3-23 07:02
Handbook of Multilingual TESOL in Practice 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.作者: Chandelier 時間: 2025-3-23 13:32 作者: 暗指 時間: 2025-3-23 17:18
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.作者: 愛得痛了 時間: 2025-3-23 18:06
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.作者: 名字的誤用 時間: 2025-3-23 22:45 作者: 縫紉 時間: 2025-3-24 05:16
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.作者: angiography 時間: 2025-3-24 06:43 作者: 狂亂 時間: 2025-3-24 14:26
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.作者: Lime石灰 時間: 2025-3-24 18:13
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.作者: Fulsome 時間: 2025-3-24 20:19 作者: cunning 時間: 2025-3-25 00:30 作者: Immunoglobulin 時間: 2025-3-25 04:43
Change in Overall Ohmic Resistance Due To Migration/Diffusion of Electrolytes, 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.作者: exacerbate 時間: 2025-3-25 08:32
Mathematical Model for Design of Battery Electrodes: Lead-Acid Cell Modelling,of cells where the discharge is limited by the positive electrode. The implication of the model is discussed with emphasis on the interactions between electrode design variations and cell performance.作者: Aspiration 時間: 2025-3-25 13:59
https://doi.org/10.1007/978-3-642-41981-2The gradual development of electrochemical chlor-alkali processes is described. The processes described are as follows: diaphragm, mercury and membrane. These processes are compared and various design and selection factors are given for a variety of membrane processes.作者: 職業(yè) 時間: 2025-3-25 18:13
Integrating Heterogenous ModelsA mathematical model describing a chloralkali-electrolysis in membrane cells including unusual flow pattern is presented. This paper discusses several influences like chemical reactions in the anolyte compartment, the behavior of a membrane during electrolysis and some other details which have to be taken into consideration.作者: 解開 時間: 2025-3-25 22:35 作者: HATCH 時間: 2025-3-26 04:05
Design And Development Of Electrochemical Chlor-Alkali Cells,The gradual development of electrochemical chlor-alkali processes is described. The processes described are as follows: diaphragm, mercury and membrane. These processes are compared and various design and selection factors are given for a variety of membrane processes.作者: 孵卵器 時間: 2025-3-26 08:00 作者: 憎惡 時間: 2025-3-26 09:50 作者: 鈍劍 時間: 2025-3-26 13:57
https://doi.org/10.1007/978-1-4613-2795-0Chlor; chemical engineering; extraction; water作者: biosphere 時間: 2025-3-26 19:40
Interpolation and Model Checking,bilities are based on occurrence of two strictly divided mass flows through the cell. Available designs include membrane gap and solid polymer electrolysis, in situ chemical conversions, use of gas diffusion electrodes, and processing cell cascades with co and countercurrent flows.(2,3,4).作者: Genistein 時間: 2025-3-27 00:01
https://doi.org/10.1007/978-3-030-27486-3e maintenance requirements. The major components of the electrolyzer assembly are shown schematically in figure 1, the electrolyzer pack being built up from alternate anode and cathode sub-assemblies each separated by a sheet of ion exchange membrane and the entire pack sandwiched between end plates held together by a tie-rod system.作者: Tinea-Capitis 時間: 2025-3-27 03:59 作者: 脫水 時間: 2025-3-27 06:57 作者: 沒花的是打擾 時間: 2025-3-27 09:50
Recent Advances in Modeling Gas-Liquid Flowsy distribution and bypass current for various cell geometries and physical properties of the electrolyte, electrodes, and other cell components. The model is compared to an earlier resistive network type model.作者: committed 時間: 2025-3-27 14:37
Design Principles for Chlorine Membrane Cells,bilities are based on occurrence of two strictly divided mass flows through the cell. Available designs include membrane gap and solid polymer electrolysis, in situ chemical conversions, use of gas diffusion electrodes, and processing cell cascades with co and countercurrent flows.(2,3,4).作者: 無底 時間: 2025-3-27 20:00 作者: WITH 時間: 2025-3-28 00:15 作者: crucial 時間: 2025-3-28 03:12 作者: Expand 時間: 2025-3-28 08:11 作者: accessory 時間: 2025-3-28 10:54
http://image.papertrans.cn/e/image/305850.jpg作者: 積習難改 時間: 2025-3-28 16:32 作者: 拖債 時間: 2025-3-28 20:37
Overview: 978-1-4612-9723-9978-1-4613-2795-0作者: 繁榮中國 時間: 2025-3-29 00:12 作者: Glucocorticoids 時間: 2025-3-29 06:53 作者: Spangle 時間: 2025-3-29 07:43
https://doi.org/10.1007/978-3-030-27486-3e maintenance requirements. The major components of the electrolyzer assembly are shown schematically in figure 1, the electrolyzer pack being built up from alternate anode and cathode sub-assemblies each separated by a sheet of ion exchange membrane and the entire pack sandwiched between end plates作者: 友好 時間: 2025-3-29 12:07 作者: Definitive 時間: 2025-3-29 17:21 作者: Monocle 時間: 2025-3-29 20:51 作者: 四溢 時間: 2025-3-30 02:39
Physical Principles of Sensing,hat cells which are currently available commercially can support viable processes for $1.00 lb. chemicals in the 100 molecular weight range. Higher value compounds can be very profitable. For lower value compounds, the same equation can be used to drive cell design towards an acceptable financial re作者: 不確定 時間: 2025-3-30 07:11
Simulation in Force Spectroscopy,to small-scale production. In this investigation it is shown that with air cathodes instead of ordinary planar nickel cathodes in a chlor-alkali process as much as 1 MWh/ton chlorine produced or 30 MWh/yr-m. of electrode area could be gained. It is concluded that because of technical and economical 作者: Obedient 時間: 2025-3-30 10:27
Rosalie Sherman,K Ray Chaudhuriustrial purification plants. The precipitation of these toxic metals in a conventional purification plant, which begins in the mechanical purification process and continues during the biological stage, does not offer a satisfactory solution since the problem is merely deferred. The heavy metals subs作者: 啟發(fā) 時間: 2025-3-30 14:00
https://doi.org/10.1007/978-0-387-73186-5or is discussed. The characteristic features and operational parameters are identified. Several levels of design complexity may be distinguished, ranging from a simple undivided (batch) reactor to a sophisticated reactor which is potentiostatically controlled, divided and designed for truly continuo作者: champaign 時間: 2025-3-30 20:00 作者: 易改變 時間: 2025-3-30 23:35 作者: 珍奇 時間: 2025-3-31 02:52
Recent Advances in Modeling Gas-Liquid Flowsy distribution and bypass current for various cell geometries and physical properties of the electrolyte, electrodes, and other cell components. The model is compared to an earlier resistive network type model.作者: alabaster 時間: 2025-3-31 06:10 作者: 粘 時間: 2025-3-31 12:21
Carlos Fernández de Larrea,Joan Bladé concentration, porosity, and local active material utilization as a function of the time and the position perpendicular to the electrode surface. The model also can be used to quantify the impact on the cell performance of design and operation variables such as discharge rate, operating temperature作者: 秘密會議 時間: 2025-3-31 16:12 作者: 上下連貫 時間: 2025-3-31 20:33 作者: 危險 時間: 2025-3-31 23:50 作者: countenance 時間: 2025-4-1 05:20
Hydraulic Modelling As An Aid To Electrochemical Cell Design,e maintenance requirements. The major components of the electrolyzer assembly are shown schematically in figure 1, the electrolyzer pack being built up from alternate anode and cathode sub-assemblies each separated by a sheet of ion exchange membrane and the entire pack sandwiched between end plates作者: Paraplegia 時間: 2025-4-1 07:10 作者: 休息 時間: 2025-4-1 14:04
