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隔膜电解法再生废铬酸液的改进研究
引用本文:李玉江,陈祖盛,徐传宁.隔膜电解法再生废铬酸液的改进研究[J].环境科学研究,1996,9(4):56-59.
作者姓名:李玉江  陈祖盛  徐传宁
作者单位:1.山东工业大学化学工程系 济南 250014
摘    要:以阳离子交换膜为隔膜,电解处理塑料粗化过程中产生的废铬酸液。大大优于陶瓷隔膜电解法。离子交换膜法的条件:在温度40~50℃,槽电压2.5~3.0 V的条件下,控制〔Cr3++〕下限值10g/L。电解过程的电流密度为3.5~4.0A/dm2,电流效率可达72%~80%,电耗仅为150~170 kW·h/m3。 

关 键 词:离子交换膜    隔膜电解    废铬酸
收稿时间:1995/3/27 0:00:00

Disposal of the Waste Solution of Chromic Acid by the Cationexchange Membrane Diaphragm Electrolysis
LI Yujiang,CHEN Zusheng and XU Chuanning.Disposal of the Waste Solution of Chromic Acid by the Cationexchange Membrane Diaphragm Electrolysis[J].Research of Environmental Sciences,1996,9(4):56-59.
Authors:LI Yujiang  CHEN Zusheng and XU Chuanning
Institution:1.Department of Chemical Engineering, Shandong University of Technology, Jinan 2500142.Department of Environmental Engineering, East China University of Science and Technology, Shanghai 20023
Abstract:The problem discussed in this article is the disposal of waste chromic acid solution produced from the plastic roughing by diaphragm electrolysis in which the diaphragm is used as the cation exchange membrane. On the conditiorr that the temperature is at 40—50℃, the applied voltage is 2.5—3.0 V, and the least value of Cr3++] is controlled at 10g/L, the current density is 3.5—4.0A/dm2, the current efficiency reaches 72%—80% and the electric energy consumption is only 150—170 kW·h/m3. The new technique has a great advantage over the ceramic diaphragm electrolysis. 
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