摘要
从理论上对离子膜碱与隔膜碱工艺装置回收盐水的综合利用可行性进行了分析,通过工艺优化设计,在同等规模产量的情况下掺卤比例理论上可接近100%,经济效益比较显著。
The comprehensive utilization of recovered brine in diaphragm and ionic membrane caustic soda process were analyzed. Through design optimization of process, adding rate of bittern under the same scale and capacity from principles were about 100%, and economic benefits was obvious.
出处
《中国氯碱》
CAS
2006年第1期42-44,共3页
China Chlor-Alkali
关键词
离子膜烧碱
隔膜法烧碱
卤水
回收盐水
综合利用
ionic membrane caustic soda
diaphragm membrane caustic soda
bittern
recovered brine
comprehensive utilization
