摘要
介绍了2万t/a 45%离子膜法烧碱的工艺特点,改造了工艺不合理之处,达到了提高生产效率、降低生产成本的目的。
The characteristics of the production process of 45 wt% ion -exchange membrane caustic soda were introduced, and the unreasonable matters were corrected. So the aim of increasing production efficiency and decreasing production cost was obtained.
出处
《氯碱工业》
CAS
2007年第4期26-26,28,共2页
Chlor-Alkali Industry
关键词
旋转薄膜蒸发器
冷凝水
节能降耗
rotary thin - film evaporator
condensate
energy - saving and consumption reduction