酸性水回收装置运行中的问题及解决措施

来源 :第十一届全国硝酸硝酸盐技术交流会 | 被引量 : 0次 | 上传用户:l100890628
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本文对酸性水回收装置进行了介绍,分析了塔釜液浓度低、硝酸镁结晶堵塞等问题的原因,提出了重新修订工艺指标,硝镁蒸发器负压指标范围修订为-60~-80KPa硝镁蒸发器投用时采用两步提压法,即先将蒸发器负压提升至-50KPa,运行8小时后再进一步提升负压至-60-80KPa。(3)浓缩塔切换时关注稀镁槽和浓镁槽液位,液位异常下降时检查蒸发器。(4)开停车过程中,控制回收塔塔顶采出量在1m3/h,回收塔内的物料优先从塔釜流出等合理有效的解决措施,保证了酸性水回收装置的正常运行.
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