摘要
分析了对羟基左旋苯甘氨酸母液浓缩结晶过程存在的问题,介绍了三效热泵蒸发结晶工艺。该工艺采用三效并流流程,利用降膜蒸发器、热泵技术进行低温真空蒸发操作。充分利用了一效蒸发器产生的二次蒸汽,新工艺汽水蒸发比降至0.35t/t,左旋苯甘氨酸产量提高约50%。三效热泵蒸发工艺适用于物料处理量大、沸点升高小、蒸发温度低的物料的浓缩结晶。
The problems which existed in the D-p-hydroxyphenylglycine concentrative crystallization process are analyzed. The triple-effect heat-pump falling-film evaporative crystallization technology used in the preparation of D-p- hydroxyphenylglycine is introduced. The triple-effect co-current flow process is adopted. The evaporation process is accomplished under low-temperature and vacuum conditions with falling-film evaporators and heat-pumps technology. The secondary steam from the first-effect evaporator is sufficiently utilized, and the evaporative ratio of steam to water is reduced to 0.35 t/t,and the production is improved by 50%. The technology can be used in the process when the amount of concentrative liquid is large, change of raised boiling point is small and evaporation temperature is low.
出处
《现代化工》
EI
CAS
CSCD
北大核心
2007年第4期49-51,53,共4页
Modern Chemical Industry
关键词
对羟基左旋苯甘氨酸
热泵
结晶
节能
D-p-hydroxyphenylglycine
heat pump
crystallization
energy-saving