无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ

无机盐工业 ›› 2014, Vol. 46 ›› Issue (2): 51-.

• 论文 • 上一篇    下一篇

食用氯化钾生产工艺节能改造

张 浩1,祝桂林1,2,李明达1,2   

  1. 1.连云港职业技术学院,江苏连云港 222006;2.连云港树人科创食品添加剂有限公司
  • 出版日期:2014-02-10 发布日期:2014-01-24

Energy saving reconstruction for edible potassium chloride production technology

Zhang Hao1,Zhu Guilin1,2,Li Mingda1,2   

  1. 1.Lianyungang Technical College,Lianyungang 222006,China;2.Lianyungang Shuren Kechuang Food Additives Co.,Ltd.
  • Online:2014-02-10 Published:2014-01-24

摘要: 在蒸发结晶法生产食用氯化钾工艺中,存在高能耗、高碳排放的问题。每生产1 t食用氯化钾需消耗2 t蒸汽,而80%的蒸汽消耗产生在氯化钾的结晶过程中。为了解决这个问题,利用DTB结晶器和MVR蒸汽压缩技术对结晶工艺进行了改造。结果表明:改造后工艺与原工艺相比,结晶工段蒸汽实现零消耗,总的蒸汽消耗降至0.4 t,蒸汽消耗减少80%,每1 t产品成本节约了 280元,以年产1万t食用氯化钾计,生产系统可节约成本 280万元;同时,二氧化碳的排放量也比过去减少80%以上,实现了节能减排的目的。

关键词: 食用氯化钾 工艺 , 节能 , 改造

Abstract: There are the problems of high energy consumption and high carbon emission in the production technology of edible potassium chloride by evaporation crystallization process.1 t edible potassium chloride product will consume 2 t steam, and 80% of the steam consumption is in the crystallization process of potassium chloride.In order to solve these problems, DTB crystallizer and MVR steam compressor technologies were used on the process.Results showed that: compared with the original technology,crystallization process realized steam zero consumption after the transformation;the total steam consumption was reduced to 0.4 t,and steam consumption reduced by 80%;280 Yuan cost was saved per 1 t product; with an annual output of 10 000 t edible potassium chloride, annual cost savings of production system was up to 2.8 million Yuan;at the same time,carbon dioxide emission also reduced by more than 80%,and therefore the purpose of energy saving and emission reduction was achieved.

Key words: edible potassium chloride, technology, energy saving, reconstruction

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