食品科学 ›› 2012, Vol. 33 ›› Issue (12): 69-74.doi: 10.7506/spkx1002-6630-201212014

• 工艺技术 • 上一篇    下一篇

连续离子交换法分离L- 乳酸的工艺设计及优化

姜绍通,于力涛,李兴江,吴学凤   

  1. 合肥工业大学生物与食品工程学院,安徽省农产品精深加工省级实验室
  • 出版日期:2012-06-25 发布日期:2012-07-27
  • 基金资助:
    国家自然科学基金面上项目(31071636);安徽省自然科学基金项目(090411015)

Process Design and Optimization for Separation of L-Lactic Acid by Continuous Ion Exchange

JIANG Shao-tong,YU Li-tao,LI Xing-jiang,WU Xue-feng   

  1. (School of Biotechnology and Food Engineering, Hefei University of Technology, Key Laboratory for Agricultural Products Proceeding of Anhui Province, Hefei 230009, China)
  • Online:2012-06-25 Published:2012-07-27

摘要: 与传统固定床离子交换工艺相比,连续离子交换分离L-乳酸具有连续、稳定、高效等显著优点。本实验基于静态吸附和固定床离子交换实验结果,设计优化连续离子交换工艺,实现了L-乳酸经济、连续、高效分离。通过静态吸附实验,筛选出最优树脂为732树脂,可在1min内达到吸附平衡,吸附量达345.97mg/g;最佳解吸剂为0.5moL/L H2SO4溶液。通过固定床离子交换实验,确定最佳进料流速40mL/min、最佳高径比7.5:1、穿透时间21.5min,用0.5mol/L H2SO4溶液进行解吸,解吸率超过97%。通过连续离子交换实验,确定了交换区(1#~6#)、交换后水洗区(18#~20#)、再生区(12#~17#)、再生后水洗区(9#~11#)和产品顶水区(7#~8#)的最佳进料流速分别为40、40、140、35mL/min和20mL/min,且各出口浓度呈周期性稳定变化。

关键词: L-乳酸铵, L-乳酸, 分离, 静态吸附, 固定床, 连续离子交换

Abstract: Over the traditional fixed bed ion exchange, continuous ion exchange has several significant advantages for the separation of L-lactic acid, such as continuous, stable and efficient. Economic, continuous and efficient separation of L-lactic acid was achieved using a continuous ion exchange process designed based on the results of static adsorption and fixed-bed ion exchange. Through static adsorption experiments, 732 type resin was identified as the best resin, which could reach adsorption equilibrium within 1 min with a maximum adsorption quantity of 345.97 mg/g. The best desportion agent was 0.5 mol/L H2SO4. In fixed bed ion exchange experiments, a desorption rate of over 97% was obtained under the conditions: sample loading flow rate 40 mL/min, column height-to-diameter ratio 7.5:1, breakthrough time 21.5 min, and desportion with 0.5 mol/L H2SO4. In continuous ion exchange experiments, the optimal sample loading flow rate at the exchange areas (1#-6#), washing areas after exchange (18#-20#), regeneration areas (12#-17#), washing areas after regeneration (9#-11#), top water areas with product (7#-8#) were 40, 40, 140, 35 mL/min and 20 mL/min, respectively. Each outlet concentration showed a cyclical change.

Key words: L-lactic ammonium, L-lactic acid, separation, static adsorption, fixed bed, continuous ion exchange

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