中国组织工程研究

中国组织工程研究 ›› 2011, Vol. 15 ›› Issue (25): 4572-4574.doi: 10.3969/j.issn.1673-8225.2011.25.004

• 膜生物材料 membrane biomaterials • 上一篇    下一篇

超滤血红蛋白过程中膜通量的传质特性均呈现阶段性特性

肖  科，刘  峰，高  玮，王  翔，王  莹   

  1. 教育部生物流变科学与技术重点实验室，重庆大学生物工程学院，重庆市  400030
  • 收稿日期:2010-11-28 修回日期:2011-01-17 出版日期:2011-06-18 发布日期:2014-01-10
  • 通讯作者: 王翔，教授，博士生导师，重庆大学生物工程学院，重庆市 400030 xwangchn@vipsina.com
  • 作者简介:肖科★，男，1983年生，重庆市人，汉族，2010年重庆大学毕业，硕士，主要从事生物医学工程专业研究。 Xiaoke83@yahoo.cn
  • 基金资助:

    国家自然科学基金(10572159)，重庆市科委科技计划项目攻关项目(2006ba5010)，高等学校学科创新引智计划(B06023)，重庆大学大型仪器设备开放基金(2074920060080)。

Mass transfer characteristics of hemoglobin solution in ultrafiltration process

Xiao Ke, Liu Feng, Gao Wei, Wang Xiang, Wang Ying   

  1. Key Laboratory of Biorheological Science and Technology, Ministry of Education, College of Bioengineering, Chongqing University, Chongqing  400030, China
  • Received:2010-11-28 Revised:2011-01-17 Online:2011-06-18 Published:2014-01-10
  • Contact: Wang Xiang, Professor, Doctoral supervisor, Key Laboratory of Biorheological Science and Technology, Ministry of Education, College of Bioengineering, Chongqing University, Chongqing 400030, China xwangchn@vipsina.com
  • About author:Xiao Ke★, Master, Key Laboratory of Biorheological Science and Technology, Ministry of Education, College of Bioengineering, Chongqing University, Chongqing 400030, China Xiaoke83@yahoo.cn
  • Supported by:

    National Natural Science Foundation of China, No. 10572159*; the Science and Technology Planning Projects of Chongqing Science and Technology Committee, No. 2006ba5010*; Innovation and Indraught Program of Higher Education, No. B06023*; Open Foundation of Large Instruments and Equipment of Chongqing University, No. 2074920060080*

PDF

368

被引次数

3

摘要：

背景：膜超滤具有对蛋白质天然构象破坏较小以及回收率较高的特性，被应用于蛋白质的分离及纯化上。
目的：利用所建立的传质模型优化血红蛋白超滤操作条件以分离出高纯度的血红蛋白。
方法：利用膜超滤分离纯化的方法，研究浓缩血红蛋白溶液在超滤过程中溶液水分的渗透通量，溶液浓度和滤膜内外压力差之间的相互关系，对膜阻力和浓差极化阻力进行了定量描述，建立传质模型。
结果与结论：①在压力为0.04 MPa，温度为12 ℃条件下，溶液浓度分别为1.18，1.30，1.39，1.56 g/L时，溶液的超滤渗透通量分别1.937 5，1.875 0，1.812 4，1.750 0 L/(m2•h)。②在相同单位时间条件下，压力为0.02，0.03，0.04，0.05，0.06 MPa时，溶液的超滤渗透通量为0.165，0.245，0.325，0.400，0.475 L/(m2•h)。③试验的膜阻力Rm为0.118 2，压力系数a等于0.128。随着蛋白浓度逐步升高，凝胶层逐渐形成，当达到凝胶浓度后再浓缩较困难。在试验条件下血红蛋白溶液凝胶浓度 Cg 为18.82 g/L，超滤传质系数k为0.700 8。

关键词: 血红蛋白, 超滤, 传质模型, 膜通量, 凝胶

Abstract:

BACKGROUND: Ultrafiltration membrane has the characteristics of little destruction of the natural conformation of the protein and high recovery, which has been used in the isolation and purification of protein.
OBJECTIVE: To optimize utrafiltration of hemoglobin by using of the mass transfer model in order to isolate highly purified hemoglobin.
METHODS: Penetration flux, concentration of solution and the relationship between pressure and flux of enrichment hemoglobin solution in the process of ultrafiltration were studied by membrane ultrafiltration isolation and purification methods. Membrane resistance and concentration polarization resistance were quantitatively described and the mass transfer model was established.
RESULTS AND CONCLUSION: ①For the solution concentration of 1.18, 1.30, 1.39, 1.56 g/L, the ultrafiltration flux was   1.937 5, 1.875 0, 1.812 4, 1.750 0 L/(m2•h) respectively at the pressure of 0.04 MPa, 12 ℃;  ②For the different pressure: 0.02, 0.03, 0.04, 0.05, 0.06 MPa, the ultrafiltration flux was 0.165, 0.245, 0.325, 0.400, 0.475 L/(m2•h) respectively with the same time; ③The membrane resistance was 0.118 2, and the pressure coefficient was 0.128. However, the gel layer was gradually formed with the increase of protein concentration; it was hard to concentrate the hemoglobin when the concentration was equal to the gel concentration. The gel concentration Cg was 18.82 g/L, and the ultrafiltration mass transfer coefficient k was 0.700 8.

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