陶瓷膜浓缩Iota卡拉胶的初步研究
作者:邓杨桦12,张凯松1
单位: 1.中国科学院城市环境研究所,厦门361021; 2.中国科学院大学,北京100049
关键词: iota-卡拉胶;陶瓷膜;浓缩
出版年,卷(期):页码: 2015,35(1):91-96

摘要:
 本文以Al2O3 /ZrO2陶瓷膜浓缩Iota卡拉胶.实验中考察了不同初始浓度,操作压力,膜面流速和运行温度等因素对膜通量、卡拉胶浓缩倍数、膜总阻力的影响.结果表面:受到凝胶层厚度,粘度等的影响,陶瓷膜的浓缩效果不同。获得的最佳操作参数是:当初始浓度为1%时,操作压力为0.2MPa,错流速度为4.8m/s,运行温度为70℃.该结果采用陶瓷膜浓缩Iota卡拉胶的广阔前景.
In this work, the different operation parameters were compared in terms of water flux,concentration
times and membrane total resistance . The concentration of iota carrageenan solutions were carried out in a tube Al2O3 /ZrO2 ceramic membrane. Although a similar overall driving force and other parameters was used, the attenuation of membrane flux obtained using the high concentration 2% was less than half of that observed using the less concentration 0.25 %, due to gel layer effects. A faster results can observed on proper trans-membrane pressure, cross flow velocity. From these studies, it could be concluded
that, the 3.6 m/s and 0.2MPa has advantages over other parameters , not only in terms of  water  flux, but also concentration times and membrane total resistance. Finally, the concentration of different operation temperature was carried out. Due to the presence of low dynamic viscosity in high temperature, a
lower  mass transfer resistance was observed at 70℃. The results show the good potential of the ceramic membrane for concentration of iota carrageenan.
邓杨桦(1986年-),男,四川乐山人,硕士研究生,主要研究领域:膜制备与应用

参考文献:

[1] 唐家骏. 卡拉胶的生化特性及其应用.[J]. 生物化学与生物物理进展. 1986, 4: 8.
 [2] 王加春. 卡拉胶在啤酒酿造过程的应用.[J]. 食品科学. 1999, 20(11): 37-39.
 [3] Yuan H, Song J, Li X, et al. Immunomodulation and antitumor activity of κ-carrageenan oligosaccharides.[J]. Cancer letters. 2006, 243(2): 228-234.
 [4] 罗驾欧. 新型牙膏粘合剂—卡拉胶.[J]. 牙膏工业. 1994, 2.
 [5] Bixler H J, Porse H. A decade of change in the seaweed hydrocolloids industry.[J]. Journal of applied Phycology. 2011, 23(3): 321-335.
 [6] 韩国华,李海霞. 菲律宾刺生麒麟菜提取ι—卡拉胶的工艺探讨.[J]. 食品与机械. 2001(3): 31-32.
 [7] Beran M, Cao X, Estrov Z, et al. Selective inhibition of cell proliferation and BCR-ABL phosphorylation in acute lymphoblastic leukemia cells expressing Mr 190,000 BCR-ABL protein by a tyrosine kinase inhibitor (CGP-57148).[J]. Clinical Cancer Research. 1998, 4(7): 1661-1672.
 [8] 刘芳,赵谋明,徐建祥,等. 卡拉胶生产中碱处理工艺的作用机理.[J]. 食品科学. 2000, 21(11): 11-14.
 [9] 郭卫强,陈亚民,肖海萍. 膜法卡拉胶浓缩技术提高食用卡拉胶品质的工业化生产研究.[J]. 现代食品科技. 2011, 27(4): 415-417.
[10] Daufin G, Escudier J, Carrere H, et al. Recent and emerging applications of membrane processes in the food and dairy industry.[J]. Food and Bioproducts Processing. 2001, 79(2): 89-102.
[11] Osmond A, Bart F, Carrère H. Concentration of thickening & gelling food additives by ultrafiltration: comparison of flat sheet and tubular membranes.[J]. Filtration & separation. 2002, 39(6): 34-35.
[12] 邱全国. 一种用于卡拉胶生产的膜浓缩工艺[P].CN 102911278A ,2013-02–06.
[13] 谷和平. 陶瓷膜处理含油乳化废水的技术开发及传递模型研究[D]. 南京工业大学, 2003.72-74.
[14] 赵宜江,姚建民. 无机膜提取栀子黄色素的工艺研究.[J]. 南京化工大学学报. 1997, 19(1): 77-81.
[15] 甄宗晴,王长进,郑凯,等. 陶瓷膜处理切削液乳化废水.[J]. 南京工业大学学报: 自然科学版. 2009, 30(6): 79-82.
[16] Marcel Mulder 李琳(译). 膜技术基本原理[M]. 北京: 清华大学出版社, 1999.11-11.
[17] Bacchin P, Aimar P, Field R W. Critical and sustainable fluxes: theory, experiments and applications.[J]. Journal of Membrane Science. 2006, 281(1): 42-69.
[18] Chu H, Zhang Y, Zhou X, et al. Dynamic membrane bioreactor for wastewater treatment: Operation, critical flux, and dynamic membrane structure.[J]. Journal of Membrane Science. 2014, 450: 265-271.
[19] 徐超. 油田含油污水陶瓷膜处理技术研究[D]. 青岛: 中国石油大学, 2010.42-45.
 

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