Study on the Concentration Process of Glutamic Supernatant Fluid by Vacuum Membrane Distillation and the Reuse of Product Water

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The optimal decoloring conditions for glutamate supernatant in orthogonal experiment are: 15g/l bentonite concentration, 2h decoloring time, and 40°C decoloring temperature. VMD technology can concentrate glutamate supernatant filtrate from 2.01% to 5.35%, and bring down flux from 6.71 L/m2h to 1.94L/m2h, at a concentration rate of 1.72 times. The glutamic acid concentration in supernatant fluid is enriched from 2.03% to 5.16%, and flux attenuated from 5.47 L/m2h to 1.91 L/m2h. As glutamic acid concentration in supernatant increases, membrane flux gradually decreases. Analysis of water production in glutamate supernatant membrane distillation and the meteorological chromatograms of glutamic acid filtrate prove that the difference between water-yielding peak time of supernatant fluid and that of the filtrate is less than 0.1 min. The volatile substances during water production are from glutamic acid filtrate and are of the same matter. Therefore, the product water in supernatant fluid membrane distillation can be reused to improve water production efficiency.

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November 2012

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] B.R. Bodell,silicone rubber vapor diffusion in saline water distillation, US Patent No.285,032(1963)

Google Scholar

[2] M.E. Findley, Vaporization Through Porous Membranes, lnd. Eng. Chem.Process Des. Dev.6 (1967)226-230

DOI: 10.1021/i260022a013

Google Scholar

[3] J.H. Kim S.S. Kim M.S. Jang,Effects of precursor properties on the preparation of polyethylene hollow fiber membranes by strenching,J.Membr.Sci.318(2008)201-209.

DOI: 10.1016/j.memsci.2008.02.050

Google Scholar

[4] H.Matsuyama ,H.Okafuji, T.Maki,M.Teramoto,N.Kubot,Preparation of polyethylene hollow fiber membrane via thermally induced phase separation,J.Membr.Sci.223(2003)119-126

DOI: 10.1016/s0376-7388(03)00314-4

Google Scholar

[5] S.H. Tabatabaei,P,J.Carreau,A.Ajji,Microporous membranes obtained from polypropylene blend films by stretching,J.Membr.Sci.325(2008)772-782

DOI: 10.1016/j.memsci.2008.09.001

Google Scholar

[6] H.Matsuyama,M.Yuasa,Y.Kitamura,M.Teraoto D.R. Lloyd,Strcuture control of anisotropic and asymmetric polypropylene membrane prepared by thermally induced phase separation,J.Membr.Sci.179(2000)91-100

DOI: 10.1016/s0376-7388(00)00506-8

Google Scholar

[7] X.Y. Tan, S.P. Tan, W.K. Teo,K.Li, polyvinylidene fluoride(PVDF)hollow fiber for ammonia removal from water,J.Membr.Sci.271

DOI: 10.1016/j.memsci.2005.06.057

Google Scholar

[8] K.l.Kurumada, N.Kitamura, M.Fukumoto, M.Oshima, M.Tanigaki, S.l.kanazawa, Structure Generation in PTFE Porous Membranes Induced by the Uniaxial and Biaxial Stretching Operations, J.Membr.Sci.149(1998)51-57

DOI: 10.1016/s0376-7388(98)00179-3

Google Scholar

[9] S.Bandini, C.Gostili, G.C. Sarti, separation efficiency in vacuum membrane distillation, J.Membr.Sci.73(1992)217.

Google Scholar

[10] G.C. Sarti, C.Gostili, S.Bandini, Extraction of organic components from aqueous streams by vacuum membrane distillation,J.Membri.Sci.80(1993)21.

DOI: 10.1016/0376-7388(93)85129-k

Google Scholar

[11] N.Couffin,C.Cabassud,V.Lahoussine-Turcaud,A new process to remove halogenated VOCs for drinking water production:vacuum membrane distillation,Desalination 117(1998)233.

DOI: 10.1016/s0011-9164(98)00103-9

Google Scholar

[12] Zhang kexu, Ning Chen series. metabolic control fermentation. 1998, Beijing: China light industry publishing house.(in Chinese)

Google Scholar

[13] Liao Rong. anion exchange extraction glutamic acid [j]. chemistry research and applications, 2003,15 (4): 564-566(in chinese)

Google Scholar

[14] Chang Xiulian. macroporous NH4+ study on extraction glutamic acid cation-exchange resin by ion exchange [j]. amino acids and bio-capital Source, 1998,20 (3): 17-19(in Chinese)

Google Scholar

[15] Wu Cailian, Guo Changjiang. purification and separation of amino acids by ion exchange [j]. amino acids and bio-resources, 2005,27 (4): 50~53(in Chinese)

Google Scholar

[16] Zhou Tao. study on extraction technology of pollution-free glutamic acid [D]:[master degree thesis]. Jiangsu: Southern Yangtze University environment engineering, 2004(in chinese)

Google Scholar

[17] Wu YongLie. membrane distillation technology and its applications [j]. membrane science and technology, 2003,3 (4): 67-79.(in Chinese)

Google Scholar

[18] Kevin W, Lawson, Douglas R Lloyd. Membrane distillationⅠ.module design and perormance evaluation using vacuummembrane distillation.[J].Journal of Membrane Science,1997,124:1-25.

Google Scholar