扩散渗析法回收精氨酸生产过程中的盐酸
作者:李传润12,王虎传1,张旭2,陶振1,华伟1,杨伟华2,徐铜文2
单位: 1.安徽中医学院 药学院,合肥 230031;2. 中国科学技术大学 化学与材料科学学院 功能膜研究室,合肥 230026
关键词: 酸回收;扩散渗析;膜;精氨酸
出版年,卷(期):页码: 2012,32(4):102-106

摘要:
为了解决精氨酸生产过程中的无机酸回收和循环再利用问题,本文采用阴膜扩散渗析法,针对模拟的精氨酸和盐酸混合液,在静态扩散条件下测定了盐酸的渗析系数,并考察了动态扩散渗析操作参数如流速、流速比对酸回收率的影响。结果表明,采用DF-120阴离子交换膜,在静态扩散渗析中,盐酸能够顺利地透过膜,精氨酸几乎不能透过;动态扩散实验中流速、流速比对酸的回收率和回收酸的浓度有重要影响,随着流速的增加,盐酸的回收率逐渐降低,精氨酸的截留率基本上没有改变,均达到98.5%以上。流速为2mL/min时,盐酸回收率最高,可达82%,水/料液流速比增大时,盐酸的回收率增大,但是过高的水/料液流速比又会使回收酸的浓度降低。经济核算表明,对于一个年产30吨精氨酸的企业,相对于中和法,膜扩散渗析法一年能节省的化学原料总费用约98万元,投资回收期为8个月。
 Diffusion dialysis with DF-120 anion exchange membrane was adopted to achieve the objective of waste hydrochloric acid recycling and reusing during the Arginine (Arg) production process. The experiment was performed in a series of static and dynamic tests with a mixed Arginine and HCl industrial simulated waste acid. The diffusion dialysis coefficient of HCl across the chosen DF-120 anion exchange was measured in the static test, while some operation parameters such as flow rate and flow rate ratio on the performance of the diffusion dialysis process were investigated in the dynamic test. Results from the static experiment indicated that HCl could transport across the membrane while Arg was completely rejected and it could not be detected in the diffusate solution. Dynamic experimental results showed that the performance of the diffusion dialysis process was declined with an increase of flow rate, while the performance was enhanced with an increase of flow rate ratio. A high Arg rejection ratio of about 98.5% could be obtained and there was no obviously change of this ratio during the recovery process. The concentration of HCl in the diffusate and dialysate were decreased with an increase of water flow rate. A maximum HCl recovery ratio of about 82% could be achieved at a flow rate of 2 mL/min. A preliminary economic evaluation indicated that a 30 t/a Arg produced company could save ¥98000 per year compared with the conventional neutralization method for spent hydrochloric acid. The diffusion dialysis system also revealed that the investment-recovered period was short as about 8 months.
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参考文献:
[1] M.B.Esteban, A.J.Garcia, P.Ramos, et al . Sub-critical water hydrolysis of hog hair for amino acid production. [J]. Bioresource Technology, 2010, 101(7): 2472-2476.
[2] 冷亮. 一种精氨酸的制备方法 [P]. 中国,200510045464.5. 2006-05-24.
[3] 尹刚明,李冰,唐德松,等. 从头发中提取L-精氨酸的研究. [J]. 现代食品科技,2008,24(9):921-923.
[4] T.W. Xu, W.H. Yang. Sulfuric acid recovery from titanium white (pigment) waste liquor using diffusion dialysis with a new series of anion exchange membranes - static runs. [J]. Journal of Membrane Science, 2001, 183(2): 193-200.
[5] Z. Palaty, A. Zakova. Separation of H2SO4+ZnSO4 mixture by diffusion dialysis. [J]. Desalination, 2004, 169(3): 277-285.
[6] M. Hichour, F. Persin, J. Molenat, et al. Fluoride removal from diluted solutions by Donnan dialysis with anion-exchange membranes. [J]. Desalination, 1999, 122(1): 53-62.
[7] S.H. Lin, M.C. Lo. Recovery of sulfuric acid from waste aluminum surface processing solution by diffusion dialysis. [J]. Journal of Hazardous Materials, 1998, 60(3): 247-257.
[8] J. Jeong, M-S. Kim, B-S. Kim, et al. Recovery of H2SO4 from waste acid solution by a diffusion dialysis method. [J]. Journal of Hazardous Materials, 2005, 124(1-3): 230-235.
[9] Z. Palaty, A. Zakova. Transport of nitric acid through the anion-exchange membrane NEOSEPTA-AFN. [J]. Desalination, 2004, 160(1): 51-66.
[10] T.W. Xu, W.H. Yang. Industrial recovery of mixed acid (HF+HNO3) from the titanium spent leaching solutions by diffusion dialysis with a new series of anion exchange membranes. [J]. Journal of Membrane Science,2003, 220(1-2): 89-95.
[11] J.Y. Luo, C.M. Wu, Y.H. Wu, et al. Diffusion dialysis of hydrochloride acid at different temperatures using PPO-SiO2 hybrid anion exchange membranes. [J]. Journal of Membrane Science, 2010, 347: 240-249.
[12] P.S. Francis, N.W. Barnett, R.C. Foitzik, et al. Chemiluminescence from the Sakaguchi reaction. [J]. Analytical Biochemistry, 2004, 329(2): 340-341.

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