双水相萃取菠萝蛋白酶的研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
双水相萃取技术是近年来发展起来的一种新型的生化分离技术,该技术具有生物相容性高,分离条件温和,分离步骤简单,易于放大,且不存在有机溶剂残留等优点。已广泛用于各类酶、核酸、生长激素及各种植物中有效成分的提纯。
     本文首先研究了构造双水相体系的成相组分及不同操作条件对菠萝蛋白酶活性的影响。实验表明,不同分子量的聚乙二醇(PEG)以及在双水相成相浓度范围内PE61000对菠萝蛋白酶活性影响不大;在选定的浓度范围,(NH_4)_2SO_4、阴离子型表面活性剂十二烷基硫酸钠(SDS)和阳离子型表面活性剂十六烷基三甲基溴化铵(CTAB)对菠萝蛋白酶活性无显著影响;菠萝蛋白酶活性适合的温度范围为20℃~50℃;适合的pH范围为4.0~10.0;对于加入一定浓度的金属盐,NaCl和NaBr对菠萝蛋白酶活性影响不大,而加入MgCl_2和CaCl_2明显使菠萝蛋白酶活性降低。
     本文研究菠萝蛋白酶在PEG/(NH_4)_2SO_4双水相体系,阴、阳离子表面活性剂双水相体系和PEG/羟丙基变性淀粉双水相体系中的分配行为及影响菠萝蛋白酶分配的因素。
     在PEG/(NH_4)_2SO_4双水相中研究了PEG分子量、PEG浓度、(NH_4)_2SO_4浓度、NaCl等因素对菠萝蛋白酶在两相中的分配系数、酶活性回收率
    
    的影响。实验结果表明,在以下的实验条件下获得了较高的酶活性回
    收率:PEG平均分子量1 000,浓度17%,(NH4)2504浓度14%,pH为7.0,
    室温的情况下,其分配系数达到3.9,酶活性回收率可达到引%。
     通过实验测定了SDS和CTA日水溶液混合体系双水相的相图,考察
    了温度和外加盐NaBr对双水相形成区域的影响。在构造的阴、阳离子
    表面活性剂双水相双水相体系中,研究了温度、pH等因素对菠萝蛋白
    酶分配行为的影响。在选定的实验条件下,SDS/CTAB/H 20双水相体系
    对菠萝蛋白酶有很好的萃取作用,在成相的两个区间,酶活性回收率
    均可以达到80%以上。
     研究了以木薯淀粉为原料,用环氧丙烷为醚化剂制备轻丙基淀粉
    过程,以轻丙基淀粉的取代度为考察指标,考察了工艺条件和操作条
    件对制备经丙基淀粉过程的影响。用制备的轻丙基淀粉与pEG构造双
    水相体系,测定了该体系的部分相图,并对菠萝蛋白酶在该双水相中
    的分配行为进行了初步研究。在轻丙基淀粉的质量分率为11%,P〔Gl oco
    质量分率为10.5%,NaCI的浓度0.15mol/L的条件下,菠萝蛋白酶
    分配系数为3.23,菠萝蛋白酶活性回收率最高达到71%。
     对三个双水相体系用于菠萝蛋白酶分离的优点及存在的问题进行
    了分析,并提出了解决所存在问题的一些建议。本项目获得广西青年
    科学基金(桂科青01 35029)和广西教育厅科研基金资助。
Aqueous two-phase extraction is a new bioseparation technique developed in recent years. The bioseparation technique has many advantages such as higher biocompatibility, less separation procedures, milder operating condition, easier engineering amplification, less residue of organic solvents in the product and so on. It has been widely used to purify different enzymes, nucleic acids, growth hormone and bioactive component in plants.
    In this experiment, the effects of several factors on bromelain activity were investigated. These factors included the components of aqueous two-phase system and different operating conditions. The experiment results show that the different molecular masses of polyethylene glycol (PEG) and the condition of PEG1000 in the experiment range have little effect to bromelain activity. In the selected concentration range, (NH4)2SO4, anionic surfactant sodium dodecyl sulfonate (SDS) and cationic surfactant cetyl trimethyl amine bromide(CTAB) all have little effect to bromelain activity. The experiment results also show that the suitable temperature range of bromelain activity is from 20C to 50C and the suitable pH value range of reaction is from 4.0 to 10.0. In the range of experiment, NaCl and NaBr have no obviously effect on enzyme activity, but MgCl2 and CaCl2 all inhibited the bromelain activity.
    It was investigated that the distribution behaviour and influence factors on distribution of bromelain in the PEG/(NH4)2SO4, SDS/CTAB, PEG/ hydroxypropyl starch aqueous two-phase systems.
    In the PEG/(NH4)2SO4 aqueous two-phase system, the effects of the PEG
    
    
    
    with different molecular masses, concentrations of PEG, concentrations of (NH4)2SO4i and NaCl on the distribution factor of bromelain in two phase, the volume ratio of the top phase to the bottom phase and the recovery of bromelain were investigated. Under the selected separation conditions, a high recovery of bromelain was obtained from the mixed fluid. The experiment results show that the suitable extraction conditions are 17% PEG1000, 14% (NH4)2SO4, pH 7.0, and the distribution coefficient of K =3.9 and the yield of bromelain can reach 91% at room temperature.
    Through the experiment, the phase diagrams of SDS and CTAB aqueous mixtures were discussed. The influence of temperature and added salt sodium bromide(NaBr) on the aqueous two-phase regions have been observed. Besides, bromelain was extracted under the condition of different temperatures and pH values and added salt. The experiment results show that the yield of bromelain can reach 80% in the system of SDS/CTAB/H2O.
    Finally, the synthetis method of hydroxypropyl starch using maniocca as raw material and the effect of technological conditions on the substitution were investigated. Using the hydroxypropyl starch and PEG construct aqueous two-phase system, the phase diagrams and distribution behaviour of bromelain in this aqueous two-phase system was determined. The experiment results show that the suitable extraction conditions were 11% PEG1000, 10.5% hydroxypropyl starch, pH 7.0, 0.15 mol/L NaCl, and the distribution coefficient of K =3.23 and the yield of bromelain can reach 71% at room temperature.
    In this paper, the advantages and the disadvantages of using three aqueous two-phase systems to extract bromelain were analyzed and some suggests to existing questions were put in forward. The project is subsidized by the Young People Fund of Guangxi Science and Technology Department (No 0135029) and the Scientific Research Fund of Guangxi Education Department.
引文
[1]严希康.生化分离工程.北京:化学工业出版社,2001,(2):169~187
    [2]郭黎平等.双水相萃取技术的研究进展.东北师大学报自然科学版,2000,2(9):34~40
    [3]董军芳,林金清.双水相萃取技术在分离提纯生物物质中的应用.江西化工,2002,(2):3~6
    [4]陆强,邓修.提取与分离天然产物中有效成分的新方法—双水相萃取技术.中成药,2000,(9):653~656
    [5]Albertsson P A. Nature. 1956:177~771
    [6]Metzig C, Grabowska E, Eckert K, et al. Bromelain preteases reduce human platelet aggregation in vitro,adhesion to bovine endothelial cells and thrombus formation in rat vessels in vivo[J]. In Vivo, 1999, (1): 7~15
    [7]林东强,朱自强等.生化分离过程的新探索—双水相分配与相关技术的集成化.化工学报,2000,51(2):1~6
    [8]李伟,朱自强,梅乐和.双水相萃取技术在药物分离和提取中的应用.化工进展,1998,(1):26~29
    [9]Datar R, Rosen C G. J Biotech, 1986, (3): 207~219
    [10]Hart R A, Ogez J R, Builder S E. Bioseparation, 1995, (5): 113~121
    [11]谭天伟等.用双水相萃取分离纯化磷酸甘油酸激酶和磷酸甘油醛脱氢酶.生物工程学报,1996,(12):167~171
    [12]M.C. Almeida. Custinase purification on poly(ethylene glycol)—hydroxypropyl starch aqueous two-phase systems, Journal of Chromatography B, 1998, 711: 151~159
    [13]谭平华,林金清等.双水相萃取技术研究进展及应用.化工生产与技术,2003,10(1):19~24
    [14]J. X. Xiao. G. X.Zhao, Chin. J. Chem, 1994, 12(6): 555
    [15]肖进新,黄建滨等.蛋白质在表面活性剂与高分子共组双水相体系中的分配.化学学报,2000,(7):922~924
    [16]童爱军等.阴阳离子型表面活性剂双水相萃取色氨酸衍生物和牛血清白蛋白.分析化学研究简报,1998,(5):535~537
    
    
    [17]吴瑛.表面活性剂双水相体系及其对某些氨基酸的萃取分离.塔里木农垦大学学报,1998,(6):37~39
    [18]彭华松,宗敏华,梁世中.双水相生物反应体系的研究进展.化学反应工程与工艺,2002,18(2):174~179
    [19]梅乐和,林东强.双水相分配结合温度诱导相分离从酵母中提取谷胱甘肽.[J]化工学报,1998(4):470~474
    [20]李勉,朱自强,梅乐和.聚合物/聚合物双水相系统相平衡计算.化学工程,1996,(2):60~65
    [21]朱自强,关怡新,李勉.双水相系统在抗生素提取和合成中的应用.化工学报,2001,(12):1039~1048
    [22]陈莉,叶汝强,刘洪来.正、负离子表面活性剂混合溶液的胶束性质.华东理工大学学报,2002,28(3):278~232
    [23]朱自强,关怡新等.双水相分配技术提取生物小分子的进展.国内外新技术,1996,(4):29~36
    [24]秦德华.用双水相萃取丙酰螺旋梅素的研究.中国抗生素杂志,1998,23(2):144~147
    [25]Modlin R F, Aired P A, Tjemeld E J. Chromatogr. A, 1994, 66(8): 229~236
    [26]Li M, Zhu Z Q, Mei L H. Biotecnol. Prog, 1997, 13(1): 105~108
    [27]李伟.浙江大学学位论文.1998
    [28]Hustedt H, Kroner K H, Papamichael N. Process Biochem, 1988, (23): 129~137
    [29]Cunha T, Ares-Barros R. In: Kaul R, ed. Aqueous Two-phase Systems Methods and Protocols. Totowa: Humana press, 2000:391~409
    [30]Jafarabad K R, Sawant S.B, Joshi J B, Sikdar S K. Chem. Eng. Sci, 1992, 47(1): 57~68
    [31]成坚.双水相体系萃取分离技术及其在生物技术中的应用.仲恺农业技术学院学报,2000,13(2):52~58
    [32]Harris P A, Karlstrom G, Tjemeld F. Bioseparation, 1992, (1): 237~246
    [33]Alred P A, T jerneld F, Kozlowski A, Harris J M. Bioseparation, 1993, (2): 363-373
    [34]Kamihira M, Kaul R, Mattiasson B. Biotechnol. Biotechnol, 1992, 40:1381~1387
    [35]Josefine Persson, Anita Kaul, Polymer recycling in aqueous two—phase extractions using thermoseparating ethylene oxide—propylene oxide copolymers, Journal of
    
    Chromatography B, 743(2000): 115~126
    [36]Mos van Berlo, Karel Ch.A.M. Luyben, Luuk A.M. van der Wielen, Poly(ethylene glycol)—salt aqueous two phase systems with easily recyclable volatile salts, Jounal of Chromatography B,711 (1998): 61~68
    [37]王志华,马会民,马泉莉等.双水相萃取体系的研究.应用化学,2001,18(3):173~175
    [38]吴显荣.菠萝蛋白酶.热带作物科技,1996,(2):64~65
    [39]章佩芬,陈敏华,郭利平.菠萝蛋白酶应用的性质研究.广州食品工业科技,2002,18(2):16~17
    [40]章佩芬,郭勇,罗焕敏.菠萝蛋白酶的研究与应用进展.中华西药学杂志,2002,17(2):128~129
    [41]Vanhoof, Greet, Cooreman, et al. Bromelain[J]. Drugs Pharm Sci,1997:84~131
    [42]王平诸.提取菠萝蛋白酶工艺.食品与机械,1997,(2):31~32
    [43]王平诸,孙军社.菠萝蛋白酶的三种生产工艺比较.河南化工,2002,(7):1~3
    [44]Eckert K, Grabowska E, Stange R, et al. Effects of oral bromelain administration on the impaired immunocytotoxicity of mononuclear cells from mammary tumor patients [J]. Oncol Re, 1999, (6): 1191~1199
    [45]M. Lauwereys, P. De Geus, J. De Meutter, P. Stanssens and G. Matthyssens, in L. Alberghina, R.D. Schmid and R. Verger, Lipases; Structure, Mechanism and Genetic Engineering, Marcel Dekker, New york, 1990, Ch. 10, pp:243~251
    [46]关岳.双水相系统.科学前沿,1996,48(1):30~33
    [47]刘会洲,陈家镛.过程工业中重要分离技术的新进展.化工学报,2000,(s):29~34
    [48]周晓云,傅美景.双水相体系提取脂肪酶的研究.浙江农业大学学报,1997,23(2):205~210
    [49]Josefine Persson, Anita Kaul, Folke Tjemeld. Journal of Chromatography B, 2000, 743: 115~126
    [50]J.G. Huddleston, H.D. Willauer, S.T Griffin, R.D. Rogers, Ind. Eng. Chem. Res. 1999, 38:2523
    [51]Josefine Persson, Purification of protein and recycling in a new aqueous two—phase using thermoseparating polymers, Journal of Chromatography A, 1999, 864:31~48