乙醇-磷酸氢二钾双水相体系萃取L-精氨酸

采用乙醇-磷酸氢二钾(K2HPO4)双水相体系萃取L-精氨酸。实验考察了乙醇浓度、K2HPO4浓度、pH、萃取温度对萃取分离L-精氨酸的影响。结果表明,L-精氨酸在该双水相体系的分配系数K随体系乙醇浓度、K2HPO4浓度的增大、萃取温度的升高而增大,随着体系pH的增大而减小;L-精氨酸在该双水相体系的萃取率随体系乙醇浓度和pH的增大而减小,随着体系K2HPO4浓度增大、萃取温度的升高而增大。     

反胶束萃取技术分离胰激肽原酶

研究了用十六烷基三甲基溴化铵（CTAB）/正己醇/正辛烷反胶束溶液萃取和反萃取商业用胰激肽原酶时,水相pH值、离子强度和种类、CTAB浓度和助表面活性剂浓度等因素对分离效率的影响,并从反胶束微观结构给予解释。结果表明：［CTAB］＝0.02 mol•L-1,正己醇／正辛烷(V/V)＝1：5,萃取pH＝9.0,反萃pH＝7.0,萃取［KBr］＝0.1 mol•L-1,反萃［KBr］＝1.5 mol•L-1,反萃取加15％乙醇(V/V)时,萃取率接近100%,反萃取活性回收得率在80%以上。商业用酶的纯化倍数最高为1.97倍,粗酶为7.15倍,且粗酶纯化后比活在200U／mg以上,电泳分析证实了纯化效果,显示了很好的工业前景。     

微生物转谷氨酰胺酶(MTGase)的AOT反胶束纯化研究

研究微生物转谷氨酰胺酶(MTGase)反胶束纯化的工艺和条件,调节MTGase离心上清液等电点,除去部分杂蛋白,MTGase活力升高7.5倍;用截留分子量为10000的超滤膜除去小分子杂蛋白,MTGase活力升高1.33倍;用0.05mol/L的AOT/异辛烷反胶束进一步纯化MTGase,其最适萃取条件是粗MTGase蛋白质浓度20mg/mL,[Na ]0.12mol/L,水相pH4.80～5.20,相比1:1(v/v);荷载MTGase的AOT反胶束用2.0mol/LKCl进行反萃取,MTGase活力为14.2U/g,纯化8.875倍;冷冻干燥脱盐反萃取液,获得MTGase冻干粉,其活力为110.3U/g,与粗酶液相比较,纯化689.4倍。经过AOT/异辛烷反胶束萃取纯化的MTGase,其SDS-聚丙烯酰胺凝胶电泳为一条带。Ca2 与表面活性剂非极性尾上丁二酰羰基氧、极性头磺酸基硫氧基氧及MTGase分子表面具有孤电子对的基团的配位结合放大了AOT反胶束的另一种萃取作用——配位萃取,致使其对MTGase的萃取率高于K 而接近Na 。     

生姜蛋白酶提取及反胶束纯化工艺初步研究

本文研究了生姜中生姜蛋白酶的分布及贮藏中的活力变化 ,研究了从新鲜生姜中提取生姜粗蛋白酶及用AOT 异辛烷和CTAB庚烷 /辛醇反胶束萃取该酶的工艺和方法。实验结果指出 :在贮藏茎中生姜蛋白酶的活力为 2 .7μg/mL·min-1,在膨大茎中该酶活力为 0 .6 8μg/mL·min-1,而在幼嫩茎中活力最低 ,仅为0 .4 8μg/mL·min-1。新鲜生姜在 0℃下贮藏 2 4h即完全丧失活力 ,在室温下贮藏 3d后其活力损失达38 2 5 %。用 10倍 0 .2mol/L、pH =6 .0的磷酸缓冲液 (4℃ )三次提取生姜蛋白酶 ,其提取率分别为 6 4 .75 %、14 .2 8%和 5 .2 %。用 6 5 %饱和度的 (NH4) 2 SO4沉淀提取液中的生姜蛋白酶 ,再以 pH 6 .2、0 .1mol/L的柠檬酸缓冲液溶解 ,其比活力达到 4 .2 1(μgPro/ μgPro·min-1)。生姜蛋白酶的 pI =5 .4～ 5 .5 ,在pH 5 .4以上 ,用AOT 异辛烷反胶束不能萃取出生姜蛋白酶 ,但却可以萃取出 71.86 %的杂蛋白。用CTAB庚烷 /辛醇反胶束二次萃取AOT 异辛烷萃余液 ,其蛋白质萃取率为 6 0 .2 5 % ,萃取液中生姜蛋白酶理论比活力达到 4 9.77(μgPro/ μgPro·min-1)。     

发酵液中多拉菌素的提取和萃取条件研究

采用单因素实验,分别研究提取试剂、发酵液放置时间、pH值和温度对发酵液中多拉菌素提取效果的影响;然后以乙酸乙酯为萃取试剂,研究萃取次数及萃取体积对多拉菌素萃取效果的影响。结果显示,甲醇为最佳提取试剂;发酵液在pH为3～11、温度为20～80℃的条件下放置144 h,多拉菌素均能稳定存在,提取得到的多拉菌素的质量浓度没有显著变化;浓缩提取液液经2倍体积乙酸乙酯萃取2次即可。该条件下多拉菌素的质量浓度和萃取率分别为151.78μg/mL和98.00%。     

Mg~(2 )对巯基修饰类囊体膜H~ -ATP酶的质子传导途径的调节效应

镁离子为巯基修饰类囊体还原型H~ -ATP酶光活化所必需。介质中MgCl_2浓度由2mmol/L增加到10mmol/L时,解联剂NH_4Cl对H~ -ATP酶光活化的抑制作用明显减弱,而对跨膜⊿pH的消除效应并未减轻。介质中Mg~(2 )浓度的增加不影响DCMU对H~ -ATP酶光活化的抑制作用。 介质中含40μmol/LADP时,低浓度NH_4Cl对H~ -ATP酶催化的刺激效应被消除,仅呈现抑制作用。这种NH_4Cl对H~ -ATP酶催化活性的抑制作用随着反应介质中Mg~(2 )浓度的增加而降低,因此认为Mg~(2 )参与质子传导途径的调节。     

植物细胞表面蛋白的研究——Ⅱ.烟草细胞表面蛋白束缚二价金属离子的能力

烟草细胞表面蛋白(TCSP)能溶于稀碱(0.1NNaOH)溶液,微溶于中性盐溶液,但难溶于二价金属盐溶液中。在中性盐溶液中,pH(2—9)对其溶解度无多大影响。用乙醇和丙酮分级沉淀时,90%乙醇的得率只有58%左右,而同样浓度丙酮的得率可达70%以上。在有Mg~( )离子存在的条件下TCSP 特征光谱由270毫微米向长波方向漂移20毫微米,并在波长230毫微米处出现一个新的吸收峰。用ANS 探测结果表明,在添加Ca~( )或Mg~( )离子后,TCSP暴露的疏水链区减少。以SDS 增溶的TCSP对Mg~( )离子进行透析时,解聚的TCSP 发生重新聚合,电泳淌度也有改变。用Mg~( )离子滴定SDS 增溶的TCSP 溶液时,pH变化曲线不同于SDS 的滴定曲线。在不同离子环境中透析以降低SDS 浓度,即可形成TCSP 的聚合体,并具有不同形状。这些结果表明:TCSP 有束缚二价金属离子的能力。     

白地霉脂肪酶的双水相萃取和反胶团提取

对影响双水相萃取和反胶团提取脂肪酶的各种因素进行了探讨,并通过正交实验进一步优化提取条件,PEG浓度15%,(NH4)2SO4浓度22.5%,pH8.0的条件下进行双水相萃取,脂肪酶纯化倍数达到7.5倍;CTAB浓度150mmol/L,相体积比4/2,水相pH8.0,温度40℃的条件下进行反胶团提取,脂肪酶的比活力达到最大,但其比活力稍有下降,约为原来的0.9倍。     

氯化三辛基甲胺/氯仿/正丁醇反胶束萃取地木耳多糖

采用阳离子表面活性剂氯化三辛基甲胺(TOMAC)/氯仿/正丁醇反胶束体系萃取地木耳中的多糖。分析有机溶剂氯仿与助表面活性剂正丁醇比例、TOMAC浓度、多糖粗提液浓度、促溶剂盐酸胍浓度、盐离子种类和浓度对前萃取率的影响。结果表明:向0.5 mg/m L多糖粗提液中加入10 mmol/L盐酸胍(Gu HCl)和0.06 mol/L Na Cl,与等体积25 mmol/L TOMAC/氯仿-正丁醇(V∶V=3∶1)的反胶束体系混合,地木耳多糖前萃取率为53.21%;反萃时水相中Na Cl浓度为0.14 mol/L,盐酸胍浓度浓度为0.6 mol/L,在此条件下地木耳多糖反萃取率为93.2%。     

Mg~(2+)离子对紫膜表面电位效应的自旋探针—ESR研究

本文根据带正电荷自旋探针CAT_(12)在紫膜结合相和水相的分布,利用自旋探针顺磁共振(ESR)技术测定了Mg~(2+)对紫膜表面电位的影响,我们的结果表明紫膜具有σ为3.02×10~(-4)Ch-arges/(?)~2的表面电荷密度.据此σ用Gouy-Chapman理论计算得到Mg~(2+)离子浓度与表面电位((?)_i)的关系与实验结果极为一致,这表明离子通过表面电位的变化引起紫膜的表面pH值的改变从而影响紫膜的结构与功能,Mg~(2+)对紫膜表面电位的影响明显地比K~+要大,说明镁离子可能在紫膜的结构与功能中有更为重要的作用.     

Solubilizing water involved in protein extraction using reversed micelles

The extraction of protein using reversed micelles was investigated in relation to the amount of solubilizing water in the reversed micellar organic phase. The minimal concentration of amphiphilic molecule di-2-ethylhexyl sodium sulfosuccinate (C(20)H(37)O(7)Na) (AOT) required for 100% cytochrome c extraction was recognized. This critical AOT concentration increased with protein concentration in the aqueous phase. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein was found to be a constant of 3500 under C(KCI) = 1.0 x 10(2) mol . m(-3) in this system. This ratio means the hydrophillic surroundings required for extracting one protein molecule into the micellar organic phase under the suitable pH and salt concentration for the forward extraction. In this regard, AOT molecules seemed to take the part of water solubilizing agent in the reversed micellar extraction. This role of AOT is important to extract protein under the suitable pH and salt concentration. The amount of solubilizing water in the protein-containing system was larger than in the protein-free system. This difference shows that the water molecules accompany the extracted protein into the reversed micellar organic phase at constant ratio 2200 under C(KCI) = 1.0 x 10(2) mol . m(-3), i.e., accompanying water molecules per one extracted protein. The minimal AOT concentration increased with ionic strength. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein also increased with ionic strength, so that in higher ionic strength, more solubilizing water was required. Then more AOT was required to provide the hydrophillic surroundings for protein. The pH affected the minimal AOT concentration required for 100% protein extraction.     

Study of the factors affecting the extraction of soybean protein by reverse micelles

In this work, the forward and back extraction of soybean protein by reverse micelles was studied. The reverse micellar systems were formed by anionic surfactant sodium bis(2-ethyl hexyl) sulfosuccinate (AOT), isooctane and KCl solution. The effects of AOT concentration, aqueous pH, KCl concentration and phase volume ratio on the extraction efficiency of soybean protein were tested. Suitability of reverse micelles of AOT and Triton-X-100/AOT mixture in organic solvent toluene for soybean protein extraction was also investigated. The experimental results lead to complete forward extraction at the AOT concentration 120 mmol l⁻¹, aqueous pH 5.5 and KCl concentration 0.8 mol l⁻¹. The backward extraction with aqueous phase (pH 5.5) resulted in 100% extraction of soybean protein from the organic phase.     

Downstream processing of soy hull peroxidase employing reverse micellar extraction

Phase transfer studies were conducted to evaluate the solubilization of soy hull peroxidase (SHP) in reverse micelles formed in isooctane/butanol/hexanol using the cationic surfactant cetyltrimethylammonium bromide (CTAB). The effect of various parameters such as pH, ionic strength, surfactant concentration of the initial aqueous phase for forward extraction and buffer pH, type and concentration of salt, concentration of isopropyl alcohol and volume ratio for back extraction was studied to improve the efficiency of reverse micellar extraction. The active SHP was recovered after a complete cycle of forward and back extraction. A forward extraction efficiency of 100%, back extraction efficiency of 36%, overall activity recovery of 90% and purification fold of 4.72 were obtained under optimised conditions. Anionic surfactant sodium bis (2-ethylhexyl) sulfosuccinate (AOT) did not yield good results under the conditions studied. The phase transfer of soy hull peroxidase was found to be controlled by electrostatic and hydrophobic interactions during forward and back extraction respectively.     

Extraction of monoclonal antibodies (IgG1) using anionic and anionic/nonionic reverse micelles

Purification schemes for antibody production based on affinity chromatography are trying to keep pace with increases in cell culture expression levels and many current research initiatives are focused on finding alternatives to chromatography for the purification of Monoclonal antibodies (MAbs). In this article, we have investigated an alternative separation technique based on liquid–liquid extraction called the reverse micellar extraction. We extracted MAb (IgG1) using reverse micelles of an anionic surfactant, sodium bis 2‐ethyl‐hexyl sulfosuccinate (AOT) and a combination of anionic (AOT) and nonionic surfactants (Brij‐30, Tween‐85, Span‐85) using isooctane as the solvent system. The extraction efficiency of IgG1 was studied by varying parameters, such as pH of the aqueous phase, cation concentration, and type and surfactant concentration. Using the AOT/Isooctane reverse micellar system, we could achieve good overall extraction of IgG1 (between 80 and 90%), but only 30% of the bioactivity of IgG1 could be recovered at the end of the extraction by using its binding to affinity chromatography columns as a surrogate measure of activity. As anionic surfactants were suspected as being one of the reasons for the reduced activity, we decided to combine a nonionic surfactant with an anionic surfactant and then study its effect on the extraction efficiency and bioactivity. The best results were obtained using an AOT/Brij‐30/Isooctane reverse micellar system, which gave an overall extraction above 90 and 59% overall activity recovery. An AOT/Tween‐85/Isooctane reverse micellar system gave an overall extraction of between 75 and 80% and overall activity recovery of around 40–45%. The results showed that the activity recovery of IgG1 can be significantly enhanced using different surfactant combination systems, and if the recovery of IgG1 can be further enhanced, the technique shows considerable promise for the downstream purification of MAbs. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

荔枝果皮花色苷提取及稳定性研究

通过对荔枝果皮花色苷提取方法的比较,认为盐酸甲醇为最适提取剂,提取的色素液对光照和温度均较稳定,而pH值显著影响花色苷的稳定性。     

Application of reverse micelle extraction process for amylase recovery using response surface methodology

The effect of different process variables of reverse micelle extraction process like pH, addition of surfactant (AOT) concentration and potassium chloride (KCl) concentration on amylase recovery has been studied and analysed. Solid-state fermentation was used for the production of amylase enzyme. Response surface methodology (RSM) using central composite rotatable design (CCRD) was employed to analyse and optimize the enzyme extraction process. The regression analysis indicates that the effect of AOT concentration, and KCl concentration were significant, whereas the effect of pH was non-significant on enzyme recovery. For the maximum recovery of enzyme, the optimum operating condition for pH, AOT concentration (M) and KCl concentration were 10.43, 0.05 and 1.00, respectively. Under these optimal conditions, the enzyme recovery was 83.16%.     

超声波协同复合酶法提取姬松茸多糖

研究了超声波协同复合酶法提取姬松茸多糖的最佳工艺条件。采用均匀设计法分别考察不同时间、pH值、温度、酶浓度、固液比对纤维素酶、果胶酶以及木瓜蛋白酶酶解反应的影响,并研究三种酶联合使用时的加酶方式以及超声波协同提取时的最佳条件。结果表明,超声波协同复合酶法可显著提高姬松茸多糖的提取率,其最佳提取条件为：超声波作用20min,分步加酶法（先加果胶酶：pH值3．8、温度50℃、时间90min、加酶量7000U／g、固液比1：45;然后加纤维素酶：pH值3．6、温度75℃、时间120min、加酶量150U／g、固液比1：45;最后加木瓜蛋白酶：pH值3．6、温度75℃、时间120min、加酶量20000U／g、固液比1：45）,多糖提取率达到14．51％。     

Extraction of bovine serum albumin using nanoparticulate reverse micelles

The extraction of a relatively large molecular weight protein, bovine serum albumin (BSA), using nano-sized reverse micelles of nonionic surfactant polyoxyethylene p-t-octylphenol (Triton-X-100) is attempted for the first time. Suitability of reverse micelles of anionic surfactant sodium bis (2-ethyl hexyl) sulfosuccinate (AOT) and Triton-X-100/AOT mixture in organic solvent toluene for BSA extraction is also investigated. Although, the size of the Triton-X-100 reverse micelle in toluene is large enough to host BSA molecule in the hydraulic core, the overall extraction efficiency is found to be low, which may be due to lack of strong driving force. AOT/toluene system resulted in complete forward extraction at aqueous pH 5.5 and a surfactant concentration of 160 mM. The back extraction with aqueous phase (pH 5.5) resulted in 100% extraction of BSA from the organic phase. The addition of Triton-X-100 to AOT reduced the extraction efficiency of AOT reverse micelles, which may be attributed to reduced hydrophobic interaction. The circular dichroism (CD) spectrum of BSA extracted using AOT/toluene reverse micelles indicated the structural stability of the protein extracted.     

Channel formation properties of black widow venom

Black widow venom in the concentration 1--10 mkg/ml added on one side of the bilayer of common bovine brain phospholipids induces the formation of conductivity channels with high cation-anion selectivity with the number of cation transfer for K+, Ca2+, Sr2+, Mg2+, Na+, Cs+, Li+ equaling 0.98, 0.97, 0.96, 0.94. 0.88. 0.82, 0.82 correspondingly (at pH = 7.5). At pH less than 3.5 the channels are slightly selective for anions (the number of cation transfer 0.4). Potential-dependence of the channels is found, which is explained by microstructural reconstruction of their protein complex.