双相(O/W)识别手性萃取分离α-环己基扁桃酸对映体

提出一种新的手性分离技术双相(O/W)识别手性萃取. 研究了α-环己基扁桃酸对映体在D(L)-酒石酸异丁酯1,2-二氯乙烷有机相和β-环糊精衍生物水相萃取体系中的分配行为; 考察了β-环糊精衍生物种类和浓度、酒石酸酯构型和浓度、水相pH 值等因素对萃取性能的影响. 实验结果表明, 双相(O/W)识别手性萃取具有很强的手性分离能力, 羟丙基β-环糊精、羟乙基β-环糊精、甲基β-环糊精均对S-α-环己基扁桃酸对映体的识别能力大于对R-α-环己基扁桃酸对映体的识别能力, 其中以羟丙基β-环糊精的识别能力最强; 而D-酒石酸异丁酯的识别能力刚好相反; 在羟丙基β-环糊精和D-酒石酸异丁酯萃取体系中, α-环己基扁桃酸外消旋体一次萃取分离后, 水相中S-对映体e.e.%达到27.6%, R-和S-对映体的分配系数(k_R和k_S)分别为2.44和0.98, 分离因子(α)达2.49; 同时pH值和萃取剂浓度对手性分离能力有显著影响. 双相(O/W)识别手性萃取对外消旋体化合物的制备性分离有着十分重要的意义.     

醇/盐双水相体系中α-环己基扁桃酸手性分子识别

以含羟丙基-β-环糊精（HP-β-CD）手性识别剂的醇/盐双水相体系作为一种新型的手性识别萃取体系,研究了α-环己基扁桃酸(CHMA)对映体在其中的手性识别行为.详细考察了HP-β-CD浓度、CHMA浓度、乙醇和硫酸铵质量分数、体系温度和pH值等因素对CHMA对映体分配比（D）和分离因子(α)的影响.结果显示,含有手性识别剂HP-β-CD的乙醇∕硫酸铵双水相体系对CHMA对映体具有很强的手性识别能力;体系中HP-β-CD浓度、乙醇质量分数、温度和pH值等因素对对映体的分离度影响较大;在体系温度为40 ℃,pH值为2,乙醇质量分数为30%,硫酸铵质量分数为15%,HP-β-CD的浓度为50 g.L-1,CHMA浓度为0.5 mmol.L-1时,手性识别分离效果最佳,分离因子（α）达到了1.86.     

氰基柱上手性流动相添加剂法拆分4-氯扁桃酸

用羟丙基-β-环糊精(HP-β-CD)作为手性流动相添加剂,在UFCN(220×4.6 mm×5μm)氰基柱上通过反相高效液相色谱实现了4-氯扁桃酸(4-Cl MA)对映体的拆分。考察了水相HP-β-CD浓度,NaH_2PO_4浓度,p H,流动相中甲醇的比例及柱温等因素对分离度的影响。确定的最优色谱条件为:水相(5 mmol/L HP-β-CD,8 mmol/L NaH_2PO_4,p H 2.8),V水相/V甲醇=95:5,柱温25℃,流速1 m L/min。此条件下4-Cl M A对映体的分离度可达1.80。同时在此色谱条件下考察了3-氯扁桃酸(3-Cl MA),2-氯扁桃酸(2-Cl MA)与扁桃酸(MA)对映体的色谱拆分结果。结果发现在此条件下,3-Cl M A对映体分离度为1.51,而2-Cl M A与M A完全没有分开。对方法进行了验证,(S),(R)-4-Cl MA两对映体低、中、高浓度日内和日间精密度的RSD均小于1.1%;(S),(R)-4-Cl M A两对映体回收率分别为101.0%和100.6%;(S),(R)-4-Cl M A两对映体检出限与定量限分别为0.028,0.030 mg/L与0.093,0.098 mg/L。     

聚丙二醇-硫酸铵双水相萃取银杏黄酮

研究了银杏叶黄酮在聚丙二醇(PPG)400-(NH_4)_2SO_4双水相体系中的分配情况。探讨了单因素p H、PPG400质量分数、(NH_4)_2SO_4质量分数、料液比、温度、萃取时间对萃取率(Y%)和分配系数(K)的影响,并通过正交试验进一步优化双水相萃取条件。结果表明,各个因素对Y%和K影响为PPG400质量分数pH(NH_4)_2SO_4质量分数萃取时间萃取温度料液比。最佳萃取条件为p H 6、PPG400质量分数25%、(NH_4)_2SO_4质量分数15%、料液比1∶15、萃取温度40℃、萃取时间60min,黄酮萃取率达到98%以上。PPG400-(NH_4)_2SO_4双水相体系对银杏叶黄酮有较好的萃取效果。     

扁桃酸甲酯对映体的毛细管电泳手性拆分

采用β-环糊精及其衍生物作为手性选择剂，对扁桃酸甲酯对映体进行毛细管电泳分离，考察了不同环糊精种类和浓度、背景电解质类型及pH对分离效果的影响；实验结果表明，pH6．0、50g／L磺酸化环糊精(Su-β-CD)、20mmol/L Tris的磷酸缓冲液，可以使扁桃酸甲酯对映体得到基线分离。     

手性流动相HPLC法拆分萘普生对映体的研究

将β-环糊精、甲基-β-环糊精、羟丙基-β-环糊精、L-脯氨酸作为手性流动相添加剂,系统地研究了D,L-萘普生在RP-HPLC系统中的拆分.分别考察了手性流动相的种类,手性试剂羟丙基-β-环糊精的浓度,流动相的pH值,修饰剂的种类及浓度,三乙胺浓度和柱温等对拆分效果的影响,以HP-β-CD为手性流动相添加剂,建立了HP-β-CD手性流动相分离萘普生对映体的方法.结果表明：当流动相为25 mol/L HP-β-CD、体积分数15%乙醇、体积分数0.5%三乙胺、pH3.5、柱温t25℃、流速V=1 mL/min时萘普生对映体得到了良好的基线分离,分离因子α可达1.29.     

二(2-乙基己基)磷酸与酒石酸衍生物复合萃取拆分扁桃酸外消旋体

本文研究了扁桃酸对映体在含二(2-乙基己基)磷酸(D2EHPA)与酒石酸衍生物复合手性选择剂的正辛醇-水两相体系中的萃取分配行为,考察了酒石酸衍生物的种类和初始浓度、D2EHPA的初始浓度、扁桃酸的初始浓度、萃取温度对分配系数和分离因子的影响.结果显示,复合手性选择剂能提高分配系数和分离因子,D2EHPA与D-酒石酸衍生物的复合手性选择剂与L-扁桃酸对映体比与D-扁桃酸对映体形成更稳定的非对映体复合物;且D2EHPA与二对甲基苯甲酰酒石酸(DTTA)的复合手性选择剂的手性选择性大于D2EHPA与二苯甲酰酒石酸(DBTA)的复合手性选择剂;同时,扁桃酸的初始浓度、萃取温度对分配系数和分离因子的影响较大.     

固相萃取-毛细管电泳法测定免血清中的山茛菪碱对映体

建立一种可用于定量的毛细管电泳法分离山莨菪碱对映体.系统研究了三种手性选择剂:羟丙基-β-环糊精(HP-β-CD),甲基-β-环糊精(Me-β-CD),羧甲基-β-环糊精(CM-β-CD)及其浓度、缓冲溶液浓度和pH对山莨菪碱拆分的影响.在110 mmol/L Tris-H3PO4缓冲液中加入20.0 mg/mL HP-β-CD和5.0 mg/mL CM-β-CD(pH 4.0)条件下,山莨菪碱的4个对映体达到基线分离.血清样品通过崮相萃取预处理和浓缩,对映体的固相萃取回收率在82.9%～90.7%,相对标准偏差RSD%均小于7%.山莨菪碱的4个对映体血标准溶液浓度与电泳峰面积在77.86～0.39μg/mL范围内呈良好的线,r≥0.999,检出限(S/N=3)为0.08 μg/mL.平均日内和日间精密度(RSD%)分别小于4.2%和6.5%,方法回收率为95.1%和105%.建立的方法准确、可靠,应用于监测兔连续3 d口服75 mg山莨菪碱后血清中山莨菪碱的血药浓度,结果满意.     

固相萃取-毛细管电泳法测定兔血清中的山莨菪碱对映体

建立一种可用于定量的毛细管电泳法分离山莨菪碱对映体. 系统研究了三种手性选择剂: 羟丙基-β-环糊精 (HP-β-CD), 甲基-β-环糊精 (Me-β-CD), 羧甲基-β-环糊精(CM-β-CD) 及其浓度、缓冲溶液浓度和 pH 对山莨菪碱拆分的影响. 在110 mmol/L Tris-H3PO4缓冲液中加入20.0 mg/mL HP-β-CD和5.0 mg/mL CM-β-CD (pH 4.0)条件下, 山莨菪碱的4个对映体达到基线分离. 血清样品通过固相萃取预处理和浓缩, 对映体的固相萃取回收率在82.9%～90.7%, 相对标准偏差RSD%均小于7 %. 山莨菪碱的4个对映体血标准溶液浓度与电泳峰面积在77.86～0.39 μg/mL范围内呈良好的线性, r≥0.999, 检出限(S/N＝3)为0.08 μg/mL. 平均日间和日内精密度(RSD% )分别小于6.1% 和4.8%, 方法回收率为97.4% 和105.4%. 建立的方法准确、可靠, 应用于监测兔连续3 d口服75 mg 山莨菪碱后血清中山莨菪碱的血药浓度, 结果满意.     

聚合-β-环糊精作手性选择剂的毛细管电泳法分离4种光学活性农药中间体

以聚合-β-环糊精作为毛细管区带电泳手性选择剂,成功分离了2-苯氧丙酸(PPA)、顺式-功夫菊酸(cis-PA)、1-苯基-2-(对甲苯基)乙胺(PTE)和1-苯基-2-(对甲氧基苯基)乙胺(PME)4种光学活性农药中间体的对映体。考察了不同手性选择剂及其浓度、背景电解质的pH等操作条件对分离的影响。结果表明,在12kV操作电压下、30mmol／Ltris-HCl背景电解质中,用14g／L聚合-β-CD作为手性选择剂,PPA和cis-PA对映体在pH6．0时,PIE和PME对映体分别在pH2．5和pH3．0时可以被较好分离。在优化的分离条件下,用聚合-β-CD作毛细管区带电泳手性选择剂分离PIE对映体的分离度为1．513,成功测定了两种旋光性PIE的对映体过量值。     

Enantioselective extraction of mandelic acid enantiomers by aqueous two-phase systems of polyethylene glycol and ammonium sulfate containing ��-cyclodextrin as chiral selector

A new chiral separation technology, aqueous two-phase extraction, was proposed for the separation of racemic mandelic acid. The distribution behavior of mandelic acid enantiomers was investigated in aqueous two-phase systems composed of polyethylene glycol and ammonium sulfate containing ??-cyclodextrin as chiral selector. The influences of the pH, the mass fraction of polyethylene glycol and ammonium sulfate, the polymerization degree of polyethylene glycol, the initial concentration of ??-cyclodextrin, mandelic acid enantiomers and extractive temperature on the distribution behavior were studied respectively. The results show that ??-cyclodextrin is inclined to recognize L-enantiomer; under the optimized conditions, the separation factor reaches 2.46 and the enantiomeric excess is 42.13% in the top phase and 40.43% in the bottom phase, respectively. Aqueous two phase chiral-extraction with strong chiral separation ability, plays great role in preparative separation of racemic compounds and is important for the development of aqueous two phase extraction technique.     

高效液相色谱手性流动相添加剂分离乳酸对映体

分别将β-环糊精、2,6－二甲基－β－环瑚精和2,3,6－三甲基－β－环糊精作为手性流动相添加剂,系统地研究了D,L-乳酸在反相HPLC系统中的拆分,考察了流动相种类,pH值和手性流动相添加剂的浓度对手性分离的影响,建立了甲基化β-环糊精动态手性固定相分离乳酸对映体的方法。     

A Density Functional Theory Study of the Hydrates of 2NH_3:H_2SO_4 and Its Implications for the Formation of Atmosphere Particles

Density functional theory was used at the B3LYP/6-311++G(d,p) level of theory to study the hydrates of 2NH3:H2SO4:nH2O for n = 0～4. Neutrals of the most stable clusters, when n = 0 and 1, spontaneously formed and were determined to be hydrogen-bonded molecular complexes of monomeric species. Double ions (clusters containing a NH4+ cation and a HSO4- anion) or even ternary ions (clusters with two NH4+ cations and one SO42- anion) spontaneously formed in the most stable clusters of 2NH3:H2SO4:nH2O (n = 2, 3, 4). The energetics of binding and incremental association was also calculated. Double ions are not energetically favorable until 2NH3:H2SO4:2H2O because of the about equal free energies for forming the neutral (the most stable) and double ion (the second stable) isomers. The free energy of incremental association from free H2O and 2NH3:H2SO4:nH2O has a maximum at n = 2 at room temperature with ΔG ≈ -2 kcal/mol. The comparison of incremental association energies between 2NH3:H2SO4:nH2O, NH3:H2SO4:nH2O and H2SO4:nH2O clusters revealed that NH3 plays an important role in the atmospheric particle nucleation.     

3-位烯丙基及甲基衍生的β-环糊精固定相的合成及气相色谱性能研究

制备了一种新的β-环糊精衍生物固定相2,6-二-O-戊基-3-O-[(甲基)5(烯丙基)2]-β-CD,并对其气相色谱分离性能进行研究。实验显示,该固定相具有良好的柱表面性能和较强的色谱分离能力,对一些芳香族位置异构体的分离能力优于2,6-二-O-戊基-3-O-烯丙基-β-CD衍生物,对10余种手性物质显示出较好的选择性能,且对α-位取代的丙酸酯类手性分离效果明显优于杂环类β-CD衍生物。与2,6-二-O-戊基-3-O-烯丙基-β-CD固定相的分离性能比较表明,β-CD 3位羟基部分甲基基团的引入能增强对芳香族位置异构体的选择能力,但不能明显改变烯丙基衍生物的手性分离能力。     

Separation of endo-polygalacturonase using aqueous two-phase partitioning

The partitioning of endo-polygalacturonase (endo-PG) in polyethylene glycol (PEG)-polyvinyl alcohol (PVA10000) and PEG-hydroxypropyl starch (Reppal PES100) aqueous two-phase systems was studied, and revealed the possibility of using aqueous two-phase extraction to purify and concentrate endo-PG from its clarified fermentation broth. For the PEG8000-PVA10000 system, endo-PG presented in the fermentation broth (at concentration that is more than 40% of total protein) mainly dominates in the top phase with a partitioning coefficient of 6, while total protein concentrates in the bottom phase. A separation scheme consisting of two consecutive aqueous two-phase extraction steps was proposed: a first extraction in polyethylene glycol (PEG8000)-polyvinyl alcohol system, followed by a second extraction in PEG8000-(NH4)2SO4 system. This allowed the separation of endo-PG from polymer and the recycling of PEG polymer, since endo-PG was very strongly partitioned into the bottom phase of the PEG8000-(NH4)2SO4 system. Laboratory-scale experiments were performed to test the efficiency of this scheme. It was found that enzyme recovery was up to 91% with a total purification factor of about 1.9 and a concentration factor of more than 5. About 90% of the total PEG added into the systems can be recovered, and no reduction was obtained in the purification factor using recycled PEG.     

手性流动相添加法拆分酮康唑外消旋体

采用C18反相色谱柱,利用在流动相中加入手性选择剂的方法实现酮康唑对映体的拆分。研究了手性选择剂的种类及浓度、流动相pH值、甲醇比例和柱温等因素对酮康唑手性分离的影响,结果表明磺丁基-β-环糊精可以使酮康唑对映体完全分离,最后选择的流动相组成为甲醇-0.02 mol/L磷酸二氢钠(体积比为60∶40,含0.02%三乙胺和1.0 mmol/L磺丁基-β-环糊精,用稀磷酸调节pH值到3.00)。酮康唑对映体在6 min内得到基线分离,分离度为2.05。方法简便,分离效果好,对酮康唑对映体的拆分具有应用价值。     

Enantiomeric separation of (R, S)-naproxen by recycling high speed counter-current chromatography with hydroxypropyl-β-cyclodextrin as chiral selector

Recycling high speed counter-current chromatography (HSCCC) was successfully applied to resolution of (R, S)-naproxen (NAP) using hydroxypropyl-β-cyclodextrin (HP-β-CD) as chiral selector. The two-phase solvent system composed of n-hexane-ethyl acetate-0.1 mol L(-1) phosphate buffer solution with pH=2.67 (8:2:10, v/v/v) was selected. Influence factors for the chiral separation process were investigated, including concentration of HP-β-CD, equilibrium temperature and pH of aqueous phase. Suitable elution mode was selected for HSCCC enantioseparation of (R, S)-NAP. Under optimum separation conditions, 29 mg of (R, S)-NAP was separated using preparative recycling HSCCC with the molar ratio HP-β-CD/NAP racemate 83:1. Technical details for recycling elution mode were discussed as for chiral HSCCC separation. The purities of both (S)-NAP and (R)-NAP were over 99.5% as determined by HPLC. Enantiomeric excess of (S)-NAP and (R)-NAP reached 99.4%. Recovery for NAP enantiomers from HSCCC fractions was 82-89%, yielding 13 mg of (S)-NAP and 12 mg of (R)-NAP.     

溶液中铝还原制备Ni-Fe合金纳米粉体及其还原过程

用多相合成方法, 以金属铝粉作还原剂还原FeSO₄·(NH₄)₂SO₄和NiSO₄·(NH₄)₂SO₄的混合溶液, 制备了Ni-Fe合金的钠米粉体, 并对反应的过程进行了讨论.