青霉素G亚砜对-硝基苄酯的合成工艺研究

以青霉素G钾为原料制备青霉素G亚砜对-硝基苄酯.氧化反应的条件为:青霉素G钾与过氧乙酸的投料比(mol)为1:1.15,氧化温度＜5℃,反应时间2h,青霉素G亚砜收率为93.5%;酯化反应最佳反应条件为:DMF的用量为4.28ml/1g青霉素亚砜,青霉素亚砜与对一硝基溴苄的投料比(mol)为1:1.15,反应温度为室温,反应时间为24小时,酯化收率为83.36%,反应总收率为77.92%.此方法可控制产品质量,确保操作安全简便,对工业化生产具有参考意义.     

青霉素发酵液直接氧化制备青霉素G亚砜反应条件优化

以过氧乙酸为氧化剂,研究了青霉素发酵液直接氧化制备青霉素G亚砜的过程,考察了不同影响因素对青霉素G亚砜转化率的影响,分析了氧化后菌丝中青霉素残留,建立并优化了青霉素发酵液直接氧化工艺。结果表明,搅拌转速、反应温度、过氧乙酸投料量、过氧乙酸浓度等因素是青霉素G亚砜转化率的关键影响因素,其他因素对青霉素发酵液直接氧化过程影响较小。过氧乙酸直接氧化青霉素发酵液可释放出残留在菌丝体内的青霉素,相比氧化青霉素G钾盐的转化率更高。最佳氧化工艺条件为反应温度5~10℃,搅拌转速100 r/min,30 min匀速加入青霉素摩尔量1.3倍的高浓度过氧乙酸,继续搅拌反应10 min。青霉素G亚砜的转化率可达98.6%,比青霉素G钾盐为原料的转化率提高1.2%。     

Electrically enhanced extraction of penicillin G into dichloromethane

The application of electrically enhanced liquid-liquid extraction techniques to the recovery and purification of penicillin G from aqueous solutions and from untreated mycelial culture broth is described. Experiments at laboratory scale have shown that extraction rates into dichloromethane at pH 4.0 may be increased by factors of up to five-fold by electrostatically spraying penicillin G solutions into a continuum of solvent held in electrical tension. The experimental studies revealed that in small spray column contactors, electrostatic spray conditions, once initiated at nozzle voltages in excess of 10 kV, could be sustained at nozzle voltages as little as 4 kV. The results demonstrate the potential of this technique as an alternative to mechanically augmented liquid-liquid contact for the intensification of whole broth extraction processes.     

Direct extraction of phenylacetic acid from immobilised enzymatic hydrolysis of penicillin G with cloud point extraction

The enzymatic hydrolysis of potassium salt of penicillin G (Pen G) into phenylacetic acid (PAA) and potassium salt of 6‐aminopenicillanic acid (APA) is inhibited not only by the substrate and the product APA but also by the by‐product PAA. The partitioning behaviour of PAA in a cloud point system, a novel two‐phase partitioning system, was determined. Direct extraction of PAA in the process of immobilised penicillin acylase hydrolysis of Pen G without pH control was achieved. Pen G was hydrolysed almost completely and the product APA concentration in the cloud point system was much higher than in the control, suggesting that the cloud point system may be applied as a novel extractive bioreactor for the enzymatic hydrolysis of Pen G. Copyright © 2006 Society of Chemical Industry     

磁性微粒对青霉素G酰化酶的固定化研究

将无机磁性粒子Fe3O4与有机材料海藻酸钠结合起来制成一种复合的磁性微粒,并将其进行表面修饰,通过化学共价法来固定青霉素G酰化酶。通过扫描电镜等对微粒进行形态学观察,并用傅立叶红外图谱表征微粒表面修饰基团。酶学性质研究表明,该微粒固定化的青霉素G酰化酶的最适pH值为7.5,最适温度为40℃。固定化酶与底物的亲和力有所降低,但是稳定性显著提高。重复催化研究结果表明,固定化酶具有比游离酶更广泛的温度及pH值适用范围,并且具有良好的热稳定性、可循环使用性和贮存稳定性。     

Penicillin G extraction from model media using an emulsion liquid membrane: Determination of optimum extraction conditions

Penicillin G extraction by an emulsion liquid membrane (ELM) was investigated. The effects of surfactants, diluents, and carrier mixtures, together with their combined effects on the initial extraction rate and the emulsion stability were examined. Surfactants, diluents, and carriers used were Span80 (sorbitan monooleate)/ECA4360J (nonionic polyamine), n-butyl acetate/kerosene, and DOA (dioctylamine)/Amberlite LA-2 (secondary amine), respectively. The optimum extraction conditions were found to be 20% (v/v) of Span80 in ECA4360J as a surfactant, kerosene as a diluent and Amberlite LA-2 as a carrier.     

青霉素G亚砜对-硝基苄酯的制备研究

对青霉素G钾制备青霉素G亚砜对-硝基苄酯工艺进行了研究。在青霉素G钾:过氧乙酸(mol)为1∶1.15,氧化温度<5℃,反应时间2 h的条件下,青霉素G亚砜收率为89.0%。酯化反应最佳反应条件为:DMF的用量为4.28 mL/1 g青霉素亚砜,反应温度为室温,青霉素亚砜与对-硝基氯苄的投料比(mol)为1∶1.15,反应时间为24 h,在此条件下酯化收率为80.23%。此方法对于控制产品品质和确保操作安全简便,对工业化生产具有参考意义。     

Extraction of penicillin G from simulated media by an emulsion liquid membrane process

The extraction of penicillin G from simulated media was performed by water/oil/water (w/o/w) emulsion liquid membranes (ELMs) and studied under various operational conditions in a batch system. The degree of extraction achieved was between 80% and 95% under specific conditions. A concentration of greater than nine times the initial concentration of penicillin G in the external phase was obtained in the internal phase. The pH of the internal aqueous solution, containing a basic salt, was theoretically calculated on the basis of the amount of penicillin G transported into the internal phase. The calculated results agreed with the experimental data well and were used to select a suitable type and concentration of a basic salt in the internal phase to give a pH within the range 5 to 8 where penicillin G was stable after the termination of extraction. The extraction of penicillin G was successfully performed by the ELM process with sodium carbonate in the internal phase.     

青霉素G亚砜的合成

以青霉素G钾盐为原料,采用15%左右低浓度过氧乙酸为氧化剂合成青霉素G亚砜,反应时间2～2.5h,n(过氧乙酸):n(青霉素G钾盐)=(1.1～1.2):1.0,反应温度和结晶温度在0～5℃,总收率可达96%以上。所得青霉素G亚砜可直接从溶液中结晶析出,解决了产物与反应体系的分离。产品纯度较高。     

青霉素G亚砜二苯甲酯的合成研究

以青霉素G钾为原料制备青霉素G亚砜二苯甲酯。氧化反应优化条件为:n(过氧乙酸)∶n(青霉素G钾)=1.2∶1.0,氧化温度0～5℃,反应时间2h,青霉素G亚砜酸收率为97.3%;酯化反应优化条件为:二氯甲烷的用量为17mL/g青霉素G亚砜,投料比n(二苯甲醇)∶n(青霉素G亚砜)=1.8∶1.0,反应温度为-15℃,反应时间为60min,酯化收率为79.5%,反应总收率为77.4%。此工艺成本低廉,操作安全简便,对工业化生产具有积极意义。     

Effects of ethylene glycol on the synthesis of ampicillin using immobilized penicillin G acylase

The effects of organic cosolvents on the synthesis of ampicillin from phenylglycine methyl ester (PGME) and 6‐amino penicillanic acid (6‐APA) using immobilized Bacillus megaterium penicillin G acylase have been examined. Several cosolvents were tested for their influence on the enzyme in terms of enzyme stability and hydrophobicity. Among the cosolvents tested, ethylene glycol was found to increase the yield of ampicillin by 39–50%. The effects of ethylene glycol on the pK_a of PGME, the hydrolysis of ampicillin and PGME, and synthetase/amidase and esterase/amidase ratios were also studied. Experimental data indicated that ethylene glycol inhibited more the hydrolysis of the ampicillin than the hydrolysis of the PGME and the synthetase/amidase ratio varied from 0.2 to 0.88 when the concentration (v/v) of the cosolvent increased from 0 to 40%. The enhancement of the synthesis yield was mainly caused by the reduction in the hydrolysis of acyl donor (PGME) and product (ampicillin) in the water–cosolvent system. © 2003 Society of Chemical Industry     

浊点系统中青霉素水解物系的分配及固定化青霉素酰化酶的稳定性

引言 青霉素是生产β-内酰胺抗生素关键中间体6-氨基青霉烷酸(6-APA)的重要原材料.常规酶法水解工艺的底物为结晶青霉素,水解工艺和青霉素发酵工艺不协调;水解反应在控制pH 7～8的环境中进行,不但消耗中和剂氨而且产生工业废物[1].     

Stabilization of native penicillin G acylase by ionic liquids

Five different ionic liquids, based on dialkylimidazolium cations associated with perfluorinated and bis{(trifluoromethyl)sulfonyl}imide anions, were used to investigate the scope and limitations of these new solvents as media for penicillin G acylase‐catalyzed reactions. Deactivation of the native enzyme in ionic liquids (ILs) and in organic solvents (toluene, dichloromethane and 2‐propanol) at low water content and 40 °C was investigated using the hydrolysis of penicillin G as activity test. Native penicillin G acylase shows greater stability in IL media than in organic solvents. For example, a half‐life time of 23 h was obtained in 1‐ethyl‐3‐methylimidazolium bis{(trifluoromethyl)sulfonyl}imide, [emim⁺][Tf₂N^?], which was about 2000‐fold higher than that in 2‐propanol. An enhancement of the PGA stability was observed by the presence of substrate in ionic liquids based on tetrafluoroborate and hexafluorophosphate anions, achieving the highest increase of the half‐life time in 1‐butyl‐3‐methylimidazolium hexafluorophosphate ([bmim⁺][PF₆^?]), which was about 9‐fold higher than the half‐life time in the absence of substrate. Copyright © 2007 Society of Chemical Industry     

Kinetics and reaction engineering of penicillin G hydrolysis

A general diffusion reaction model for immobilised biocatalysis has been developed. The model has been used to study the deacylation of penicillin G to 6-aminopenicillanic acid using two commercially available immobilised Penicillin acylases. The values of D_e/R² for the enzyme pellets have been estimated using data on uptake of 6-aminopenicillanic acid and phenylacetic acid by the enzyme pellets. The kinetic parameters of the model were individually estimated from a suitably designed set of experiments. The values of the Thiele modulus from the kinetic parameters so calculated have been found to be in the range 1·67 to 9·8 for the two enzymes studied, implying that diffusional effects cannot be ignored. The effect of such diffusional limitations on the overall rates and hence on the utilisation of the intrinsic kinetic ability of the enzyme has been demonstrated. This paper also reports on the implementation of the fed-batch strategy for this system. The proposed strategy, which involves maintaining the substrate concentration at the optimum value for a large part of the conversion, results in higher product concentrations than in batch operation, thereby reducing downstream procesing costs. The productivity was also shown to be considerably higher than for batch operation. Further, the ease of implementation of this mode of operation has been demonstrated.     

Penicillin G extraction from model media using an emulsion liquid membrane: A theoretical model of product decomposition

To confirm the applicability for the extraction of penicillin G by an emulsion liquid membrane (ELM), the degree of decomposition of penicillin G during extraction was theoretically calculated. Decomposition was less than 1% provided that the initial sodium carbonate concentration in the internal phase was correctly determined, which proved the applicability of the ELM process. The procedure to determine the initial carbonate concentration in the internal phase was also described in order that the pH in the internal phase should be within the relatively stable range for penicillin G at the end of the extraction.     

Selective reverse micellar extraction of penicillin acylase from E coli

The recovery of penicillin acylase from E coli by a new reverse micellar treatment is described. The results are compared with the cell disruption by ultrasound followed by reverse micellar extraction. The process gave selective extraction of penicillin acylase directly from the periplasmic space of E coli without disrupting the cells. Unlike ultrasonication which breaks open the cells entirely, making subsequent processing difficult and expensive, reverse micellar treatment of cells gave a moderate recovery of 60% of enzyme activity in a highly pure form. © 2001 Society of Chemical Industry     

青霉素G钾/钠在含乙酸丁酯混合溶剂中的溶解度

测定了青霉素G钾在乙酸丁酯与水混合溶剂100mL中,其中含水0．6mL至9．0mL,温度为23.5℃、46．7℃和52．0℃时的溶解度;以及青素霉G钾和钠在含乙酸丁酯、水、乙酸和乙醇等几个特定组成溶剂中,温度范围27．0至50．0℃的溶解度。试验结果可用于青霉素G钾或青霉素G钠结晶过程。     

Effect of dextran polymers on the stability of soluble Escherichia coli penicillin G acylase

The stabilisation of Escherichia coli penicillin G acylase (PGA) by dextran polymers (of molecular weight 11.5, 37.7 and 71 kDa) was studied. The inactivation of both the native and dextran‐containing enzyme preparations obeyed first‐order kinetics at the temperature and pH values studied. The optimal concentrations of dextran polymers of molecular weight 11.5, 37.7 and 71 kDa stabilising PGA against inactivation were 50, 20 and 7.5 mmol dm⁻³ respectively. Dextran 11500 (11.5 kDa) gave 100‐fold protection of PGA against thermal inactivation of enzyme above 50 °C. The kinetic constants of the enzyme were slightly altered, but temperature and pH profiles were not altered by the dextrans. © 1999 Society of Chemical Industry     

A thermal study on the use of immobilized penicillin G acylase in the formation of 7‐amino‐3‐deacetoxy cephalosporanic acid from cephalosporin G

Penicillin G acylase (PGA) is an important enzyme for the industrial production of 7‐amino‐3‐deacetoxy cephalosporanic acid (7‐ADCA) from cephalosporin G (Ceph‐G), and 6‐aminopenicillanic acid (6‐APA) from penicillin G (Pen‐G). These products are used for the manufacture of semi‐synthetic cephalosporins and penicillins. In this study, immobilized PGA was utilized to catalyze the conversion of Ceph‐G to 7‐ADCA. The optimal conditions were found to be an operating temperature of 45 °C, 0.2 M phosphate buffer, a substrate concentration of 30 mg cm^?3 and a catalyst particle concentration of 0.01 g cm^?3 (specific activity of 623.2 U g^?1). Up to 45 °C the reaction was characterized by an activation energy of 38.66 kJ mol^?1. Beyond 57.5 °C there was a sharp decline of activity, characterized by a deactivation energy of 235.88 kJ mol^?1. Copyright © 2004 Society of Chemical Industry     

醋酸丁酯及二正辛基亚砜萃取青霉素的研究

通过化学分析、计算机数据处理及FT—IR红外光谱的确证,提出了醋酸丁酯及二正辛基亚砜萃取青霉素的萃合反应式及萃合物的键合结构;研究中观察到青霉素在醋酸丁酯中形成了反胶团,胶团半径可达0.6μm.