固定化青霉素酰化酶在光-pH敏感可回用两水相中裂解青霉素G为6-APA

两水相体系在发展中存在的关键问题是相体系回收困难.由于生产成本及降低污染的原因, 用过的相体系需要回收和重复使用.用环境敏感型溶解可逆聚合物形成可回用两水相体系是当前是为可行的回收方法。本文在光敏感可回用高聚物PNBC与pH敏感型可回用高聚物PADB形成的两水相体系中进行固定化青霉素酰化酶的相转移催化青霉素G产生6-APA的反应。在这个两水相体系中,通过优化,在1% NaCl 存在下,６－ＡＰＡ的分配系数可达5.78。催化动力学显示,达平衡的时间近7h,反应最高得率约85.3%（pH 7.8, 20℃）。较相近条件下的单水相反应得率提高近20%。在反应过程中,通过底物及产物的分配系数检测,发现底物分配系数变化不大,而产物6-APA及苯乙酸的分配系数发生很大变化,从而引起产物的得率变化。在两水相中,底物及产物主要分配在上相,固定化酶分配在下相,底物青霉素G进入下相经酶催化产生的6-APA及苯乙酸又转入上相,从而解除了青霉素酰化酶催化反应的底物及产物抑制作用,达到提高产物得率的效果。此外,采用固定化酶较固定化细胞效率高,占用下相体积小,较游离酶稳定性高,且完全单侧分配在下相。因此,在两水相中进行固定化酶的催化反应具有明显的优越性。形成两水相的高聚物PNBC通过488 nm 的激光照射或经滤光的450nm 光源照射得到回收;pH敏感型成相聚合物PADB可通等电点 4.1沉淀可实现循环利用,高聚物的回收率在95%-98%之间,按此回收率计算,聚合物可使用60次以上。     

Integration of bioconversion and downstream processing: starch hydrolysis in an aqueous two-phase system

Integration of bioconversion and the first step(s) of down stream processing can be used as a means to increase the productivity of bioprocesses. This integration also gives the possibility to run the bioconversion in a continuous mode. We demonstrate the use of an aqueous two-phase system in combination with ultrafiltration to accomplish this. Conversion of native starch to glucose by alpha-amylase and glucoamylase was carried out in an aqueous two-phase system in connection with a membrane filtration unit. In this way, a continuous stream of glucose in buffer solution was obtained; the phase-forming polymers as well as the starch-degrading enzymes were recycled, and clogging of the ultrafiltration membrane was avoided. The process was carried out continuously in a mixer-settler reactor for a period of 8 days. The enzyme activities in the top and bottom phases and in the mixing chamber were monitored intermittently throughout the experiment. The optimum pH, temperature, and ionic strength for the activity of the enzyme mixture were determined. The settling time of phase systems containing varying amounts of PEG, crude dextran, and solid starch was studied. The activity and stability of enzyme mixtures was studied both in buffer medium and in the medium containing the polymers. The enzymes were found to be more active and stable in medium containing polymers than in the buffer solutions.     

Extractive bioconversion in aqueous two-phase systems

Summary The transformation of hydrocortisone to prednisolone was studied in aqueous two-phase systems, as a model for the extractive bioconversion of fine chemicals. The bacterium, Arthrobacter simplex, was able to grow in the two-phase system and the cells could be revitalized after a period of use. Use of aqueous two-phase systems made it possible to operate the reaction at higher substrate concentrations than in pure buffer solution. An adsorptive method to remove the product from the top phase was tested and shown to be both efficient and compatible with the overall process. In order to reduce the costs of operation in aqueous two-phase systems, a cheaper starch-based polymer, Reppal-PES, was successfully used as a substitute for dextran.Dedicated to Professor Dr. Georg Manecke on the occasion of his 70th birthday     

A multiphasic hollow fiber reactor for the whole-cell bioconversion of 2-methyl-1,3-propanediol to (r)-beta-hydroxyisobutyric acid

This paper describes the bioconversion of 2-methyl-1,3-propanediol to (R)-beta-hydoxyisobutyric acid (HIBA) by Acetobacter ALEI in a hollow fiber membrane bioreaction system arrangement that allows the integration of three liquid phases: the aqueous bioconversion phase, the organic phase consisting of a solution of trioctyl phosphine oxide (TOPO) in isooctane, and the third phase consisting of a basic stripping solution that allows reextraction of HIBA from the organic phase. A comparison of HIBA mass transfer experiments was carried out in the membrane reactor with two and three phases for different pH and TOPO concentrations. The use of the three-phase arrangement allows the extraction of high quantities of HIBA from the aqueous medium (higher than 85%) independently of the pH, whereas in the two-phase system the percentage of HIBA extracted from the aqueous medium was lower, 42% in the best case, and strongly influenced by the pH. The percentage of the extractive agent TOPO in the organic phase influenced on the mass transfer rate in both bi- and triphasic arrangements. By simply integrating the re-extraction phase in the system it was possible to increase the extraction yield by 2-fold, reduce the amount of TOPO by 4-fold, and operate at the more favorable pH 4. A bioconversion experiment was done in these conditions (pH = 4, TOPO = 5%) to confirm the advantages of including the third stripping solution. Fed-batch operation of the triphasic membrane reactor was maintained for more than 20 h, reaching an HIBA concentration in the stripping solution of 29 g L(-)(1).     

ENHANCED PRODUCTION OF 6-AMINOPENICILLANIC ACID IN AQUEOUS METHYL ISOBUTYL KETONE SYSTEM WITH IMMOBILIZED PENICILLIN G ACYLASE

Enzymatic hydrolysis of penicillin G for production of 6-amino-penicillanic-acid (6-APA) was achieved by using penicillin G acylase as catalyst in an aqueous-methylisobutyl ketone (MIBK) system. The optimization was carried out and it was found that the best conversion was improved 10% more than the aqueous system, which was obtained at the conditions: initial pH 8.0, 5.0% (W/V) substrate (penicillin G), and temperature at 35°C, and the ratio of aqueous and organic phase was 3:1. The stability of the biocatalyst was studied at the operational conditions. After 5 cycles of semi-batch reactions, the residual activity of penicillin G acylase was 69.2% of the initial activity. There was no apparent loss of the yield of product. This process has a potential application in the industrial scale production of 6-APA because it simplifies the process effectively.     

Bioconversions in aqueous two-phase systems.

Bioconversions involving enzymes and/or microbial cells in aqueous two-phase systems are reviewed. The partitioning of biocatalysts, substrates, and products is discussed in relation to their size. The efficiency of retaining biocatalysts in aqueous two-phase systems is summarized in relation to other methods of recirculating. The influence of phase components on the activity and the stability of enzymatic biocatalysts is exemplified with penicillin acylase and the cellulolytic enzyme system, and the effect of phase components on biocatalytic living cells is exemplified with the production of alpha-amylase with Bacillus sp. Process design costs in bioconversions in aqueous two-phase systems are briefly summarized.     

Production of alkaline protease by Bacillus licheniformis in an aqueous two-phase system

Alkaline protease production by Bacillus licheniformis was studied in an aqueous two-phase system composed of 5% (w/w) polyethylene glycol 6000 (PEG 6000) and 5% (w/w) dextran T500. The top phase was continuous and rich in PEG while the bottom phase was dispersed and rich in dextran. The cells were retained in the bottom phase and at the interface. The two-phase system produced less enzyme in total amount than the control in the early phase, but after 50 h the enzyme produced in the control system decreased while the aqueous two-phase system continued its production and finally the total enzyme activity reached 1.3 times that of the control culture. In order to improve the productivity of protease, repeated batch cultivation were successfully carried out four times by optimizing the top phas composition of freshly added media, which resulted in 13.8, 35.9, 27.8 and 34.7 units ml⁻¹ h⁻¹ of protease based on the amounts of replaced top phases, respectively.     

Liquid–liquid extraction of a recombinant protein, cytochrome b5, from an impure extract using aqueous two-phase systems

The recovery and purification of a recombinant protein, cytochrome b₅, from an impure extract of Escherichia coli disrupted cells was carried out in one step using a liquid–liquid extraction process of aqueous two-phase systems of polyethylene glycol (PEG) and potassium phosphate salts. With this separation process it was possible in one single step to remove the cell debris, that precipitate at interface of the system, and to obtain relatively high recovery yields, nearly 67%, of the target protein in the salt-rich phase, with purification factors up to 6.     

Variation of penicillin acylase partition coefficient with phase volume ratio in poly(ethylene glycol)–sodium citrate aqueous two-phase systems

The influence of phase volume ratio on partition and purification of penicillin acylase from Escherichia coli on poly(ethylene glycol)–sodium citrate aqueous two-phase systems was studied. In PEG 1000 systems both partition coefficients of the enzyme and total protein increased with decreasing phase volume ratio. However, in PEG 3350 containing NaCl, penicillin acylase follows a reverse trend, while total protein behaves in the same way. Implications for protein purification designs are discussed.     

Extractive bioconversion of geraniol by a Vitis vinifera cell suspension employing a two-phase system

Among the problems associated with the bioconversion of monoterpenes by plant cell suspensions are the toxicity of some substrates and/or products at low concentrations, the transient state of nascent products and the length of time required to obtain the cell suspension. We investigated the extractive bioconversion of geraniol by a Vitis vinifera c.v. Muscat de Frontignan cell suspension in a two-phase system consisting of an aqueous nutrient phase surmounted by a lipid (Miglyol 812) phase. This system proved to be advantageous as it allowed a five-fold increase in the substrate load without causing any detrimental effect on the cell suspension, it improved the persistence of nascent products and it permitted the recycling or re-use of the cell suspension in a monoterpene bioconversion process.CRASH contribution no. 060     

Purification of (S)-3-cyano-5-methylhexanoic acid from bioconversion broth using an acetone/ammonium sulfate aqueous two-phase system

(S)-3-Cyano-5-methylhexanoic acid ((S)-CMHA) is the key chiral intermediate of pregabalin. In this paper, an aqueous two-phase system (ATPS) was developed to extract (S)-CMHA from nitrilase-catalyzed bioconversion broth. Inorganic salts and hydrophilic solvents were screened to form ATPS, among which an acetone/ammonium sulfate ATPS was investigated in detail, including phase diagram, effect of phase composition and stability of (S)-CMHA. The maximum product recovery of 99.15% was obtained by an optimized ATPS system composed of 15% (w/w) ammonium sulfate and 35% (w/w) acetone with the removal of 99% cells and 86.27% proteins. The total (S)-CMHA yield reached 92.11% after back-extraction. The recycling use of ammonium sulfate was investigated, and 93.10% of salt in the salt-rich phase was recovered with the addition of methanol. The results demonstrated the efficiency of the two-step extraction process for separation of (S)-CMHA.     

Production of immobilized penicillin acylase using aqueous polymer systems for enzyme purification and in situ immobilization

A novel approach for the isolation and purification of penicillin acylase (PA), which couples aqueous two-phase partitioning and enzyme immobilization has been investigated.A PA yield of 90% was achieved by treating E. coli cells with 4% butyl acetate, freeze-thawing step, and pressure homogenization. PA purification (93% recovery) was achieved by (1) removing cell debris via precipitation with polyethylene glycol (PEG 2000); (2) aqueous two-phase partitioning using a PEG 2000 + phosphate system (87% recovery).An in situ enzyme immobilization approach, using oxirane acrylic or aldehyde-agarose beads dispersed in the PEG-rich phase, was explored for the conversion of penicillin G to 6-aminopenicillanic acid. An appropriate immobilization reaction time was found. The catalytic performance of the enzyme, when immobilized, was found not to be affected by recycling of the phase-forming components.     

Effect of mass transfer limitations on the enzymatic kinetic resolution of epoxides in a two-liquid-phase system

Optically active epoxides can be obtained by kinetic resolution of racemic mixtures using enantioselective epoxide hydrolases. To increase the productivity of the conversion of sparingly aqueous soluble epoxides, we investigated the use of a two-phase aqueous/organic system. A kinetic model which takes into account interphase mass transfer, enzymatic reaction, and enzyme inactivation was developed to describe epoxide conversion in the system by the epoxide hydrolase from Agrobacterium radiobacter. A Lewis cell was used to determine model parameters and results from resolutions carried out in the Lewis cell were compared to model predictions to validate the model. It was found that n-octane is a biocompatible immiscible solvent suitable for use as the organic phase. Good agreement between the model predictions and experimental data was found when the enzyme inactivation rate was fitted. Simulations showed that mass transfer limitations have to be avoided in order to maximize the yield of enantiomerically pure epoxide. Resolution of a 39 g/L solution of racemic styrene oxide in octane was successfully carried out in an emulsion batch reactor to obtain (S)-styrene oxide in high enantiomeric excess (>95% e.e.) with a yield of 30%.     

Enzymatic conversion in aqueous two-phase systems: deacylation of benzylpenicillin to 6-aminopenicillanic acid with penicillin acylase

The conversion of benzylpenicillin (BP) to 6-aminopenicillanic acid (6-APA) using penicillin acylase (penicillin amidohydrolase, EC 3.5.1.11) has been studied in aqueous two-phase systems. In a system composed of 8.9% (w/w) PEG 20000/7.6% (w/w) potassium phosphate the enzyme was almost completely partitioned to the bottom phase (K < 0.01), which allowed repeated batch conversions, recirculating the enzyme several times. The initial specific productivities were 0.31–1.47 μmol 6-APA mg protein^?1 min^?1 in repeated conversions over five steps. The yield obtained from the top phase was 0.47–0.71 mol 6-APA mol BP^?1. The results are discussed in relation to recirculating the enzyme by immobilizing it to a solid matrix. Despite the high phosphate concentration in the bottom phase the system needs to be titrated in order for the reaction to proceed. Titration of the top phase alone protected the enzyme from denaturation by strong alkali used for the titration.     

Efficient Repeated Use of Alcohol Dehydrogenase with NAD + Regeneration in an Aqueous-organic Two-phase System

Bioconversion of cinnamyl alcohol to cinnamaldehyde was carried out in an aqueous-organic two-phase reaction system by the repeated use of horse liver alcohol dehydrogenase (HLADH) and NAD + with coenzyme regeneration. Both HLADH and the coenzyme were efficiently entrapped in the aqueous phase, while the substrate was supplied successively from the organic phase and the product was accumulated in the organic phase. Optimum conditions for cinnamaldehyde production in the aqueous-organic two-phase system were also examined, including substrate concentration, pH, and organic solvent type. Under suitable conditions, both HLADH and NAD + in the aqueous-organic two-phase system could be reused, and NAD + cycling numbers of 3040 were obtained after repeated operation for 40 &#117 h.     

Efficient Repeated Use of Alcohol Dehydrogenase with NAD + Regeneration in an Aqueous-organic Two-phase System

Bioconversion of cinnamyl alcohol to cinnamaldehyde was carried out in an aqueous-organic two-phase reaction system by the repeated use of horse liver alcohol dehydrogenase (HLADH) and NAD + with coenzyme regeneration. Both HLADH and the coenzyme were efficiently entrapped in the aqueous phase, while the substrate was supplied successively from the organic phase and the product was accumulated in the organic phase. Optimum conditions for cinnamaldehyde production in the aqueous-organic two-phase system were also examined, including substrate concentration, pH, and organic solvent type. Under suitable conditions, both HLADH and NAD + in the aqueous-organic two-phase system could be reused, and NAD + cycling numbers of 3040 were obtained after repeated operation for 40 λh.     

Downstream processing of luciferase from fireflies (Photinus pyralis) using aqueous two-phase extraction

The firefly luciferase has been extensively used for sensitive detection of bacteria, gene expression and environmental toxins (biosensors). The aim of the present study was to design a simple and more efficient method for the purification and concentration of luciferase using aqueous two-phase extraction (ATPE). Downstream processing of luciferase from North American Firefly Photinus pyralis was carried out, for the first time, using polymer/salt aqueous two phase system (ATPS) at 4 °C. The enzyme was observed to preferentially partition to the polyethylene glycol (PEG) rich top phase. The best results of purification (13.69 fold) and enzyme activity recovery (118.34%) were observed in the system containing 4.0% (w/w) PEG (1500) and 20.5% (w/w) (NH₄)₂SO₄ with a phase volume ratio of 0.21.     

Use of aqueous two-phase systems for in situ extraction of water soluble antibiotics during their synthesis by enzymes immobilized on porous supports

Yields of kinetically controlled synthesis of antibiotics catalyzed by penicillin G acylase from Escherichia coli (PGA) have been greatly increased by continuous extraction of water soluble products (cephalexin) away from the surroundings of the enzyme. In this way its very rapid enzymatic hydrolysis has been avoided. Enzymes covalently immobilized inside porous supports acting in aqueous two-phase systems have been used to achieve such improvements of synthetic yields. Before the reaction is started, the porous structure of the biocatalyst can be washed and filled with one selected phase. In this way, when the pre-equilibrated biocatalyst is mixed with the second phase (where the reaction product will be extracted), the immobilized enzyme remains in the first selected phase in spite of its possibly different natural trend. Partition coefficients (K) of cephalexin in very different aqueous two-phase systems were firstly evaluated. High K values were obtained under drastic conditions. The best K value for cephalexin (23) was found in 100% PEG 600-3 M ammonium sulfate where cephalexin was extracted to the PEG phase. Pre-incubation of immobilized PGA derivatives in ammonium sulfate and further suspension with 100% PEG 600 allowed us to obtain a 90% synthetic yield of cephalexin from 150 mM phenylglycine methyl ester and 100 mM 7-amino desacetoxicephalosporanic acid (7-ADCA). In this reaction system, the immobilized enzyme remains in the ammonium sulfate phase and hydrolysis of the antibiotic becomes suppressed because of its continuous extraction to the PEG phase. On the contrary, synthetic yields of a similar process carried out in monophasic systems were much lower (55%) because of a rapid enzymatic hydrolysis of cephalexin.     

11α-Hydroxylation of 16α,17-epoxyprogesterone by Rhizopus nigricans in a biphasic ionic liquid aqueous system

11α-Hydroxylation of 16α,17-epoxyprogesterone (EP) by Rhizopus nigricans is an essential step in the synthesis of many steroidal drugs, while low conversion of the biohydroxylation is a tough problem to be solved urgently in industry. Two ionic liquids (ILs) of [BMIm][PF(6)] and [BMIm][NTf(2)] were used in the biotransformation of EP by R. nigricans. The results indicated that the conversion carried out in [BMIm][PF(6)]-aqueous biphasic system was greatly increased to above 90% at 18 g/L feeding concentration. A simplified mechanism was proposed to explain the improvement of the bioconversion in a biphasic ionic liquid aqueous system. Besides, successive three batches of bioconversion were carried out in the biphasic system with a total conversion of 87% at phase ratio 10 and 75% at phase ratio 5, respectively. Since recycling of the [BMIm][PF(6)] is quite easy, there is a great potential for the application of ILs in fungi biotransformation to implement green production.     

The extractive purification of peroxidase from plant raw materials in aqueous two-phase systems

The extractive purification of peroxidase from Armoracia rusticana roots and Glycine max seed coats in temperature-induced and affinity microsphere-containing aqueous two-phase systems was stuied. The extractive purification of peroxidase from Glycine max seed coats was carried out in a temperature-induced aqueous two-phase system formed by Triton X-45, Triton X-100 and sodium acetate at pH 5.5 A 99% yield with a 6-fold purification factor was obtained. When the clear top phase was subjected to concanavalin-A affinity chromatography, the purification factor rose to 41 and the yield dropped to 28%. A two-step purification process for peroxidase from Armoracia rusticana roots was developed by adding concanavalin-A affinity microspheres to a PEG/phosphate aqueous two-phase system. The method allows a 60% recovery of high purity peroxidase (1,860 guaiacol units per mg). A lower recovery rate and degree of purification of this enzyme was achieved after temperature-induced aqueous two-phase partition or acetone precipitation and concanavalin-A affinity column chromatography.