水-有机溶剂两相体系中甲基单孢菌Z201细胞催化丙烯环氧化的初步研究

Laabe于1987年提出了生物催化剂工程(Biocatalyst engineering)和介质工程(Medium engineering)的概念^[1]。有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚步。本文以甲基单胞菌(Methylomonas Z201)完整细胞为生物催化剂．丙烯环氧化为指标反应．研究有机溶剂对活性的影响并对催化活性——溶剂疏水性进行了相关性分析。研究了水一十六烷两相体系中十六烷含量和搅拌速度对丙烯环氧化速度的影响和细胞的操作稳定性。     

水-有机溶剂两相体系中甲基单胞菌Z201催化丙烯环氧化的初步研究

Lanne于1987年提出了生物催化剂工程（Biocatalyst engimeering）和介质工程（Medium enineering）的概念^[1].有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚少。本文以甲基单胞菌（Methylomonos）Z201完整细胞为生物催化剂,丙烯环氧化为指标反应,研究有机溶剂对活性的影响并对催化活性-溶剂疏水性进行了相关性分析。研究了水-十六烷两相体系中十六烷含量和搅拦速度对丙烯环氧化速度的影响和细胞的操作稳定性。     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Biodegradation of phenol at high initial concentrations in two-phase partitioning batch and fed-batch bioreactors

A two-phase organic-aqueous system was used to degrade phenol in both batch and fed-batch culture. The solvent, which contained the phenol and partitioned it into the aqueous phase, was systematically selected based on volatility, solubility in the aqueous phase, partition coefficient for phenol, biocompatibility, and cost. The two-phase partitioning bioreactor used 500 mL of 2-undecanone loaded with high concentrations of phenol to deliver the xenobiotic to Pseudomonas putida ATCC 11172 in the 1-L aqueous phase, at subinhibitory levels. The initial concentrations of phenol selected for the aqueous phase were predicted using the experimentally determined partition coefficient for this ternary system of 47.6. This system was initially observed to degrade 4 g of phenol in just over 48 h in batch culture. Further loading of the organic phase in subsequent experiments demonstrated that the system was capable of degrading 10 g of phenol to completion in approximately 72 h. The higher levels of phenol in the system caused a modest increase in the duration of the lag phase, but did not lead to complete inhibition or cell death. The use of a fed-batch approach allowed the system to ultimately consume 28 g of phenol in approximately 165 h, without experiencing substrate toxicity. In this system, phenol delivery to the aqueous phase is demand based, and is directly related to the metabolic activity of the cells. This system permits high loading of phenol without the corresponding substrate inhibition commonly seen in conventional bioreactors. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 155-162, 1997.     

Enhanced taxol production and release in Taxus chinensis cell suspension cultures with selected organic solvents and sucrose feeding

Suspension culture of Taxus chinensis cells was carried out in aqueous-organic two-phase systems for the production and in situ solvent extraction of taxol (paclitaxel). Three organic solvents, hexadecane, decanol, and dibutylphthalate, were tested at 5-20% (v/v) in the culture liquid. All of these solvents stimulated taxol release and the yield per cell, though decanol and higher concentrations of the other two solvents depressed biomass growth significantly. Ten percent dibutylphthalate was the optimal solvent for improving taxol production and release with minimal cell growth inhibition. The time of solvent addition to the culture also affected taxol production, with the addition during the late-log growth phase being most favorable. By feeding sucrose to the culture near the stationary growth phase, the cell growth and taxol production period was extended from 27 to 42 days. The combining of the two-phase culture and sucrose feeding increased the taxol yield by about 6-fold compared with the single-phase batch culture, to 36.0 +/- 3.5 mg/L, with up to 63% taxol released. This study shows that in situ solvent extraction combined with nutrient feeding is an effective process strategy for production and recovery of secondary metabolites in plant cell suspension culture.     

Metabolism characteristics of <Emphasis Type="Italic">Chelativorans oligotrophicus</Emphasis> by two-phase growth on the mixture of EDTA and glucose

The obligate destructor of ethylene diamine tetraacetate—a culture of Chelativorans oligotrophicus LPM-4—did not grow on a medium with glucose, but it was good to use it under cultivation on a mixture with EDTA after considerable decrease of the EDTA concentration in the medium (two-phase growth). Strong inhibition of hexokinase and glucose 6-phosphate dehydrogenase in cell exracts 4 mM EDTA was revealed. Using EDTA, cells accumulated polyphosphates whose rate decreased during glucose utilization phase. High activities of polyphosphate biosynthesis ferments (adenylat kinase and polyphosphate kinase) were distinguished during the first phase of the cultivation; considerable decrease of them and increase of polyphosphate glucokinase were found during the second phase of the cultivation. This points to the possible participating of polyphosphates in glucose metabolism as a supplementary energy source.     

Enhanced production of lactic acid through the use of a novel aqueous two-phase system as an extractive fermentation system

 In order to enhance the productivity of lactic acid and reduce the end-product inhibition of fermentation, the partitioning and growth of four different strains of lactic acid bacteria in three different aqueous two-phase systems were studied. Polyethyleneglycol/ dextran, polyethyleneglycol/hydroxypropyl starch polymer (HPS), and a random copolymer of ethylene oxide and propylene oxide (EO-PO)/HPS were used as polymer systems. One strain each of Lactococcus lactis subsp. lactis and of Lactobacillus delbrueckii subsp. delbrueckii partitioned completely to the interface and bottom phase in two-phase systems with low polymer concentrations of EO-PO/HPS100 and EO-PO/ HPS200. The growth and production of lactic acid by two of three L. lactis strains in a two-phase system with 5.5% (w/w) EO-PO and 12.0% (w/w) HPS100 were reduced by less than 10% compared with a reference fermentation in a normal growth medium. The viability of L. lactis subsp. lactis ATCC 19435 was maintained for at least 50 h and with four top-phase replacements during extractive fermentation in the EO-PO/HPS100 system. Moreover, when cell density reached the stationary phase in the first extractive fermentation, the lactate production in this aqueous two-phase system was maintained. Received: 2 October 1995/Received revision: 16 January 1996/Accepted: 22 January 1996     

Alginate as immobilization matrix and stabilizing agent in a two-phase liquid system: application in lipase-catalysed reactions.

Alginate was evaluated as an immobilization matrix for enzyme-catalyzed reactions in organic solvents. In contrast to most hydrogels, calcium alginate was found to be stable in a range of organic solvents and to retain the enzyme inside the gel matrix. In hydrophobic solvents, the alginate gel (greater than 95% water) thus provided a stable, two-phase liquid system. The lipase from Candida cylindracea, after immobilization in alginate beads, catalysed esterification and transesterification in n-hexane under both batch and continuous-flow conditions. The operational stability of the lipase was markedly enhanced by alginate entrapment. In the esterification of butanoic acid with n-butanol, better results were obtained in the typical hydrophilic calcium alginate beads than in less hydrophilic matrices. The effects of substrate concentration, matrix area, and polarity of the substrate alcohols and of the organic solvent on the esterification activity were examined. The transesterification of octyl 2-bromopropanoate with ethanol was less efficient than that of ethyl 2-bromopropanoate with octanol. By using the hydrophilic alginate gel as an immobilization matrix in combination with a mobile hydrophobic phase, a two-phase liquid system was achieved with definite advantages for a continuous, enzyme-catalysed process.     

Penicillin acylase-catalyzed synthesis of cefazolin in water–solvent mixtures: enhancement effect of ethyl acetate and carbon tetrachloride on the synthetic yield

The effects of organic solvents on the penicillin acylase-catalyzed, kinetically controlled synthesis of cefazolin have been examined in various water–solvent mixtures. In the presence of water-miscible solvents, the initial rate and maximum yield of cefazolin (CEZ) synthesis reaction were found to be reduced. The extent of inhibition was increased with increasing hydrophobicity of the solvent in the reaction mixtures. Enzymatic synthesis of cefazolin was also carried out in the water–solvent biphasic systems. Among the water-immiscible solvents tested, ethyl acetate (EtOAc) and carbon tetrachloride (CCl₄) were found to markedly improve the yield of cefazolin in the two-phase reaction system. Our study showed that the enhancement effect of EtOAc and CCl₄ on the synthetic yield was mainly caused by a reduction of the hydrolysis of acyl donor and product in the two-phase system rather than extraction of the product into the solvent phase.     

Reversible structural changes in a hydrophobic protein,elastin, as indicated by fluorescence probe analysis

Fluorescent probe analysis of purified elastin using 1-anilinonaphthalene-8-sulfonate has been used to investigate reversible structural changes that accompany stretching of this rubberlike protein. There is a specific binding of 1-anilinonaphthalene-8-sulfonate to elastin with a single dye molecule attached per 74,000 molecular-weight protein subunit. When labeled elastin is stretched, the intensity of the 1-anilinonaphthalene-8-sulfonate fluorescence decreases reversibly, and this decrease appears to be linked to an increase in the environmental polarity in the immediate vicinity of the bound dye molecule. The results of experiments carried out in H₂O and D₂O indicate that this polarity change is due to an increase in the exposure of the 1-anilinonaphthalene-8-sulfonate to water as the hydrophobic interior of the protein subunit is unfolded during stretching. The data are consistent with the proposal that the elastin network is a two-phase system of hydrophobic protein globules surrounded by free solvent spaces.     

Physiological properties of a Pseudomonas strain which grows with p-xylene in a two-phase (organic-aqueous) medium.

Pseudomonas putida Idaho utilizes toluene, m-xylene, p-xylene, 1,2,4-trimethylbenzene, and 3-ethyltoluene as growth substrates when these hydrocarbons are provided in a two-phase system at 5 to 50% (vol/vol). Growth also occurs on Luria-Bertani medium in the presence of a wide range of organic solvents. The ability of the organism to grow in the presence of organic solvents is correlated with the logarithm of the octanol-water partition coefficient, with dimethyl-phthalate (log P(OCT) = 2.3) being the most polar solvent tolerated. During growth with p-xylene (20% [vol/vol]), there was an initial lag period accompanied by cell death, which was followed by a period of exponential growth. The stationary phase of growth was characterized by a dramatic decrease in cell viability, although cell dry weight and turbidity measurements slowly increased. Electron micrographs revealed that during growth in the presence of p-xylene, the outer cell membrane becomes convoluted and membrane fragments are shed into the culture medium. At the same time, the cytoplasmic membrane invaginates, forming vesicles, and becomes disorganized. Electron-dense intracellular inclusions were observed in cells grown with p-xylene (20% [vol/vol]) and p-xylene vapors, which are not present in cells grown with succinate. Attempts to demonstrate the presence of plasmid DNA in P. putida Idaho were negative. However, polarographic studies indicated that the organism utilizes the same pathway for the degradation of toluene, m-xylene, and p-xylene as that used by P. putida mt-2 which contains the TOL plasmid pWWO.(ABSTRACT TRUNCATED AT 250 WORDS)     

Physiological properties of a Pseudomonas strain which grows with p-xylene in a two-phase (organic-aqueous) medium.

Pseudomonas putida Idaho utilizes toluene, m-xylene, p-xylene, 1,2,4-trimethylbenzene, and 3-ethyltoluene as growth substrates when these hydrocarbons are provided in a two-phase system at 5 to 50% (vol/vol). Growth also occurs on Luria-Bertani medium in the presence of a wide range of organic solvents. The ability of the organism to grow in the presence of organic solvents is correlated with the logarithm of the octanol-water partition coefficient, with dimethyl-phthalate (log P(OCT) = 2.3) being the most polar solvent tolerated. During growth with p-xylene (20% [vol/vol]), there was an initial lag period accompanied by cell death, which was followed by a period of exponential growth. The stationary phase of growth was characterized by a dramatic decrease in cell viability, although cell dry weight and turbidity measurements slowly increased. Electron micrographs revealed that during growth in the presence of p-xylene, the outer cell membrane becomes convoluted and membrane fragments are shed into the culture medium. At the same time, the cytoplasmic membrane invaginates, forming vesicles, and becomes disorganized. Electron-dense intracellular inclusions were observed in cells grown with p-xylene (20% [vol/vol]) and p-xylene vapors, which are not present in cells grown with succinate. Attempts to demonstrate the presence of plasmid DNA in P. putida Idaho were negative. However, polarographic studies indicated that the organism utilizes the same pathway for the degradation of toluene, m-xylene, and p-xylene as that used by P. putida mt-2 which contains the TOL plasmid pWWO.(ABSTRACT TRUNCATED AT 250 WORDS)     

Solvent selection for enhanced bioproduction of 3-methylcatechol in a two-phase partitioning bioreactor

The biotransformation of toluene to 3-methycatechol (3MC) via Pseudomonas putida MC2 was used as a model system for the development of a biphasic process offering enhanced overall volumetric productivity. Three factors were investigated for the identification of an appropriate organic solvent and they included solvent toxicity, bioavailability of the solvent as well as solvent affinity for 3MC. The critical log P (log P(crit)) of the biocatalyst was found to be 3.1 and log P values were used to predict a solvent's toxicity. The presence of various functional groups of candidate solvents were used to predict the absorption of 3MC and it was found that solvents possessing polarity showed an affinity towards 3MC. Bis (2-ethylhexyl) sebecate was selected for use in the biphasic system as it fulfilled all selection criteria. A two-phase biotransformation with BES and a 50% phase volume ratio, achieved an overall volumetric productivity of 440 mg 3MC/L-h, which was an improvement by a factor of approximately 4 over previously operated systems. Additional work focused on reducing the toluene feed in order to minimize possible toxicity and decrease loss of substrate (toluene), a result of volatilization. Toluene losses were reduced by a factor of 4, compared to previously operated systems, without suffering an appreciable loss in overall volumetric productivity.     

Growth of Gram-negative bacteria in the presence of organic solvents

The growth behavior of Gram-negative bacteria when exposed to high concentrations (50% v/v) of water-insoluble organic solvents was investigated. The solvents were chosen according to their polarity values as denoted by a logarithmically expressed parameter log P, where P is the partition coefficient of a given solvent in an equimolar mixture of octanol and water. The cell growth was measured by the number of colonies developed on a solid agar medium in direct contact with the solvents. All 31 strains tested showed characteristic growth patterns. The survival and subsequent growth of bacteria increased with the increase in the log P value and was found to be strain specific. For all the strains, 100% cell growth was reached from 0% within 0.1–0.4 log P units. Log P₅₀ values, defined as the log P values at which 50% of the cells form colonies, were determined for each bacterial strain. On the whole, Pseudomonas strains were found to be more resistant to apolar solvents than all other bacteria tested. This resistance was dependent not only on the polarities but also on the toxic nature of different organic solvents, the cell membrane components, and to a limited extent, the growth medium. A tenfold increase in the Mg²⁺ concentration in the growth medium enhanced the solvent resistance of E. coli but had no such effect on Pseudomonads. In general, different growth temperatures had no impact on the solvent resistance of the Gram-negative bacteria tested.     

Prediction of the adaptability of Pseudomonas putida DOT-T1E to a second phase of a solvent for economically sound two-phase biotransformations

The strain Pseudomonas putida DOT-T1E was tested for its ability to tolerate second phases of different alkanols for their use as solvents in two-liquid-phase biotransformations. Although 1-decanol showed an about 10-fold higher toxicity to the cells than 1-octanol, the cells were able to adapt completely to 1-decanol only and could not be adapted in order to grow stably in the presence of a second phase of 1-octanol. The main explanation for this observation can be seen in the higher water and membrane solubility of 1-octanol. The hydrophobicity (log P) of a substance correlates with a certain partitioning of that compound into the membrane. Combining the log P value with the water solubility, the maximum membrane concentration of a compound can be calculated. With this simple calculation, it is possible to predict the property of an organic chemical for its potential applicability as a solvent for two-liquid-phase biotransformations with solvent-tolerant P. putida strains. Only compounds that show a maximum membrane concentration of less than 400 mM, such as 1-decanol, seem to be tolerated by these bacterial strains when applied in supersaturating concentrations to the medium. Taking into consideration that a solvent for a two-liquid-phase system should possess partitioning properties for potential substrates and products of a fine chemical synthesis, it can be seen that 1-decanol is a suitable solvent for such biotransformation processes. This was also demonstrated in shake cultures, where increasing amounts of a second phase of 1-decanol led to bacteria tolerating higher concentrations of the model substrate 3-nitrotoluene. Transferring this example to a 5-liter-scale bioreactor with 10% (vol/vol) 1-decanol, the amount of 3-nitrotoluene tolerated by the cells is up to 200-fold higher than in pure aqueous medium. The system demonstrates the usefulness of two-phase biotransformations utilizing solvent-tolerant bacteria.     

Integrated bioproduction and extraction of 3-methylcatechol

Pseudomonas putida MC2 is a solvent-tolerant strain that accumulates 3-methylcatechol. In aqueous media, 10 mM of 3-methylcatechol was produced and production was limited by 3-methylcatechol toxicity to the biocatalyst. Production levels increased by introduction of a second, organic phase that provides the substrate toluene and extracts the product from the culture medium. Octanol was shown to be an appropriate second phase with respect to tolerance of the strain for this solvent and with respect to partitioning of both substrate and product. Per unit of overall reactor volume (octanol and water), best results were obtained with 50% (v/v) of octanol: an overall 3-methylcatechol concentration of 25 mM was reached with 96% of the product present in the octanol phase. These product concentrations are much higher than in aqueous media without organic solvent, indicating that biocatalysis in an organic/aqueous two-phase system is an improved set-up for high production levels of 3-methylcatechol.     

Reaction Medium Selection for An Enzymatic Peptide Synthesis in An Aqueous-Organic Two-Phase System

Efficient development of enzymatic synthesis in two-phase systems is closely related with appropriate selection of the reaction medium (especially the solvent and phase ratio). A selection procedure based on the calculation of the theoretically allowable conversion and product concentration is presented and applied to a peptide synthesis using papain. For the synthesis of the dipeptide Boc-Gly-Phe-OMe, the operating conditions have been determined, and the two-phase system to be used has been successfully selected (with trichloroethylene being the best solvent).     

2-Heptanone Production by Spores of Penicillium roquefortii in a Water-Organic Solvent Two-Phase System

The production of 2-heptanone from octanoic acid may be performed by free and entrapped spores of Penicillium roquefortii in a water-organic solvent two phase system.

An industrial, isoparafflnic solvent, i.e. Hydrosol IP 230 O.S., which may be considered as tetradecane, is well suited for the process. Activities nearly double those achieved with aqueous systems are observed using an initial fatty acid content in the organic layer close to 100 mM and a ratio of the volume of the organic phase to the total volume of the medium of 0.88. The presence of the solvent allows a better recovery of the metabolite by lowering its activity coefficient.

Fed-batch experiments performed in an aerated, stirred reactor show that the bioconversion may proceed in the two-phase system for at least 300 h. These conditions allow conversion of 750 mM (108 g · 1^-1) fatty acid, and production of 600 mM (68.5 g · 1^-1) 2-heptanone.     

双水相电泳分离蛋白质的研究

近几年来,随着生物技术的迅速发展,制备型电泳技术的研究得到了重视。然而由于技术上的原因,大规模的制备型电泳技术的研究还未能取得突破。阻碍电泳放大的一个主要问题是由于电加热作用而导致的热对流对电泳分离的破坏。为解决这一问题,人们提出了许多方法。例如,在太空的微重力环境下进行电泳,应力稳定自由流动电泳,循环等电聚焦和区带电泳,色谱电泳和等电膜等电聚焦等。这些方法在电泳放大上都取得了一定的进展,但各有其局限性。最近,Clark提出利用双水相的液液界面阻止热对流的设想,为开发大规模的制备型电泳技术开辟了一条新途径、Raghava Rao等在两种双水相体系上施加电场后成倍地缩短了分相时间。Levine和Bier采用U型管电泳装置研究了双水相体系中血红蛋白的电泳迁移率,观测到界面有阻滞作用。Clark在柱型电泳装置中进行了一组双水相萃取肌红蛋白的简单实验。在10mA的恒电流下电泳40min之后,肌红蛋白的分配系数为7.5,而当电场反向后,分配系数变为0.04,界面阻力并不显著,两者结论并不一致。