氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸

3-羟基丙酸是一种潜在的重要化工产品,可作为中间体合成多种有经济价值的工业用化合物。文中利用氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸。首先在50 mL摇瓶中(转化体系为10 mL)考察细胞加入量、底物和产物浓度等对催化反应的影响。在此基础上,在2 L鼓泡塔中(转化体系为1 L),采取适当的补料方式和生物转化与分离相耦合的手段解除抑制,以提高目标产物终浓度。结果表明:高底物和产物浓度通过降低反应初速度抑制转化的进行,并确定了最佳催化反应条件为6 g/L菌体量,pH 5.5。利用流加补料方式维持反应体系中底物浓度在15~20 g/L,经过60 h的反应,3-羟基丙酸的浓度达到60.8 g/L,生产强度为1.0g/(L.h),转化率为84.3%。采用生物转化与分离相耦合的方法,经过50 h的转化反应,3-羟基丙酸的总产量达76.3 g/L,生产强度为1.5 g/(L.h),转化率83.7%。研究结果对利用氧化葡萄糖酸杆菌的不完全氧化醇类化合物特性实现其在工业生物催化中的应用具有一定的指导意义。     

Trends and innovations in industrial biocatalysis for the production of fine chemicals

Biocatalysis has become an established technology for the industrial manufacture of fine chemicals. In recent years, a multitude of chemical companies have embraced biocatalysis for the manufacture of desired stereoisomers, and new or improved methods for the synthesis of enantiomerically pure alpha- and beta-amino acids, amines, amides, peptides, nitriles, alcohols, organic acids and epoxides have emerged. Furthermore, the selectivity and mild operational conditions of biocatalysts are increasingly applied in industry to modify complex target molecules. These recent innovations in the manufacture of industrial fine chemicals using biocatalysis are discussed from an industrial perspective.     

Immobilization of <Emphasis Type="Italic">Acetobacter</Emphasis> sp. CGMCC 8142 for efficient biocatalysis of 1, 3-propanediol to 3-hydroxypropionic acid

3-hydroxypropionic acid (3-HP) is an important chemical platform organic in material industry, daily chemical industry and biomedicine field due to its numerous valuable derivatives. However, no mature methods have been established in the synthesis industry for direct large scale production. The bacterium Acetobacter sp. CGMCC 8142 with high efficiency of alcohols oxidation property was immobilized for biosynthesis of 3-HP from 1, 3-propanediol (1, 3-PDO). Parameter values in mass transfer modeling indicated that mass transfer of immobilized biocatalysts affected the oxidation reaction (the internal effectiveness factor η _i < 1) but was not the rate-limiting step if Thiele modulus 1 > φ > 0.3. The optimal immobilization conditions for 3-HP biocatalysis was sodium alginate 40 g/L, gel beads diameter 1 mm, cross-linkage time 2 h and 0.1mM FeCl₂. Immobilized cells showed promising substrate tolerance, pH stability, thermal stability and storability. After 5 cycles of reaction, 3-HP molar yield of immobilized beads was retained to 80.26%, and 66.95 g/L 3-HP were produced from 70 g/L 1, 3-PDO. The biocatalysis process of immobilized cells introduced in this study may provide an economical and efficiency alternative route for practical production of 3-HP.     

Flows of Chemical Risk Information in the Consumer Paint Product Chain

In this study the flows of chemical risk information for paint as a consumer product were investigated from a product chain perspective. The main method of research involved semi‐structured interviews with Swedish manufacturers of paint and chemicals. In addition, retailers and consumers were interviewed. The flows of chemical risk information between actors within (e.g., manufacturers, retailers, and consumers) and outside (e.g., industry associations and regulators) the paint product chain are described. Because the European chemical legislation REACH (Registration, Evaluation, Authorization and restriction of CHemicals) plays a large role in the management of chemical risk information at companies, some consequences of REACH on actors in the paint product chain are described. Examples of such consequences are that importing of chemicals from non–European Union (EU) countries may be discouraged and that some low‐volume chemicals may no longer be produced. However, manufacturers do not yet see these consequences as impediments to innovation. The results of this work show that chemical risk information is most comprehensive during the manufacturing steps of the product chain. This is due not only to tradition and industry initiatives, but also to REACH and other legislation. The results also illustrate the need for evaluation of how chemical risk information is used in different contexts and the importance of directing the right information at the right target group. Following legislative development, more specialized information is required in the safety data sheet (SDS), and because of this many manufacturers find it necessary to create simplified safety sheets that make the most pertinent safety and hazard information easily accessible to individuals that handle the chemicals in their factories. The study found that in creating the simplified safety sheets, the content and use of chemical risk information is evaluated and adjusted for presentation to this particular target group. It is evident that the Swedish Paint and Printing Ink Makers Association plays an important role in the interpretation of legal requirements and even in agreements for providing information that exceeds legal requirements.     

On oxygen limitation in a whole cell biocatalytic Baeyer-Villiger oxidation process

In this article, a recombinant cyclohexanone monooxygenase (CHMO), overexpressed in Escherichia coli has been used to study the oxidation of bicyclo[3.2.0]hept-2-en-6-one to its two corresponding lactones at very high enantiomeric excess. The reaction is a useful model for the study of biocatalytic oxidations to create optically pure molecules. The major limitations to a highly productive biocatalytic oxidation in this case are oxygen supply, product inhibition, and biocatalyst stability. In this article, we investigate the effects of whole cell biocatalyst concentration on the rate of reaction at a range of scales from shake flasks to 75 L bioreactors. At low cell concentrations (<2 g(dcw)/L) the maximum specific rate (0.65 g/g(dcw).h) is observed. However, at higher cell concentrations (> 2 g(dcw)/L), the reaction becomes oxygen limited and both the specific rate and absolute rate decrease with further increases in cell concentration. The role of oxygen limitation in reducing the rate of reaction with scale was investigated by increasing the maximum oxygen transfer rate in the reactor at a high cell concentration and observing the increase in product formation rate. We propose a qualitative model demonstrating the relationship between oxygen limitation, biocatalyst concentration, and the rate of reaction. This conceptual model will be a useful guide in the industrial scale-up of whole cell mediated Baeyer-Villiger biocatalysis.     

Enhancement of substrate concentration in microbial stereoinversion through one-pot oxidation and reduction by aqueous two-phase system

An extractive biocatalytic method of aqueous two-phase system was employed for stereoinversing (R)-1-phenyl-1,2-ethanediol into (S)-1-phenyl-1,2-ethanediol by Candida parapsilosis CCTCC M203011. It was observed that substrate and product inhibitions in microbial stereoinversion through one-pot oxidation and reduction were removed efficiently by extractive biocatalysis in aqueous two-phase system with PEG 4000/phosphate potassium system, and that the substrate concentration was enhanced from 15 to 30 g/L with product optical purity of 99.02% e.e. and yield of 90% after 60 h. Simultaneously, it was observed that change in cell morphology impedes the further enhancement of substrate concentration in this system but can be reversibly changed after stereoinversion or cultivation in systems without PEG.     

A novel synthesis of iminodiacetic acid: biocatalysis by whole Alcaligenes faecalis ZJB-09133 cells from iminodiacetonitrile

Iminodiacetic acid (IDA) has been widely used as an important intermediate in the fine chemical industry. In this study, a novel synthesis route of IDA from iminodiacetonitrile by whole microorganisms was investigated. A strain with the capability of producing nitrilase, ZJB-09133, was isolated and identified, and later named Alcaligenes faecalis ZJB-09133. In addition, the detailed biocatalysis of iminodiacetonitrile to produce IDA using ZJB-09133 was investigated. The results showed that the conversion reached 65.3% in Na(2)HPO(4)-NaH(2)PO(4) buffer of pH 8.0 under the following conditions: cells in the amount of 0.075-g DCW/L, 1.5% substrate, conversion time of 8 h, and a reaction temperature of 35°C. To the best of our knowledge, this is the first time that the production of IDA using a biocatalysis method has been reported.     

冲击生物技术第三次浪潮

工业生物催化是继医药、农业之后的生物技术第三次浪潮。从21世纪化学工业发展的前沿特点,介绍生物催化加工过程及生产方式,主要解决传统产业改造和新的应用领域的开拓,提出发展生物催化产业的策略和加强支持力度的建设。     

Biotransformation of β‐hydroxypyruvate and glycolaldehyde to l‐erythrulose by Pichia pastoris strain GS115 overexpressing native transketolase

Transketolase is a proven biocatalytic tool for asymmetric carbon‐carbon bond formation, both as a purified enzyme and within bacterial whole‐cell biocatalysts. The performance of Pichia pastoris as a host for transketolase whole‐cell biocatalysis was investigated using a transketolase‐overexpressing strain to catalyze formation of l ‐erythrulose from β‐hydroxypyruvic acid and glycolaldehyde substrates. Pichia pastoris transketolase coding sequence from the locus PAS_chr1‐4_0150 was subcloned downstream of the methanol‐inducible AOX1 promoter in a plasmid for transformation of strain GS115, generating strain TK150. Whole and disrupted TK150 cells from shake flasks achieved 62% and 65% conversion, respectively, under optimal pH and methanol induction conditions. In a 300 μL reaction, TK150 samples from a 1L fed‐batch fermentation achieved a maximum l ‐erythrulose space time yield (STY) of 46.58 g L^?1 h^?1, specific activity of 155 U , product yield on substrate (Y_p/s) of 0.52 mol mol^?1 and product yield on catalyst (Y_p/x) of 2.23g . We have successfully exploited the rapid growth and high biomass characteristics of Pichia pastoris in whole cell biocatalysis. At high cell density, the engineered TK150 Pichia pastoris strain tolerated high concentrations of substrate and product to achieve high STY of the chiral sugar l ‐erythrulose. © 2017 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 34:99–106, 2018     

Inhibition of acetate accumulation leads to enhanced production of (R,R)-2,3-butanediol from glycerol in Escherichia coli

This work describes the production of (R,R)-2,3-butanediol in Escherichia coli using glycerol by metabolic engineering approaches. The introduction of a synthetic pathway converting pyruvate to (R,R)-2,3-butanediol into wild-type E. coli strain BW25113 led to the production of (R,R)-2,3-butanediol at a titer of 3.54?g/l and a yield of 0.131?g product/g glycerol (26.7?% of theoretical maximum) with acetate (around 3.00?g/l) as the dominant by-product. We therefore evaluated the impacts of deleting the genes ackA or/and poxB that are responsible for the major by-product, acetate. This increased production of (R,R)-2,3-butanediol to 9.54?g/l with a yield of 0.333?g product/g glycerol (68.0?% of theoretical maximum) in shake flask studies. The utilization of low-priced crude glycerol to produce value-added chemicals is of great significance to the economic viability of the biodiesel industry.     

Fermentation of sweet whey by ethanologenic Escherichia coli

Whey, an abundant byproduct of the dairy industry, contains large amounts of protein and lactose which could be used for fuel ethanol production. We have investigated a new organism as a candidate for such fermentations: recombinant Escherichia coli containing the genes encoding the ethanol pathway from Zymomonas mobilis. The highest level of ethanol achieved, 68 g/L, was produced after 108 hours in Luria broth containing 140 g lactose/L. Fermentations of lower lactose concentrations were completed more rapidly with approximately 88% of theoretical yields. Reconstituted sweet whey (60 g lactose/L)was fermented more slowly than lactose in Luria broth requiring 144 hours to produce 26 g ethanol/L. Supplementing sweet whey with a trace metal mix and ammonium sulfate reduced the required fermentation time to 72 hours and increased final ethanol concentration (28 g ethanol/L). By adding proteinases during fermentation, the requirement for ammonia was completely eliminated, and the rate of fermentation further improved (30 g ethanol/L after 48 hours). This latter incresed in rate of ethanol production and ethanol yield are presumed to result from incorporation of amino acids released by hydrolysis of whey proteins. The fermentation of sweet whey by ethanologenic E. coil reduced the nonvolatile residue by approximately 70%. This should reduce biological oxygen demand and reduce the cost of waste treatment. Whey supplemented with trace metals and small amounts of proteinase may represent an economically attractive feedstock for the production of ethanol and other useful chemicals.     

Altered glucose transport and shikimate pathway product yields in E. coli

Different glucose transport systems are examined for their impact on phosphoenolpyruvate availability as reflected by the yields of 3-dehydroshikimic acid and byproducts 3-deoxy-d-arabino-heptulosonic acid, 3-dehydroquinic acid, and gallic acid synthesized by Escherichia coli from glucose. 3-Dehydroshikimic acid is an advanced shikimate pathway intermediate in the syntheses of a spectrum of commodity, pseudocommodity, and fine chemicals. All constructs carried plasmid aroF(FBR) and tktA inserts encoding, respectively, a feedback-insensitive isozyme of 3-deoxy-d-arabino-heptulosonic acid 7-phosphate synthase and transketolase. Reliance on the native E. coli phosphoenolpyruvate:carbohydrate phosphotransferase system for glucose transport led in 48 h to the synthesis of 3-dehydroshikimic acid (49 g/L) and shikimate pathway byproducts in a total yield of 33% (mol/mol). Use of heterologously expressed Zymomonas mobilis glf-encoded glucose facilitator and glk-encoded glucokinase resulted in the synthesis in 48 h of 3-dehydroshikimic acid (60 g/L) and shikimate pathway byproducts in a total yield of 41% (mol/mol). Recruitment of native E. coli galP-encoded galactose permease for glucose transport required 60 h to synthesize 3-dehydroshikimic acid (60 g/L) and shikimate pathway byproducts in a total yield of 43% (mol/mol). Direct comparison of the impact of altered glucose transport on the yields of shikimate pathway products synthesized by E. coli has been previously hampered by different experimental designs and culturing conditions. In this study, the same product and byproduct mixture synthesized by E. coli constructs derived from the same progenitor strain is used to compare strategies for increasing phosphoenolpyruvate availability. Constructs are cultured under the same set of fermentor-controlled conditions.     

New opportunities for biocatalysis: driving the synthesis of chiral chemicals

Various biocatalytic methods have been developed for the synthesis of chiral chemicals, which have made their synthesis more environmentally friendly and product-specific. New opportunities for biocatalysis, including new scientific developments in genomics and protein engineering technologies, novel process developments and the increased availability of useful enzymes, offer many possibilities for the manufacture of new chiral compounds and deliver greener and economically competitive processes. In this review, new opportunities for biocatalysis in the preparation of chiral molecules are outlined and highlighted.     

A window into biocatalysis and biotransformations

Eight papers were presented in this year's symposium "Advances in Biocatalysis" at the 232nd ACS National Meeting, accentuating the most recent development in biocatalysis. Researchers from both industry and academia are addressing several fundamental problems in biocatalysis, including the limited number of commercially available enzymes that can be provided in bulk quantities, the limited enzyme stability and activity in nonaqueous environments, and the permeability issue and cell localization problems in whole-cell systems. A trend that can be discerned from these eight talks is the infusion of new tools and technologies in addressing various challenges facing biocatalysis. Nanotechnology, bioinformatics, cellular membrane engineering and metabolic engineering (for engineering whole-cell catalysts), and protein engineering (to improve enzymes and create novel enzymes) are becoming more routinely used in research laboratories and are providing satisfactory solutions to the problems in biocatalysis. Significant progress in various aspects of biocatalysis from discovery to industrial applications was highlighted in this symposium.     

Human Health Impact as a Boundary Selection Criterion in the Life Cycle Assessment of Pultruded Fiber Reinforced Polymer Composite Materials

The human health impact of fiber reinforced polymer (FRP) composite materials manufactured by the pultrusion industry is not fully understood. In particular, it is unclear whether the human health impact of toxic chemicals present in low concentrations in fire retardant pultruded FRP materials is disproportionately high. This impact may be an important criterion when making boundary selection decisions in the life cycle assessment (LCA) of these materials. The North American pultrusion industry was surveyed to determine resin mix concentration levels and workplace inhalation toxicity exposure levels. LCAs were then conducted on three building panel resin mixes to determine whether the human health impact of toxic chemicals used in the mixes was low enough to exclude the chemicals from the life cycle inventory (LCI) boundary. The first resin mix represented a typical pultruded product, the second mix removed toxic chemicals present in small concentrations, and the third mix replaced toxic chemicals present in small concentrations with a nontoxic chemical. Results showed that toxicity levels fell below exposure limits and no significant difference in human health impact existed among the LCAs. The research concludes that human health impact is a useful criterion when defining an LCI boundary. Toxic chemicals present in small concentrations in pultruded FRP materials may be excluded from the LCI boundary, as their human health impacts are low. Because these levels are marginal in North American pultrusion factories, no changes in resin mixes are recommended for the pultrusion industry.     

生物催化与生物转化研究进展

由于生物催化过程具有高效、高选择性、条件温和、环境友好等优点,因此成为可持续发展过程中替代和拓展传统有机化学合成的重要方法。近两年的进展集中于新生物催化剂的发现和改造,以及将生物催化和生物转化应用于工业过程的探索,包括开发新的反应体系,新的固定化方法等。可以预见,在医药中间体等高附加值化工产品的生产过程中,生物催化和生物转化的应用将呈现加速增长趋势。     

Industrial chemicals from fermentation

This paper examines the potential for carbohydrate fermentation as an alternative process technology for bulk organic chemicals. Major limitations restricting the broadening of scope for fermentation chemicals are identified. These involve the high process energy requirements in pretreating abundant cellulosic feedstocks, low overall conversion, low weight yield and limited product applications of directly biosynthesized fermentation chemicals. The new development directions for chemicals derived directly and indirectly from carbohydrate fermentation are reviewed. The significance of their potential impact on the evolving organic chemical industry is projected.     

A novel framework for the cell-free enzymatic production of glucaric acid

Glucaric acid (GlucA) is a valuable glucose-derived chemical with promising applications as a biodegradable and biocompatible chemical in the manufacturing of plastics, detergents and drugs. Recently, there has been a significant focus on producing GlucA microbially (in vivo) from renewable materials such as glucose, sucrose and myo-inositol. However, these in vivo GlucA production processes generally lack efficiency due to toxicity problems, metabolite competition and suboptimal enzyme ratios. Synthetic biology and accompanying cell-free biocatalysis have been proposed as a viable approach to overcome many of these limitations. However, cell-free biocatalysis faces its own limitations for industrial applications due to high enzyme costs and cofactor consumption. We have constructed a cell-free GlucA pathway and demonstrated a novel framework to overcome limitations of cell-free biocatalysis by i) the combination of both thermostable and mesophilic enzymes, ii) incorporation of a cofactor regeneration system and iii) immobilisation and recycling of the pathway enzymes. The cell-free production of GlucA was achieved from glucose-1-phosphate with a titre of 14.1 ± 0.9 mM (3.0 ± 0.2 g l⁻¹) and a molar yield of 35.2 ± 2.3% using non-immobilised enzymes, and a titre of 8.1 ± 0.2 mM (1.70 ± 0.04 g l⁻¹) and a molar yield of 20.2 ± 0.5% using immobilised enzymes with a total reaction time of 10 h. The resulting productivities (0.30 ± 0.02 g/h/l for free enzymes and 0.170 ± 0.004 g/h/l for immobilised enzymes) are the highest productivities so far reported for glucaric acid production using a synthetic enzyme pathway.     

Efficacy of Curcuma aeruginosa rhizome and Adhatoda vasica plant extracts, on red spider mite, Tetranychus urticae in Livistona rotundifolia

Queen palm, Livistona rotundifolia foliage contributes greatly in export industry. Red spider mite (RSM) (Tetranychus urticae) infests on the foliage and reduces its affordable market quality. T. urticae is found in dry environment and is one of the phytophagous mite belongs to family Tetranychidae. Different chemicals such as 80% sulphur + Diazinon @ (50g+12ml/10L) are recommended against red spider mite, but these have lesser effect on this tiny mite. Since these chemicals are not environment friendly, Green Farms Ltd., in Sri Lanka prefers to use biological agents for mite management. Extracts of Curcuma aeruginosa rhizome and Adhatoda vasica plant parts were studied separately causing mortality on T. urticae. Field experiments were conducted to study the efficacy of C. aruginosa extract for controlling RSM on L. rotundifolia leaves. Curcuma aruginosa was tested at concentrations of 2, 5, 10, 15, 20 and 25 g/L and a control with equal amount of water. C aruginosa extracts of different concentrations were treated six times at five days interval on the palms separately. Living spider mites and eggs were pre-counted in marked leaves before applying C. aruginosa extracts. Next count was taken a day prior to next spraying. The result revealed that all the concentrations except 2 g/L were found to be effective compared to control. However there was no difference between the concentrations from 5 to 25 g/L. Hence C. aruginosa rhizome extract at its lowest concentration of 5 g/L is equally effective for the control of RSM on L. rotundifolia leaves. In another experiment extracts of Adhatoda vasica bark, leaves, and flower and water as control were applied thrice with three days interval. Pre treatment counting of living spider mites and eggs were taken in marked leaves. Post count was taken a day prior to next spraying. Third and forth counting were done after three days and four weeks from final spraying respectively. The results revealed that bark, flowers were found to be more effective compared to control. Flowers and bark were the best and hence there is no need of third sprayings as almost all the spider mites population were eradicated after second spraying. Flower extraction showed best performance until three months since final spraying. Flower and bark extracts showed higher acaricidal property and leaf showed moderate acaricidal property.     

Production of polymalic acid and malic acid by Aureobasidium pullulans fermentation and acid hydrolysis

Malic acid is a dicarboxylic acid widely used in the food industry and also a potential C4 platform chemical that can be produced from biomass. However, microbial fermentation for direct malic acid production is limited by low product yield, titer, and productivity due to end‐product inhibition. In this work, a novel process for malic acid production from polymalic acid (PMA) fermentation followed by acid hydrolysis was developed. First, a PMA‐producing Aureobasidium pullulans strain ZX‐10 was screened and isolated. This microbe produced PMA as the major fermentation product at a high‐titer equivalent to 87.6 g/L of malic acid and high‐productivity of 0.61 g/L h in free‐cell fermentation in a stirred‐tank bioreactor. Fed‐batch fermentations with cells immobilized in a fibrous‐bed bioreactor (FBB) achieved the highest product titer of 144.2 g/L and productivity of 0.74 g/L h. The fermentation produced PMA was purified by adsorption with IRA‐900 anion‐exchange resins, achieving a ～100% purity and a high recovery rate of 84%. Pure malic acid was then produced from PMA by hydrolysis with 2 M sulfuric acid at 85°C, which followed the first‐order reaction kinetics. This process provides an efficient and economical way for PMA and malic acid production, and is promising for industrial application. Biotechnol. Bioeng. 2013; 110: 2105–2113. © 2013 Wiley Periodicals, Inc.