Biotransformation of l‐menthol by twelve isolates of soil‐borne plant pathogenic fungi (Rhizoctonia solani) and classification of fungi

The microbial transformation of l‐menthol ( 1 ) was investigated by using 12 isolates of soil‐borne plant pathogenic fungi, Rhizoctonia solani (AG‐1‐IA Rs24, Joichi‐2, RRG97‐1; AG‐1‐IB TR22, R147, 110.4; AG‐1‐IC F‐1, F‐4, P‐1; AG‐1‐ID RCP‐1, RCP‐3, and RCP‐7) as a biocatalyst. Rhizoctonia solani F‐1, F‐4 and P‐1 showed 89.7–99.9% yields of converted product from 1 , RCP‐1, RCP‐3, and RCP‐7 26.0–26.9% and the other isolates 0.1–12.0%. In the cases of F‐1, F‐4 and P‐1, substrate 1 was converted to (?)‐(1S,3R,4S,6S)‐6‐hydroxymenthol ( 2 ), (?)‐(1S,3R,4S)‐1‐hydroxymenthol ( 3 ) and (+)‐(1S,3R,4R,6S)‐6,8‐dihydroxymenthol ( 4 ), which was a new compound. Substrate 1 was converted to 2 and/or 3 by RRG97‐1, 110.4, RCP‐1, RCP‐3 and RCP‐7. The structures of the metabolic products were elucidated on the basis of their spectral data. In addition, metabolic pathways of the biotransformation of 1 by Rhizoctonia solani are discussed. Finally, from the main component analysis and the differences in the yields of converted product from 1 , the 12 isolates of Rhizoctonia solani were divided into three groups based on an analysis of the metabolites. Copyright © 2003 Society of Chemical Industry     

生物柴油制备方法的应用研究进展

生物柴油以其优良的环境友好性和可再生性引起广泛关注,但较高的生产成本是其商业化生产和应用的障碍之一。综述了生物柴油的化学转酯化法和以游离脂肪酶、固定化脂肪酶、全细胞为催化剂的生物转酯化法的工业研究进展,同时还指出了采用生物转酯化法制备生物柴油时面临的一些问题。     

卤过氧化物酶在有机合成中的应用研究进展

卤过氧化物酶是一种特殊的过氧化物酶,可以催化多种手性化合物的合成。自上世纪60年代被发现以来,卤过氧化物酶在有机合成中的应用一直是研究热点。综述了卤过氧化物酶的种类及其在手性有机合成中的应用,重点关注了卤化、氧化、环氧化、磺化氧化等反应,并讨论了目前在该领域所面临的问题及今后的发展趋势。     

A highly stable whole‐cell biocatalyst for the enantioselective synthesis of optically active alpha‐hydroxy acids

BACKGROUND: Biocatalysts have gained increasing attention because of their inherent advantages over chemical catalysts. However, the poor operational stability has always prevented their broad application. In this study, (R)‐mandelic acid was chosen as a model compound of alpha‐hydroxy acids. The objective was to obtain a new biocatalyst with desired operational stability for the preparation of (R)‐mandelic acid as well as other optically pure alpha‐hydroxy acids of pharmaceutical importance. RESULTS: Using a two‐step screening strategy, Saccharomyces ellipsoideus GIM2.105 was selected as an effective biocatalyst with high enantioselectivity and remarkable operational stability. After 20 cycles of reuse, whole cells of S. ellipsoideus GIM2.105 maintained its activity, and no obvious decrease in conversion or enantiomeric excess (ee) was observed. Furthermore, effects of various reaction parameters, including pH, temperature, co‐substrate (type, concentration), substrate concentration and reaction time, on the bioreduction were studied. Under optimal conditions, (R)‐mandelic acid and four substituted aromatic (R)‐alpha‐hydroxy acids were prepared in high ee (95–>99%) and good conversion (>90%). CONCLUSION: The high enantioselectivity, remarkable operational stability and mild reaction conditions showed S. ellipsoideus GIM2.105 to be an economical biocatalyst with great industrial application potential for the production of optically active alpha‐hydroxy acids. Copyright © 2009 Society of Chemical Industry     

Biotransformation of isoflavones by Aspergillus niger as biocatalyst

Biotransformation of the isoflavones, 6,7,4′‐trimethoxyisoflavone ( 1 ) and 5,7,4′‐trimethoxyisoflavone ( 2 ) by Aspergillus niger was investigated. Compound 1 was transformed to 4′‐hydroxy‐6,7‐dimethoxyisoflavone ( 3 ) and 2 to 4′‐hydroxy‐5,7‐dimethoxyisoflavone ( 4 ). This suggested that 1 and 2 were demethylated at the C‐4′ position with regioselectivity by Aspergillus niger. Copyright © 2006 Society of Chemical Industry     

A comparative study of a fluidised bed reactor and a gas lift loop reactor for the IBE process: Part I. Reactor design and scale down approach

For the continuous production of isopropanol-butanol mixtures by immobilised Clostridium spp. (the IBE process) two reactor types were studied: a fluidised bed reactor with liquid recycling (FBR) and an external loop gas lift reactor (GLR). A large scale design (50–65 m³) was made for both reactors. A regime analysis, by evaluating the time constants for e.g. mixing and conversion, identified the ruling regime. Via the scale down approach two representative model reactors were developed: a 10 dm³ FBR reactor (H/D=25, D=0.08 m) and a 15 dm³ external loop GLR (H/D = 12.5, D_r=D_d=0.08 m). For both reactors the hydrodynamical behaviour and the total reactor performance were studied and are described in parts II and III of this study.     

纤维素酶的应用研究进展

植物纤维原料是地球上极为丰富、廉价而又可再生的资源,它的利用一直是国内外的研究热点。纤维素酶是一种高活性生物催化剂,是一组能够降解纤维素生成葡萄糖的酶的总称,在食品、饲料、酿酒、纺织、中药提取和造纸等众多的工业领域有广泛的应用价值。     

Analytical effectiveness calculations concerning the formation of an inhibitive fermentation product associated with growth of biomass films immobilized in or around carriers

A reaction engineering model is presented for the bioproduction of chemicals associated with the growth of immobilized biomass in or around carriers. The model describes multiple-substrate diffusion limitations and first-order growth inhibition by one of the products. Analytical solutions are presented for intra-biofilm substrate and product concentrations, active biofilm thickness, biocatalyst effectiveness factor and degree of catalyst utilization. Simple criteria for optimal catalyst design are derived. Where applicable, the presented explicit analytical solutions for the biocatalyst effectiveness factor are much more convenient to incorporate into a macro-reactor model than the numerical alternatives.