Lignocellulolytic enzyme production on pretreated poplar wood by filamentous fungi

Gliocladium sp. TUB F-498, a wild strain of a lignocellulolytic fungus with a fast growth rate and enzyme production rate was selected as a potential in situ enzyme source for the bioprocessing of pretreated poplar wood (PPW) to ethanol in a simultaneous saccharification and fermentation process. TUB F-498 produced 77 filter paper units of cellulase activity and 246 IU of -glucosidase activity per g dry weight of substrate utilized, as compared with the highly successful mutant reference strain Trichoderma reesei Rut-C30, which produced 100 filter paper units and 92 IU per g dry weight substrate in a stirred-tank fermentation. TUB F-498 also produced more xylanase and endoglucanase activity than Rut-C30 on PPW in shake-flask fermentations.     

Production of ethanol from guava pulp by yeast strains

Guava pulp used for ethanol production by three yeast strains contained 10% (w/v) total sugars and was pH 4.1. Ethanol production at the optimum sugar concentration of 10%, at pH 4.1 and 30°C was 1.5%, 3.6% and 3.9% (w/v) by Saccharomyces cerevisiae MTCC 1972, Isolate-1 and Isolate-2, respectively, at 60 h fermentation. Higher sugar concentrations at 15 and 20% were inhibitory for ethanol production by all test cultures. The maximum production of ethanol at optimum natural sugar concentration (10%) of guava pulp, was 5.8% (w/v) at pH 5.0 by Isolate-2 over 36 h fermentation, which was only slightly more than the quantity of ethanol produced by Saccharomyces cerevisiae (5.0%) and Isolate-1 (5.3%) over 36 and 60h fermentation, respectively.     

The generation of metabolic energy by solute transport

Secondary metabolic-energy-generating systems generate a proton motive force (pmf) or a sodium ion motive force (smf) by a process that involves the action of secondary transporters. The (electro)chemical gradient of the solute(s) is converted into the electrochemical gradient of protons or sodium ions. The most straightforward systems are the excretion systems by which a metabolic end product is excreted out of the cell in symport with protons or sodium ions (energy recycling). Similarly, solutes that were accumulated and stored in the cell under conditions of abundant energy supply may be excreted again in symport with protons when conditions become worse (energy storage). In fermentative bacteria, a proton motive force is generated by fermentation of weak acids, such as malate and citrate. The two components of the pmf, the membrane potential and the pH gradient, are generated in separate steps. The weak acid is taken up by a secondary transporter either in exchange with a fermentation product (precursor/product exchange) or by a uniporter mechanism. In both cases, net negative charge is translocated into the cell, thereby generating a membrane potential. Decarboxylation reactions in the metabolic breakdown of the weak acid consume cytoplasmic protons, thereby generating a pH gradient across the membrane. In this review, several examples of these different types of secondary metabolic energy generation will be discussed.     

Changes in the intracellular concentrations of the adenosine phosphates and nicotinamide adenine dinucleotides ofSaccharomyces cerevisiae during batch fermentation

Significant changes in the intracellular concentrations of adenosine phosphates and nicotinamide adenine dinucleotides were observed during fermentation of grape must by three different strains ofSaccharomyces cerevisiae: S. cerevisiae var.cerevisiae, a typical fermentative yeast strain and two flor-veil-forming strains,S. cerevisiae var.bayanus andS. cerevisiae var.capensis. The intracellular concentration of ATP was always higher inS. cerevisiae var.cerevisiae than in the flor-veil-forming strains. NAD⁺ and NADP⁺ concentrations decreased at faster rates in the flor-veil-forming yeasts than in the other yeast but NADH concentration was the same in all yeasts for the first 10 days of fermentation. NADPH concentration was always lower inS. cerevisiae var.cerevisiae than in the other yeasts and this yeast also showed higher rates of growth and fermentation during the early stages of the fermentation and the presence of non-viable cells at the end of fermentation. In contrast, the flor-veil-forming strains maintained growth and fermentation capabilities for a relatively long time and viable cells were present throughout the entire fermentation process (31 days).The authors are with the Department of Microbiology, Faculty of Sciences, University of Cordoba, Avda. San Alberto Magno s/n, 14004-Córdoba, Spain     

Solid-state fermentation of sugarcane bagasse with Flammulina velutipes and Trametes versicolor

The mushroom Flammulina velutipes and the white-rot fungus Trametes versicolor were cultivated separately on sugarcane bagasse for 40 days. Trametes versicolor produced laccase and manganese-peroxidase activities, showing a simultaneous degradation of lignin and holocellulose. However, only phenoloxidase activity was found with Flammulina velutipes. A preferential degradation of lignin was detected in F. velutipes, which exhibited a greater reduction in the ratio of weight loss to lignin loss than T. versicolor. A decrease in the syringyl/guaiacyl ratio observed with both fungi indicated the preferential degradation of non-condensed (syringyl-type) lignin units. An increase in the relative abundance of aromatic carboxylic acids suggested that the oxidative transformation of lignin unit side-chains was occurring. This was more noticeable with Flammulina velutipes than with T. versicolor.     

Cellulase production by the edible mushroom Volvariella diplasia

Volvariella diplasia produced cellulolytic enzymes (550 U CM-cellulase and 69 U filter-paper cellulase/l) when grown in shake culture at pH 5.4 and 28°C with 0.5% cellulose powder as carbon source. Alkali-treated as well as untreated cellulosic substrates were hydrolysed by both enzymes (sp. act. 2.75 U/mg protein), with cellobiose and glucose as the end products.The author is with NCIM, Division of Biochemical Sciences, National Chemical Laboratory, Pune 411 008, Maharashtra, IndiaNCL Communication No. 6168.     

Solid-state fermentation of carob pods byAspergillus niger for protein production: effect of particle size

Two strains ofAspergillus niger were cultured in solid-state fermentation system on carob pods ground from 1.25 to 8 mm diam. A particle size of 2.5 mm gave the highest protein content of the final product (20%, w/w) and 52% of the total soluble carbohydrates were utilized. The total tannin concentration of the carob pods decreased by 83% in 4 days of fermentation.T. Smail and O. Salhi are with the Laboratory of Microbiology, U.R.B.A.F., Institute of Biology, Tizi-Ouzou University, Algeria. J.S. Knapp is with the Department of Microbiology, The University of Leeds, Leeds LS2 9JT, UK;     

柠檬酸发酵过程的动力学

发酵动力学是微生物培养过程研究中的一个重要部分,它让人们从理论和定量的角度了解和分析微生物的培养过程,是过程设计和控制的基础．柠檬酸发酵过程的动力学．Chemiel^[1]、Kristiansen^〔2〕、Khan^〔3〕、Rohr^〔4〕、Vaija^〔5〕等曾作过研究。本文在考察前人工作的基础上．结合实验研究．进行如下探索。     

鳜鱼的耗氧率及其池塘养殖

本文较详细地报道了鳜鱼的耗氧率和窒息点,并对鳜鱼和作其饲料的鱼同池饲养的可能性进行了探讨。结果表明,鳜鱼耗氧量和体重正相关（ｒ＝０．９９）,耗氧率与体重反相关（ｒ＝－０．９７）;在水温２０℃,鱼种耗氧率约为０．１４ｍｇ／ｇ．ｈ．,成鱼约为０．１２ｍｇ／ｇ．ｈ．;耗氧量和耗氧率均与水温正相关（ｒ＝０．９０,ｒ＝０．９４）,水温１３—３０℃时,体重２３０±１１．７ｇ的鳜鱼。耗氧量为１４．３１—４２．１３ｍｇ／尾。ｈ．,耗氧率为０．０５９—０．１７５ｍｇ／ｇ．ｈ．;鳜鱼耗氧率昼夜变化与家鱼相反,黄昏至凌晨是高峰期,为０．１２—０．１５ｍｇ／ｇ．ｈ．（Ｔ＝２０℃）,白天是低谷期,为０．０７—０．１０ｍｇ／ｇ．ｈ;;鳜鱼的窒息点与家鱼类较接近,变化范围为０．４５—０．７６ｍｇ／Ｌ;鳜鱼和作其饲料的鱼在同一池塘中饲养,既可持续不断地提供鳜鱼充足的适口饵料,又简单易行,成本低,效益高,有较大的价值。     

Spatial distribution of seston in an artificially mixed system

Seston size distribution was determined with a Coulter Counter to investigate seston interaction and its effects on phytoplankton production. Spatial distribution patterns of the non-productive component of the seston were as complex as those commonly associated with algae. Seston might interact influencing production by changes in optical depth, abrasive actions and nutrient adsorption.