Production and characterization of ligninolytic enzymes ofBjerkandera adusta grown on wood meal/wheat bran culture and production of these enzymes using a rotary-solid fermenter

Manganese peroxidase (MnP) and lignin peroxidase (LiP) were produced by growing a white-rot fungusBjerkandera adusta statically, on a wood meal/wheat bran culture in flasks. MnP and LiP reached their maximum activity after 6 and 19 days of inoculation, respectively. Both MnP and LiP are thought to be important enzymes in lignin biodegradation byB. adusta. Ion exchange chromatography showed thatB. adusta produced a single LiP and a single MnP enzyme in wood meal/wheat bran culture. These enzymes were separated and characterized. The molecular weight of MnP was 46,500 with a pl of 3.9. The molecular weight of LiP was estimated to be 47,000 with a pl of 3.5. Spectral analysis demonstrated that both enzymes are heme proteins. Production of these enzymes was also achieved using a rotarysolid culture fermenter. MnP, LiP and veratryl alcohol oxidase were produced byB. adusta in the fermenter.     

Performances of a full-scale novel multiplate anaerobic reactor treating cheese whey effluent

A 450-m(3) multiplate anaerobic reactor (MPAR) has been started-up in April 1992 for treating wastewater (whey permeate and domestic wastewater) at the Nutrinor (Lactel) cheese factory in Chambord (Québec, Canada). The MPAR consists of four superimposed sections. The liquid flows upwards from one section to the next, while the gas is collected below each plate and evacuated through side-outlets. The wastewater is concurrently distributed at the bottom of the first, second, and third sections, as 50%, 33%, and 17% of the total influent stream, respectively. Granular anaerobic sludge at an initial concentration of 30 kg of volatile suspended solids (VSS) per cubic meter of reactor liquid volume was used to inoculate the reactor. Under normal operation of the factory, the chemical oxygen demand (COD) concentration of the influent ranged from 20 to 37 kg COD m(-3). The reactor organic loading rate (OLR) fluctuated between 9 and 14.7 kg COD m(-3) d(-1) for hydraulic retention times (HRT) maintained between 55 and 68 h. At the highest OLR, the MPAR showed an efficiency of 98% and 92% for soluble and total COD removal, respectively, and a methane production rate averaging around 4 m(3) m(-3) d(-1).Biomass-specific activities ranged between 7 and 51, 1.3 and 8.5, 5.3 and 12.2, 60 and 119, and 119 and 211 mmol g(-1) VSS d(-1) for glucose, propionate, acetate, formate, and hydrogen, respectively. Average equivalent-diameter of the granules was around 0.65 mm. The MPAR reactor generally showed a large capacity for solid retention with a biomass content between 32 and 37 kg VSS m(-3). (c) 1995 John Wiley & Sons, Inc.     

Production of a lipopeptide antibiotic, surfactin, by recombinant Bacillus subtilis in solid state fermentation

Production of a lipopeptide antibiotic, surfactin, in solid state fermentation (SSF) on soybean curd residue, Okara, as a solid substrate was carried out using Bacillus subtilis MI113 with a recombinant plasmid pC112, which contains lpa-14, a gene related to surfactin production cloned at our laboratory from a wild-type surfactin producer, B. subtilis RB14. The optimal moisture content and temperature for the production of surfactin were 82% and 37 degrees C, respectively. The amount of surfactin produced by MI113 (pC112) was as high as 2.0 g/kg wet weight, which was eight times as high as that of the original B. subtilis RB14 at the optimal temperature for surfactin production, 30 degrees C. Although the stability of the plasmid showed a similar pattern in both SSF and submerged fermentation (SMF), production of surfactin in SSF was 4-5 times more efficient than in SMF. (c) 1995 John Wiley & Sons, Inc.     

抗菌肽的固相合成,分离纯化与构效关系的研究

应用手工固相ＤＣＣ／ＨＯＢｔ法合成ＣｅｃｒｏｐｉｎＢ、Ｓｈｉｖａｌ１、ＡＢＰ３、ＷＨＤ４种抗菌肽,各抗菌肽的Ｃ－端均为酰胺化,最终用ＨＰＬＣ分离纯化,这４种肽对大肠杆菌Ｋ１２Ｄ３１,野生型大肠杆菌,产气杆菌及４种植物病原菌青枯菌,临床致病理大肠杆菌,伤寒杆菌,硝酸盐杆菌均有明显的杀伤或抑制作用,对白血病细胞Ｋ５６０,肺癌细胞Ａ５４９也有杀伤作用,其中尤以ＷＨＤ杀伤作用最为明显,并用对其它３种肽不能     

Culturing the fairy shrimp Streptocephalus dichotomus Baird using livestock waste – a reclamation study

The present study describes a defined culturetechnique for the fairy shrimp, Streptocephalusdichotomus. It emphasizes reclamation of low-cost organiclive-stock waste(cow-dung), lime powder, and urea. These compounds wereused to enrich algal and diatom populations in themedium. These algae and diatoms were fed to filter feedingfairy shrimps to yield anostracanbiomass. A production of 262 ± 6 animals l^–1was obtained in an experimental tank compared to 36 ± 4animals l^–1 in the controls. Interestingly,the total number of clutches in experimentalfemales (12 ± 2), relative to the control (7 ± 1),increased too.     

光合细菌产氢条件的研究

从被有机物污染的土壤及水域中分离得到13株属于红螺菌科的光合细菌,对其在苹果酸、乳酸、葡萄糖、乙酸、丙酸及丁酸中的光致产氢现象进行了研究。最高产氢量为39.8ml·20ml菌液~(-1)·48h~(-1),产氢活性为7.8ml·g生物量~(-1)·h~(-1)”。底物对不同菌株的产氢量与产氢活性均具有影响,pH对产氢过程也有明显的作用,大于6000lx的光强度对提高产氢活性已无明显作用。固定化细胞在静态培养条件下也能提高产氢能力,但延长产氢时间的作用不明显。     

Removal of toluene in waste gases using a biological trickling filter

The removal of toluene from waste gas was studied in a trickling biofilter. A high level of water recirculation (4.7 m h^–1) was maintained in order to keep the liquid phase concentration constant and to achieve a high degree of wetting. For loads in the range from 6 to 150 g m^–3 h^–1 the maximum volumetric removal rate (elimination capacity) was 35±10 g m^–3 h^–1, corresponding to a zero order removal rate of 0.11±0.03 g m^–2 h^–1 per unit of nominal surface area. The surface removal was zero order above the liquid phase concentrations of approximately 1.0 g m^–3, corresponding to inlet gas concentrations above 0.7–0.8 g m^–3. Below this concentration the surface removal was roughly of first order. The magnitude of the first order surface removal rate constant, k_1A , was estimated to be 0.08–0.27 m h^–1 (k_1A a=24–86 h^–1). Near-equilibrium conditions existed in the gas effluent, so mass transfer from gas to liquid was obviously relatively fast compared to the biological degradation. An analytical model based on a constant liquid phase concentration through the trickling filter column predicts the effluent gas concentration and the liquid phase concentration for a first and a zero order surface removal. The experimental results were in reasonable agreement with a very simple model valid for conditions with an overall removal governed by the biological degradation and independent of the gas/liquid mass transfer. The overall liquid mass transfer coefficient, K_La, was found to be a factor 6 higher in the system with biofilm compared to the system without. The difference may be explained by: 1. Difference in the wetting of the packing material, 2. Mass transfer occurring directly from the gas phase to the biofilm, and 3. Enlarged contact area between the gas phase and the biofilm due to a rough biofilm surface.     

Methanogenic granular sludge formation in an upflow anaerobic sludge blanket reactir treating synthetic methanolic waste

A laboratory upflow anaerobic sludge blanket reactor, seeded with fine, suspended, bacterial floc with 1.76 g volatile suspended solids/l, was used to treat synthetic methanolic waste. After 180 days of continuous peration, granular sludge with discrete granules of 1 to 2 mm diam. was formed, with 52 g volatile suspended solids/l. Granules were brown, relatively soft and had a settling velocity of 1.61 cm/s. Extracellular polymeric matter extracted from the granular sludge had high carbohydrate content but low nucleic acid content. The ash of the granular sludge contained Na⁺, K⁺ and Mg²⁺ up to 15.0, 11.7 and 3.75 mg/g, respectively. Scanning and transmission electron microscopy revealed that the granular sludge was dominated by methanogens resembling Methanosarcina.The authors are with the Department of Environmental Engineering, Faculty of Engineering, Osaka University, 2-1 Yamadaoka, Suita, Osaka 565, Japan     

The microbiological basis of process control in methanogenic fermentation of soluble wastes

The essential requirement for anaerobic digestion of industrial wastes is that the process should operate reliably at high performance. In the digestion of dilute, soluble wastes it is necessary to retain the active biomass within the digester at short liquid retention times for the process to be economically feasible and this is reflected in digester design. Performance of digesters can only be assessed by interpretation of measurable parameters such as pH₂, E_h, pH, volatile fatty acid concentrations, temperature, gas production, biomass content and feed rate and composition. The effects of changes in these parameters on the microbiology of methanogenic digestion and the application of this knowledge in control of the process is discussed.     

组织型纤溶酶原激活剂的发光分析法及其应用

 本文建立了组织型纤溶酶原激活剂(t-PA)活力的发光固相测定方法。用氨基乙基丁基异鲁米诺(ABEI)标记纤维蛋白原(Fg),在一定条件下,t-PA作用于固相(包被ABEI-Fg),产生纤维蛋白的降解产物。测定可溶性降解产物的发光强度,即能计算t-PA活性。该方法的标准曲线范围对t-PA为0.156IU/mL～40IU/mL。灵敏度可达0.156IU/mL。回收率为98.6％(n=27)。批内批间变异系数分别为6.6％及10.3％。该方法曾用于检测细胞培养液中提取t-PA样品及t-PA基因表达时培养液中t-PA的活性。也曾用于检测从组织中纯化t-PA样品及血浆中t-PA活性的测定。文中讨论了该方法与其它方法优缺点的比较。