4株正十六烷降解菌的降解能力及代谢动力学特性

从处理采油废水的活性污泥中分离出4株产生物表面活性剂的正十六烷高效降解菌。菌株A14和B45为非脱羧勒克菌（Leclercia adecarboxylata）,菌株C28和A27为肠杆菌（Enterobacter sp.）。在NaCl质量浓度15~25 g/L、pH 6.0~7.0、接种量10%（φ）,培养温度37 ℃,摇床转速160 r/min、正十六烷体积分数0.30%的条件下降解16 d后,菌株A14、B45、C28和A27的正十六烷降解率分别为93.7%,87.8%,73.3%,65.7%。4株菌所产生的生物表面活性剂均为磷脂类表面活性剂。菌体生长满足逻辑斯蒂模型,正十六烷的降解满足一级反应动力学模型。菌株C28、A27的生长速率快于菌株A14、B45,菌株A14、B45的正十六烷降解速率快于菌株C28、A27。     

Simultaneous biodegradation of bifenthrin and chlorpyrifos by Pseudomonas sp. CB2

The degradation of bifenthrin (BF) and chlorpyrifos (CP), either together or individually, by a bacterial strain (CB2) isolated from activated sludge was investigated. Strain CB2 was identified as belonging to genus Pseudomonas based on the morphological, physiological, and biochemical characteristics and a homological analysis of the 16S rDNA sequence. Strain CB2 has the potential to degrade BF and CP, either individually or in a mixture. The optimum conditions for mixture degradation were as follows: OD_600nm = 0.5; incubation temperature = 30°C; pH = 7.0; BF-CP mixture (10 mg L^?1 of each). Under these optimal conditions, the degradation rate constants (and half-lives) were 0.4308 d^?1 (1.61 d) and 0.3377 d^?1 (2.05 d) for individual BF and CP samples, respectively, and 0.3463 d^?1 (2.00 d) and 0.2931 d^?1 (2.36 d) for the BF-CP mixture. Major metabolites of BF and CP were 2-methyl-3-biphenylyl methanol and 3,5,6-trichloro-2-pyridinol, respectively. No metabolite bioaccumulation was observed. The ability of CB2 to efficiently degrade BF and CP, particularly in a mixture, may be useful in bioremediation efforts.     

土壤分离菌株去除水溶液中铅离子研究

金属及微生物种类、pH和接触时间是决定生物吸附效果的关键因素.从受铅污染的土壤中分离出5株有生物吸附铅离子能力的菌株,并鉴定吸附能力最强的菌株1为芽孢杆菌;试验了pH、接触时间和初始铅离子浓度对该芽孢杆菌生物吸附铅的影响,在温度为25℃时,pH值3.0、初始铅离子浓度250 mg/L、吸附时间不超过15 min有最大吸附量92.27 mg/g,此时去除率为73.82%,且25℃吸附平衡基本符合Langmuir等温模型.因此,用该芽孢杆菌生物吸附去除水溶液中铅是可行的.     

耐酸性异养菌的分离及其在制革污泥重金属生物淋滤中的作用

从制革污泥中分离出一株异养微生物,经鉴定属于红酵母菌属(Rhodotorula sp.)R30, 测定菌株R30的适宜生长pH范围为3～7,但能耐受pH 2.5至1.5的酸性环境,最适生长温度28℃.酵母R30在污泥水溶性有机物(DOM)中培养96h,水溶性有机碳(DOC)从1485mg/L降至345mg/L,菌数达4.8×10⁷mL^-1.将污泥预酸化至pH 6.5,在进行污泥的生物淋滤过程中,添加酵母处理与不添加酵母处理的对照相比,淋滤时间减少了4d,淋滤周期显著缩短,在7d的淋滤时间内,重金属Cr的溶出率提高39%.     

农药降解酶的固定化及其降解特性

采用海藻酸钙凝胶将 Ａｌｃａｌｉｇｅｎｅｓ ｓｐ ． Ｙ Ｆ１１ 农药降解酶进行固定化,并测定了固定化酶对杀灭菊酯的降解特性． 农药降解酶的固定化条件为：海藻酸钠质量浓度,３０ ｇ／ Ｌ;蛋白质量浓度,０ ．２ ｇ／ Ｌ;固定化时间ｔ ＝ １６ｈ ;粒径４ ｍｍ ． 固定化酶降解杀灭菊酯的最适ｐ Ｈ 为８ ．０ 、最适温度为３５ ℃, Ｋｍ５５ ．０ μｍｏｌ／ Ｌ     

皮革废物铬革屑的微生物学处理研究Ⅰ:降解铬革屑的微生物筛选及诱变

从不同来源的微生物中筛选出能粗效降解革屑的皱绒青霉 Ａ Ｓ３ ．１０６６ 菌株,可溶性蛋白得率达５３ ．５ ％ ;该株经紫外诱变获得高产蛋白酶诱变株 Ａ Ｓ３ ．１０６６ Ｅ,其蛋白酶活性较原始菌株高３ 倍     

石油降解菌的分离、鉴定及其降解能力的研究

从含油污泥中,筛选出能以２０ ＃ 机械润滑油为唯一碳源的３ 株石油降解菌菌株,经鉴定分别为动胶菌属（ Ｚｏｏｇｌｏｅａ ｓｐ ．） 、氮单胞菌属（ Ａｚｏｍｏｎａｓｓｐ ．） 和假单胞菌属（ Ｐｓｅｕｄｏｍｏｎａｓ ｓｐ ．） ．通过其降解能力的测试,以动胶菌 Ｄ２ 菌株对２０ ＃ 机油的降解能力最强：在含油浓度ρ＝ ５００ ～１ ５００ ｍｇ／ Ｌ 的摇瓶试验中,其除油率为２０ ．８ ％ ～２５ ％ ．利用动胶菌 Ｄ２ 菌株进行生物接触氧化法处理含油废水模拟试验,当入流浓度为１ ０００ ｍｇ／ Ｌ 时,除油率可达９０ ．５ ％ ～１００ ％ ．这一结果表明,动胶菌 Ｄ２ 菌株生物接触氧化法处理含油废水具有很好的应用前景     

叉鞭金藻对微量锌、镉的吸附效应研究

研究了叉鞭金藻对微量Zn^2 ,Cd^2 的生物吸附及其机理。结果表明,叉鞭金藻对Zn^2 ,Cd^2 的生物吸附主要经历了快速的吸附和缓慢的吸附两个步骤。pH为6～7时,叉鞭金藻对Zn^2 ,Cd^2 有较好的吸附作用,且死体藻细胞比活体藻细胞能富集更多的Zn^2 ,Cd^2 。吸附符合Freundlich等温吸附模型。     

炼厂"三泥"的生物处理研究

从大港油田筛选和分离出3株以原油为碳源的石油降解菌,初步鉴定为假单胞菌属(Pseudomonas sp.),用这3株菌混合处理某炼厂的"三泥",在适宜的降解条件下,仅需投加混合菌液,无需添加营养物(N,P),可使含油污泥A的残油量从67g/kg降至7.7g/kg,混合油泥试样AB的残油量从19.7g/kg降至3.1g/kg,平均去除率为84%以上,可以实现含油污泥的较为经济的、有效的处理.经生物处理后含油污泥的恶臭味完全消失.     

Kinetic analysis of the anaerobic digestion of untreated vinasses and vinasses previously treated with Penicillium decumbens

A kinetic study was carried out on the anaerobic digestion of untreated vinasses and vinasses previously fermented with Penicillium decumbens. Two 1-l volume continuous-flow stirred tank reactors (CFSTR) operating at mesophilic temperature (35 degrees C) were used for the study. One reactor was fed with untreated vinasses (COD concentration of 80.5 g/l) and the other with vinasses previously fermented (COD concentration of 23.0 g/l). Both reactors were operated at organic loading rates in the range of 1.5-7.5 g chemical oxygen demand (COD)/l-d. The results obtained were evaluated using the Chen-Hashimoto methane production model to determine the values of the maximum specific growth rate (micromax) and the model kinetic constant (K) of the process for each case studied. The kinetic constants (micromax and K) were affected by the pre-treatment, and the respective values were 9.6 and 6.9 times higher for pretreated vinasses than those of untreated vinasses. This was significant at the 95% confidence level. This behaviour is believed to be due to the lower levels of phenolic compounds present in the pretreated vinasses, as compared to untreated vinasses, resulting in an improved process performance, kinetics and stability. Finally, the experimental values of methane production were reproduced with deviations equal to or less than 4% and 10% for pretreated and untreated vinasses, respectively.