膜生物法降解TNT弹药销毁废水的重要影响因素

采用水解酸化一好氧膜生物工艺对弹药销毁废水中TNT进行降解试验研究。结果表明,共代谢外加碳源对TNT的生物降解影响显著。无共代谢外加碳源的情况下,HRT=40h,TNT的去除率仅为53．4％。有共代谢外加碳源的情况下,外加碳源COD与TNT提供COD比值宜大于4．8,系统对TNT的去除率可高达99％。温度对水解酸化影响重大,当温度低于15℃时,水解酸化对TNT去除率低于33．3％,而当温度高于20℃时,水解酸化对TNT的去除率不小于83％。     

Optimization of thermo-chemical pretreatment and enzymatic hydrolysis of kitchen wastes

The use of abundant waste materials with high carbohydrate content may contribute substantially to reduction of biofuels production cost. The present study aimed at optimizing the combined effect of thermo-chemical pretreatment and enzymatic hydrolysis of kitchen wastes (KW) for maximizing the production of fermentable soluble sugars. To this end, acid pretreatment of KW samples was performed with hydrochloric acid (0–3% HCl) at 30–100 °C for 0–120 min treatment time. Alternatively, alkaline pretreatment of KW samples was performed with potassium hydroxide solution (0–11%) at constant temperature and time (0 °C and 20 min, respectively). KOH pretreatment at such conditions targets to degrade the resistant starch of KW samples. Both acid and alkaline pretreatments were followed by addition of variable levels of enzyme dosage (0–3.6% v/v α-amylase and 0–3.2% v/v amyloglucosidase-AMG) at constant pH, temperature and time (pH = 5, T = 50 °C and t = 30 min, respectively). Based on our results, glucose concentration increased by ～300% after pretreatment with either acid or KOH in combination with enzymatic hydrolysis (2% HCl, 85 °C, 80 min, 0.1% α-amylase, AMG, and 1% KOH, 0 °C, 20 min, 1.1% α-amylase, 0.4% AMG) compared to raw (untreated) KW. Estimating the different Y_G yields at KW loading of 5%, an increase of 192% and 121% for total soluble monosugars and total soluble sugars, respectively, was succeeded compared to untreated KW. The effect of solids loading on the obtained sugar yields using the optimum conditions for thermo-chemical pretreatment followed by enzymatic hydrolysis was also tested resulting to 27.5% increase of the soluble glucose yield when half of the solids loading (2.5%) was used. A decrease of total soluble sugars yield by 32.2% was observed when solely acid hydrolysis at optimum conditions from our previous study was applied at 30% solids loading.     

A+OSA污泥减量工艺碳元素平衡与减量机制研究

为深入研究OSA工艺减量途径,揭示其污泥减量机制,对缺氧-好氧-沉淀-厌氧(A+OSA)污泥减量系统和AO参照系统进行碳元素平衡分析,以考察贮泥池插入对减量系统的影响;辨识两系统各单元碳元素在固液气三相间的迁移转化途径,推测减量驱动机制.碳平衡结果表明,在贮泥池停留时间7.14 h时,碳元素在减量系统剩余污泥中的比例比参照系统高约50%,与减量系统达到49.98%的污泥减量效果相对应.贮泥池的插入能有效减少污泥产量.各单元碳元素变化量表明,减量系统缺氧池与好氧池(主体反应区)用于生物合成的碳元素量高于参照系统;贮泥池中污泥出现负增长,且释放CH4量较主体反应区有大幅增加.DGGE图谱证实了贮泥池中存在与污泥衰减有关的水解发酵型细菌.A+OSA工艺污泥减量是贮泥池污泥衰减和主体反应区补偿性增长共同作用的结果.     

Profiling of the assembly of RecA nucleofilaments implies a potential target for environmental factors to disturb DNA repair

Double-strand breaks (DSBs), one class of the most harmful DNA damage forms that bring elevated health risks, need to be repaired timely and effectively. However, an increasing number of environmental pollutants have been identified to impair DSB repair from various mechanisms. Our previous work indicated that the formation of unsaturated RecA nucleofilaments plays an essential role in homology recombination (HR) pathway which can accurately repair DSBs. In this study, by developing a benzonase cutting protection assay and combining it with traditional electrophoretic mobility shift assay (EMSA) analysis, we further investigated the assembly patterns of four RecA mutants that display differential DSB repair ability and ATPase activity. We observed that the mutants (G204S and S69G) possessing both ATP hydrolysis and DSB repair activities form unsaturated nucleofilaments similar to that formed by the wild type RecA, whereas the other two ATP hydrolysis-deficient mutants (K72R and E96D) that fail to mediate HR form more compacted nucleofilaments in the presence of ATP. These results establish a coupling of ATPase activity and effective DSB repair ability via the assembly status of RecA nucleofilaments. This linkage provides a potential target for environmental factors to disturb the essential HR pathway for DSB repair by suppressing the ATPase activity and altering the assembly pattern of nucleofilaments.     

三峡库区澎溪河流域消落带土壤有机磷生物有效性研究

选取了澎溪河流域六个点位消落带土壤和岸边土壤,以NaOH-EDTA提取土壤中有机磷,并采用酶水解技术表征有机磷生物有效性。结果表明：①消落带土壤NaOH-EDTA提取液中总磷含量为74.55～140.54 mg/kg,无机磷含量为49.91～104.23 mg/kg,有机磷含量为14.61～36.31 mg/kg。消落带土壤有机磷含量低于岸边土壤。②消落带土壤有机磷中总可酶解有机磷（EHP）含量均值为6.23 mg/kg,占土壤有机磷含量的26.7%。消落带土壤EHP含量与有机磷含量呈极显著正相关（n=6,p<0.01）。③消落带土壤EHP含量、活性单酯磷含量与土壤有机质含量呈显著正相关（n=6,p<0.01）,土壤有机质含量是影响有机磷生物有效性的重要因素。④消落带土壤与岸边土壤EHP组分特征相同,含量由高到低依次为类植酸磷、活性单酯磷、二酯磷,但消落带土壤EHP含量显著低于岸边土壤。周期性的干湿交替会造成消落带土壤有机磷向库区水体释放,消落带土壤有机磷地球化学循环对库区水体的潜在影响不容忽视。     

不同氧化剂辅助光催化反应对提高木质纤维素酶解效果的影响

木质纤维素以其可再生、丰富等优点成为可替代能源的理想选择,然而木质纤维素的致密结构使得后续的酶解过程极其困难,因此木质纤维素的预处理显得尤为重要.为了探讨氧化剂对光催化反应预处理木质纤维素的影响,在TiO₂/UV体系中添加不同种类的氧化剂对稻秆进行预处理,考察TiO₂/UV体系中影响光催化的因素〔ρ（TiO₂）、溶液pH及光催化时间〕,并进一步探讨在TiO₂/UV体系中添加O₃、SPC（过碳酸钠）、K₂S₂O₈及KIO₄等氧化剂对稻秆酶解效果的影响.结果表明:在TiO₂/UV体系中,当光催化时间为3 h、ρ（TiO₂）为10 g/L、pH为8时,稻秆的酶解效果最佳（310.17 mg/g）.TiO₂/UV/O₃光催化体系对稻秆的预处理效果强于TiO₂/UV/氧化剂体系,TiO₂/UV/O₃体系预处理稻秆酶解后产生的w（还原糖）最高,达到356.40 mg/g.TiO₂/UV/O₃体系预处理稻秆成分分析显示,木质素去除率为15.52%.FE-SEM（场发射扫描电镜）、FT-IR（红外光谱）及PXRD（X-射线粉末衍射）等表征分析结果表明,TiO₂/UV/O₃体系预处理能够对稻秆结构进行破坏.研究显示,TiO₂/UV/O₃光催化体系对稻秆进行预处理能够有效提高酶解效率.      

荣成天鹅湖沉积物有机磷的生物有效性及其时空动态

有机磷是沉积物磷的重要组成部分,有机磷经酶水解后可以提供活性磷.研究沉积物有机磷的生物有效性及其变化规律对于深入了解湖泊富营养化形成机制具有重要意义.本研究选取富营养化的海岸泻湖—荣成天鹅湖湿地为研究对象,通过采集表层沉积物,结合酶水解技术分析了有机磷的生物有效性及其时空变化规律.结果表明,天鹅湖沉积物有机磷含量为107.9~161.9 mg·kg~(-1),平均含量为125.3 mg·kg~(-1).其中潜在生物有效性磷即酶水解有机磷含量为21.8~100.3 mg·kg~(-1),平均含量为53.2 mg·kg~(-1),占有机磷含量的26%~56%.有机磷的潜在的生物有效性大小遵循:植酸磷(21.5 mg·kg~(-1))≈二酯磷(20.7 mg·kg~(-1))磷酸单酯磷(14.1 mg·kg~(-1)).酶水解有机磷(包括Monoester-P、Phytic-P)的含量呈夏秋低,冬春高的特点.有机磷空间分布不均衡,有机磷主要分布集北部入河口和南部藻类区域,这和不同方位污染物质的来源、水生动植物的分布和沉积物粒度等差异有关.相关性分析表明,金属氧化物(Al、Fe、Mg、Ca)是有机磷的主要结合介质,金属氧化物含量和形态变化将决定有机磷分解矿化和生物有效性.总之,有机磷的水解是水体活性磷的重要补偿途径,也是维持天鹅湖富营养化的重要机制.在水体磷污染治理过程中应把有机磷纳入评价范畴,应该防止沉积物有机磷的矿化分解.     

荆州市印染废水集中处理工程改造方案研究

通过对荆州市中环水业有限公司一期和二期印染废水处理工程差异的比较,在调查园区废水水质水量变化的基础上,对比了两期废水处理工程的工艺及处理效果,为二期工程的高效运行提供有价值参考.同时,通过对不同处理单元的设计规模、设计要求及运行参数等的综合分析,结合实际运行过程水质水量的调查,以COD、NH3-N、色度和悬浮物为主要评价参数,分析了工艺特点及处理效果,确定了各处理单元的最佳运行条件和对不同污染组分的去除特征,优化了各处理单元的运行条件和参数.     

强化污泥利用水解反应器改善碳源与污泥减量作用研究

通过改进传统水解池,强化水解池中的初沉污泥水解,以改善优质碳源比例.强化污泥利用水解反应器集悬浮物的沉淀分离和污泥的水解酸化为一体,经强化污泥利用水解反应器处理后,废水中SS去除率达到81.4%,SS/BOD5由进水的2.4下降至0.4;SCOD/COD、COD0.45～5/COD分别提高了35.4%和17.7%,而COD>100/COD下降了53.2%;BOD5/TN从3.7提高至4.7;BOD5/TP从23.8提高至36.4.废水的碳源结构得到了改善.同时,在强化污泥利用水解反应器中完成了对污泥的处理,污泥水解率达到51.9%,实现了污泥的资源化与减量化.     

水解酸化-两级接触氧化工艺在啤酒废水处理中的应用

啤酒废水具有有机物含量高、悬浮物浓度高、温度高、 pH 值变化大及可生化性较好等特点,生化处理成为国内外啤酒废水处理的主要工艺。公司采用“水解酸化-两级生物接触氧化”工艺对啤酒废水进行处理,运行结果表明,废水pH在8～9, SS、 CODCr、 NH3-N平均浓度分别为710 mg/L、1910 mg/L、49 mg/L时,处理后出水pH在6.5～8.5, SS、 CODCr、NH3-N平均浓度分别为52 mg/L、70 mg/L、11 mg/L, SS、 CODCr、 NH3-N平均去除率分别为93％、96％、77％,满足啤酒废水排放标准的要求。该工艺对废水具有较好的适应性。