硫酸盐还原菌厌氧颗粒污泥的形成条件

硫酸盐还原菌是利用硫酸盐或其他氧化态硫化物作为电子受体来异化有机物的严格厌氧菌。介绍了硫酸盐还原菌的生物化学性质、代谢机理和生理学特征，综述了硫酸盐还原菌厌氧颗粒污泥的形成条件和影响因素，如进水SO4^2-含量，碳源、氮源和磷源，COD与SO4^2-质量浓度比，H2S，pH，温度，氧气及微量元素等。     

钛白废水中硫酸盐生物还原影响因素的研究

在厌氧序批式反应器中,采用硫酸盐还原菌(SRB)对钛白废水中硫酸盐生物还原的影响因素及厌氧序批式反应器的运行条件进行了研究。研究结果表明,模拟废水的SO24-去除效果比实际钛白废水的SO24-去除效果好。SRB还原实际钛白废水中SO24-的最佳运行条件为:进水SO24-质量浓度不超过2000m g/L、反应温度(35±1)℃、pH6.5~8.0、CODρ/(SO24-)2.0~3.0、HRT24h、反应器运行周期8h(进水0.5h,反应6.0h,沉淀1.0h,出水0.5h)、循环间歇搅拌(搅拌1.5h,搅拌停止2.0h)方式。在此条件下SO24-去除率可达90%。     

一种生物处理酸性矿山废水的工艺

该发明涉及一种含硫酸盐酸性废水生物处理并回收单质硫的工艺，其特征在于是一种利用污水厂污泥酸性发酵产物为硫酸盐还原菌的碳源处理酸性硫酸盐废水并回收单质硫的工艺：厌氧生物反应器中硫酸盐还原菌（SRB）将SO4^2-生物还原为H2S或S2-；好氧生物膜反应器中无色硫细菌（CSB）将H2S或S2-生物氧化为单质硫；慢砂滤池过滤、刮砂，采用萃取设备充分溶锯砂滤料中的单质硫，     

荷兰的烟气生物脱硫工艺

烟气中的SO2通过水膜除尘器或吸收塔溶解于水并转化为亚硫酸盐、硫酸盐；在厌氧环境及有外加碳源的条件下，硫酸盐还原菌(SRB)将亚硫酸盐、硫酸盐还原成硫化物；然后再在好氧的条件下通过好氧微生物的作用将硫化物转化为单质硫，从而将硫从系统中去除。可以将烟气生物脱硫过程划分为两个阶段，即SO2的吸收过程和含硫吸收液的生物脱硫过程。     

硫酸盐还原菌原位修复六价铬污染土壤

以FeSO₄化学还原法为对照,开展硫酸盐还原菌原位修复铬污染土壤的田间试验研究。试验结果表明:微生物法处理后,土壤中Cr(Ⅵ)含量从6.48 mg/kg降至0.95 mg/kg,下降率为85.33%,修复后的土地质量符合国家一类建设用地的标准;土壤浸出液中Cr(Ⅵ)质量浓度从0.162 mg/L降至0.004 mg/L,下降率为97.53%;土壤中硫酸根浓度略有降低,硫酸盐还原菌的丰度显著增加。微生物原位修复铬污染土壤的效果好于化学还原法。     

一株吡啶降解菌的筛选及其降解性能

以吡啶为唯一碳源,从焦化厂活性污泥中分离得到一株对吡啶具有高效降解能力的菌株B1,对其进行了菌种鉴定。通过单因素实验研究了菌株B1适宜的降解条件,对反应过程进行了动力学拟合,并考察了菌株B1对焦化废水中吡啶的降解效果。实验结果表明:菌株B1为革兰氏阴性菌,属于不动杆菌属(Acinetobacter sp.);菌株B1适宜的降解条件为降解温度30℃、初始pH为7、摇床转速150 r/min;菌株B1对吡啶的降解过程符合零级反应动力学模型,当初始吡啶质量浓度为300 mg/L时,降解速率常数最高达到21.103 mg/(L·h);用菌株B1对初始吡啶质量浓度为430 mg/L的实际焦化废水处理74 h后,吡啶降解率可达74.26%。     

厌氧膨胀颗粒污泥床生物膜反应器同步产甲烷-硫酸盐还原的快速启动

采用新型厌氧膨胀颗粒污泥床生物膜反应器(EGSBBR)处理含硫酸盐有机废水.在不添加硫酸盐的条件下,运行30 d后系统产甲烷成功启动;随后逐步提高硫酸盐质量浓度至100 mg/L,运行71 d后系统COD去除率和SO42-去除率分别达98.1％和74.7％,甲烷产生量为470.7 mL/d,成功实现了同步产甲烷-硫酸盐...     

用Ti/SnO2-RuO2电极处理黑索金废水

利用刷涂法制备了Ti/SnO2-RuO2电极,并通过SEM、XRD等测试手段对其进行形貌及结构表征。利用该电极为阳极处理黑索金(RDX)废水,考察了电解质种类、电解质质量浓度、废水pH、电流密度以及电解时间等对RDX电催化氧化效果的影响。实验结果表明,当处理100 mL质量浓度为50 mg/L的RDX废水时,以Na2SO4为电解质、Na2SO4质量浓度为5.0 g/L、废水pH为7、电流密度为15 mA/cm2、电解时间为300 min的条件下,RDX去除率达到82.55%,COD去除率达到55.41%。     

纳滤处理炼化污水反渗透浓水

分别采用4种纳滤膜处理某炼化公司的反渗透浓水。在初始COD为57.8 mg/L、TOC为23.94 mg/L、ρ(Ca2+)为289.0 mg/L、ρ(Mg2+)为54.6 mg/L、ρ(SO42-)为327.7 mg/L、ρ(Cl-)为1 106.8 mg/L的条件下,经纳滤处理后COD去除率达60%以上,污水COD降至30 mg/L以下,TOC去除率为31.9%~85.5%,阳离子的去除率为33.9%~97.0%,SO42-的去除率为63.3%~97.6%,Cl-的去除率较低。膜A的膜孔分布密集,具有很高的通量,对有机物和无机盐的截留效果较差;膜B和膜C对有机物和二价离子的截留效果较好;膜D的膜孔分布稀松,膜通量最低,对有机物和无机盐的截留能力均较强,但随出水体积的增加,对无机盐的截留能力下降较为明显。4种纳滤膜的性能各异,可满足不同企业的需求,具有良好的应用前景。     

活性艳蓝X-BR降解菌的筛选

从某印染厂废水排放出口的污泥中分离到一株活性艳蓝X-BR染料高效降解菌LPY68-14,经生理生化鉴定,该菌为埃希氏菌(Escherichia sp.).研究了影响菌株LPY68-14降解效果的因素,实验结果表明:在缺氧、质量分数为0.2%葡萄糖为外加碳源、温度37℃、接种量4 mL、pH 7的最佳条件下,质量浓度为30 mg/L的活性艳蓝X-BR经菌株LPY68-14处理24 h后的降解率可达80%;当活性艳蓝X-BR质量浓度为100～400 mg/L时,该菌处理48 h后的降解率可稳定在70%左右.     

Treatment of acid lignite mine flooding water by means of microbial sulfate reduction

During and after mining activities acidic waters containing high amounts of heavy metals and sulfate often occur. In addition to precipitation processes, water purification is also possible with the help of sulfate-reducing bacteria (SRB). A mixed culture of SRB was adapted to methanol as a cheap carbon source. In order to receive high sulfate-reduction rates immobilization on porous materials proved to be advantageous. Continuous laboratory experiments based on immobilized SRB were carried out with original water from a lignite mining site reaching sulfate-reducing rates up to 132 mg SO4(2-)/(1 h). Based on these results a process for the treatment of such waters was designed. Heavy metals are removed by recycling sulfide containing effluent, excess sulfide can be oxidized to elemental sulfur by addition of hydrogen peroxide. The plant with a 3.9 m3 bioreactor with immobilized SRB was constructed at the mine site. This pilot plant was operated successfully for some months. The removal of heavy metals was close to 100%, the pH of the acidic water increased from 3.0 to 6.9. The sulfate-reducing rate again reached 134 mg SO4(2-)/(1 h). The production of sulfur from the excess sulfide is possible.     

冷冻固定化硝化菌去除废水中氨氮的研究

采用聚乙烯醇(PVA)循环冷冻法制备固定化硝化菌颗粒,经活化后在颗粒填充率为9％的三相流化床中进行氨氮废水处理试验。处理低浓度氨氮有机废水(NH3-N质量浓度为75mg／L．COD约为400mg／L,水力停留时间为4h)时,NH3-N去除率约为90％,COD、TIN的去除率可达82％和60％左右;处理高浓度氨氮废水(NH3-N质量浓度450～500mg／L,水力停留时间为20h)时,NH3-N去除率在98％以上,氨氧化产物中NO2^--N质量分数在95％以上,为亚硝酸盐反硝化提供了有利条件。用该法制成的硝化菌颗粒寿命在3个月以上。     

Nickel and cobalt recycling from lithium-ion batteries by electrochemical processes

The presence of LiCoO(2) and LiCo(x)Ni((1-x))O(2) in the cathodic material of Li-ion and Li-polymer batteries has stimulated the recovery of Co and Ni by hydrometallurgical processes. In particular, the two metals were separated by SX method and then recovered by electrochemical (galvanostatic and potentiostatic) processes. The metallic Ni has been electrowon at 250 A/m(2), pH 3-3.2 and 50 degrees C, with 87% current efficiency and 2.96 kWh/kg specific energy consumption. Potentiostatic electrolysis produces a very poor Ni powder in about 1 h with current efficiency changing from 70% to 45% depending on Ni concentration in the electrolyte. Current efficiency of 96% and specific energy consumption of 2.8 kWh/kg were obtained for Co at 250 A/m(2), pH 4-4.2 and 50 degrees C, by using a solution containing manganese and (NH(4))(2)SO(4). The Co powder, produced in potentiostatic conditions (-0.9 V vs. SCE, pH 4, room temperature) appears particularly suitable for Co recycling as cobaltite in new batteries.     

Municipal Wastes Treatment and Production of Polyhydroxyalkanoate by Modified Two-Stage Batch Reactor

The municipal wastes were utilized as substrate for polyhydroxyalkanoate (PHA) using two strains of Bacillus licheniformis (PHAs-007, wild type and M2-12, mutant). Municipal wastes were subjected to separate wastewater and biosolid. Municipal biosolid was digested by anaerobic bacteria thereafter only the supernatant with soluble organic compounds was subjected into the PHA-producing reactor containing municipal wastewater. The mutant strain M2-12 gave the highest value of biomass (42.0 ± 2.0 g/L) and PHA concentration (37.4 ± 1.0 g/L with 88.9 % of dry cell weight, DCW) and reduced 76.5 % of soluble chemical oxygen demand after 60 h of cultivation. The value of pH, biochemical oxygen demand and total solid of the reclaimed wastewater after PHA recovery was 7.1, 20 and 97 mg/L, respectively. Moreover, the polymers produced by both strains of B. licheniformis were characterized. The resultant polymer from B. licheniformis PHAs-007 and M2-12 cultivated in the PHA-producing reactor was identified as poly-3-hydroxybutyrate-co-3-hydroxyvalerate [P(3HB-co-3HV)] and poly-3-hydroxybutyrate-co-4-hydroxybutyrate [P(3HB-co-4HB)], respectively. The results suggesting that the production of PHA by municipal wastes is feasible thus the PHA production stage can be integrated in waste treatment to produce PHA and treated municipal wastes at the same time.     

NiO-CuO/ZSM-5催化剂对催化裂化烟气的脱硫脱硝性能

采用浸渍法制备了不同NiO和CuO质量分数的NiO-CuO/ZSM-5催化剂，并以CH4为还原剂研究了NiO-CuO/ZSM-5催化剂对催化裂化烟气的脱硫脱硝活性。XRD分析结果表明，NiO质量分数为4%、CuO质量分数为6%的催化剂4%NiO-6%CuO/ZSM-5中的ZSM-5结构完好，CuO和NiO高度分散在ZSM-5骨架中，表明具有较好的催化活性。4%NiO-6%CuO/ZSM-5的脱硫脱硝起活温度均较低，无氧条件下最高NO转化率和SO2转化率分别为94.7%和95.9%，O2体积分数为1.0%时的NO转化率和SO2转化率分别为97.7%和89.0%。     

高效石油烃降解菌的筛选及其对原油污染土壤的修复

从陕北原油污染土壤中筛选出7株高效石油烃降解菌,其中黄杆菌属CC-2、不动细菌属SC-5、假单胞菌属SC-6表现出较强的石油烃降解能力。通过单因素试验和正交试验考察总石油烃(TPH)降解效果的影响因素,得出各因素对TPH降解率影响程度的大小次序为:溶液p H降解温度降解菌接种量摇床转速,且在降解菌接种量为7%(φ)、溶液p H为7、降解温度为30℃、摇床转速为150 r/min的最适处理条件下,菌株SC-6的TPH降解率可达61.23%。原油污染土壤生物修复实验结果表明:高效石油烃降解菌的投加有利于土壤TPH降解率和酶活性的提高;"菌株SC-6+营养剂"组修复处理42 d后的TPH降解率可达57.59%。     

Leaching from MSWI bottom ash: evaluation of non-equilibrium in column percolation experiments

Impacts of non-equilibrium on results of percolation experiments on municipal solid waste incineration (MSWI) bottom ash were investigated. Three parallel column experiments were performed: two columns with undisturbed percolation and one column with two sets of 1-month-long flow interruptions applied at liquid-to-solid (L/S) ratios of L/S 2L/kg and 12L/kg, respectively. Concentrations of Na, K, Cl(-), Ca, Si, SO(4)(2-), Al, Cu, Ni, Mo, Ba, Pb, Zn, and dissolved organic carbon (DOC) were monitored throughout the entire leaching period; geochemical modeling was used to identify non-equilibrium-induced changes in the solubility control. Despite both physical and chemical non-equilibrium, the columns were found to provide adequate information for readily soluble compounds (i.e., Na, Cl(-), and K) and solubility-controlled elements (i.e., Ca, SO(4)(2-), Ba, Si, Al, Zn, and Pb). The leaching of Cu and Ni was shown to depend strongly on DOC leaching, which was likely affected by physical non-equilibrium during flow interruptions. Consequently, the leaching of Cu and Ni in the undisturbed columns was shown to be by about one order of magnitude lower compared with the interrupted column. The results indicate that the leaching of DOC-related metals in laboratory column experiments may be considerably underestimated compared with full-scale scenarios in which the impacts from non-equilibrium may be significantly lower. The leaching of Mo (or MoO(4)(2-)) may be controlled solely by its availability in the mobile zone, which in turn appeared to be controlled by diffusion from the stagnant zone; no Mo controlling minerals were predicted by the geochemical modeling.     

赖氨酸废水的处理和氨回收

对赖氨酸浓废水调 p H沉淀处理后的澄清水进行预处理 :先加入石灰乳 ,搅拌、沉淀 ,SO42 -从 2 0 0 0 0 m g/ L 左右降至 130 0 mg/ L 左右 ,去除率为 94%左右 ,然后进行空气吹脱 ,NH3- N从 5 0 0 0 mg/ L左右降至 80 m g/ L左右 ,去除率 >98%。吹脱出水经厌氧生化处理后 ,再进行空气吹脱 ,NH3- N从 70 0 mg/ L 左右降至 85 mg/ L 左右 ,去除率 >86 %。再吹脱出水与稀废水混合后进行好氧生化和 A/ O、O系统处理 ,出水的 COD<10 0 m g/ L,BOD5<2 0 mg/ L,SS<70 mg/ L,NH3- N<2 5 m g/ L。对浓废水与石灰乳混合后搅拌过程中及两次空气吹脱过程中挥发的 NH3进行回收 ,将其与 H2 SO4反应 ,生成的 (NH4) 2 SO4回用于生产     

Biotransformation of explosive-grade nitrocellulose under denitrifying and sulfidogenic conditions

Waste nitrocellulose (NC) is regulated as a hazardous material. The objective of this study was to determine if NC exposed to denitrifying and sulfidogenic conditions would undergo sufficient removal of the nitro groups to yield a material that is no longer explosive. Enrichment cultures were established with methanol as the electron donor for nitrate-reducing conditions and lactate for sulfate-reducing conditions. NC was added to the cultures at 10 g/l. A statistically significant decrease in the nitrogen (N) content of NC occurred in both enrichment cultures, from approximately 13.1-13.2% in virgin NC to 12.2-12.4%. This was accompanied by an increase in nitrogen gas formation. The presence of a primary substrate (methanol and lactate) was necessary to affect this change; NC itself did not serve as an electron donor. In cultures that were carrying out denitrification but were then depleted of nitrate, with methanol still present, a slightly greater removal of nitro groups from NC occurred along with additional formation of nitrogen gas. NC did not have an inhibitory affect on the denitrification process but it did significantly slow the rate of lactate consumption and sulfate reduction. Fourier Transform Infrared Spectroscopy (FTIR) results indicated that NC exposed to denitrifying conditions was enriched in hydroxyl groups, consistent with removal of some of the nitro groups by hydrolysis of the nitrate esters. NC exposed to nitrate- and sulfate-reducing conditions and virgin NC were also compared based on their explosive properties using a small-scale burning test. The biologically treated NC exhibited somewhat less reactivity, but was still rated as explosive. The decrease in%N, increase in N2, and FTIR results demonstrated that NC does undergo biotransformation in the presence of nitrate- and sulfate-reducing enrichment cultures, but the extent of denitration does not appear to be adequate to yield a nonhazardous product.