Fe3+(NTA)还原菌的固定化小球制备及还原特性

采用海藻酸钠包埋驯化得到的优势铁还原菌,用于还原络合吸收法脱除NOx过程中形成的中间副产物Fe^3＋（NTA）。结果表明,最佳包埋条件为海藻酸钠质量浓度4%,菌体质量浓度0.2%,CaC l2质量浓度3%,此条件下制备的小球还原性能好,在微生物用量为20 g（湿重）/L时还原10 mmol/L Fe^3＋（NTA）,经12 h反应后还原率达到96.1%,而相同条件下游离微生物的还原率仅为11.8%,但反应16 h后游离微生物与固定化小球的还原率相近,均为97%左右。但此法制备的小球机械强度不高,溶胀、破裂现象严重。通过添加聚乙烯醇和硅藻土改良固定化小球,可强化小球的机械强度、降低小球的溶胀及破裂现象,对Fe^3＋（NTA）的还原效果也较改良前的小球有所提高,两者最佳添加量均为20 g/L。改良后的小球与游离微生物相比,耐酸性增强,在pH=5的条件下,仍具有79.8%的还原效率,远高于相同条件下游离微生物的39.5%,但对温度的适应范围两者基本一致。     

亚铁离子生物氧化-还原法连续脱除硫化氢

为了降低工业废气中的硫化氢去除工艺成本和运行费用,对三价铁盐吸收与氧化亚铁硫杆菌对Fe²⁺的生物氧化联合作用脱除H₂S进行了研究。通过生物氧化塔中的固定化氧化亚铁硫杆菌细胞再生的Fe³⁺溶液,在H₂S还原吸收塔中脱除H₂S。通过单因素实验分别优化了生物氧化塔和H₂S吸收塔的运行参数,在生物氧化塔曝气量为150 L/h,停留时间为11 h,吸收液中Fe³⁺浓度为0.121~0.143 mol/L,吸收液流量为0.3 L/h,进气量为100 L/h条件下,进气中H₂S浓度分别为2.28和9.11 mg/L,系统连续运行至200 min时趋于相对稳定,当系统连续运行稳定时,H₂S的脱除率可分别达到95%和91%,脱除效果显著。     

生物催化氧化法脱除H2S的试验研究

针对H₂S污染的严峻形势，构建了包括催化再生装置和生物滴滤器的生物催化氧化装置。该装置以沸石为填料，以氧化亚铁硫杆菌为脱硫菌种，通过微生物和Fe³⁺的双重氧化作用高效脱除H₂S。试验确定了装置的适宜喷淋量和沸石的最佳粒径。在温度为30℃，进气量为0.25 m³/h，进气H₂S浓度为2500mg/m³，喷淋量为1000mL/h，喷淋液的pH值为1.97、Fe³⁺浓度为0.05 mol/L的条件下，出气H₂S浓度足以达到GB14554-93规定的一级厂界标准值。试验证明，生物催化氧化法是一种新型高效的脱硫技术，应进一步开展中试研究。     

UV-Fenton光催化氧化处理高浓度邻苯二甲酸二辛酯生产废水

采用UV-Fenton技术光催化氧化高浓度邻苯二甲酸二辛酯（DOP）生产废水，确定最佳操作条件为：初始pH=3.8，H₂O₂浓度为9.99 g/L，H₂O₂/Fe²⁺摩尔比为20∶1，光照反应60 min。此条件下的废水COD去除率为89.1%，出水COD值在570 mg/L左右。经正交试验确定影响处理效果各因素的重要性顺序为：H₂O₂浓度＞H₂O₂/Fe²⁺摩尔比＞光照反应时间＞pH。UV的加入与单独的Fenton体系存在正相关的协同作用。废水降解的表观过程符合一级反应动力学模式。     

Fe0钝化膜的生物还原及其脱氮除磷

微生物的异化Fe(Ⅲ)还原是一种能够利用Fe(Ⅲ)作为末端电子受体在无氧条件下氧化有机物的产能过程。结合这一特性,考察了在兼性厌氧/严格厌氧条件下Fe⁰钝化膜作为Fe(Ⅲ)源时的生物还原能力以及对N、P等营养元素的去除效果。结果表明,严格厌氧条件下微生物异化Fe(Ⅲ)还原能力较好,富集培养至7 d,累计Fe(Ⅱ)浓度达到最大,最大产生速率为98.69 mg/(L·d),同时TP去除率高达97.1%以上。而体系对NH₄⁺-N、TN的去除相对滞后,培养至13 d,去除率开始增大,最终分别达到86.6%和76.1%。这为装填有海绵铁+聚氨酯泡沫载体的SBBR中填料的原位再生问题提供了解决思路。     

蒽的高效降解菌的固定化小球的制备及其降解特性

旨在利用固定化高效降解菌小球去除水中蒽,充分发挥累托石的吸附和生物降解的协同作用,以累托石、聚乙烯醇(PVA)、海藻酸钠(SA)作为固定化载体材料,硼酸和氯化钙作为交联剂,将蒽的高效降解菌包埋制备固定化微生物小球.考察了累托石用量、PVA投加量、海藻酸钠用量、氯化钙用量、微生物包埋量和交联时间等因素对微生物小球活性的影响,通过正交实验确定了微生物小球的最佳制备条件.结果表明,制备固定化微生物小球的最佳条件为:累托石2.5%,PVA 12%,SA 0.3%,CaCl24%,交联时间28 h,微生物包埋量10%.对40 mgJ/L的蒽溶液,游离微生物在50 h后开始发挥明显的降解作用,经过68 h蒽的去除率达到35.65%;而固定化微生物小球经过9 h即可使蒽的去除率达到81.8%,23 h后葸的去除率可达100%.固定化微生物小球对水中蒽的去除机理与吸附-降解工艺的机理类似,即固定化微生物小球类似于一个一体化的微型反应器,经过迟滞期后,在该反应器内同时发生吸附和降解作用.     

不同高级氧化法对水中低浓度药物甲硝唑降解过程的比较

采用UV、H₂O₂、UV/H₂O₂、Fenton、UV/Fenton和UV/TiO₂方法,对水中低浓度的药物甲硝唑进行降解。通过HPLC和UV-Vis光谱得到的甲硝唑去除率。详细讨论了Fe²⁺、TiO₂和H₂O₂的初始浓度以及溶液的初始pH值对降解效率的影响。结果表明,UV/Fenton和UV/TiO₂ 2种系统对水中低浓度甲硝唑均有很好的去除效果,但前者的光催化效率更高。在甲硝唑浓度=6 μmol/L,H₂O₂和Fe²⁺的初始浓度分别为0.5 mg/L和2.94 μmol/L,pH=4的条件下,UV/Fenton方法对甲硝唑水溶液光催化的最佳效率为95.8%。     

天然沸石负载La2O3-ZnO-TiO2光催化降解活性艳红K-2BP

利用80目天然斜发沸石作载体制备La₂O₃(0.5%)-ZnO(20%)-TiO₂/沸石复合光催化剂,以20 W紫外灯为光源,在自制的光催化反应器中降解活性艳红K-2BP,考察了光照时间、空气通入量、催化剂用量、溶液初始浓度、H₂O₂与Fe³⁺投加量等对活性艳红K-2BP光催化降解率的影响。结果表明,当溶液初始浓度为60 mg/L,催化剂投加量为12 g/L,通气量为1 200 mL/min,光照2.5 h,活性艳红K-2BP的降解率可达99.2%;H₂O₂和Fe³⁺投加量为4 mL/L和3 g/L时,光照1 h活性艳红K-2BP降解率分别为100%和97.2%。紫外可见吸收光谱显示,LZTZ光催化剂可有效降解印染废水。     

用H2O2/Fe3+处理高浓度含甲醛废水的研究

研究采用H₂O₂/Fe³⁺催化氧化处理高浓度含甲醛废水,探讨了双氧水和催化剂投加量、反应pH及反应温度等操作条件对处理效果的影响,并通过酸溶解回用失活催化剂。结果表明,较优的操作条件为：H₂O₂/COD（质量比）=2.2～2.6,Fe³⁺/H₂O₂（摩尔比）=0.048～0.058,反应pH 1.80～2.68,反应温度50℃,反应时间40 min;在上述操作条件下,甲醛去除率达到99%以上,COD去除率达到85%以上。失活的催化剂可通过稀酸溶解后循环使用,其效果与三价铁盐作催化剂的基本相同。采用H₂O₂/Fe³⁺处理含甲醛废水具有比采用H₂O₂/Fe³⁺较优的效果。     

Fe0/厌氧微生物联合体系处理2,4,6-三氯酚影响因素的研究

利用Fe⁰/厌氧微生物联合体系对2,4,6-三氯酚(2,4,6-TCP)进行降解研究。结果表明,Fe0/厌氧微生物联合体系可以有效降解2,4,6-TCP,Fe⁰与厌氧微生物之间存在明显的协同效应。Fe⁰/厌氧微生物联合体系处理2,4,6-TCP的最优条件为：微生物接种量0.434 g VSS/L,Fe⁰投加量15 g/L,体系初始pH值7.0～8.0。     

Treatment of phenol-containing wastewater by photoelectro-Fenton method using supported nanoscale zero-valent iron

This study presents the degradation of phenol by the photoelectro-Fenton method using nano zero-valent iron (nZVI) immobilized in polyvinyl alcohol–alginate beads. The effect of nZVI loading, H₂O₂ concentration, pH, and initial phenol concentration on phenol degradation and chemical oxygen demand reduction was studied. The scanning electron microscope images of the nZVI beads were used to analyze their morphology, and their diameters were in the range of 500–600 μm. The concentration of nZVI in the beads was varied from 0.1 to 0.6 g/L. Fe²⁺ leakage of 1 and 3 % was observed with 0.5 and 0.6 g/L of nZVI, respectively, and the observed beads' fracture frequency was 2 %, which confirmed the stability of the beads. The optimum operating conditions that arrived for better degradation were 0.5 g/L of nZVI, pH 6.2, and 400 mg H₂O₂/L. The treatment of effluent by this method increased the biodegradability index of the effluent, and the degradation data were found to follow pseudo first-order kinetics.     

固定化菌藻微球的制备、表征及其对富营养化湖水的修复

以聚乙烯醇(PVA)和海藻酸钠(SA)为主要包埋材料,以活性炭、SiO2和CaCO3作添加剂,采用普通小球藻(Chlorella vulgaris)和活性污泥制备固定化菌藻微球。采用正交实验对微球的制备条件进行了优化,并对最优化条件下制得的微球进行了表征,还考察了固定化菌藻微球对某富营养化湖水的修复效果。结果表明,固定化菌藻微球的最优化制备条件为:PVA用量10%(m/v),微生物包埋量15 mL,海藻酸钠用量0.6%(m/v),氯化钙浓度2.0%(m/v)。制得的微球具有较大的比表面积,内部呈网状结构,孔径分布均匀,中孔居多,适合小球藻和微生物生长。采用固定化菌藻微球可有效修复上述湖泊的实际富营养化湖水,微球可重复使用3~4个循环,在前4个循环中,每个循环历时96 h,TN平均去除率达80%以上;TP平均去除率达90%以上;COD平均去除率达85%以上,表明固定化菌藻微球在富营养化湖水的修复方面具有潜在的应用价值。     

卡拉胶、膨润土改性PVA包埋小球

对PVA+卡拉胶包埋小球和PVA+海藻酸钠包埋小球的性能进行比较,并首次使用PVA+卡拉胶+膨润土混合包埋材料制作包埋小球.结果表明,PVA+海藻酸钠包埋小球在制作过程中有一定的拖尾现象,红墨水到达小球中心的时间为80 min,6d可去除50％的COD;PVA+卡拉胶包埋小球更容易成球,而且红墨水到达小球中心的时间为50 min,6d可去除56％的COD.此外,在PVA+卡拉胶包埋材料中添加适量的膨润土可以将红墨水到达小球中心的时间由50 min缩短到30 min.因此,使用PVA+卡拉胶+膨润土的混合材料制作包埋小球是可行的.最后,通过包埋小球处理抗生素废水的正交实验,得出包埋材料中各组分的最佳配比:PVA浓度11％、卡拉胶浓度0.5％、膨润土浓度2.5％.在这种配比下,包埋小球对抗生素废水中COD的去除率可以达到65％左右.     

用于处理冲厕海水的固定化生物硅藻土小球的制备

选用聚乙烯醇（PVA）和海藻酸钠（SA）混合物作为包埋载体,对筛选出的耐盐复合菌群固定化制备方法进行了研究。通过正交实验分别研究了包埋载体不同配比、包菌量、硅藻土投加量和交联时间对固定化生物硅藻土小球的性能及其对冲厕污水中COD去除效果的影响。研究结果表明,固定化生物硅藻土小球最佳包埋条件是：聚乙烯醇9％,海藻酸钠0．5％,包菌量l：1,硅藻土20g／L,交联时间为24h。在该条件下,小球成球效果较好,机械强度高,对海水冲厕污水中COD的去除率达86．95％。     

Biodegradation of quinoline by gel immobilized Burkholderia sp

Burkholderia sp, a gram-negative, rod-shaped, aerobe, capable of degrading quinoline was immobilized in calcium alginate gel beads and used for degradation of quinoline in aqueous solution in the reactor. The optimal conditions for immobilization of the microorganism, such as alginate concentration, calcium ion concentration, initial cell loading, hardening time and bead size, were determined with a view to improving the quinoline degradation rate. The characteristics of quinoline degradation by immobilized microbial cells were investigated. The repeated use of immobilized cells for quinoline degradation was performed and the results revealed that the bioactivity of immobilized cells was stable over 100 h in the repeated batch cultivation for quinoline degradation.     

大孔树脂白球固定化微生物强化处理对甲苯胺废水的研究

采用大孔树脂白球固定化微生物强化SBR处理含对Ep苯胺废水,与对照组相比,通过投加大孔树脂白球固定化微生物可以有效提高反应器的处理效率。在进水TOC为434．8mg／L,对甲苯胺为326．9mg／L的条件下,强化组可在180min内将TOC和对甲苯胺基本去除完全,去除率在98％以上,对照组则需要300min才能达到相同的去除效果。强化组对氨氮的去除同样具有较好的处理效果。     

Alginate immobilized enrichment culture for atrazine degradation in soil and water system

An atrazine degrading enrichment culture, a consortium of bacteria of genus Bacillus along with Pseudomonas and Burkholderia, was immobilized in sodium alginate and was used to study atrazine degradation in mineral salts medium (MSM), soil and wastewater effluent. Sodium alginate immobilized consortium, when stored at room temperature (24 ± 5°C), was effective in degrading atrazine in MSM up to 90 days of storage. The survival of bacteria in alginate beads, based on colony formation unit (CFU) counts, suggested survival up to 90 days and population counts decreased to 1/5^th on 120 days. Comparison of atrazine degrading ability of the freely suspended enrichment culture and immobilized culture suggested that the immobilized culture took longer time for complete degradation of atrazine as a lag phase of 2 days was observed in the MSM inoculated with alginate immobilized culture. The free cells resulted in complete degradation of atrazine within 6 days, while immobilized cells took 10 days for 100% atrazine degradation. Further, immobilized cultures were able to degrade atrazine in soil and wastewater effluent. Alginate beads were stable and effective in degrading atrazine till 3rd transfer and disintegrated thereafter. The study suggested that immobilized enrichment culture, due to its better storage and application, can be used to degrade atrazine in soil water system.     

Effect of immobilized microalgal bead concentrations on wastewater nutrient removal

A unicellular green microalga, Chlorella vulgaris, entrapped in calcium alginate as algal beads were employed to remove nutrients (N and P) from simulated settled domestic wastewater. A significantly higher nutrient reduction was found in bioreactors containing algal beads (at concentrations ranging from 4 to 20 beads ml(-1) wastewater) than the blank alginate beads (without algae). A complete removal of NH(4)(+)-N and around 95% reduction of PO(4)(3-)-P was achieved within 24 h of treatment in bioreactors having the optimal algal bead concentration (12 beads ml(-1), equivalent to 1:3 algal beads:wastewater, v/v). The NH(4)(+)-N removal was significantly lower at low (around 4 beads ml(-1)) and high (>15 beads ml(-1)) algal bead concentrations. On the other hand, the effect of bead concentration on phosphate removal was less obvious, and bead concentrations ranging from 8 to 20 beads ml(-1) showed comparable percentages of phosphate reduction. Algal uptake and adsorption on alginate gels were found to be the major processes involved in the removal of N and phosphate in the present study. In addition, NH(4)(+)-N could be lost via ammonia volatilization while PO(4)(3-)-P was removed by chemical precipitation, as alkaline pH was recorded in the immobilized microalgal treatment system.     

Hemoglobin (Hb) immobilized on amino-modified magnetic nanoparticles for the catalytic removal of bisphenol A

Catalytic removal of bisphenol A from aqueous solution with hemoglobin immobilized on amino-modified magnetic nanoparticles as an enzyme catalyst was reported. The amino-modified magnetite nanoparticles were firstly prepared by the coprecipitation of Fe²⁺ and Fe³⁺ with NH₃·H₂O and then modified by 3-aminopropyltriethoxysilane. The immobilization process was optimized by examining enzyme concentration, glutaraldehyde concentration, cross-link time, and immobilization time. The optimum conditions for the removal of bisphenol A with immobilized hemoglobin were also investigated. Under the optimality conditions, the removal efficiency of bisphenol A was about 80.3%. The immobilization had a beneficial effect on the stability of hemoglobin and conversions of bisphenol A. According to the proposed breakdown pathway and the intermediates, the enzyme-catalytic removal of bisphenol A by the immobilized hemoglobin is considered to be an effective method.     

粉煤灰制备混凝剂及其对黄河水的处理效果

以粉煤灰和铁泥为原料、加入一定量NaCl作助溶剂室温下制备粉煤灰混凝剂,考察酸灰比与酸浓度对Fe3+、Al3+溶出率及混凝剂对黄河水处理效果的影响。结果表明,Fe3+、Al3+的最佳溶出条件为酸灰比3 mL/g、HCl浓度4 mol/L,此时Fe3+溶出率为28.1%,浓度为11.81 g/L;Al3+溶出率为5.2%,浓度为1.86 g/L。粉煤灰混凝剂对黄河水的处理效果在投加量2.38 mL/L、沉降时间30 min、pH 6.2～7.5时最佳,对浊度、SS和CODMn平均去除率分别为89.7%、83.6%和62.3%,优于传统市售混凝剂PAC和FC,Fe3+、Al3+同时存在有利于各自优势的发挥从而提高混凝效果。