UV/H2O2 oxidation of tri(2-chloroethyl) phosphate: Intermediate products, degradation pathway and toxicity evaluation

Tri(2-chloroethyl) phosphate (TCEP) with the initial concentration of 5 mg/L was degraded by UV/H₂O₂ oxidation process. The removal rate of TCEP in the UV/H₂O₂ system was 89.1% with the production of Cl^? and PO₄^3? of 0.23 and 0.64 mg/L. The removal rate of total organic carbon of the reaction was 48.8% and the pH reached 3.3 after the reaction. The oxidative degradation process of TCEP in the UV/H₂O₂ system obeyed the first order kinetic reaction with the apparent rate constant of 0.0025 min^?1 (R²=0.9788). The intermediate products were isolated and identified by gas chromatography-mass spectrometer. The addition reaction of HO? and H₂O and the oxidation reaction with H₂O₂ were found during the degradation pathway of 5 mg/L TCEP in the UV/H₂O₂ system. For the first time, environment risk was estimated via the “ecological structure activity relationships” program and acute and chronic toxicity changes of intermediate products were pointed out. The luminescence inhibition rate of photobacterium was used to evaluate the acute toxicity of intermediate products. The results showed that the toxicity of the intermediate products increased with the increase of reaction time, which may be due to the production of chlorine compounds. Some measures should be introduced to the UV/H₂O₂ system to remove the highly toxic Cl-containing compounds, such as a nanofiltration or reverse osmosis unit.     

Formation of halonitromethanes from methylamine in the presence of bromide during UV/Cl2 disinfection

The UV/Cl₂ process is commonly used to achieve a multiple-barrier disinfection and maintain residuals. The study chose methylamine as a precursor to study the formation of high-toxic halonitromethanes (HNMs) in the presence of bromide ions (Br⁻) during UV/Cl₂ disinfection. The maximum yield of HNMs increased first and then decreased with increasing concentration of Br⁻. An excessively high concentration of Br⁻ induced the maximum yield of HNMs in advance. The maximum bromine incorporation factor (BIF) increased, while the maximum bromine utilization factor (BUF) decreased with the increase of Br⁻ concentration. The maximum yield of HNMs decreased as pH value increased from 6.0 to 8.0 due to the deprotonation process. The BUF value remained relatively higher under an acidic condition, while pH value had no evident influence on the BIF value. The maximum yield of HNMs and value of BUF maximized at a Cl₂:Br⁻ ratio of 12.5, whereas the BIF value remained relatively higher at low Cl₂:Br⁻ ratios (2.5 and 5). The amino group in methylamine was first halogenated, and then released into solution as inorganic nitrogen by the rupture of C-N bond or transformed to nitro group by oxidation and elimination pathways. The maximum yield of HNMs in real waters was higher than that in pure water due to the high content of dissolved organic carbon. Two real waters were sampled to verify the law of HNMs formation. This study helps to understand the HNMs formation (especially brominated species) when the UV/Cl₂ process is adopted as a disinfection technique.     

Effect of organic wastes on the plant-microbe remediation for removal of aged PAHs in soils

The effectiveness of in-situ bioremediation of polycyclic aromatic hydrocarbons (PAHs) may be inhibited by low nutrients and organic carbon. To evaluate the effect of organic wastes on the PAHs removal efficiency of a plant-microbe remediation system, contaminated agricultural soils were amended with different dosages of sewage sludge (SS) and cattle manure (CM) in the presence of alfalfa (Medicago sativa L.) and PAHs-degraders (Bacillus sp. and Flavobacterium sp.). The results indicated that the alfalfa mean biomasses varied from 0.56 to 2.23 g/pot in root dry weight and from 1.80 to 4.88 g/pot in shoot dry weight. Low dose amendments, with rates of SS at 0.1% and CM at 1%, had prominent effects on plant growth and soil PAHs degradation. After 60-day incubation, compared with about 5.6% in the control, 25.8% PAHs removal was observed for treatments in the presence of alfalfa and PAHs-degraders; furthermore, when amended with different dosages of SS and CM, the removed PAHs from soils increased by 35.5%-44.9% and 25.5%-42.3%, respectively. In particular, the degradation of high-molecular-weight PAHs was up to 42.4%. Dehydrogenase activities (DH) ranged between 0.41 and 1.83 μupg triphenylformazan/(g dry soil. hr) and the numbers of PAHs-degrading microbes (PDM) ranged from 1.14× 10⁶ to 16.6× 10⁶ most-probable-number/g dry soil. Further investigation of the underlying microbial mechanism revealed that both DH and PDM were stimulated by the addition of organic wastes and significantly correlated with the removal ratio of PAHs. In conclusion, the effect of organic waste application on soil PAHs removal to a great extent is dependent on the interactional effect of nutrients and dissolved organic matter in organic waste and soil microorganisms.     

Carbonate-induced enhancement of phenols degradation in CuS/peroxymonosulfate system: A clear correlation between this enhancement and electronic effects of phenols substituents

This study investigated the enhancement effects of dissolved carbonates on the peroxymonosulfate-based advanced oxidation process with CuS as a catalyst. It was found that the added CO₃²⁻ increased both the catalytic activity and the stability of the catalyst. Under optimized reaction conditions in the presence of CO₃²⁻, the degradation removal of 4-methylphenol (4-MP) within 2 min reached 100%, and this was maintained in consecutive multi-cycle experiments. The degradation rate constant of 4-MP was 2.159 min⁻¹, being 685% greater than that in the absence of CO₃²⁻ (0.315 min⁻¹). The comparison of dominated active species and 4-MP degradation pathways in both CO₃²⁻-free and CO₃²⁻-containing systems suggested that more CO₃•⁻/¹O₂ was produced in the case of CO₃²⁻deducing an electron transfer medium, which tending to react with electron-rich moieties. Meanwhile, Characterization by X-ray photoelectron spectroscopic and cyclic voltammetry measurement verified CO₃²⁻ enabled the effective reduction of Cu²⁺ to Cu⁺. By investigating the degradation of 11 phenolics with different substituents, the dependence of degradation kinetic rate constant of the phenolics on their chemical structures indicated that there was a good linear relationship between the Hammett constants σ_p of the aromatic phenolics and the logarithm of k in the CO₃²⁻-containing system. This work provides a new strategy for efficient removal of electron-rich moieties under the driving of carbonate being widely present in actual water bodies.     

Decomplexation of Cu-1-hydroxyethylidene-1,1-diphosphonic acid by a three-dimensional electrolysis system with activated biochar as particle electrodes

The feasibility of decomplexation removal of typical contaminants in electroplating wastewater, complexed Cu(II) with 1-hydroxyethylidene-1,1-diphosphonic acid (Cu-HEDP), was first performed by a three-dimensional electric reactor with activated biochar as particle electrodes. For the case of 50 mg/L Cu-HEDP, Cu(II) removal (90.7%) and PO initial pH 7, acid-treated almond shell biochar (AASB) addition 20 g/L, and reaction time 180 min, with second-order rate constants of 1.10 × 10⁻³ and 1.94 × 10⁻⁵ min⁻¹respectively. The growing chelating effect between Cu(II) and HEDP and the comprehensive actions of adsorptive accumulation, direct and indirect oxidation given by particle electrodes accounted for the enhanced removal of Cu-HEDP, even though the mineralization of HEDP was mainly dependent on anode oxidation. The performance attenuation of AASB particle electrodes was ascribed to the excessive consumption of oxygen-containing functionalities during the reaction, especially acidic carboxylic groups and quinones on particle electrodes, which decreased from 446.74 to 291.48 µmol/g, and 377.55 to 247.71 µmol/g, respectively. Based on the determination of adsorption behavior and indirect electrochemical oxidation mediated by in situ electrogenerated H₂O₂ and reactive oxygen species (e.g., •OH), a possible removal mechanism of Cu-HEDP by three-dimensional electrolysis was further proposed.     

PM2.5 chemical composition and health risks by inhalation near a chemical complex

Particulate matter (PM_2.5) samples were collected in the vicinity of an industrial chemical pole and analysed for organic and elemental carbon (OC and EC), 47 trace elements and around 150 organic constituents. On average, OC and EC accounted for 25.2% and 11.4% of the PM_2.5 mass, respectively. Organic compounds comprised polycyclic aromatic hydrocarbons (PAHs), alkylated PAHs, anhydrosugars, phenolics, aromatic ketones, glycerol derivatives, aliphatic alcohols, sterols, and carboxyl groups, including aromatic, carboxylic and dicarboxylic acids. Enrichment factors > 100 were obtained for Pb, Cd, Zn, Cu, Sn, B, Se, Bi, Sb and Mo, showing the contribution of industrial emissions and nearby major roads. Principal component analysis revealed that vehicle, industrial and biomass burning emissions accounted for 66%, 11% and 9%, respectively, of the total PM_2.5-bound PAHs. Some of the detected organic constituents are likely associated with plasticiser ingredients and thermal stabilisers used in the manufacture of PVC and other plastics in the industrial complex. Photooxidation products of both anthropogenic (e.g., toluene) and biogenic (e.g., isoprene and pinenes) precursors were also observed. It was estimated that biomass burning accounted for 13.8% of the PM_2.5 concentrations and that secondary OC represented 37.6% of the total OC. The lifetime cancer risk from inhalation exposure to PM_2.5-bound PAHs was found to be negligible, but it exceeded the threshold of 10⁻⁶ for metal(loi)s, mainly due to Cr and As.     

Feasibility of bioleaching combined with Fenton oxidation to improve sewage sludge dewaterability

A novel joint method of bioleaching with Fenton oxidation was applied to condition sewage sludge. The specific resistance to filtration (SRF) and moisture of sludge cake (MSC) were adopted to evaluate the improvement of sludge dewaterability. After 2-day bioleaching, the sludge pH dropped to about 2.5 which satisfied the acidic condition for Fenton oxidation. Meanwhile, the SRF declined from 6.45 × 10¹⁰ to 2.07 × 10¹⁰ s²/g, and MSC decreased from 91.42% to 87.66%. The bioleached sludge was further conditionedwith Fenton oxidation. From an economical point of view, the optimal dosages of H₂O₂ and Fe2+ were 0.12 and 0.036 mol/L, respectively, and the optimal reaction time was 60 min. Under optimal conditions, SRF, volatile solids reduction, and MSC were 3.43 × 10⁸ s²/g, 36.93%, and 79.58%, respectively. The stability and settleability of sewage sludge were both improved significantly. Besides, the results indicated that bioleaching-Fenton oxidation was more efficient in dewatering the sewage sludge than traditional Fenton oxidation. The sludge conditioningmechanisms by bioleaching-Fenton oxidationmight mainly include the flocculation effects and the releases of extracellular polymeric substances-bound water and intercellular water.     

Molecular characterization of transformation and halogenation of natural organic matter during the UV/chlorine AOP using FT-ICR mass spectrometry

UV/chlorine process, as an emerging advanced oxidation process (AOP), was effective for removing micro-pollutants via various reactive radicals, but it also led to the changes of natural organic matter (NOM) and formation of disinfection byproducts (DBPs). By using negative ion electrospray ionization coupled with Fourier transform ion cyclotron resonance mass spectrometry (ESI FT-ICR MS), the transformation of Suwannee River NOM (SRNOM) and the formation of chlorinated DBPs (Cl-DBPs) in the UV/chlorine AOP and subsequent post-chlorination were tracked and compared with dark chlorination. In comparison to dark chlorination, the involvement of ClO^?, Cl^?, and HO^? in the UV/chlorine AOP promoted the transformation of NOM by removing the compounds owning higher aromaticity (AI_mod) value and DBE (double-bond equivalence)/C ratio and causing the decrease in the proportion of aromatic compounds. Meanwhile, more compounds which contained only C, H, O, N atoms (CHON) were observed after the UV/chlorine AOP compared with dark chlorination via photolysis of organic chloramines or radical reactions. A total of 833 compounds contained C, H, O, Cl atoms (CHOCl) were observed after the UV/chlorine AOP, higher than 789 CHOCl compounds in dark chlorination, and one-chlorine-containing components were the dominant species. The different products from chlorine substitution reactions (SR) and addition reactions (AR) suggested that SR often occurred in the precursors owning higher H/C ratio and AR often occurred in the precursors owning higher aromaticity. Post-chlorination further caused the cleavages of NOM structures into small molecular weight compounds, removed CHON compounds and enhanced the formation of Cl-DBPs. The results provide information about NOM transformation and Cl-DBPs formation at molecular levels in the UV/chlorine AOP.     

A strategy for enhancing anaerobic digestion of waste activated sludge: Driving anodic oxidation by adding nitrate into microbial electrolysis cell

Cathodic reduction of CO₂ and anodic oxidation of organic matters are crucial to methane-producing microbial electrolysis cell (MEC) applied in anaerobic digestion of waste activated sludge. However, cathodic CO₂ reduction is usually restrained by slow metabolism rates of H₂-utilizing methanogens and low electron-capturing capacity of CO₂, which consequently slows down the anodic oxidation that participates to sludge disintegration. Herein, a strategy with adding nitrate as electron acceptor to foster electronic transfer between the anode and cathode was proposed to improve anodic oxidation. Results showed that the average efficiency of anodic oxidation in the nitrate-added MEC increased by 55.9%. Accordingly, volatile suspended solid removal efficiency in the nitrate-added MEC was 21.9% higher than that of control MEC. Although the initial cumulative methane production in the nitrate-added MEC was lower than that of control MEC, the cumulative methane production in 24?days was 8.9% higher. Fourier transform infrared spectroscopy analysis indicated that anodic oxidation of MEC with nitrate accelerated the disintegration of sludge flocs and cell walls. Calculation on current signal further revealed that anodic oxidation driven by cathodic nitrate reduction was the main mechanism responsible for the improved sludge digestion.     

Dosing low-level ferrous iron in coagulation enhances the removal of micropollutants, chlorite and chlorate during advanced water treatment

Drinking water utilities are interested in upgrading their treatment facilities to enhance micropollutant removal and byproduct control. Pre-oxidation by chlorine dioxide (ClO₂) followed by coagulation-flocculation-sedimentation and advanced oxidation processes (AOPs) is one of the promising solutions. However, the chlorite (ClO₂^–) formed from the ClO₂ pre-oxidation stage cannot be removed by the conventional coagulation process using aluminum sulfate. ClO₂^– negatively affects the post-UV/chlorine process due to its strong radical scavenging effect, and it also enhances the formation of chlorate (ClO₃^–). In this study, dosing micromolar-level ferrous iron (Fe(II)) into aluminum-based coagulants was proposed to eliminate the ClO₂^– generated from ClO₂ pre-oxidation and benefit the post-UV/chlorine process in radical production and ClO₃^– reduction. Results showed that the addition of 52.1-µmol/L FeSO₄ effectively eliminated the ClO₂^– generated from the pre-oxidation using 1.0 mg/L (14.8 µmol/L) of ClO₂. Reduction of ClO₂^– increased the degradation rate constant of a model micropollutant (carbamazepine) by 55.0% in the post-UV/chlorine process. The enhanced degradation was verified to be attributed to the increased steady-state concentrations of HO^· and ClO^· by Fe(II) addition. Moreover, Fe(II) addition also decreased the ClO₃^– formation by 53.8% in the UV/chlorine process and its impact on the formation of chloro-organic byproducts was rather minor. The findings demonstrated a promising strategy to improve the drinking water quality and safety by adding low-level Fe(II) in coagulation in an advanced drinking water treatment train.     

辽河干流消落区沉积物重金属污染特征研究

通过测定辽河干流消落区10个断面中0~5cm、5~15cm、15~30cm深沉积物中重金属Pb、Cu、Zn、Cd含量,揭示消落区干－湿交替下沉积物重金属的污染特征.采用原子吸收分光光度计测定重金属含量,并采用地质累积指数与潜在生态危害指数评估重金属污染状况.结果表明,除Cd外,Cu、Zn与Pb的含量均值分别为31.4mg/kg、28.14mg/kg、43.75mg/kg,均低于中国土壤环境质量标准I级土壤标准;Cd含量均值1.438mg/kg,是中国土壤环境质量标准I级土壤标准的7.19倍,是辽河水系沉积物平均值的1.29倍,辽宁省土壤背景值的13.31倍,表明研究区Cd污染严重.地质累积指数评价表明,Pb、Cu、Zn的污染程度低于1级,Cd达2级中度污染以上,在通江口达3.92,为5级强污染;据潜在生态危害评价,达牛渡口上游干流潜在生态危害指数为强以上,通江口生态危害指数最高,且生态危害主要来源于Cd.相关性分析表明,Pb、Cu与Zn间相关性极显著,可能有相同的污染源,Cd有单独的污染源.     

四溴双酚-A和五溴酚对红鲫甲状腺激素和脱碘酶的影响

将红鲫(Carassius auratus)分别暴露于0.5mg·L-1四滇双酚-A(TBBPA)和0.1 mg·L-1五澳酚(PBP)中28 d,采用放射性免疫分析法和化学发光酶联免疫分析法检测红鲫的血清甲状腺激素水平和肝脏脱碘酶活性.结果显示,TBBPA能使红鲫血清TT4和TT3水平降低,rT3水平、肝脏脱碘酶ID2和ID3活性升高.PBP对红鲫甲状腺系统的干扰要小于TBBPA,它对红鲫血清TT3水平和ID2活性几乎没有影响.上述结果表明,TBBPA和PBP能够干扰红鲫体内甲状腺激素的稳态,加速甲状腺激素在肝脏内的转化和代谢;这可能是通过抑制甲状腺激素与运载蛋白的结合来实现的.     

油田采出水膜法处理技术应用研究进展

油田采出水的处理回用是一种必然的趋势.膜法处理技术可以解决传统水处理中存在的问题,有效地去除采出水中的油类、细菌、硬度,防止油层堵塞、结垢和外排水的环境污染,对于促进油气田可持续发展、水资源再利用和环境保护具有非常重要的意义.微滤、超滤和纳滤、反渗透膜技术在油田采出水处理中已有较多的应用研究.超滤在除油和除浊方面表现出...     

四氯乙烯胁迫对草鱼抗氧化酶活性的影响及其机理

研究了四氯乙烯(PCE)对草鱼的肝胰脏、肾脏和鳃组织的超氧化物歧化酶(SOD)和过氧化物酶(POD)的影响.结果表明:草鱼肝胰脏SOD活性,在PCE低浓度胁迫时其SOD活性“先升后降”[72h SOD是(6665.84±106.87)U/g·FW,168h SOD是(3021.26±16.96)U/g·FW],高浓度胁迫时“先降后升再降”[24h SOD是(2175.16±185.14)U/g·FW, 96h SOD是(5692.19±44.17)U/g·FW,168h SOD是(1297.70±11.52)U/g·FW];草鱼肾脏SOD活性在PCE所有浓度组胁迫均是“先降后升再降”的趋势;草鱼鳃组织SOD酶活性只有在PCE较低浓度短时间内没有显著变化,其它情况始终降低.在PCE低浓度和中等浓度胁迫时,草鱼肝胰脏POD活性始终降低,较低浓度和高浓度胁迫时肝胰脏POD活性“先降后升再降”;草鱼肾脏POD活性在PCE低浓度胁迫时“先升后降再升又降”的趋势,而高浓度胁迫时“先降后升又降”;PCE对草鱼鳃组织POD活性“先升后降”的趋势.但是草鱼鳃组织的SOD和POD活性明显低于肝胰脏和肾脏组织的SOD和POD活性.     

P对小麦Cd和As吸收与转运的影响

为了探究磷（P）对小麦幼苗镉（Cd）和砷（As）吸收转运生理机制的影响,通过水培试验,以百农207为供试材料,研究了Cd和As胁迫条件下,外源供P和缺P处理对小麦幼苗生长、根系形态、光合参数、抗氧化系统、离子含量和根茎转移系数的影响.结果表明,与缺P处理相比,外源P供应显著增加As胁迫下小麦幼苗叶绿素的含量,促进根系的生长发育,提高了生物量,而对Cd胁迫下小麦幼苗的生长影响不显著.外源P供应时显著增加了Cd胁迫条件下根系的P和Cd含量,降低了地上部的P和Cd含量;同时显著提高了As胁迫条件下地上部的P和As含量以及As向地上部的转移系数.因此,供P与否对小麦幼苗Cd和As毒害的影响表现出明显的差异性;As胁迫时,外源供P提高了As向地上部的转运能力以及根系的CAT活性,降低了As对小麦的毒害,从而促进了小麦幼苗生物量的累积;而在Cd胁迫条件下,P与Cd之间表现出一定的协同效应,外源供P在一定程度上加重了Cd对小麦的毒害效应.     

垃圾焚烧厂渗滤液处置工艺中溶解性有机物变化特性

采用“物化+生物处理+深度处理”组合工艺处理垃圾焚烧厂渗滤液,探索组合工艺对渗滤液的实际去除效果,考察渗滤液中溶解性有机物(DOM)的组成及其结构特性随组合工艺的变化规律,并对其机理进行了初步探讨.结果表明,当进水COD和氨氮的平均值分别为17825,1946mg/L时,组合工艺对渗滤液中COD和氨氮去除率均达到99%左右,出水COD、氨氮、色度分别为57mg/L、5mg/L、15倍.组合工艺对渗滤液DOM中腐殖酸(HA)、富里酸(FA)和亲水性有机物(HyI)的去除率均达到99%左右,对HA、FA、HyI削减显著的工艺单元分别为混凝2、厌氧和颗粒活性炭(GAC),削减率分别达到86%、77%和84%.出水HA、FA和HyI的COD浓度分别为10,23,6mg/L,其中分子量较小的FA为出水主要组分.随着组合工艺处理过程的进行,渗滤液中DOM的紫外区吸光度值显著下降,DOM的E254、E253/E203分别由1.55、0.64下降至0.012和0.024,说明DOM的芳香性和复杂程度显著降低,脂肪链芳香化合物逐渐增加;此外,E300/E400和E465/E665分别由2.65和2.17增加至9.78和8.03,表明渗滤液中溶解性有机物腐殖化程度不断降低,芳香构化程度不断减小.     

DOM对纳滤膜去除磺胺甲恶唑效果影响研究

试验研究几种不同可溶性有机物(DOM)对纳滤膜(NF)去除抗生素磺胺甲恶唑(SMZ)的影响效果.试验所用DOM选定腐殖酸(HA)、单宁酸(TA)和海藻酸钠(SA).结果显示3种DOM对SMZ去除率和通量影响迥异,并与DOM的亲疏水性有密切的关系.为更好了解DOM对NF去除SMZ的影响机理,试验对臭氧化HA也进行了研究.臭氧化HA相对于臭氧前HA亲水性显著提高,对SMZ去除率的影响相应提高.结果表明在有多种DOM共同存在的天然原水中,SMZ的去除机理十分复杂,DOM的本身物理化学性质对于目标物的去除效果十分重要.     

氯氰菊酯对小鼠脑细胞的氧化损伤及维生素E的抗氧化作用

以昆明小鼠为受试动物,随机分为6组,包括1个阴性对照组、3个氯氰菊酯染毒组、1个维生素E组和1个高剂量氯氰菊酯加维生素E组,染毒组按10,20,40mg/kg 3个剂量水平,维生素E的剂量为100mg/kg,灌胃染毒小鼠7d.以脑组织匀浆测定活性氧(ROS)、还原型谷胱甘肽(GSH)和丙二醛(MDA)的含量;以脑组织细胞测定DNA-蛋白质交联(DPC)系数.随着氯氰菊酯染毒剂量的升高,脑组织的ROS、MDA含量和DPC系数逐渐上升,GSH含量逐渐降低,各指标呈一定的剂量-效应关系.染毒剂量320mg/kg时,ROS含量(841.3±100.34)、GSH含量[(12.54±1.316)nmol/L]和DPC系数(0.054±0.004)有显著差异(P<0.05);染毒剂量340mg/kg时,GSH含量[(10.51±1.545)nmol/L]有显著差异(P<0.05),ROS含量(1014.3±81.67)、MDA含量[(2.849±0.218)μmol/L]和DPC系数(0.079±0.005)有极显著差异(P<0.01).高剂量染毒加维生素E组与高剂量染毒组相比较,脑组织的ROS、MDA含量和DPC系数均有下降,GSH含量上升.脑组织的ROS(719.5±74.56)、GSH[(16.52±1.985)nmol/L]和DPC系数(0.055±0.005)有显著差异(P<0.05),MDA含量[(1.662±0.265)μmol/L]有极显著差异(P<0.01).较高剂量(320mg/kg)的氯氰菊酯能造成小鼠脑组织的氧化损伤,维生素E有抗氧化作用.     

胞外聚合物和信号分子对厌氧氨氧化污泥活性的影响

为了探究胞外聚合物（EPS）对厌氧氨氧化颗粒污泥活性的影响,分别向厌氧氨氧化颗粒污泥中投加30mg/L的总胞外聚合物（IN-EPS）,松散结合型胞外聚合物（LB-EPS）和紧密结合型胞外聚合物（TB-EPS）.结果表明,3种EPS均可提高厌氧氨氧化颗粒污泥的活性.对于添加了IN-EPS,LB-EPS和TB-EPS的实验组,厌氧氨氧化颗粒污泥的氨氮去除速率分别增加了6.68%,10.5%和19.29%,厌氧氨氧化菌的生长速率分别增加了18.25%,21%,16.3%.三维荧光光谱法分析发现3种EPS的组成基本相同,以芳香族蛋白质和可溶性微生物产物为主.对EPS中的高丝氨酸内酯类（AHLs）信号分子进行检测,发现EPS中含有3种信号分子,分别是C4-HSL,C6-HSL和C10-HSL,外源投加这3种AHLs到厌氧氨氧化颗粒污泥中,结果发现C4-HSL和C6-HSL可以提高厌氧氨氧化颗粒污泥的活性和生长速率,这是EPS可以提高厌氧氨氧化菌活性的原因.     

污泥掺烧过程中Cl/S/P/矿物质的热交互作用对Cd迁移转化行为的影响

采用化学热力学平衡分析方法,应用污泥实测数据模拟计算了污泥掺烧过程中Cl/S/P与矿物质的交互作用,重点模拟研究了Cl/S/P/矿物质交互体系对Cd迁移转化的影响.研究结果表明,污泥掺烧过程含Cl、S及P逸出气体以HCl(g)、SO_2(g)及(P_2O_5)_2(g)形式排放.污泥掺烧含有CaO-SiO_2-Al_2O_3体系中,CaO可以抑制S以SO_2(g)释放,而SiO_2及Al_2O_3对SO_2(g)逸出有促进作用,同时CaO及Al_2O_3可以抑制P的挥发.污泥掺烧过程中SiO_2及Al_2O_3对Cd挥发都有一定抑制作用,但CaO及Fe_2O_3对Cd基本无影响;当Cl存在时,Ti O2和SiO_2对Cd吸附作用减弱,并使Al_2O_3吸附剂失效;当S存在时,可导致吸附剂对Cd中毒,而P可导致Al_2O_3吸附剂失效;Cl-S-P耦合体系中,单一矿物质对Cd迁移转化影响主要受Cl和S控制.SiO_2+CaO+Al_2O_3共存体系中,Cl的存在可导致固体吸附剂SiO_2和Al_2O_3失效;S、S+Cl、S+P、S+Cl+P的存在受控元素为S,并且可以抑制Cd的挥发;P、Cl+P的存在对Cd影响受控元素为Cl,可促进Cd挥发.