膜法处理难降解石化废水的预处理工艺研究

采用混凝法分别以聚合氯化铁（PFC）、聚合氯化铝（PAC）和聚合硫酸铁（PFS）为混凝剂处理天津某石油化工厂二级氧化处理工艺出水，PFC对废水COD的去除效果最好，在PFC加入量为120mg／L时，废水的COD去除率最高，为22．35％。经正交实验确定了Fenton试剂氧化法处理废水的最佳实验条件为：Fe^2＋加入量290mg／L、H2O2加入量100mg／L、pH=6、反应时间30min，此时COD去除率为20．45％。活性炭吸附法对废水的处理效果随活性炭加入量增加而改善，活性炭的最佳加入量为2000mg／L，此时废水的COD去除率最高，为87．78％。     

聚硅硫酸铝的制备及其絮凝性能

以Na2SiO3·9H2O，Al2（SO4）3·18H2O为原料，加入一定量稳定剂，采用复合法制备出高铝含量且稳定的聚硅硫酸铝（PASS）。研究结果表明：采用磷酸氢二钠与烷基糖苷（质量比为1：1）作为复合稳定剂，在碱化度为1．5～1．8、Ⅳ（A1）：Ⅳ（Si）=1．0～3．0的条件下，合成的PASS絮凝效果最佳；复合稳定剂对废水的COD去除率及浊度去除率影响不大，但能显著改善絮凝产品的稳定性；PASS可用于处理pH范围较宽（pH为6．0—11．0）的工业废水，且处理前后废水pH变化不大；PASS对低温低浊度废水有较好的絮凝效果；在加入量相同的情况下，PASS的絮凝性能明显优于聚合硫酸铝、硫酸铝、聚合硫酸铁，当PASS加入量为40～100恤L／L时，废水浊度去除率达98％以上。     

聚合硅酸氯化铝铁的制备及其絮凝性能

利用盐酸酸洗废液制备聚合硅酸氯化铝铁（PSAFC），并用PSAFC处理造纸脱墨废水，考察了各种因素对絮凝效果的影响。实验结果表明：在废水pH为6、PSAFC加入量为240mg／L、搅拌转速为150r／min、搅拌时间为2min，静置时间为25min的条件下，COD、浊度、色度的去除率分别为87．2％，99．2％，94．5％；PSAFC的絮凝效果明显好于市售的聚合氯化铝和聚合氯化铁.     

经济型阳离子淀粉絮凝剂的制备及其对印染废水的处理效果

采用玉米淀粉为原料、氯化缩水甘油三甲基铵（GTA）作阳离子化试剂、水-乙醇混合液作分散剂、NaOH作碱催化剂，制备了经济型阳离子淀粉絮凝剂（简称经济型阳离子淀粉）。实验结果表明：在淀粉加入量110g、GTA加入量30g、NaOH加入量1．6g、分散剂中m（水）：m（乙醇）=1：1、m（分散剂）：m（淀粉）=0．50：1、反应温度80℃、反应时间2．5h的条件下，可制得取代度（DS）为0．31的经济型阳离子淀粉；用该经济型阳离子淀粉与聚丙烯酰胺（PAM）联用处理印染废水，当经济型阳离子淀粉加入量为140mg／L、PAM加入量为4mg/L、废水pH为8时，印染废水的色度去除率和COD去除率分别达92％和82％。该方法絮凝效果好，药剂费用低，产生的污泥少。     

絮凝沉淀-Fenton试剂氧化法处理含高浓度硫酸盐的洗涤剂生产废水

采用絮凝沉淀-Fenton试剂氧化法处理含高浓度硫酸盐的洗涤剂生产废水（简称废水），考察了各种因素对COD去除率的影响。实验结果表明：根据实际废水的水质情况，选用聚合氯化铝（PAC）为絮凝剂，PAC最佳加入量为0．3g／L，经絮凝处理后COD去除率为42．3％；Fenton试剂氧化的最佳操作条件为：n（H2O2）：n（Fe^2＋）=0．5、H2O2加入量为7mmol／L、反应时间为2h，不调节废水初始pH，经Fenton试剂氧化处理后COD去除率为70％以上。经絮凝沉淀-Fenton试剂氧化法处理后，废水COD由1950mg／L降至240mg／L，总的COD去除率为87．7％，废水处理效果良好。     

聚合氯化铝锌絮凝剂的制备及其性能

用在AlCl，与ZnCl2溶液中加NaOH溶液的方法制备无机高分子絮凝剂聚合氯化铝锌（PAZC），通过正交实验确定的最佳制备条件为：反应时间10min、碱化度2．2、氯化铝浓度0．5mol／L、NaOH溶液浓度0．5mol／L。在n（Zn）：n（Al）=0．6、水样pH=7．8、PAZC加入量为5mg／L的条件下，浊度和COD去除率分别为98．9％和88．2％。PAZC与聚合氯化铝对各种工业废水的处理效果比较结果表明，PAZC对各种工业废水的处理效果较好。从废水处理成本来看，PAZC具有较好的经济效益。     

微波-改性活性炭-Fenton试剂氧化法降解水中2,4-二氯酚

以经Fe2（SO4）3溶液浸渍改性的活性炭作催化剂、Fenton试剂作氧化剂，采用微波-改性活性炭-Fenton试剂氧化法降解水中的2，4-二氯酚。考察了改性活性炭加入量、H2O2与Fe^2＋摩尔比、Fenton试剂加入量、微波功率和2，4-二氯酚溶液初始pH对2，4-二氯酚降解效果的影响。在改性活性炭加入量1．0g／L、n（H2O2）：n（Fe^2＋）=16．7（H2O2加入量6．0mmol／L、Fe^2＋加入量0．36mmol／L）、Fenton试剂加入量为6．36mmol／L、微波功率600W、微波辐射时间10min、2，4-二氯酚溶液初始pH为6．0的条件下，2，4-二氯酚降解率和TOC去除率分别可达98．7％和84．0％。     

混凝—催化氧化法处理丁苯橡胶生产废水

以聚合氯化铝（PAC）、阴离子聚丙烯酰胺（PAM）为混凝剂，以H2O2-O3为氧化剂，采用混凝-催化氧化法处理对丁苯橡胶生产废水。考察了混凝剂种类及其加入量、废水pH对混凝处理效果的影响，氧化剂及其加入量、反应时间和废水pH对COD去除率的影响。实验得出的最佳工艺条件：混凝实验，废水pH为7、PAC和PAM加入量为400mg／L和4mg／L；催化氧化实验，废水pH为7～8、H2O2加入量为200mg／L、H2O2与O3的质量比为0．5。处理后，废水COD从860mg／L降至145mg／L，COD去除率达83．1％，出水水质达到国家二级排放标准。     

改性粉煤灰吸附-高级氧化法处理奥里油废水

将氯化铁改性粉煤灰（简称改性粉煤灰）吸附处理与高级氧化和生物处理等技术进行优化组合，以期得到简便而有效的处理奥里油废水（简称废水）的组合工艺。研究结果表明：在废水COD平均为4600mg／L、改性粉煤灰加入量为50g／L、废水pH为7～9、吸附时间为1h的条件下，COD去除率达30％。采用“改性粉煤灰一次吸附-湿式均相催化氧化-厌氧生物过程-改性粉煤灰二次吸附”组合工艺处理废水时，改性粉煤灰不但具有较好的预处理效果，且还有较好的后处理能力；湿式均相催化氧化的催化剂用量少（Cu（NO3）2为2．0g／L）、操作条件温和（2．5MPa，180℃，pH5—7，1h）；厌氧生物过程中不需特殊筛选的菌种，易操作控制；经该组合工艺处理后，废水COD从4600mg／L降至55mg／L，COD去除率为98．4％，达到GB8978-1996《污水综合排放标准》的一级排放标准。     

Fenton试剂氧化—石灰法处理苎麻脱胶废水

采用Fenton试剂氧化一石灰法处理苎麻脱胶废水（简称废水）。在pH为8．3的废水中FeSO4·7H2O、H2O2、饱和石灰乳的加入量分别为1．5g／L、1．0mL／L和1．0mL／L的条件下对废水进行处理，废水COD由650mg／L降至200mg／L以下，COD去除率约为70％；色度由500倍降至70倍以下，色度去除率约为90％，出水COD和色度均达到GB8978-1996（污水综合排放标准）中的二级排放标准。     

Fe(Ⅱ)、Fe(Ⅲ)和Fe(Ⅵ)活化过硫酸盐氧化降解水中的菲

分别采用Fe(Ⅱ)、Fe(Ⅲ)和Fe(Ⅵ)活化过硫酸盐(PS)氧化降解水中的菲,考察了反应pH、药剂投加量及氧化时间等因素的影响,并对比了不同价态铁活化PS对菲的氧化降解效果.在反应pH为8、n(菲):n(Fe):n(PS)为1:2:2的优化条件下,反应60 min后Fe(Ⅱ)-PS和Fe(Ⅲ)-PS体系对菲的去除率分...     

Rapid discrimination of plastic packaging materials using MIR spectroscopy coupled with independent components analysis (ICA)

Plastic packaging wastes increased considerably in recent decades, raising a major and serious public concern on political, economical and environmental levels. Dealing with this kind of problems is generally done by landfilling and energy recovery. However, these two methods are becoming more and more expensive, hazardous to the public health and the environment. Therefore, recycling is gaining worldwide consideration as a solution to decrease the growing volume of plastic packaging wastes and simultaneously reduce the consumption of oil required to produce virgin resin. Nevertheless, a major shortage is encountered in recycling which is related to the sorting of plastic wastes. In this paper, a feasibility study was performed in order to test the potential of an innovative approach combining mid infrared (MIR) spectroscopy with independent components analysis (ICA), as a simple and fast approach which could achieve high separation rates. This approach (MIR-ICA) gave 100% discrimination rates in the separation of all studied plastics: polyethylene terephthalate (PET), polyethylene (PE), polypropylene (PP), polystyrene (PS) and polylactide (PLA). In addition, some more specific discriminations were obtained separating plastic materials belonging to the same polymer family e.g. high density polyethylene (HDPE) from low density polyethylene (LDPE). High discrimination rates were obtained despite the heterogeneity among samples especially differences in colors, thicknesses and surface textures. The reproducibility of the proposed approach was also tested using two spectrometers with considerable differences in their sensitivities. Discrimination rates were not affected proving that the developed approach could be extrapolated to different spectrometers. MIR combined with ICA is a promising tool for plastic waste separation that can help improve performance in this field; however further technological improvements and developments are required before it can be applied at an industrial level given that all tests presented here were performed under laboratory conditions.     

Volatilization and Biodegradation of VOCs in Membrane Bioreactors (MBR)

Volatilization and biodegradation are major competitive volatile organic compound (VOC) removal mechanisms in biological wastewater treatment process, which depend on compound specific properties and system design/operational parameters. In this study, a mathematical model was used to determine major removal pathways at various organic loading rates (OLR), solids residence time (SRT) and dissolved oxygen (DO) concentrations in a biological process for vinyl acetate. Model results showed that biological treatment process should be designed with long SRT, high OLR and low DO concentrations to maximize biodegradation and minimize volatilization of VOCs. Unless a VOC is toxic to microorganisms under the given conditions, low VOC emission rates are an inherent advantage of MBRs, which operate at higher OLR and longer SRT compared to conventional activated sludge process. A lab scale membrane bioreactor (MBR) was operated at varying OLR to investigate the relative volatilization and biodegradation rates for acetaldehyde, butyraldehyde and vinyl acetate. Synthetic wastewater containing three VOCs was introduced to the MBR. The DO concentration and SRT was maintained at 2.0 mg L^{− 1} and 100 days, respectively. The overall VOC removal rate was more than 99.7% for three VOCs at all the OLR. For vinyl acetate, the biodegradation rate increased from 93.87 to 99.40% and the volatilization removal rate decreased from 6.09 to 0.59% as OLR was increased from 1.1 to 2.0 kg COD m^{− 3} d^{− 1}. It was confirmed that a MBR can be a promising solution to reduce VOC emissions from wastewater.     

Microbial degradation of poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) in compost

The microbial degradation of tensile test pieces made of poly(3-hydroxybutyrate) [P(3HB)] or copolymers with 10% [P(3HB-co-10%3HV)] and 20% [P(3HB-co-20%3HV)] 3-hydroxyvaleric acid was studied in small household compost heaps. Degradation was measured through loss of weight (surface erosion) and changes in molecular weight and mechanical strength. It was concluded, on the basis of weight loss and loss of mechanical properties, that P(3HB) and P(3HB-co-3HV) plastics were degraded in compost by the action of microorganisms. No decrease inM _w could be detected during the degradation process. The P(3HB-co-20%3HV) copolymer was degraded much faster than the homopolymer and P(3HB-co-10%3HV). One hundred nine microbial strains capable of degrading the polymersin vitro were isolated from the samples used in the biodegradation studies, as well as from two other composts, and identified. They consisted of 61 Gram-negative bacteria (e.g.,Acidovorax facilis), 10 Gram-positive bacteria (mainlyBacillus megaterium), 35Streptomyces strains, and 3 molds.     

Sustainable design for automotive products: Dismantling and recycling of end-of-life vehicles

The growth in automotive production has increased the number of end-of-life vehicles (ELVs) annually. The traditional approach ELV processing involves dismantling, shredding, and landfill disposal. The “3R” (i.e., reduce, reuse, and recycle) principle has been increasingly employed in processing ELVs, particularly ELV parts, to promote sustainable development. The first step in processing ELVs is dismantling. However, certain parts of the vehicle are difficult to disassemble and use in practice. The extended producer responsibility policy requires carmakers to contribute in the processing of scrap cars either for their own developmental needs or for social responsibility. The design for dismantling approach can be an effective solution to the existing difficulties in dismantling ELVs. This approach can also provide guidelines in the design of automotive products. This paper illustrates the difficulty of handling polymers in dashboards. The physical properties of polymers prevent easy separation and recycling by using mechanical methods. Thus, dealers have to rely on chemical methods such as pyrolysis. Therefore, car designers should use a single material to benefit dealers. The use of materials for effective end-of-life processing without sacrificing the original performance requirements of the vehicle should be explored.     

pH对厌氧氨氧化反应脱氮效能的影响

采用具有恒定pH功能的SBR接种厌氧氨氧化颗粒污泥,研究了pH对厌氧氨氧化菌脱氮效能的影响。实验结果表明:在进水ρ(氨氮)和ρ(亚硝酸盐氮)分别为58.00 mg/L和79.28 mg/L、TN容积负荷为0.82 kg/(m3·d)、不控制反应pH的条件下,随着反应的进行,pH不断升高,当pH=8.02时,菌种的去除效能最高;在进水ρ(氨氮)和ρ(亚硝酸盐氮)分别为120.00 mg/L和159.33 mg/L、TN容积负荷为1.62 kg/(m3·d)、恒定反应pH为8.00的条件下,反应4.0 h时的容积基质氮去除速率(NRR)达到1.42 kg/(m3·d),氨氮去除率达98.39%,亚硝酸盐氮去除率达99.48%;拟合曲线推导的最适pH的理论值为7.85,反应4.0 h时的NRR理论最大值达1.52 kg/(m3·d)。     

氯苯类生产过程POPs污染风险点分析及环境管理建议

我国氯苯类生产过程中的二噁英类、五氯苯、六氯苯等非故意产生类持久性有机污染物对环境具有潜在风险。对具有典型工艺特征的氯苯类生产过程中关键节点的二噁英类进行了检测和分析,在残渣、残液、废水和副产品(多氯苯混合物)中发现高浓度二噁英类,主要成分为多氯代二苯并呋喃,推测可能与原料中呋喃类杂质有关。为践行我国《关于持久性有机污染物的斯德哥尔摩公约》的履约责任和控制二噁英类排放造成的环境风险,结合国内外相关管理制度提出了法规制度、监督管理、工艺改进、产品质控和废物处置等方面的环境管理建议。     

Characterization of Shredder Residues generated and deposited in Denmark

This study presents a detailed characterization of Shredder residues (SR) generated and deposited in Denmark from 1990 to 2010. It represents approximately 85% of total Danish SR. A comprehensive sampling, size fractionation and chemical analysis was carried out on entire samples as well as on each individual size fraction. All significant elemental contents except oxygen were analyzed. The unexplained “balance” was subsequently explained by oxygen content in metal oxides, carbonates, sulphates and in organics, mainly cellulose. Using mass and calorific balance approaches, it was possible to balance the composition and, thereby, estimate the degree of oxidation of elements including metals. This revealed that larger fractions (>10 mm, 10–4 mm, 4–1 mm) contain significant amount of valuable free metals for recovery. The fractionation revealed that the >10 mm coarse fraction was the largest amount of SR being 35–40% (w/w) with a metal content constituting about 4–9% of the total SR by weight and the <1 mm fine fraction constituted 27–37% (w/w) of the total weight. The lower heat value (LHV) of SR samples over different time periods (1990–2010) was between 7 and 17 MJ/kg, declining with decreasing particle size. The SR composition is greatly dependent on the applied shredding and post shredding processes at the shredding plants causing some variations. There are uncertainties related to sampling and preparation of samples for analyses due to its heterogeneous nature and uncertainties in the chemical analyses results (≈15–25%). This exhaustive characterization is believed to constitute hitherto the best data platform for assessing potential value and feasibility of further resource recovery from SR.     

Evaluation of Poly(ethylene-terephthalate) Products of Chemical Recycling by Differential Scanning Calorimetry

Poly (ethylene-terephthalate), (PET) bottles waste was chemically recycled by glycolysis and hydrolysis. The depolymerization processes were carried out in different time intervals from 5 to 360 min, in two different molar ratios of PET/EG, 1:5 and 1:18 and at different temperatures. The PET glycolysis leads to formation of bis(2-hydroxy-ethyl)terephthalate (BHET) monomer and PET oligomers with hydroxyl and carboxyl end groups while PET hydrolysis is followed by formation of monomers terephthalic acid (TPA) and ethylene glycol (EG). Fractions of monomers and oligomers were further characterized by FTIR spectroscopy and by differential scanning calorimetry (DSC). The results show that DSC is successful method to describe the different structures of oligomers formed during chemical recycling of PET.     

A historical perspective of Global Warming Potential from Municipal Solid Waste Management

The Municipal Solid Waste Management (MSWM) sector has developed considerably during the past century, paving the way for maximum resource (materials and energy) recovery and minimising environmental impacts such as global warming associated with it. The current study is assessing the historical development of MSWM in the municipality of Aalborg, Denmark throughout the period of 1970 to 2010, and its implications regarding Global Warming Potential (GWP₁₀₀), using the Life Cycle Assessment (LCA) approach. Historical data regarding MSW composition, and different treatment technologies such as incineration, recycling and composting has been used in order to perform the analysis. The LCA results show a continuous improvement in environmental performance of MSWM from 1970 to 2010 mainly due to the changes in treatment options, improved efficiency of various treatment technologies and increasing focus on recycling, resulting in a shift from net emission of 618 kg CO₂-eq. tonne^?1 to net saving of 670 kg CO₂-eq. tonne^?1 of MSWM.