膨胀颗粒污泥床反应器处理啤酒废水

对接种市政消化污泥的膨胀颗粒污泥床（EGSB）反应器的启动及启动成功后在35℃和15℃时的运行特性进行了研究。结果表明：EGSB反应器采用低进水COD、高有机负荷方式，46d快速启动成功；在35℃、HRT为3．4h、液体上升流速为2．80m／h的条件下，COD去除率均能保持在90．0％以上；温度在进水COD为450mg／L左右时对COD去除率影响不明显，但在1700mg／L左右时影响明显；EGSB反应器能在15℃的低温条件下稳定高效运行；在短时间内经历15℃→50℃→15℃的温度冲击和4．32kg／（m^3·d）到15．50kg／（m^3·d）的负荷冲击后能在8d和14d内快速恢复；经历35℃→17℃→35℃的温度冲击后，COD去除率的恢复没有出现滞后期。     

EGSB—MBBR处理高浓度聚酯废水

采用膨胀床颗粒污泥反应器(EGSB)—移动床生物膜反应器(MBBR)处理高浓度、难降解(COD≥10000mg/L,BOD5/COD0.3)聚酯废水。实验结果表明:在(37±1)℃、停留时间(HRT)为15.4h、进水COD为10000mg/L的条件下,EGSB反应器容积负荷达5.31kg/(m3.d),COD去除率达95%以上;在室温、HRT为48.0h的条件下,MBBR反应器出水COD100mg/L,BOD530mg/L,出水水质达到GB8978—1996《污水综合排放标准》中的一级排放标准。     

散射光下铁(III)-丙酮酸盐配合物还原铬(VI)的研究

研究了在散射光下铁(III)-丙酮酸盐配合物对铬(V I)的光还原反应;考察了溶液pH、铁(III)、丙酮酸钠、铬(V I)浓度对反应的影响;分析了铬(V I)光还原反应的动力学。实验结果表明:铁(III)-丙酮酸盐配合物体系能在较弱的散射光下还原铬(V I)。在铬(V I)浓度为19.2μm o l/L、铁(III)浓度为10.0μm o l/L、丙酮酸钠浓度为240μm o l/L、pH为3.0、光照240m in的条件下,铬(V I)的还原率达到99.7%。从表观动力学方程的反应级数看,铁(III)的级数(0.83)最高,铁(III)浓度是影响铬(V I)光还原反应速率的主要因素,铁(II)是铬(V I)光还原的主要还原剂。     

EGSB出水回流对EGSB—SBR工艺处理果汁废水的影响

采用EGSB—SBR工艺处理实际果汁废水(COD 2 608~6 500 mg/L,p H 5.0~7.0)。在EGSB反应器成功启动及驯化完成的情况下,连续运行49 d。实验结果表明:第25天起,控制EGSB回流比为3.00∶1,EGSB反应器可在无须添加Na HCO3的条件下稳定运行,从而降低了废水处理成本;第25天起,平均进水COD,BOD5,SS分别为5 968,2 130,1 020 mg/L,平均出水COD,BOD5,SS分别降至131,11,50 mg/L,平均COD,BOD5,SS去除率分别为98%,99%,95%;组合工艺对该实际果汁废水具有良好的处理效果。     

高活性萘降解细菌Hydrogenophaga Palleronii LHJ38的研究

为了研究微生物对多环芳烃的降解和转化规律,以萘作为研究对象,从餐厨油烟污染土壤中筛选到一株萘降解活性较高的细菌菌株,经菌种鉴定,定名为帕氏氢噬胞菌(H ydrogenophaga Palleronii)LH J38。测定了该菌的生长曲线和萘降解曲线,建立了菌株对萘的降解活性的定量测定方法,并研究了其最适生长条件。结果表明,在28℃、初始pH6.6、碳氮摩尔比为4的最适培养条件下,LH J38对初始质量浓度为2 000m g/L的萘在96h内的降解率可达98%以上;处于对数生长期的LH J38对萘的降解活性可达47.3nm o l/(m g.m in)。     

二氧化钛对活性艳红X-3B的光催化降解研究

以TiO2作为光催化剂,研究了TiO2对活性艳红X-3B的光催化氧化降解行为。结果表明,以锐钛矿为主的混晶型Ti02的催化活性最好;X-3B的光催化降解动力学符合Langmuir-Hinshelwood动力学模式,并求出其动力学参数女(表观反应速率常数)为0．5921,KA(吸附平衡常数)为0．1725;温度对X-3B的降解影响很小,其活化能仅为6．04kJ／mol;溶液中盐度的增加会不断降低TiO2对X-3B的光催化降解速率。     

IC反应器厌氧处理MTO废水

以初步驯化后的絮状污泥作为内循环(IC)反应器的接种污泥,厌氧处理甲醇制烯烃(MTO)废水(COD大于50 000 mg/L、TOC大于10 000 mg/L),以高负荷、高进水浓度方式培养颗粒污泥,考察了反应器运行过程中废水处理效果及污泥性状的变化情况。实验结果表明:IC反应器的进水COD容积负荷可达29.0 kg/(m~3·d),COD和TOC去除率可稳定在96%以上;在污泥培养阶段,废水升流速率宜采用0.4~0.6 m/h;在颗粒污泥未成熟时废水升流速率不宜提高过快,而在颗粒污泥成熟后,废水升流速率可在一定范围内快速提高。     

针-板放电等离子体反应器结构参数对甲基橙脱色反应速率常数的影响

采用针-板放电等离子体反应器处理模拟甲基橙(MO)废水,研究了反应器结构参数对MO脱色反应速率常数的影响.实验得出最佳反应器结构参数:阳极为5根不锈钢针并联,针间距为17 mm,针电极长度为2 mm,电极间距为10 mm,O2流量为0.18 m3/h,阴极丝网目数为20目,在阳极上部设置5层间距为15 mm的不锈钢丝介...     

介质阻挡放电低温等离子体协同催化降解苯乙烯

采用介质阻挡放电(DBD)低温等离子体协同催化降解苯乙烯，考察了输入功率、初始苯乙烯质量浓度、气体湿度、停留时间、脉冲频率等因素对苯乙烯降解率和能量效率的影响，建立了苯乙烯降解动力学模型，探讨了苯乙烯的降解机理。结果表明：在输入功率30 W、初始苯乙烯质量浓度464 mg/m³、气体相对湿度30%、停留时间0.18 s、脉冲频率200 Hz的最佳工艺条件下，苯乙烯降解率为62.20%，能量效率为36.10 g/(kW·h);DBD等离子体降解苯乙烯的动力学过程符合准一级动力学模型，相应的反应速率常数为0.109 4 m3^/(W·h)。DBD等离子体降解苯乙烯主要通过活性物种e^-、·O、·OH和NO₂·等对苯乙烯进行氧化。与单独DBD等离子体工艺相比，在相同输入功率下，DBD协同催化工艺能有效提高苯乙烯降解率和矿化率，降低反应器出口O₃浓度。     

两株柴油降解菌的性能研究

以0#柴油为惟一碳源,对两株柴油降解菌DS-Ⅰ菌和DS-Ⅲ菌降低液体表面张力的能力、柴油降解动力学及表面活性物质成分进行了研究。实验结果表明:DS-Ⅰ菌和DS-Ⅲ菌在生长过程中均可产生糖脂类生物表面活性物质,使发酵液表面张力降低;在11d的发酵时间内,DS-Ⅰ菌和DS-Ⅲ菌使发酵液中柴油的质量浓度从48.72m g/L分别降至16.64m g/L和9.17m g/L,柴油降解率分别为65.84%和81.18%,柴油降解速率分别为5.16m g/(L.d)和5.96m g/(L.d)。发酵液表面张力的降低与柴油的降解效果有显著的相关性。DS-Ⅲ菌在疏水性、对柴油的生长适应性和柴油降解速率等方面比DS-Ⅰ菌更好。     

低温等离子体处理废液技术

低温等离子体技术包括热等离子体技术和冷等离子体技术。该技术处理废液具有范围广，快速，高交，无二次污染等优点，尤其对难降解有毒废液的处理，其先进性和优越性更为突出，被认为是21世纪环境污染物处理领域中最有发展前途的新技术之一。综述了低温等离子体处理废液技术的研究和应用进展，重点分析了冷等离子体技术处理难降解有机废液的作用机理，探讨了两种技术现存的主要问题，并指出了今后需要研究的方向。     

低压直流电电解剩余活性污泥

采用低压直流电电解剩余活性污泥，优化了支持电解质的种类、加入量及电压梯度等工艺条件，并考察了在最佳工艺条件下SS去除率、污泥中有机物的质量分数（以VSS/SS计）、污泥pH及污泥沉降性能随电解时间的变化情况。实验结果表明，低压直流电电解污泥的最佳工艺条件为：电压梯度7 V/cm;支持电解质Na₂SO₄加入量0.4.0 mmol/g（以每克干污泥计）。在最佳工艺条件下电解pH为5.8、SS=（7 850 ±200）mg/L、VSS=（6 150±150）mg/L、溶解性化学需氧量（SCOD）为（61.2 ±20）mg/L的污泥，电解60 min时污泥的SCOD最大，达393.3 mg/L，SS去除率达14.4%，VSS/SS为58.5%，污泥pH为3.1。电解后污泥中微生物的细胞结构已不完整，污泥絮体被严重破坏。电解时间越长，污泥的沉降速率越快。     

空气涡轮制冷低温粉碎法回收废弃橡胶

利用带回冷循环的空气涡轮制冷系统，在低温条件下，将废旧橡胶进行冷冻、粉碎、制成６０目以上的精细胶粉。此法的冷冻能耗成本仅为国际上通用的液氮法的１／１０，整具工艺过程不产生二次污染，为废旧橡胶的综合利用提供了一条新途径。     

烟气组分对低温等离子体协同TiO_2光催化工艺氧化Hg~0的影响

采用介质阻挡放电低温等离子体协同TiO2光催化工艺氧化烟气中Hg0,考察了烟气组分对氧化效果的影响。实验结果表明:低温等离子体放电会产生大量近紫外光;在6 k V电压下,低温等离子体协同TiO2光催化工艺时N2/Hg0氛围下Hg0的氧化率达86%,显著高于单一等离子体时的30%;O2和H2O产生的活性粒子会使Hg0氧化率进一步提高,在5 k V电压下,N2/Hg0氛围中添加5%(φ)O2或5%(φ)H2O,低温等离子体协同TiO2光催化工艺时可分别获得96%和94%的氧化率;NO与Hg0的竞争关系会导致作用于Hg0的活性粒子减少,抑制低温等离子体对Hg0的氧化,而在低温等离子体协同TiO2光催化时,抑制作用减弱;在复杂烟气氛围下,低温等离子体协同TiO2光催化对Hg0仍保持了较高的氧化率,3次重复实验的Hg0氧化率均接近92%。     

柴油低温临界吸收法回收装车挥发油气

研究了采用柴油低温临界吸收法回收装车挥发油气的效果。实验结果表明：按装车挥发油气中的总烃体积分数为20.88%、装车挥发油气流量为280 m³/h、年运行时间为2 668 h计，装置年回收油气量为291 t，装置年最大运行功率为206.770 MW，装置投资回收期为3 a;处理后净化气中的总烃体积分数为1.24%，排放质量浓度低于25 g/m³，油气回收率达95%。处理后净化气满足GB 20950—2007《储油库大气污染物排放标准》，取得了较好的环保效益和经济效益。     

Effects of Lime and Ash Treatments on DOC Fractions and Low Molecular Weight Organic Acids in Soil Solutions of Acidified Podzolic Soils

Dissolved organic carbon (DOC) fractions and different low molecular weight organic acids (LMWOAs) were determined in soil solutions from two lime or ash treated Norway spruce sites in the south of Sweden. At Hasslöv, 3.45 t ha^-1 or 8.75 t ha^-1 dolomite were applied 15 years before sampling. Horröd was treated with 4.28 t ha^-1 ash and 3.25 t ha^-1 dolomite and sampled four years later. Propionate (7–268 M) and malonate (2–34 M) were the LMWOAsfound in the highest concentrations at Hasslöv. Two other LMWOAs dominated at Horröd, namely citrate (18–64 M)and fumarate (5–31 M). The differences in concentration of most of the determined LMWOAs at Hasslöv were significantly increased due to treatment. The LMWOAs comprised between 1.1–6.3% of the DOC at Hasslöv and 4.5–17.6% at Horröd. At Hasslöv normally 3–10% of the total acidity (TA) was due to LMWOAs and the average specific buffer capacity was 74 ± 22 mmol mol^-1C.The total DOC concentration in the mor layer solution was 16 mM for the dolomite treated plots compared to 10 mM at the untreated plot. A major part of the increase in DOC at the treated plots apparently had a hydrophobic character and was of high molecular weight corresponding to 3–10 kDa. The concentration of DOC < 1 kDa in the control and treated plots was similar.     

低NOx燃烧技术

介绍了锅炉燃烧中降低NOx的主要措施和几种国内外主要低NOx燃烧技术的脱硝原理.发展低NOx燃烧技术,对环境保护具有重大意义.     

Low intervention soil remediation approaches

Traditional bioremediation approaches have been used to treat petroleum source contamination in readily accessible soils and sludges. Contamination under existing structures is a greater challenge. Options to deal with this problem have usually been in the extreme (i.e., to dismantle the facility and excavate to an acceptable regulated residual, or to pump and treat for an inordinately long period of time). The excavated material must be further remediated and cleanfill must be added to close the excavation. If site assessments were too conservative or incomplete, new contamination adulterating fill soils may result in additional excavation at some later date. Innovative, cost-efficient technologies must be developed to remove preexisting wastes under structures and to reduce future remediation episodes. An innovative soil bioremediation treatment method was developed and evaluated in petroleum hydrocarbon contaminated (PHC) soils at compressor stations of a natural gas pipeline running through Louisiana. The in-situ protocol was developed for remediating significant acreage subjected to contamination by petroleum-based lubricants and other PHC products resulting from a chronic leakage of lubricating oil used to maintain the pipeline itself. Initial total petroleum hydrocarbon (TPH) measurements revealed values of up to 12,000 mg/kg soil dry weight. The aim of the remediation project was to reduce TPH concentration in the contaminated soils to a level of <200 mg/kg soil dry weight, a level negotiated to be acceptable to state and federal regulators. After monitoring the system for 122 days, all sites showed greater than 99-percent reduction in TPH concentration.     

Low energy comsumption management of agricultural residues

In this paper, a mechanical filtering system to treat pig slurry is proposed. The filter was made from the aerobic decomposition product of the organic fraction of municipal wastes and wheat straw was used as the support.Using a pilot plant to treat 2100 liters of swine slurry, an adequate reduction in BOD₅; COD, and other parameters was obtained. The organic matter content of the material trapped in the filter was similar to that of compost and farmyard manure, but the nitrogen and phosphorous levels and the C/N ratio were more similar to farmyard manure. After passing through a filtering system, the treated liquid can be used for fertirrigation and as a feed for algae ponds. After a period of stabilization, the solid material can be mixed to produce manure. Although wheat straw was used as the support in this experiment, other agricultural wastes such as rice straw, corn stalks, millet stems, banana, cotton, and coconut trash can be used. Rather than municipal solid waste compost, other kinds of compost obtained from agricultural wastes such as leaves, bark, husks, etc., can be used as the filter.