2010年度国家鼓励发展的环境保护技术目录

一、城镇污水、污泥处理及水体修复技术 1．A^2／O城市污水处理技术技术内容：该技术采用分离池型的反应池,单独设立缺氧池（除磷时还应没厌氧池）及好氧池,并采取内部循环的混合液回流、鼓风微孔曝气或射流曝气方式。COD去除率大于85％,BOD;去除率大于95％,氨氮去除率大于90％,总氮去除率大于75％,SS去除率大于95％。     

UASB—接触氧化法处理沤麻废水的研究

本试验采用ＵＡＳＢ—接触氧化工艺对沤麻废水的处理进行了研究，系统启动两个月后达到稳定的处理效果，厌氧段进水ＣＯＤ浓度为７００ｍｇ／１，有机负荷为９．２５ｋｇＣＯＤ／ｍ３·ｄ，停留时间为２４小时，ＣＯＤ去除率可达到８９．３％，好氧段接触氧化池的有机负荷为２．ＩｋｇＣＯＤ／ｍ３·ｄ，处理时间为１０小时，整个系统总的ＣＯＤ去除率可达到９７％，该工艺是处理高浓度沤麻废水行之有效的方法。     

Cu／Fe内电解预处理焦化废水的研究

采用混凝沉淀一厌氧水解酸化一催化铁内电解（即Cu／Fe体系）一好氧组合工艺处理焦化废水,研究了催化铁内电解法用于焦化废水的预处理时,对焦化废水的COD、色度、总磷的去除率。结果表明,催化铁用于焦化废水的预处理,可以提高废水的可生化性,使好氧处理的COD去除率提高,达到80％-90％;催化铁对焦化废水有较好的脱色效果,色度去除率为77．7％-89．3％;催化铁能够去除部分总磷,但是由于微生物生长需要,需在厌氧段补充磷。试验证明,催化铁内电解法是一种有效的焦化废水预处理工艺。     

水解(酸化)-好氧工艺处理混合工业废水试验研究

水解（酸化）＋好氧工艺可以有效地用于城市污水与工业废水处理，试验研究了不同工况条件下，水解（酸化）＋好氧工艺处理混合工业废水的效果，通过投加悬浮填料对水工艺过程进行优化，使其处理系统更为有效。在总的水力停留时间分别为11.5h、14.5h、19.0h,CODCr总的平均除率分别为72.1%、76.7%、77.6%,BOD5的去除率为89.6%、90.7%、91.5%，废水经水解（酸化）处理后，BOD5／CODCr有上升趋势，水解时间3.5h、4.5h、6h对应的BOD5／CODCr比值分别提高了3％、11％、17％，表明水解（酸化）提高了混合工业废水的可生化性。针对上海市某工业区混合废水建议水解（酸化）时间控制在6h以上、好氧反应控制在10.0h。     

SBR中好氧颗粒污泥的培养

采用竖式SBR作为反应器,利用城市污水处理厂剩余污泥作为接种污泥,通过不间断运行培养出好氧颗粒污泥。实验结果表明,采用非限量曝气模式好氧颗粒污泥降解模拟污水的效果较好,其COD去除率可达98％以上。曝气量对好氧颗粒污泥的形成和稳定具有重要影响,当气速为26．5m／h时,好氧颗粒污泥的性状和处理有机废水效果最佳。同时好氧颗粒污泥对pH值的变化不明显,当pH为5—8范围内,其COD去除率都可达到85％以上。但是未经驯化的好氧颗粒污泥对对硝基苯酚和对氯苯酚两种芳香类有机物较敏感,而对硝基苯酚对其毒性更大。当对硝基苯酚和。对氯苯酚浓度为10mg／L时,其COD去除率仅为42．5％和52％。     

高原地区溶解氧浓度对A2／O工艺运行效果研究

针对我国低温地区的城市污水,开展了A2／O工工艺中试研究,考察溶解氧浓度对A2／O工工艺运行效果的影响。结果表明：采用A2／O工工艺并延长好氧池HRT,在系统水温为10℃-14℃的情况下可获得良好的污水处理效果。A2／O工工艺中好氧池末端的溶解氧浓度宜控制在2．8mg／L左右,此时的系统平均出水COD、氨氮、总氮和总磷浓度分别为40mg／L、3．8mg／L、13．0mg／L和0．7mg／L,平均COD、氨氮、总氮和总磷去除率分别为92．4％、83．8％、72．7％和87．1％。     

催化铁应用于草甘膦废水处理工艺改造的可行性研究

针对某化工厂草甘膦废水经厌氧-好氧生物处理后出水总磷浓度高,无法达到该化工区污水纳管标准的情况,应用催化铁方法对该废水现有处理工艺进行改造以提高出水水质。考察了催化铁方法对原处理工艺不同处理工段出水中磷的去除效果,发现该法可有效地去除生物厌氧池出水的总磷及正磷盐,去除率分别达到52．7％和83．13％以上,且使废水的BOD5／COD值显著提高,可从0．08提高至0．31,增强了废水的可生物降解性,有利于后续好氧生物处理的进行。研究表明在原处理工艺的厌氧池后增加催化铁处理段能明显提高最终出水水质。     

改良生物接触氧化法在印染废水处理中的应用

对传统的好氧生物接触氧化池进行改造,增加污泥回流,使其兼具活性污泥曝气池的作用,新工程应用于印染废水处理后取得了良好的效果,连续运行结果表明:废水SS、COD及色度的去除率较先前有显著提高.     

深度处理生活污水以供采暖锅炉回用

针对我国水资源缺乏，作者设想“生活污水深度处理后供采暖锅炉回用”，并结合现场实际成功地进行了探索性试验─—用“缺氧水解－好氧处理”工艺深度处理生活污水。详述了工艺过程的机理及优于传统的活性污泥法之处。强调了深度处理工艺中的几个关键所在，如：好氧接触氧化法、Ａ／Ｏ生物处理系统的技术要点、氮氯基本原理及其特点等。该技术在温度较低的北方也有实用价值。生产性试验表明，应注意的问题是：冬季应采取保温措施；好氧混合液的回流量控制；水解池的使用潜力等。在辽宁盘锦地区采用的缺氧水解－好氧工艺生物处理法处理城市低浓度有机废水的生产性试验表明，它可为高效、低能耗、低成本处理城市污水提供新的途径。     

A2/O工艺处理焦化废水工程实例

本文介绍了采用厌氧-缺氧-好氧生物脱氮工艺（简称A^2／O工艺）处理焦化废水的工程设计和运行基本情况，并进行了分析总结。     

利用废铁屑处理含铬废水试验研究

通过研究在酸性条件下利用废铁屑处理剧毒的六价铬电镀废水的工艺条件 ,在最佳条件下废水中六价铬去除率达99 %以上 ,出水总铬含量为0.040mg/l,六价铬含量为0.002mg/l,大大低于国家排放标准0.500mg/l。     

一种经济有效的含油地下水预处理方法——吹脱法

吹脱法应用于低浓度废水处理,可有效去除水中的溶解性气体和挥发性油类,同时还可增加水中的溶解氧,为进一步的生物处理创造有利条件。利用现场动态实验对影响除油的因素进行了试验研究,确定最佳处理条件为：气水比５∶１、淋水密度５．０ｍ３／（ｍ２·ｈ）,实验表明在最佳运行状态下,吹脱法对地下水中油类物质的去除率能够达到５０％,还能去除水中的铁、氨氮等污染物质,是一种非常有效的预处理方法。为了弄清目前炼油厂废水的处理水平,通过对三个典型炼油废水处理厂的调查,分别对其处理流程、处理效果、采用的主要处理药剂及处理工艺进行了介绍,分析了每套处理设施的长处以及与先进设施对比存在的不足。     

Nutrient processing capacity of a constructed wetland in western Ireland

In Ireland, constructed wetland systems are increasingly being used to perform tertiary treatment on municipal waste effluent from small towns and villages located in areas whose receiving waters are deemed sensitive. The bedrock formation in the west of Ireland is primarily karst limestone and where the overburden-soil cover is very shallow, such waters are highly sensitive to pollution sources, as little or no natural attenuation and/or treatment will occur. Constructed wetland technology has been seen to offer a relatively low-cost alternative to the more conventional tertiary treatment technologies, particularly when dealing with low population numbers in small rural communities. This paper examines the waste treatment performance, in terms of nutrient (P and N) reduction, of a recently constructed surface-flow wetland system at Williamstown, County Galway, Ireland. Performance evaluation is based on more than two years of water quality and hydrological monitoring data. The N and P mass balances for the wetland indicate that the average percentage reduction over the two-year study period is 51% for total N and 13% for total P. The primary treatment process in the wetland system for suspended solids (between 84 and 90% reduction), biological oxygen demand (BOD) (on average, 49% reduction), N, and P is the physical settlement of the particulates. However, the formation of algal bloom during the growing season reduces the efficiency of the total P removal.     

Combining steam injection with hydraulic fracturing for the in situ remediation of the unsaturated zone of a fractured soil polluted by jet fuel

A steam injection pilot-scale experiment was performed on the unsaturated zone of a strongly heterogeneous fractured soil contaminated by jet fuel. Before the treatment, the soil was stimulated by creating sub-horizontal sand-filled hydraulic fractures at three depths. The steam was injected through one hydraulic fracture and gas/water/non-aqueous phase liquid (NAPL) was extracted from the remaining fractures by applying a vacuum to extraction wells. The injection strategy was designed to maximize the heat delivery over the entire cell (10 m × 10 m × 5 m). The soil temperature profile, the recovered NAPL, the extracted water, and the concentrations of volatile organic compounds (VOCs) in the gas phase were monitored during the field test. GC-MS chemical analyses of pre- and post-treatment soil samples allowed for the quantitative assessment of the remediation efficiency. The growth of the heat front followed the configuration of hydraulic fractures. The average concentration of total hydrocarbons (g/kg of soil) was reduced by ～ 43% in the upper target zone (depth = 1.5-3.9 m) and by ～ 72% over the entire zone (depth = 1.5-5.5 m). The total NAPL mass removal based on gas and liquid stream measurements and the free-NAPL product were almost 30% and 2%, respectively, of those estimated from chemical analyses of pre- and post-treatment soil samples. The dominant mechanisms of soil remediation was the vaporization of jet fuel compounds at temperatures lower than their normal boiling points (steam distillation) enhanced by the ventilation of porous matrix due to the forced convective flow of air. In addition, the significant reduction of the NAPL mass in the less-heated deeper zone may be attributed to the counter-current imbibition of condensed water from natural fractures into the porous matrix and the gravity drainage associated with seasonal fluctuations of the water table.     

“三废”资源化利用探讨

针对我国环境污染严重,资源、能源利用率低的现状,胜利油田积极开展“三废”资源化工作。通过对废水、固体废物、工业废气资源化现状的分析,科学地论证了“三废”资源化具有投资少,处理工艺简单易行,处理成本低,管理难度小等优点。找出存在的主要问题,并提出下一步工作目标。     

井下作业废水处理的试验研究

油田开发过程中,井下作业工艺尤为复杂,施工类型繁多,容易发生各种污染。针对压裂施工排出井管返出液的特点,重点提出利用絮凝-隔油法,之后再用次氯酸钠结合紫外光对废水进行深度处理,可氧化分解难处理的部分高分子有机化合物的污染。结果表明:在适宜的处理条件下,该法可有效去除水中CODCr 和Oil ,去除率分别为98.9％、98.3％。     

钻井废物综合治理技术的应用

针对急需解决的钻井废水、废气治理问题,以钻井作业大功率柴油机废气余热回收利用为出发点,研制了钻井废水废气综合治理设备。通过现场试验对钻井废水、废气治理效果及噪声影响的分析,试验结果表明,日处理钻井废水可达11～13m3/d,柴油机废气中污染物排放有一定程度的降低,柴油机高频噪声得到较明显降低,并有利于增加柴油机扭距。     

Improving saline-sodic coalbed natural gas water quality using natural zeolites

Management of saline-sodic water from the coalbed natural gas (CBNG) industry in the Powder River Basin (PRB) of Wyoming and Montana is a major environmental challenge. Clinoptilolie zeolites mined in Nevada, California, and New Mexico were evaluated for their potential to remove sodium (Na+) from CBNG waters. Based on the exchangeable cation composition, naturally occurring calcium (Ca2+)-rich zeolites from New Mexico were selected for further evaluation. Batch adsorption experiments were conducted to evaluate the potential of the Ca(2+)-rich natural clinoptilolites to remove Na+ from saline-sodic CBNG waters. Batch adsorption experiments indicated that Na+ adsorption capacity ofclinoptilolite ranged from 4.3 (4 x 6 mesh) to 7.98 g kg(-1) (14 x 40 mesh). Among the different adsorption isotherms investigated, the Freundlich Model fitted the data best for smaller-sized (6 x 8, 6 x 14, and 14 x 40 mesh) zeolites. Passing the CBNG water through Ca(2+)-rich zeolite columns reduced the salt content (electrical conductivity [EC]) by 72% with a concurrent reduction in sodium adsorption 10 mmol 1/2 L(-1/2). Zeolite technology appears to be an effective water treatment alternative to industrial membrane treatment for removing Na+ from poor-quality CBNG waters.     

稠油废水COD处理工艺研究

通过对多种絮凝剂的试验研究,筛选出UP-11混凝剂,在其投加量为2.4 mL/L时,油与COD去除效果最佳。同时在此基础上采用膜SBR法对絮凝出水做进一步处理,当运行条件为:进水0.5h、曝气4h、沉淀1h、排水0.5h时,出水完全达到国家规定的污水排放标准。     

废气治理工艺的选择

本文介绍了治理有机废气和无机废气的主要工艺，提出要针对废气的实际参数，选择高效节能的废气治理设备。