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本文在剖析绿色技术的概念内涵与特征的基础上,构建了由清洁生产技术、资源化技术、末端治理技术、生态农业技术、绿色食品技术、清洁消费技术与生态恢复技术等为主要内容的我国绿色技术体系,并从行政、经济、法律、教育及科研等五个方面阐述了促进我国可持续发展的绿色技术实施策略。 相似文献
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污染场地修复技术的种类 总被引:3,自引:1,他引:3
本文旨在归纳总结目前国内外对污染场地的修复的各种技术。认为场地修复通常包括污染土修复和含水层净化等2个方面。污染土常见的处理技术目前大致可归纳为6类,即微生物修复技术、化学处理技术、物理分离技术、固化/安定化技术、高温处理技术、植物修复技术等。而污染地下水的修复方法主要有5项:注气法、原位微生物修复技术、两相蒸气提取法、原位氧化法、原位反应墙技术等。 相似文献
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城市河流治理技术研究进展 总被引:1,自引:0,他引:1
城市河流水体具有生态系统复杂、污染类型齐全、污染源数量多、危害极为严重的特点。本文结合国内外最新研究成果和积累的宝贵经验,介绍了河道曝气技术、生态混凝土技术、阿科蔓复合生态技术、接触氧化技术、生态疏浚、化学强化一级处理、光催化技术等比较先进技术的研究进展,并对今后保护城市河流提出了建议。 相似文献
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详述了“3S”技术、仿真与控制技术、专家系统技术、互联网技术、多媒体与可视化技术等环境信息技术及其在烟气脱硫中的应用,提出了加强环境信息技术在烟气脱硫中应用的建议。 相似文献
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介绍了"五水分流"清洁生产技术、铬液灰液循环利用技术、制革高氨氮废水稳定达标排放技术、MicrowaterTM环境治理微生物技术体系、四相废水深度达标治理专利技术、膜处理回用技术、含铬污泥资源化利用技术等制革行业污染治理集成技术的概况;通过分析应用实例,指出该技术体系在达标治理的前提下,通过清洁生产、高效处理、中水回用、铬泥资源化利用等手段,可有效降低污染治理成本,应用前景广阔。 相似文献
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微生物菌剂在酿酒废水处理中的应用研究 总被引:6,自引:1,他引:5
采用厌氧-好氧工艺,结合微生物菌剂对酿酒废水进行了处理研究。进水CODCr浓度可达到8,456.3-22,442.0mg/L,BOD55,040.0-9.557.1mg/L,pH3-4,可不调pH,采用微生物菌剂接种可启动厌氧反应器,COD有机负荷最高达到10.2gCOD/Ld,COD去除率稳定在91-95%,BOD去除率90-94%,出水pH6.6-7.1,出水CODCr在2,000mg/L以下,BOD5800mg/L以下。厌氧污泥可全部颗粒化。好氧处理系统中接种微生物菌剂,曝气10-12小时,可保证出水中CODCr在230mg/L以下,甚至直接达到国家一级排放标准。微生物菌剂的应用是取得该处理效果的关键。 相似文献
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压裂返排液生物处理实验研究 总被引:1,自引:1,他引:0
从油田压裂返排液中筛选出EB系列菌种,可高效降解压裂返排液中的高分子和有机污染物。考察了振荡时间、温度、接种量、菌种混合比例等对压裂返排液COD去除率的影响。结果表明:48h振荡、25℃、10%接种量、菌种EB1和EB2按1∶1比例混合是较佳应用条件。EB复合菌种的应用范围较广,其pH值适用范围为6~9,矿化度适用范围为3 000~20 000mg/L。该研究提高了压裂返排液生物处理技术规模化应用的可行性。 相似文献
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含氯废水COD测定的氯耗氧曲线校正法 总被引:1,自引:0,他引:1
本文介绍了一种重铬酸钾法测定含氯废水COD的改进分析方法——氯耗氧曲线校正法,测定中不加隐蔽剂HgSO4,通过调整催化剂Ag2SO4的加入时间,测得表现COD值,再扣除Cl^-对COD的贡献值,得出实际COD值。与标准方法相比,本法的准确度高、精密性好,同时还可避免汞盐污染环境。 相似文献
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本文综述了粉煤友在印染废水中的应用。粉煤灰作为吸附剂可直接处理印染废水,处理效率较低,改性后粉煤灰可提高吸附性;利用粉煤灰的混凝作用对COD的去除率一般为50%-60%,色度去除率为80%左右;当粉煤灰与铁屑产生电化学作用时,用于印染废水预处理是行之有效的;作为印染废水助凝助沉剂,结合其他工艺,可使印染废水中COD和色度去除率分别达到90%和95%以上,并列举了粉煤灰处理印染废水成功的实例。但仍应加强理论研究,解决工程与设备问题是今后的工作方向。 相似文献
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氯离子浓度高于500mg/L时,对CODcr的测定呈混浊干扰,通过加入HgSO4络合氯离子,可消除氯离子含量达2000mg/L的干扰,过量的HgSO4对CODcr结果无影响。 相似文献
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The performance of an aerated submerged fixed-film reactor (ASFFR) under simultaneous organic and ammonium loading and its effect on nitrification was studied. Organic loadings varied in the range of 1.93 to 5.29 g chemical oxygen demand (COD) m-2 d-1 and NH4-N loadings were in the range of 116 to 318 mg NH4-N m-2 d-1. Increments of loading rates were obtained both by increasing the flow rate and increasing the influent substrate in individual pilot runs. Results showed that with organic loading rates up to 3.97 g COD m-2 d-1, complete nitrification was achievable. Although high organic loading such as 5.29 g COD m-2 d-1 could cause nitrification to stop, shifting to lower organic loadings made nitrification start and set rapidly to its previous steady-state concentrations. Comparison of results showed that in the ASFFR, nitrification would be severely affected by an organic loading rate of 5.29 g COD m-2 d-1 by increasing either the flow or the influent substrate. It should be noted that the average value of dissolved oxygen was 3.4 mg L-1 with an air supply of 15 L min-1, and there was no indication of oxygen limitation. The results of this study show the flexibility of ASFFRs under changing organic loads. Furthermore, for achieving complete nitrification and optimum application of these reactors for protecting receiving water from the environmental hazards of ammonium, the maximum organic loading that would present complete nitrification should be considered. 相似文献
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Rai HS Singh S Cheema PP Bansal TK Banerjee UC 《Journal of environmental management》2007,83(3):290-297
In the present study, decolorization of a simulated dye waste containing three different triphenylmethane (TPM) dyes--Magenta, Malachite Green and Crystal Violet, was investigated in a laboratory scale, two-stage anaerobic high-rate reactor. The effect of various parameters (influent dye concentration, hydraulic and co-substrate loading rates) on color and COD removal efficiency of the reactor has been studied. It has been shown that the influent dye concentration had little effect on overall COD and color removal efficiency. More than 99% color removal and 96% COD removal efficiency were maintained even at a dye concentration of 500 mg/l and a dye loading rate of 1000 mg/l day. However, a minimum level of glucose as supplementary carbon source is required to maintain the maximum color removal efficiency and it drops appreciably when no glucose is added to the influent. The study also showed that the acidogenic phase of the reaction plays an important role in decolorization of the TPM dyes. In addition, the two-stage anaerobic reactor was observed to have distinct advantages over the single-stage system, as the drop in color and COD removal efficiency of stage 1 are adequately compensated by stage 2 of the reactor especially under high dye loading rates accompanied by low co-substrate loading and under reduced HRTs. 相似文献