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261.
面对世纪之交,无锡市制定了“两个率先”的战略目标,这就要求在经济发展过程中注重各种资源条件的支撑以及它们的优化组合。从经济运行的角度讲,影响和制约经济发展的主要因素是把握市场的能力以及投入经济活动的各种资源要素(包括劳动力、资金和各类物资资源)和科技进步率的高低。本文就这些生产要素在未来经济发展中的供给能力及将起的作用进行了分析,认为无锡市面临老龄化和就业困难的双重压力,外资的引入仍受宏观政策影响,外延式的调整发展模式难以持续,提出无锡市可持续发展应加强人力资源的管理和培训,依靠科技进步和高新技术产业支撑精制的发展方式,逐步形成重效益的快速发展态势,严格环保政策和规范土地市场等。 相似文献
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腐蚀电池-Fenton工艺用于垃圾渗滤液的预处理研究 总被引:8,自引:1,他引:8
采用铁屑和颗粒活性炭通过原电池反应产生的Fe2 离子取代FeSO4组成腐蚀电池-Fenton工艺,采用该工艺对垃圾渗滤液进行预处理.结果表明,最佳运行条件为pH值为2、H2O2投加量为理论投加量的50%、铁屑投量为30 g(500 mL渗滤液中)、Fe/C质量比为2.5、反应时间为1 h、絮凝pH值为7,其COD去除率可达到60%(其中活性炭吸附占19%),TOC去除率可达47%(其中活性碳吸附占13%),BOD5/COD值从原水的0 35提高到出水的0.69;而传统Fenton工艺在H2O2/Fe2 比值等于5、其它条件与腐蚀电池-Fenton工艺相同的条件下,COD去除率为26%,TOC去除率为19%,BOD5/COD比值从原水的0.43提高到0.69.将腐蚀电池-Fenton工艺用于垃圾渗滤液的预处理,在有机物去除率和提高可生化性方面效果均明显优于传统Fenton工艺. 相似文献
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In this paper, a new alternative method, i.e., selective extraction by weakly basic anion exchange resin, has been developed for the removal of trace cadmium and mercury ions from drinking water sources. The mechanism of heavy metal removal is based on selective extraction as the results of LEWIS-base-acid interactions. Transfer of trace mercury species from liquid to resin phase coincides well with the performance of film diffusion. The results demonstrated that the presence of chlorine has a negligible influence on the removal of mercury. However, humic acids can strongly bind mercury by the formation of complex compounds and therefore become the obstacle in the diffusion progress. At neutral or base pH, the resin material exhibits the favorable uptake of heavy metals. In filter experiments, the studied resin material offers favorable properties in the selective extraction of trace mercury and cadmium. 相似文献
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Large amounts of 137Cs have been accidentally released to the subsurface from the Hanford nuclear site in the state of Washington, USA. The cesium-containing liquids varied in ionic strengths, and often had high electrolyte contents, mainly in the form of NaNO3 and NaOH, reaching concentrations up to several moles per liter. In this study, we investigated the effect of ionic strengths on Cs migration through two types of porous media: silica sand and Hanford sediments. Cesium sorption and transport was studied in 1, 10, 100, and 1000 mM NaCl electrolyte solutions at pH 10. Sorption isotherms were constructed from batch equilibrium experiments and the batch-derived sorption parameters were compared with column breakthrough curves. Column transport experiments were analyzed with a two-site equilibrium-nonequilibrium model. Cesium sorption to the silica sand in batch experiments showed a linear sorption isotherm for all ionic strengths, which matched well with the results from the column experiments at 100 and 1000 mM ionic strength; however, the column experiments at 1 and 10 mM ionic strength indicated a nonlinear sorption behavior of Cs to the silica sand. Transport through silica sand occurred under one-site sorption and equilibrium conditions. Cesium sorption to Hanford sediments in both batch and column experiments was best described with a nonlinear Freundlich isotherm. The column experiments indicated that Cs transport in Hanford sediments occurred under two-site equilibrium and nonequilibrium sorption. The effect of ionic strength on Cs transport was much more pronounced in Hanford sediments than in silica sands. Effective retardation factors of Cs during transport through Hanford sediments were reduced by a factor of 10 when the ionic strength increased from 100 to 1000 mM; for silica sand, the effective retardation was reduced by a factor of 10 when ionic strength increased from 1 to 1000 mM. A two order of magnitude change in ionic strength was needed in the silica sand to observe the same change in Cs retardation as in Hanford sediments. 相似文献
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