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51.
Comparison of China’s Environmental Impact Assessment (EIA) Law with the European Union (EU) EIA Directive 总被引:1,自引:0,他引:1
In this paper, we first review the development of China’s Environmental Impact Assessment (EIA) system in the past 30 years.
Then we compare the framework and operational procedures of China’s new EIA law with those of the EU EIA Directive. We also
compare public participation, as well as sanctions and control in the two EIA systems. In addition, we identify where the
processes in both EIA systems are similar or different from one another. By comparison, we noted that there are at least three
obvious weaknesses in China’s EIA system: (1) the application of new models for EIA legislation; (2) the improvement of EIA
guidance and education; and (3) the enhancement of public participation in EIA process. Our study indicates that these three
major shortcomings should be overcome and improved in China’s EIA system, when compared with the EU EIA system. 相似文献
52.
Isobe T Takada H Kanai M Tsutsumi S Isobe KO Boonyatumanond R Zakaria MP 《Environmental monitoring and assessment》2007,135(1-3):423-440
A comprehensive monitoring survey for polycyclic aromatic hydrocarbons (PAHs) and phenolic endocrine disrupting chemicals
(EDCs) utilizing mussels as sentinel organisms was conducted in South and Southeast Asia as a part of the Asian Mussel Watch
project. Green mussel (Perna viridis) samples collected from a total of 48 locations in India, Indonesia, Singapore, Malaysia, Thailand, Cambodia, Vietnam, and
the Philippines during 1994–1999 were analyzed for PAHs, EDCs including nonylphenol (NP), octylphenol (OP) and bisphenol A
(BPA), and linear alkylbenzenes (LABs) as molecular markers for sewage. Concentrations of NP ranged from 18 to 643 ng/g-dry
tissue. The highest levels of NP in Malaysia, Singapore, the Philippines, and Indonesia were comparable to those observed
in Tokyo Bay. Elevated concentrations of EDCs were not observed in Vietnam and Cambodia, probably due to the lower extent
of industrialization in these regions. No consistent relationship between concentrations of phenolic EDCs and LABs were found,
suggesting that sewage is not a major source of EDCs. Concentrations of PAHs ranged from 11 to 1,133 ng/g-dry, which were
categorized as “low to moderate” levels of pollution. The ratio of methylphenanthrenes to phenanthrene (MP/P ratio) was >1.0
in 20 out of 25 locations, indicating extensive input of petrogenic PAHs. This study provides a bench-mark for data on the
distribution of anthropogenic contaminants in this region, which is essential in evaluating temporal and spatial variation
and effect of future regulatory measures. 相似文献
53.
Samaratunga SS Nishimoto J Tabata M 《Environmental science and pollution research international》2008,15(1):27-30
BACKGROUND, AIMS AND SCOPE: Chromium enters into the aquatic environment as a result of effluent discharge from steel works, electroplating, leather tanning industries and chemical industries. As the Cr(VI) is very harmful to living organisms, it should be quickly removed from the environment when it happens to be contaminated. Therefore, the aim of this laboratory research was to develop a rapid, simple and adaptable solvent extraction system to quantitatively remove Cr(VI) from polluted waters. METHODS: Aqueous salt-solutions containing Cr(VI) as CrO4(2-) at ppm level (4-6 ppm) were prepared. Equal volumes (5 ml) of aqueous and organic (2-PrOH) phases were mixed in a 10 ml centrifuge tube for 15 min, centrifuged and separated. Concentrations of Cr(VI), in both the aqueous and organic phases, were determined by atomic absorption spectrometry. The effects of salt and acid concentrations, and phase-contact time on the extraction of Cr(VI) were investigated. In addition, the extraction of Cr(VI) was assessed in the presence of tetramethylammonium chloride (TMAC) in 2-PrOH phase. Effects of some other metals, (Cd(II), Co(II), Cu(II), Ni(II) and Zn(II)), on the extraction of Cr(VI) were also investigated. RESULTS AND DISCUSSION: The Cr(VI) at ppm level was extracted quantitatively by salting-out the homogeneous system of water and 2-propanol(2-PrOH) using chloride salts, namely CaCl2 or NaCl, under acidic chloride media. The extracted chemical species of Cr(VI) was confirmed to be the CrO3Cl-. The ion-pair complex extracted into the organic phase was rationalized as the solvated ion-pair complex of [2-PrOH2+, CrO3Cl-]. The complex was no longer stable. It implied the reaction between extracted species. Studies revealed that salts and acid directly participated in the formation of the above complex. Use of extracting agents (TMAC) didn't show any significant effect on the extraction of Cr(VI) under high salting-out conditions. There is no significant interference effect on the extraction of Cr(VI) by the presence of other metals. The Cr(VI) in the organic phase was back-extracted using an aqueous ammonia solution (1.6 mol dm(-3)) containing 3 mol dm(-3) NaCl. The extraction mechanism of Cr(VI) is also discussed. CONCLUSIONS: Salting-out of homogeneous mixed solvent of 2-propanol can be employed to extract Cr(VI) quantitatively, as an ion-pair of [2-PrOH2+ * CrO3Cl-] solvated by 2-PrOH molecules. Then, the complex becomes 'solvent-like' and is readily separated into the organic phase. The increase of Cl- ion concentration in the aqueous phase favors the extraction. The 2-PrOH, salts and acid play important roles in the extraction process. There is no need to use an extracting agent at a high salting-out condition. RECOMMENDATIONS AND PERSPECTIVES: Chromium(VI) must be quickly removed before it enters into the natural cycle. As the 2-PrOH is water-miscible in any proportion, ion-pairing between 2-PrOH2+ and CrO3Cl- becomes very fast. As a result, Cr(VI) can easily be extracted. Therefore, the method is recommended as a simple, rapid and adaptable method to quickly separate Cr(VI) from aqueous samples. 相似文献
54.
制备了聚硅酸氯化铝(PASC)絮凝剂,并用其进行了皂素废水处理实验。考察了絮凝剂投加量、pH值、搅拌速度对COD和浊度去除率的影响。结果表明,当絮凝剂投加量为9~13.5 mg/L、pH值5~7、搅拌速度150~250 r/min时,COD和浊度去除效果较好。最佳工艺条件为:絮凝剂投加量11.25 mg/L、pH值6、搅拌速度200 r/min。此时,COD去除率为93.7%,浊度去除率为97.5%。PASC的絮凝性能明显优于PAC。 相似文献
55.
56.
目的 研究腐蚀环境下单孔和多孔冷挤压强化铝合金板件的疲劳寿命退化规律和损伤机理。方法 针对2种不同孔距的三孔冷挤压强化7075-T6铝合金板件,采用模拟热带海洋大气环境的实验室加速腐蚀谱,开展不同腐蚀时间下的预腐蚀疲劳试验。结果 获得了3倍孔距的三孔挤压强化铝板以及单孔挤压强化铝板的C(t)曲线、疲劳S-N曲线和损伤形貌特征,分析了腐蚀后挤压强化试件的腐蚀机理及挤压强化作用。同时,将不同孔数试件的试验结果进行比较,探明了孔数对挤压强化铝板腐蚀和疲劳性能的影响。结论 腐蚀后挤压强化铝合金板件的疲劳性能发生显著退化,腐蚀损伤主要为剥蚀,疲劳裂纹萌生位置由孔边转移至表面。挤压孔数量对挤压强化铝合金板件的疲劳和腐蚀疲劳性能的影响较小。 相似文献
57.
58.
水淬渣人工湿地强化除磷作用研究 总被引:2,自引:2,他引:2
研究了水淬渣的磷吸附-解吸效果,构建了以水淬渣为主要基质的模拟垂直流人工湿地系统,分析了水力停留时间(HRT)和污染负荷变化对污水中磷去除的影响,探讨了湿地上行、下行流单元各层基质的除磷贡献.结果表明,水淬渣基质的磷饱和吸附量为3 333 mg.kg-1,其水溶性钙含量为0.084%,pH值为7.54,适合作为湿地除磷基质.HRT与磷除去率呈正相关,当HRT从1 d缩短为0.5 d时,TP去除率降低5.9%~4.7%,当HRT从2 d缩短为1 d时,TP去除率降低2.4%~4.7%,HRT为1 d条件下,水淬渣湿地的磷去除率>85%,说明无限延长HRT无益于强化除磷,适宜的HRT为1 d.在进水浓度稳定的条件下,进水污染负荷与磷去除率呈负相关,当污染负荷范围在12.2~36.8 g.(m2.d)-1时,水淬渣湿地的磷除去率可维持在85%,当污染负荷达到48.9 g.(m2.d)-1后,水淬渣湿地的磷除去率下降至65%,当污染负荷<36.8 g.(m2.d)-1时,水淬渣湿地的磷去除率>82%,说明高污染负荷可抑制基质表面及孔隙中Ca、Al等吸附磷的活跃位点,适宜的进水污染负荷为24.5~36.8g.(m2.d... 相似文献
59.
膜生物反应器中膜污染层胞外多糖性质及污染特征 总被引:4,自引:1,他引:4
胞外多糖是污水处理膜生物反应器中的重要膜污染物质,经醇析、Sevag法去除蛋白质、层析纯化、透析、冷冻干燥得胞外多糖样品。紫外光谱扫描鉴定该胞外多糖样品不含核酸及蛋白质,分别采用HPLC、GC、FT-IR及SEM等手段对其性质进行分析,考察其对聚偏氟乙烯膜的污染特征。结果表明,所得胞外多糖的重均分子量Mw为4.8×106,糖苷键类型主要为1-3和1-6型,是由葡萄糖、鼠李糖、木糖、甘露糖等组成、具有高度分枝网状结构的杂多糖。胞外多糖膜污染过程受沉积层控制,膜的主要污染形式为胞外多糖在膜表面的沉积。 相似文献
60.