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161.
This article addresses the use of critical loads in optimized emission abatement strategies. Critical loads represent the maximum tolerable deposition possible without adverse impacts, a limit that is highly spatially variable. As deposition targets, critical loads cannot be satisfied at all receptors in Europe. Consequently, there is a need for alternative criteria that still relate to ecological indicators, yet that are feasible, consistent, and equitable. Two criteria are suggested: the relative critical load coverage and the relative deposition reduction. Deposition goals based on these criteria will guarantee that a specified fraction of ecosystems will attain target loads and thus will be protected from adverse environmental impacts. In areas that cannot achieve target loads with the best available control measures, deposition can be reduced to a specified fraction of the unabated level. Examples are presented that demonstrate their derivation and application of the two criteria. The criteria have been implemented in the European-scale Regional Acidification Information and Simulation (RAINS) model. Results obtained indicate that optimized emission strategies based on critical loads may be similar to emission strategies based on deposition reductions at certain levels of the two criteria. This suggests that it may not be necessary to utilize critical loads to formulate deposition targets. A second example shows the effect of excluding countries from European cost minimization. A country's participation can save costs with moderate deposition targets; however, significant costs can be imposed with low (stringent) deposition targets. These preliminary results have significant implications for multilateral negotiations.  相似文献   
162.
In order to test the hypothesis of aluminium toxicity induced by acid deposition, an experimental acid irrigation was carried out in a mature Norway spruce stand in Southern Germany (Höglwald). The experiment comprised three plots: no irrigation, irrigation (170 mm a?1), and acid irrigation with diluted sulphuric acid (pH of 2.6–2.8). During the seven years of acid irrigation (1984–1990) water containing 0.43 molc m?2 a?1 of protons and sulphate was added with a mean pH of 3.2 (throughfall?+?acid irrigation water) compared to 4.9 (throughfall) on both control plots. Most of the additional proton input was consumed in the organic layer and the upper mineral soil. Acid irrigation resulted in a long lasting elevation of sulphate concentrations in the seepage water. Together with sulphate both aluminium and appreciable amounts of base cations were leached from the main rooting zone. The ratio between base cations (Ca?+?Mg?+?K) and aluminium was 0.79 during acid irrigation and 0.92 on the control. Neither tree growth and nutrition nor the pool of exchangeable cations were affected significantly. We conclude that at this site protection mechanisms against aluminium toxicity exist and that additional base cation runoff can still be compensated without further reduction of the supply of exchangeable base cations in the upper mineral soil.  相似文献   
163.
澳大利亚矿山酸性废水的管理与处理   总被引:3,自引:1,他引:2  
本文简要介绍了澳大利亚矿山含酸废弃物及酸性废水的管理与处理方法 ,将为我国的矿山环境保护提供借鉴作用。  相似文献   
164.
Acid mine drainage (AMD) results from the oxidation of sulfides, mainly pyrite, present in mine wastes, either mill tailings or waste rock. This is the second of two papers describing the coupled physical processes taking place in waste rock piles undergoing AMD production. Since the oxidation of pyrite involves the consumption of oxygen and the production of heat, the oxidation process initiates coupled processes of gas transfer by diffusion and convection as well as heat transfer. These processes influence the supply of oxygen that is required to sustain the oxidation process. This second paper describes a numerical simulator used to represent the interaction of these coupled transfer processes. Numerical simulations are applied to two large sites with extensive characterization programs and widely different properties and behavior that were described in the first paper. The South Dump of the Doyon mine in Canada is permeable and has a high pyrite oxidation rate, thus making temperature-driven air convection the main oxygen supply mechanism. The Nordhalde of the Ronnenberg mining district in Germany contains lower permeability material which is less reactive, thus leading to a more balanced contribution of gaseous diffusion and convection as oxygen supply mechanisms. Overall, simulations allow a coherent representation of the conditions monitored within the waste rock piles and the confirmation of their physical properties. Conceptual simulations are also carried out to illustrate the potential effect of border membranes and layered co-mingling as mitigation methods used to control AMD production in either active or future waste rock piles.  相似文献   
165.
用铁酸盐型磁性吸附剂去除偶氮染料酸性红B   总被引:7,自引:0,他引:7       下载免费PDF全文
通过对几种磁性铁酸盐型吸附剂Mfe2O4(M=Fe,Mn,Cu)的表面特性及去除染料酸性红B(ARB)的吸附性能与催化氧化再生性能的研究,证明该类吸附剂能够有效地吸附去除水中的酸性红B,经磁分离,用H2O2/Fe2+体系可以同时氧化有机物与再生吸附剂,吸附剂可以循环使用.pH值对吸附能力有很大影响,对于MnFe2O4和Fe3O4,发生最大吸附的pH值范围在3.5~3.8,而对于CuFe2O4 pH值则在4.5~4.8时有最大吸附能力.CuFe2O4的吸附容量最大,MnFe2O4次之,FeO4最小;3种吸附剂的吸附等温线均符合Langmuir吸附模型.在发生吸附的pH值范围内,吸附剂吸附染料后其Zeta电位比吸附前均有明显降低.再生实验表明,3种吸附剂再生后,其比表面积明显增大,表面元素组成发生很大变化,其吸附能力也明显提高.  相似文献   
166.
研究硬脂酸改性磁铁矿对石油污水中油类物质的吸附,通过改变温度、超声振荡时间和磁铁矿与硬脂酸的质量比等因素,在最佳的改性条件下制得改性磁铁矿。将改性后的磁铁矿应用于石油污水处理,改变震荡时间,用红外分光测油仪得出吸附结果。结果表明:当改性温度为35℃、改性时间为35min、硬脂酸与磁铁矿质量比为3.5%时磁铁矿改性效果最佳,当吸附时间为8min时,对石油炼化污水中油类物质的吸附效果最好,吸附量为216.65mg/g。  相似文献   
167.
Lead (Pb) coprecipitation with jarosite is common in natural and engineered environments, such as acid mine drainage (AMD) sites and hydrometallurgical industry. Despite the high relevance for environmental impact, few studies have examined the exact interaction of Pb with jarosite and the dissolution behavior of each phase. In the present work, we demonstrate that Pb mainly interacts with jarosite in four modes, namely incorporation, occlusion, physically mixing, and chemically mixing. For comparison, the four modes of Pb-bearing natrojarosite were synthesized and characterized separately. Batch dissolution experiments were undertaken on these synthetic Pb-bearing natrojarosites under pH 2 to simulate the AMD environments. The introduction of Pb decreases the final Fe releasing efficiency of jarosite-type compounds from 18.18% to 3.45%-5.01%, showing a remarkable inhibition of their dissolution. For Pb releasing behavior, PbSO4 dissolves in preference to Pb-substituted natrojarosite, i.e., (Na, Pb)-jarosite, which primarily results in the sharp increase of Pb releasing concentration (> 40 mg/L). PbSO4 occlusion by jarosite-type compounds can significantly reduce the release of Pb. The results of this study could provide useful information regarding Fe and Pb cycling in acidic natural and engineered environments.  相似文献   
168.
选取洱海不同季节全湖47个沉积物表层样品,探讨水提取态有机氮(WEON)与不同来源(上覆水、间隙水、入湖河流和湿沉降)溶解性有机氮(DON)组分特征差异,并分析其对沉积物影响.结果表明,(1)洱海沉积物WEON含量季节性变化为夏季春季秋季冬季;空间分布规律呈北部南部中部.(2)洱海沉积物WEON腐殖化程度较高,腐殖质主要以富里酸为主,主要含有紫外区类腐殖质荧光峰A和高激发类色氨酸荧光峰B,受陆源输入和湖内生物共同影响.(3)洱海沉积物及其他来源DON均含有2个荧光组分,其中组分C1为内源性可见紫外区腐殖质峰是生物降解形成的荧光峰;组分C2为类色氨酸峰;湿沉降样品类蛋白峰峰强最大,生物可利用性较高;入湖河流DON生物可利用性最低.(4)洱海上覆水DON荧光C1和C2组分和沉积物WEON含量为显著相关(r=-0.79,P0.01;r=-0.944,P0.01),上覆水DON的荧光组分特征能够很好指示沉积物WEON含量特征.研究洱海不同样品DON结构组分特征,揭示洱海富营养化的潜在风险,为防治规划提供依据.  相似文献   
169.
对南京市的18个采样点进行PM_(2.5)样品采集,并利用电感耦合等离子体质谱仪以及液相电感耦合等离子体质谱联用仪分别对样品中的总砷和4种水溶性砷进行测量,在此基础上研究PM_(2.5)中砷的形态及其时空分布特征.结果表明:南京市PM_(2.5)中的砷以无机砷为主,有机砷为辅.无机砷以三价砷(As(III))为主,五价砷(As(V))为辅,As(III)/As(V)的平均值为0.39±0.03.有机砷以二甲基胂酸(DMAs(V))为主,所有样品均未检出甲基胂酸(MMAs(V)).总砷(As_T)、As(III)、As(V)和DMAs(V)的年平均浓度分别为6.90、0.99、3.20和0.03 ng·m~(-3).PM_(2.5)中的砷浓度具有明显季节变化:总砷和As(V)最大浓度出现在冬季,As(III)最大浓度出现在夏季,DMAs(V)只在夏季出现.T检验表明:As(III)、总砷和DMAs(V)年平均浓度在城区和郊区之间存在显著差异.空间变异系数的计算结果表明DMAs(V)的空间变化最大,其空间变异系数为0.6.总砷和3种水溶性砷年平均浓度由大到小排列为:农村郊区城区.道路采样点和城市背景点的总砷年平均浓度比为0.92,说明城区交通源对PM_(2.5)中砷污染的贡献不明显.As(III)和As(V)的主要排放源可能为燃煤电厂和钢铁冶炼厂,而DMAs(V)可能主要来源于生物挥发产物的二次生成.  相似文献   
170.
Modified kaolin clays were used as adsorbents for SO(2) gas adsorptions. The clays were heated up to 900 °C previous to acid treatments with 0.5 N sulfuric acid solutions at boiling temperature during different times up to 1440 min. Equilibrium adsorption at 25 °C and 0.1 MPa was carried out by using a volumetric apparatus. The samples were characterized by chemical analysis, X-ray diffraction and infrared analysis. The heating of the clays followed by acid treatment improved the adsorption capacity of the kaolin clays. The presence of amorphous silica and hydroxyl in the final products improved SO(2) adsorption capacity. Better properties for SO(2) adsorption were found in kaolin rich in not well ordered kaolinite clay mineral.  相似文献   
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