全文获取类型
收费全文 | 1262篇 |
免费 | 100篇 |
国内免费 | 580篇 |
专业分类
安全科学 | 99篇 |
废物处理 | 66篇 |
环保管理 | 118篇 |
综合类 | 798篇 |
基础理论 | 200篇 |
污染及防治 | 467篇 |
评价与监测 | 58篇 |
社会与环境 | 56篇 |
灾害及防治 | 80篇 |
出版年
2024年 | 3篇 |
2023年 | 30篇 |
2022年 | 86篇 |
2021年 | 79篇 |
2020年 | 59篇 |
2019年 | 47篇 |
2018年 | 43篇 |
2017年 | 82篇 |
2016年 | 89篇 |
2015年 | 92篇 |
2014年 | 114篇 |
2013年 | 132篇 |
2012年 | 116篇 |
2011年 | 116篇 |
2010年 | 83篇 |
2009年 | 85篇 |
2008年 | 106篇 |
2007年 | 87篇 |
2006年 | 71篇 |
2005年 | 46篇 |
2004年 | 34篇 |
2003年 | 59篇 |
2002年 | 40篇 |
2001年 | 36篇 |
2000年 | 31篇 |
1999年 | 28篇 |
1998年 | 23篇 |
1997年 | 24篇 |
1996年 | 29篇 |
1995年 | 16篇 |
1994年 | 8篇 |
1993年 | 5篇 |
1992年 | 10篇 |
1991年 | 7篇 |
1990年 | 6篇 |
1989年 | 6篇 |
1988年 | 4篇 |
1987年 | 2篇 |
1986年 | 2篇 |
1985年 | 2篇 |
1984年 | 1篇 |
1983年 | 1篇 |
1982年 | 1篇 |
1981年 | 1篇 |
排序方式: 共有1942条查询结果,搜索用时 15 毫秒
101.
The kinetics and mechanism for degradation of omethoate (OMT) by catalytic ozonation with Fe(III)-loaded activated carbon (Fe@AC) were investigated in this study with focus on identification of degradation byproducts. The rate constants of OMT reacting with ozone and hydroxyl radical (OH) were determined to be 0.04 and 5.3 × 108 M?1 s?1 at pH 7.5 and 20 °C, respectively. OMT was predominantly degraded by OH in the catalytic ozonation with Fe@AC. The high-molecular-weight degradation byproducts identified were O,O,O-trimethyl phosphoric ester (TMP), pyrrolidin-2-one, N-methyl-2-sulfanylacetamide, 2-(methylthio)acetamide, O,O,S-trimethylthiophosphate (STMP), and N-methyl-2-(methylthio)acetamide. Besides, low-molecular-weight organic acids and inorganic anions were also detected and quantified, including formic, acetic and oxalic acids as well as nitrate, sulfate and phosphate ions. In the catalytic ozonation, TMP and phosphate were two major P-containing byproducts resulting from OMT degradation. The toxicity of OMT solution gradually decreased during the catalytic ozonation, indicating that Fe@AC is a safe catalyst for OMT removal by ozone in water. 相似文献
102.
Sulfamethoxazole (SMX) and sulfapyridine (SPY), two representative sulfonamide antibiotics, have gained increasing attention because of the ecological risks these substances pose to plants, animals, and humans. This work systematically investigated the removal of SMX and SPY by carbon nanotubes (CNTs) in fixed-bed columns under a broad range of conditions including: CNT incorporation method, solution pH, bed depth, adsorbent dosage, adsorbate initial concentration, and flow rate. Fixed-bed experiments showed that pH is a key factor that affects the adsorption capacity of antibiotics to CNTs. The Bed Depth Service Time model describes well the relationship between service time and bed depth and can be used to design appropriate column parameters. During fixed-bed regeneration, small amounts of SMX (3%) and SPY (9%) were irreversibly bonded to the CNT/sand porous media, thus reducing the column capacity for subsequent reuse from 67.9 to 50.4 mg g?1 for SMX and from 91.9 to 72.9 mg g?1 for SPY. The reduced column capacity resulted from the decrease in available adsorption sites and resulting repulsion (i.e., blocking) of incoming antibiotics from those previously adsorbed. Findings from this study demonstrate that fixed-bed columns packed with CNTs can be efficiently used and regenerated to remove antibiotics from water. 相似文献
103.
3种载体固定化菌藻共生系统脱氮除磷效果的对比 总被引:1,自引:0,他引:1
采用3种不同载体(海藻酸钠、聚乙烯醇、复合载体),分别将小球藻和栅藻与活性污泥固定成菌藻共生系统,制成菌藻凝胶小球,单独菌、单独藻的凝胶小球,用于处理人工污水。结果表明,(1)复合载体固定的菌藻共生系统氮磷去除效果最好,PVA载体的脱氮除磷效果次于复合载体优于海藻酸钠;(2)固定化菌藻共生系统的脱氮除磷效果明显优于单独固定菌和单独固定藻,固定菌的效果较差;(3)3种载体包埋下的固定化小球藻的脱氮除磷效果均较相同载体固定化的栅藻效果好。 相似文献
104.
为降低可旋转径向式微粒捕集器中的排气噪声,采用有限元法建立可旋转径向式微粒捕集器声学特性模型,分析得到了其消声特性和传递损失曲线,并采用灰色关联分析方法研究可旋转径向式微粒捕集器结构参数对消声特性的影响程度。结果表明,可旋转径向式微粒捕集器具有降噪能力,且对高频噪声消声效果明显好于低频噪声,平均消声量为20 dB左右;直径比和扩张管锥角是影响可旋转径向式微粒捕集器消声特性的2个主要因素,适当选用小的直径比和扩张管锥角,有利于提高可旋转径向式微粒捕集器的消声性能。 相似文献
105.
Chlortoluron chlorination is studied in the pH range of 3-10 at 25 ± 1 °C. The chlorination kinetics can be well described by a second-order kinetics model, first-order in chlorine and first-order in chlortoluron. The apparent rate constants were determined and found to be minimum at pH 6, maximum at pH 3 and medium at alkaline conditions. The rate constant of each predominant elementary reactions (i.e., the acid-catalyzed reaction of chlortoluron with HOCl, the reaction of chlortoluron with HOCl and the reaction of chlortoluron with OCl−) was calculated as 3.12 (± 0.10) × 107 M−2 h−1, 3.11 (±0.39) × 102 M−1 h−1 and 3.06 (±0.47) × 103 M−1 h−1, respectively. The main chlortoluron chlorination by-products were identified by gas chromatography-mass spectrometry (GC-MS) with purge-and-trap pretreatment, ultra-performance liquid chromatography-electrospray ionization-MS and GC-electron capture detector. Six volatile disinfection by-products were identified including chloroform (CF), dichloroacetonitrile, 1,1-dichloropropanone, 1,1,1-trichloropropanone, dichloronitromethane and trichloronitromethane. Degradation pathways of chlortoluron chlorination were then proposed. High concentrations of CF were generated during chlortoluron chlorination, with maximum CF yield at circumneutral pH range in solution. 相似文献
106.
Vijgen J Abhilash PC Li YF Lal R Forter M Torres J Singh N Yunus M Tian C Schäffer A Weber R 《Environmental science and pollution research international》2011,18(2):152-162
Purpose
Hexachlorocyclohexane (HCH) isomers (??-, ??- and ??- (Lindane)) were recently included as new persistent organic pollutants (POPs) in the Stockholm Convention, and therefore, the legacy of HCH and Lindane production became a contemporary topic of global relevance. This article wants to briefly summarise the outcomes of the Stockholm Convention process and make an estimation of the amount of HCH waste generated and dumped in the former Lindane/HCH-producing countries.Results
In a preliminary assessment, the countries and the respective amount of HCH residues stored and deposited from Lindane production are estimated. Between 4 and 7 million tonnes of wastes of toxic, persistent and bioaccumulative residues (largely consisting of alpha- (approx. 80%) and beta-HCH) are estimated to have been produced and discarded around the globe during 60 years of Lindane production. For approximately 1.9 million tonnes, information is available regarding deposition. Countries are: Austria, Brazil, China, Czech Republic, France, Germany, Hungary, India, Italy, Japan, Macedonia, Nigeria, Poland, Romania, Slovakia, South Africa, Spain, Switzerland, Turkey, The Netherlands, UK, USA, and former USSR. The paper highlights the environmental relevance of deposited HCH wastes and the related POPs?? contaminated sites and provides suggestions for further steps to address the challenge of the legacy of HCH/Lindane production.Conclusion
It can be expected that most locations where HCH waste was discarded/stockpiled are not secured and that critical environmental impacts are resulting from leaching and volatilisation. As parties to the Stockholm Convention are legally required to take action to stop further POPs pollution, identification and evaluation of such sites are necessary. 相似文献107.
108.
109.
介绍水射流技术在放顶煤综采中的应用。通过具体的技术经济指标说明在一定的条件下水系与放顶煤综采相结合是提高采煤效益的新途径。还说明,水射流技术在采矿工业中有着广阔的应用前景。 相似文献
110.
本文通过对芦笋的高产栽培技术与开发利用研究,提出黑龙江省可扩大芦笋的种植面积,形成开发利用规模,为发展乡镇企业开创一条致富门路,并满足黑龙江市场需求。 相似文献