全文获取类型
| 收费全文 | 7877篇 |
| 免费 | 1506篇 |
| 国内免费 | 392篇 |
专业分类
| 安全科学 | 462篇 |
| 废物处理 | 789篇 |
| 环保管理 | 1072篇 |
| 综合类 | 4930篇 |
| 基础理论 | 671篇 |
| 环境理论 | 1篇 |
| 污染及防治 | 1630篇 |
| 评价与监测 | 142篇 |
| 社会与环境 | 54篇 |
| 灾害及防治 | 24篇 |
出版年
| 2025年 | 19篇 |
| 2024年 | 120篇 |
| 2023年 | 155篇 |
| 2022年 | 164篇 |
| 2021年 | 226篇 |
| 2020年 | 199篇 |
| 2019年 | 181篇 |
| 2018年 | 168篇 |
| 2017年 | 211篇 |
| 2016年 | 258篇 |
| 2015年 | 258篇 |
| 2014年 | 385篇 |
| 2013年 | 436篇 |
| 2012年 | 509篇 |
| 2011年 | 508篇 |
| 2010年 | 404篇 |
| 2009年 | 449篇 |
| 2008年 | 373篇 |
| 2007年 | 573篇 |
| 2006年 | 688篇 |
| 2005年 | 527篇 |
| 2004年 | 452篇 |
| 2003年 | 444篇 |
| 2002年 | 374篇 |
| 2001年 | 317篇 |
| 2000年 | 284篇 |
| 1999年 | 266篇 |
| 1998年 | 191篇 |
| 1997年 | 148篇 |
| 1996年 | 113篇 |
| 1995年 | 101篇 |
| 1994年 | 83篇 |
| 1993年 | 64篇 |
| 1992年 | 33篇 |
| 1991年 | 30篇 |
| 1990年 | 10篇 |
| 1989年 | 4篇 |
| 1988年 | 4篇 |
| 1986年 | 7篇 |
| 1982年 | 3篇 |
| 1981年 | 4篇 |
| 1980年 | 3篇 |
| 1978年 | 2篇 |
| 1977年 | 2篇 |
| 1975年 | 2篇 |
| 1974年 | 3篇 |
| 1973年 | 4篇 |
| 1972年 | 3篇 |
| 1971年 | 3篇 |
| 1970年 | 2篇 |
排序方式： 共有9775条查询结果，搜索用时 107 毫秒
441.
随着染料工业的发展,其生产废水已成为主要的水体污染源。目前染料已有成千上万种之多,它们不但具有特定的颜色,而且结构复杂,以高分子络合物为多。且生物降解性较低,大多具有潜在毒性,在环境中的归趋依赖于很多未知因子。这些特点致使染料废水难以找到行之有效的处理方法。介绍了几种染料废水的处理技术及其发展趋势,这些研究对染料废水的治理具有一定的指导意义。 相似文献
442.
443.
444.
何建清 《安全．健康和环境》2005,5(7):42-44
塔河油田一号联合站(塔一联)稠油污水具有粘度大、油水密度差小、乳化严重等特点,它的回用与外排具有一定的难度.通过实验室和现场试验研制开发的破乳剂和混凝剂,强化了除油效果,减轻了过滤系统的负荷,处理污水达到了注水水质指标. 相似文献
445.
Tianlong Zheng Qunhui Wang Zhining Shi Yue Fang Shanshan Shi Juan Wang Chuanfu Wu 《环境科学学报(英文版)》2016,28(12):21-31
A three-dimensional electrochemical oxidation(3D-EC) reactor with introduction of activated carbon(AC) as particle micro-electrodes was applied for the advanced treatment of secondary wastewater effluent of a wet-spun acrylic fiber manufacturing plant. Under the optimized conditions(current density of 500 A/m~2, circulation rate of 5 mL/min, AC dosage of 50 g, and chloride concentration of 1.0 g/L), the average removal efficiencies of chemical oxygen demand(COD_(cr)), NH3–N, total organic carbon(TOC), and ultraviolet absorption at 254 nm(UV_(254)) of the 3D-EC reactor were 64.5%, 60.8%, 46.4%, and 64.8%, respectively; while the corresponding effluent concentrations of COD_(cr), NH_3–N, TOC, and UV_(254) were 76.6, 20.1, and42.5 mg/L, and 0.08 Abs/cm, respectively. The effluent concentration of COD_(cr) was less than 100 mg/L, which showed that the treated wastewater satisfied the demand of the integrated wastewater discharge standard(GB 8978-1996). The 3D-EC process remarkably improved the treatment efficiencies with synergistic effects for COD_(cr), NH_3–N, TOC, and UV_(254) during the stable stage of 44.5%, 38.8%, 27.2%, and 10.9%, respectively, as compared with the sum of the efficiencies of a two-dimensional electrochemical oxidation(2D-EC) reactor and an AC adsorption process, which was ascribed to the numerous micro-electrodes of AC in the 3D-EC reactor. Gas chromatography mass spectrometry(GC–MS) analysis revealed that electrochemical treatment did not generate more toxic organics, and it was proved that the increase in acute biotoxicity was caused primarily by the production of free chlorine. 相似文献
446.
以库区天然水培养的二形栅藻(Scenedesmus dimorphus)为研究对象,利用大气压强电场电离放电产生羟基自由基(·OH),结合压力溶气气浮前处理工艺处理高藻水.实验结果表明,对于藻密度为65.6×10~4 cells/mL,浊度为10.8NTU,COD_(Mn)为6.74mg/L的高藻水,在总氧化剂TRO浓度为1.03 mg/L时,藻类去除效率达到100%;总细菌,总大肠菌群和大肠埃希氏菌均未检出;出水COD_(Mn)由1.43 mg/L降至1.25mg/L,降低了10%;浊度由0.66NTU降至0.54NTU,降低了12.59在排放高藻水的主管路中·OH杀藻的接触反应时间仅为6s.因此汽浮-·OH强氧化组合工艺可高效快速地处理高藻水,为保障水源水的供水安全探索了一种新的思路. 相似文献
447.
A fungal consortium including Aspergillus niger, Mucor hiemalis and Galactomyces geotrichum was tested for the treatment of dairy wastewater. The bio-augmentation method was tested at lab-scale (4 L), at pilot scale (110 L) and at an industrial scale in Wastewater Treatment Plants (WWTP). The positive impact of fungal addition was confirmed when fungi was beforehand accelerated by pre-culture on whey (5 g/L lactose) or on the dairy effluent. Indeed, chemical oxygen demand (COD) removal yields increased from 55% to 75% for model medium, diluted milk. While after inoculation of an industrial biological tank from a dairy factory with the fungal consortium accelerated by pre-cultivation in a 1000 L pilot plant, the outlet COD values decreased from values above the standard one (100 mg/L) to values in the range of 50-70 mg/L. In addition, there was a clear impact of fungal addition on the ’hard’ or non-biodegradable COD owing to the significant reduction of the increase of the COD on BOD 5 ratio between the inlet and the outlet of the biological tank of WWTP. It was in the range of 451%-1111% before adding fungal consortium, and in the range of 257%-153% after bio-augmentation with fungi. An inoculated bioreactor with fungal consortium was developed at lab-scale and demonstrated successfully at pilot scale in WWTP. 相似文献
448.
The mixture of five yeast strains obtained from soil could remove about 85% TOC of oil-rich wastewater in batch test.While the highest MLSS was obtained at an N:C of 1:5,the oil removal decreased with the increase of N:C during yeast sludge cultivation.Ammonium chloride was the best nitrogen source for yeast cultivation from the viewpoint of yeast growth and oil utilizxation.An ammonia concentration of over 1300 mg/L led to mass death of yeast at a pH of 5.The ammonia concentration should be controlled at a level of 1000 mg/L or lower. 相似文献
449.
ＩｎｔｒｏｄｕｃｔｉｏｎＨｅａｖｙｍｅｔａｌｓｉｎｗａｔｅｒｂｏｄｉｅｓａｒｅｓｉｇｎｉｆｉｃａｎｔｌｙｄｉｆｆｅｒｅｎｔｆｒｏｍｏｒｇａｎｉｃｐｏｌｌｕｔａｎｔｓｔｈａｔｃａｎｂｅｍｉｃｒｏｂｉｏｌｏｇｉｃａｌｌｙｄｅｇｒａｄｅｄｏｒｄｅｃｏｍｐｏｓｅｄ .Ｇｅｎｅｒａｌｌｙ ,ｔｈｅｙａｒｅｐｕｒｉｆｉｅｄｔｈｒｏｕｇｈｔｈｅｉｒａｄｓｏｒｐｔｉｏｎｏｎｔｏｓｕｓｐｅｎｄｅｄｓｕｂｓｔｒａｔｅｓｉｎｒｉｖｅｒｓ.Ａｄｓｏｒｐｔｉｏｎｏｆｈｅａｖｙｍｅｔａｌｓｏｎｒｉｖｅｒｓｕｓｐｅｎｄｅｄｓｕｂ… 相似文献
450.
Treatment of anthraquinone dye wastewater by hydrolytic acidification-aerobic process 总被引：4，自引：0，他引：4
Experiment on microbial degradation with two kinds of biological process, hydrolytic acidification-aerobic process and aerobic process was conducted to treat the anthraquinone dye wastewater with CODc, concentration of 400 mg/L and chroma 800. The experimental result demonstrated that the hydrolytic-aerobic process could raise the biodegradability of anthraquinone dye wastewater effectively. The effluent CODc, can reach 120-170 mg/L and chroma 150 which is superior to that from simple aerobic process. 相似文献