全文获取类型
收费全文 | 385篇 |
免费 | 39篇 |
国内免费 | 230篇 |
专业分类
安全科学 | 22篇 |
废物处理 | 19篇 |
环保管理 | 51篇 |
综合类 | 424篇 |
基础理论 | 33篇 |
污染及防治 | 96篇 |
评价与监测 | 7篇 |
社会与环境 | 2篇 |
出版年
2023年 | 3篇 |
2022年 | 5篇 |
2021年 | 16篇 |
2020年 | 19篇 |
2019年 | 14篇 |
2018年 | 11篇 |
2017年 | 15篇 |
2016年 | 26篇 |
2015年 | 38篇 |
2014年 | 40篇 |
2013年 | 26篇 |
2012年 | 44篇 |
2011年 | 43篇 |
2010年 | 27篇 |
2009年 | 36篇 |
2008年 | 31篇 |
2007年 | 32篇 |
2006年 | 49篇 |
2005年 | 33篇 |
2004年 | 20篇 |
2003年 | 17篇 |
2002年 | 17篇 |
2001年 | 21篇 |
2000年 | 18篇 |
1999年 | 8篇 |
1998年 | 12篇 |
1997年 | 8篇 |
1996年 | 4篇 |
1995年 | 3篇 |
1994年 | 1篇 |
1993年 | 4篇 |
1992年 | 1篇 |
1991年 | 2篇 |
1990年 | 1篇 |
1989年 | 2篇 |
1988年 | 1篇 |
1973年 | 3篇 |
1972年 | 2篇 |
1970年 | 1篇 |
排序方式: 共有654条查询结果,搜索用时 293 毫秒
31.
针对曝气沉砂池小试装置模型,通过配砂实验对沉砂池除砂率进行统计分析,研究曝气强度与HRT对沉砂池除砂率的影响。实验结果表明,不同曝气强度下,随着HRT变化,除砂率逐渐上升,并最终趋于平衡状态;不同HRT下,曝气强度与除砂率近似呈现一定的线性关系,且随着曝气强度的增大,除砂率降低;在HRT小于1min时,砂粒的运行路径和沉降时间缩短,不利于砂粒的去除;在HRT大于1min时,其中1、3和4min,随着气水比的增加除砂率降低幅度相对较小,曝气所引起的横向环流在一定程度上有利于砂粒的沉降,而HRT为2min时,除砂率降幅却很大,这与砂粒在曝气沉砂池池体断面分布有关,即断面处旋转流速和水平流速的大小变化将影响砂粒的运动;相比曝气强度,HRT对除砂率的影响较大。 相似文献
32.
33.
为了控制污水脱氮中N2O排放,在不同曝气强度下研究了好氧硝化段同时硝化反硝化(SND)系统的N2O排放特性,并采用PCR—DGGE技术分析微生物群落特征。结果发现,随着曝气强度的增强,系统总氮去除率下降,但脱氮中N2O—N所占比例则上升,实验中从低到高3个曝气强度下,总氮去除率分别为80.01%、65.28%和58.62%,脱氮中N2O—N所占的比例为1.89%、7.84%和9.20%。PCR—DGGE分析显示,和低曝气强度下相比中、高曝气强度下系统微生物群落发生明显变化,但中曝气强度和高曝气强度下系统微生物群落表现出较高相似性。这表明,不同曝气强度下系统N2O排放受到氮素转化和微生物群落变化的影响。适宜曝气强度不仅提高总氮去除率,还可有效控制N2O排放。 相似文献
34.
为了研究不同好氧预处理方式对餐厨垃圾厌氧消化产甲烷的影响,通过建立3个模拟厌氧生物反应器,研究了传统厌氧生物反应器C1、上层好氧预处理-厌氧生物反应器C2和底部好氧预处理-厌氧生物反应器C3 3种不同操作条件下的产甲烷过程.结果表明,挥发性有机酸的累积使C1始终处于产甲烷滞后阶段;而C2、C3的好氧预处理通过加快易水解酸化组分和过量挥发性有机酸的好氧降解,有效缓解了酸性抑制,产甲烷滞后时间明显缩短至10 d内.第32天C2停止上层曝气后,在27 d内甲烷浓度达到了50%以上,同时,产甲烷速率迅速上升,并在第81天可达到峰值773 mL/(kg·d).C3在第11天停止底部曝气后,虽然经过22 d的时间甲烷浓度即上升至50%,但之后产甲烷速率经历回落阶段后再次逐渐上升,在实验结束时仅达到517 mL/(kg·d).上层曝气的好氧预处理方式所需曝气时间相对较长,但其产甲烷启动快,与底部曝气相比,其后期的甲烷化过程更稳定并可达到较高的产甲烷速率. 相似文献
35.
36.
EMMC process for combined removal of organics, nitrogen and an odor producing substance 总被引:2,自引:0,他引:2
In order to improve the process performance regarding the removal of organics, nitrogen, and an odor-causing compound (sulfide) contained in domestic wastewater, an entrapped-mixed-microbial cell (EMMC) with and without humic substances for both fixed and moving carrier reactors and conventional suspended growth culture (i.e. conventional activated sludge process) were investigated simultaneously. Both synthetic (simulated to the organics concentration of general domestic sewage) and actual domestic wastewater were investigated under operational conditions of 12 h of hydraulic retention time (HRT) with 1 h of aeration and 1 h of non-aeration, and 6 h of HRT with continuous aeration, at a room temperature of 25 +/- 2 degrees C. It was found that entrapping humic substances in the EMMC carriers had no impact on the removal of organics, nitrogen, and the odor-producing compound. Additionally, the performance of the EMMC moving carrier system for the removal of these pollutants is similar to that of the EMMC fixed carrier system. In general, the EMMC associated systems which provide high solids retention time achieve a better removal of chemical oxygen demand (COD), nitrogen, and the odor-producing substance than the suspended growth system for both HRTs of 6 h (continuous aeration) and 12 h (1 h of aeration and 1 h of non-aeration). Both the fixed and moving carrier EMMC processes, therefore, have the potential for improvement or replacement of the existing conventional activated sludge process with regard to improving the effluent qualities (such as COD, nitrogen and odor-producing compound) for reuse/disposal. 相似文献
37.
Hydrological Connectivity Between Headwater Streams and Downstream Waters: How Science Can Inform Policy1 总被引:1,自引:0,他引:1
Tracie‐Lynn Nadeau Mark Cable Rains 《Journal of the American Water Resources Association》2007,43(1):118-133
Abstract: In January 2001, the U.S. Supreme Court ruled that the U.S. Army Corps of Engineers exceeded its statutory authority by asserting Clean Water Act (CWA) jurisdiction over non‐navigable, isolated, intrastate waters based solely on their use by migratory birds. The Supreme Court’s majority opinion addressed broader issues of CWA jurisdiction by implying that the CWA intended some “connection” to navigability and that isolated waters need a “significant nexus” to navigable waters to be jurisdictional. Subsequent to this decision (SWANCC), there have been many lawsuits challenging CWA jurisdiction, many of which are focused on headwater, intermittent, and ephemeral streams. To inform the legal and policy debate surrounding this issue, we present information on the geographic distribution of headwater streams and intermittent and ephemeral streams throughout the U.S., summarize major findings from the scientific literature in considering hydrological connectivity between headwater streams and downstream waters, and relate the scientific information presented to policy issues surrounding the scope of waters protected under the CWA. Headwater streams comprise approximately 53% (2,900,000 km) of the total stream length in the U.S., excluding Alaska, and intermittent and ephemeral streams comprise approximately 59% (3,200,000 km) of the total stream length and approximately 50% (1,460,000 km) of the headwater stream length in the U.S., excluding Alaska. Hillslopes, headwater streams, and downstream waters are best described as individual elements of integrated hydrological systems. Hydrological connectivity allows for the exchange of mass, momentum, energy, and organisms longitudinally, laterally, vertically, and temporally between headwater streams and downstream waters. Via hydrological connectivity, headwater, intermittent and ephemeral streams cumulatively contribute to the functional integrity of downstream waters; hydrologically and ecologically, they are a part of the tributary system. As this debate continues, scientific input from multiple fields will be important for policymaking at the federal, state, and local levels and to inform water resource management regardless of the level at which those decisions are being made. Strengthening the interface between science, policy, and public participation is critical if we are going to achieve effective water resource management. 相似文献
38.
为研究不同浓度蓝藻水华在曝气形成的好氧条件下的光合作用,本文按叶绿素a(Chla)浓度32.5,346.8,1413.7和14250.0μg/L设4个处理组(从低到高编号依次为I、Ⅱ、Ⅲ和IV)进行实验.结果表明,各处理Chla浓度均总体呈下降趋势,但均未出现发黑或发褐现象;各处理溶氧、pH值、NH4+-N浓度和最大光合作用能力Fv/Fm均有一定差异(P<0.05).快速光响应曲线的特征参数α、ETRmax和Ik表明,处理I、Ⅱ和Ⅲ中出现较高的绿藻、硅/甲藻的光能利用效率(P<0.05),而处理IV中所有藻类的光能利用效率较低(P<0.05).曝气增氧可以防止高浓度蓝藻水华形成黑水团;蓝藻水华初始Chla浓度约为32.5、346.8、1413.7μg/L时,在曝气形成的好氧条件下,蓝藻水华中会出现其它藻类如绿藻、硅/甲藻的生长,即藻类群落结构朝着多样化变化,对蓝藻水华形成控制. 相似文献
39.
采用膜生物反应器(MBR)研究了厌氧氨氧化细菌在富集过程中的活性变化,在启动全程自养脱氮(CANON)工艺中以恒定曝气量,通过优化停曝比实现氨氧化细菌(AerAOB)和厌氧氨氧化细菌(AnAOB)协同脱氮并且有效抑制亚硝酸盐氧化菌(NOB)的活性,然后添加有机物(乙酸钠)逐步启动同步亚硝化-厌氧氨氧化耦合异养反硝化(SNAD)工艺.结果表明,在厌氧氨氧化细菌富集过程中,通过不断缩短水力停留时间(HRT)提高进水氮负荷的方式强化厌氧氨氧化细菌活性,其平均活性由0.603mgN/(h·gVSS)提高到了8.1mgN/(h·gVSS);当恒定曝气量为50mL/min,停曝比为4:10(min:min)时,AerAOB和AnAOB对氨氮的去除量分别占总氨氮去除量的58.8%和41.2%,NOB氧化亚硝态氮的量占总硝态氮生成量的15.3%,成功抑制了NOB的活性;当C/N比为0.5,调整停曝比为4:15后,反硝化过程氮去除量占总氮去除率的20.9%,厌氧氨氧化过程氮去除量占总氮去除率的79.1%,实现了AerAOB、AnAOB和反硝化细菌(DNB)协同脱氮的目的. 相似文献
40.