全文获取类型
收费全文 | 956篇 |
免费 | 86篇 |
国内免费 | 347篇 |
专业分类
安全科学 | 80篇 |
废物处理 | 52篇 |
环保管理 | 132篇 |
综合类 | 695篇 |
基础理论 | 62篇 |
污染及防治 | 164篇 |
评价与监测 | 192篇 |
社会与环境 | 5篇 |
灾害及防治 | 7篇 |
出版年
2024年 | 4篇 |
2023年 | 13篇 |
2022年 | 29篇 |
2021年 | 30篇 |
2020年 | 35篇 |
2019年 | 33篇 |
2018年 | 46篇 |
2017年 | 39篇 |
2016年 | 61篇 |
2015年 | 86篇 |
2014年 | 110篇 |
2013年 | 111篇 |
2012年 | 97篇 |
2011年 | 104篇 |
2010年 | 70篇 |
2009年 | 68篇 |
2008年 | 59篇 |
2007年 | 64篇 |
2006年 | 58篇 |
2005年 | 42篇 |
2004年 | 36篇 |
2003年 | 31篇 |
2002年 | 29篇 |
2001年 | 18篇 |
2000年 | 19篇 |
1999年 | 8篇 |
1998年 | 11篇 |
1997年 | 16篇 |
1996年 | 17篇 |
1995年 | 8篇 |
1994年 | 8篇 |
1993年 | 7篇 |
1992年 | 7篇 |
1991年 | 5篇 |
1990年 | 3篇 |
1989年 | 2篇 |
1987年 | 2篇 |
1986年 | 2篇 |
1972年 | 1篇 |
排序方式: 共有1389条查询结果,搜索用时 531 毫秒
21.
22.
为改善跳水池水质的化学安全性和生物学稳定性,保障运动员、教练员以及工作人员身体健康,结合长春市泅渡馆跳水池,阐述了基于pH和ORP的池水处理自动控制系统,确定了自动控制系统的控制参数及其控制范围,为健康跳水池池水处理系统的自动控制系统的设计提供了参考。 相似文献
23.
The addition of lipid wastes to the digestion of swine manure was studied as a means of increasing biogas production. Lipid waste was obtained from a biodiesel plant where used cooking oil is the feedstock. Digestion of this co-substrate was proposed as a way of valorising residual streams from the process of biodiesel production and to integrate the digestion process into the biorefinery concept.Batch digestion tests were performed at different co-digesting proportions obtaining as a result an increase in biogas production with the increase in the amount of co-substrate added to the mixture. Semi-continuous digestion was studied at a 7% (w/w) mass fraction of total solids. Co-digestion was successful at a hydraulic retention time (HRT) of 50 d but a decrease to 30 d resulted in a decrease in specific gas production and accumulation of volatile and long chain fatty acids. The CH4 yield obtained was 326 ± 46 l/kg VSfeed at an HRT of 50 d, while this value was reduced to 274 ± 43 l/kg VSfeed when evaluated at an HRT of 30 d. However these values were higher than the one obtained under batch conditions (266 ± 40 l/kg VSfeed), thus indicating the need of acclimation to the co-substrate. Despite of operating at low organic loading rate (OLR), measurements from respirometry assays of digestate samples (at an HRT of 50 d) suggested that the effluent could not be directly applied to the soil as fertiliser and might have a negative effect over soil or crops. 相似文献
24.
C. Riva A. Schievano G. D’Imporzano F. Adani 《Waste management (New York, N.Y.)》2014,34(8):1429-1435
The purpose of this study was to observe the economic sustainability of three different biogas full scale plants, fed with different organic matrices: energy crops (EC), manure, agro-industrial (Plants B and C) and organic fraction of municipal solid waste (OFMSW) (Plant A). The plants were observed for one year and total annual biomass feeding, biomass composition and biomass cost (€ Mg?1), initial investment cost and plant electric power production were registered. The unit costs of biogas and electric energy (€ Sm?3biogas, € kW h?1EE) were differently distributed, depending on the type of feed and plant. Plant A showed high management/maintenance cost for OFMSW treatment (0.155 € Sm?3biogas, 45% of total cost), Plant B suffered high cost for EC supply (0.130 € Sm?3biogas, 49% of total cost) and Plant C showed higher impact on the total costs because of the depreciation charge (0.146 € Sm?3biogas, 41% of total costs). The breakeven point for the tariff of electric energy, calculated for the different cases, resulted in the range 120–170 € MW h?1EE, depending on fed materials and plant scale. EC had great impact on biomass supply costs and should be reduced, in favor of organic waste and residues; plant scale still heavily influences the production costs. The EU States should drive incentives in dependence of these factors, to further develop this still promising sector. 相似文献
25.
以城市污水处理厂高含固污泥为对象,分别进行了连续厌氧消化抑硫试验和消化污泥Fe(Ⅲ)投加抑硫试验,探讨不同Fe/S(摩尔比)对污泥厌氧消化中溶解态硫化物去除效率的影响以及Fe(Ⅲ)与pH的交互作用.结果表明,热水解污泥厌氧消化采用原位抑硫技术,在Fe/S(摩尔比)为7.75时沼气中H_2S含量可由170.4×10~(-6)降至14.09×10~(-6),无需进行后续处理;当pH为7.00~7.50、Fe/S为1~11时,pH为原位抑硫主要显著影响因子,提高消化池pH有利于降低Fe(Ⅲ)投加量;高含固污泥厌氧消化沼气满足H_2S利用标准时,所需最低Fe/S为7.0;当消化池pH低于7.30时,将无法通过调节Fe/S实现H_2S浓度达标排放. 相似文献
26.
Jesus D. Fernandez-Bayo Juliano Toniato Blake A. Simmons Christopher W. Simmons 《环境科学学报(英文版)》2017,29(6):164-168
Food processing facilities often use antimicrobial quaternary ammonium compound (QAC) sanitizers to maintain cleanliness. These QACs can end up in wastewaters used as feedstock for anaerobic digestion. The aim of this study was to measure the effect of QAC contamination on biogas production and structure of microbial communities in thermophilic digester sludge. Methane production and biogas quality data were analyzed in batch anaerobic digesters containing QAC at 0, 15, 50, 100 and 150 mg/L. Increasing sanitizer concentration in the bioreactors negatively impacted methane production rate and biogas quality. Microbial community composition data was obtained through 16S rRNA gene sequencing from the QAC-contaminated sludges. Sequencing data showed no significant restructuring of the bacterial communities. However, significant restructuring was observed within the archaeal communities as QAC concentration increased. Further studies to confirm these effects on a larger scale and with a longer retention time are necessary. 相似文献
27.
28.
以苏州七子山生活垃圾焚烧厂产生的飞灰为研究对象,采用水泥作为固化剂,研究水泥飞灰固化体的应力应变特征及重金属浸出特性,并探讨了水泥飞灰配合比、养护时间等关键性因素对这些特性的影响。实验结果表明:较养护3 d的样品,其余养护时间的样品强度平均增长了约96.2%,而其破坏应变平均减小了56%。随着水泥含量和养护时间的增加,飞灰固化体的强度上升,而其破坏应变减小,该趋势主要归因于钙矾石(AFt)的形成促进了飞灰固化体强度的发展。较飞灰原样,飞灰固化体的重金属浸出浓度随着水泥含量、养护时间的增加而降低了38%~99%,重金属的迁移被限制,主要归因于水化硅酸钙(C—S—H)和钙矾石(AFt)的形成,以及飞灰和水泥水化反应创造的强碱性环境。 相似文献
29.
采用厌氧发酵处理庆大霉素菌渣,考察了含固率、接种比、接种污泥、发酵底物等因素对庆大霉素菌渣厌氧发酵的影响,并用累积净甲烷产量衡量庆大霉素菌渣进行厌氧发酵的可行性及发酵程度。试验结果证实了庆大霉素菌渣进行厌氧发酵的可行性,其中含固率和接种比对发酵的影响较大,最佳条件为含固率5%,接种比1/3;对比试验所用3种接种污泥,发现接种某造纸厂污水处理IC反应器的厌氧颗粒污泥效果最优,在最优含固率和接种比的条件下,累积净产甲烷量为28.21 m3/t;此外,试验还证实,采用不同菌渣的联合发酵表现出了明显的协同作用,在最优条件下,庆大霉素菌渣与林可霉素菌渣按1∶2的比例联合发酵的产甲烷量可达到37.5 m3/t。 相似文献
30.
采用猪粪厌氧消化的消化污泥为接种物,在中温(37℃)条件下,以连续进料的方式对餐厨垃圾的湿式厌氧消化进行了启动以及运行试验,监测整个实验过程中产气量、pH、VFA、碱度等能够反映厌氧消化的系统指标。结果表明:本实验中系统最佳有机负荷为2.8 kg/(m~3·d)(以VS计),超过此负荷后,依靠系统自身恢复和人工调节,pH很难恢复正常运行状态。正常运行过程中,pH稳定在7.5~8.0,VFA稳定在2 000 mg/L左右,碱度在6 000~9 000 mg/L,氨氮在1 500~2 000 mg/L,底物含水率为96%~98%。系统超负荷运行后,产气量和pH下降,VFA浓度上升,碱度、氨氮、含水率基本保持稳定。 相似文献