全文获取类型
收费全文 | 830篇 |
免费 | 114篇 |
国内免费 | 675篇 |
专业分类
安全科学 | 79篇 |
废物处理 | 75篇 |
环保管理 | 63篇 |
综合类 | 986篇 |
基础理论 | 69篇 |
污染及防治 | 340篇 |
评价与监测 | 3篇 |
社会与环境 | 4篇 |
出版年
2024年 | 1篇 |
2023年 | 8篇 |
2022年 | 16篇 |
2021年 | 20篇 |
2020年 | 29篇 |
2019年 | 41篇 |
2018年 | 37篇 |
2017年 | 31篇 |
2016年 | 52篇 |
2015年 | 62篇 |
2014年 | 88篇 |
2013年 | 88篇 |
2012年 | 108篇 |
2011年 | 94篇 |
2010年 | 68篇 |
2009年 | 95篇 |
2008年 | 73篇 |
2007年 | 138篇 |
2006年 | 103篇 |
2005年 | 82篇 |
2004年 | 71篇 |
2003年 | 62篇 |
2002年 | 50篇 |
2001年 | 53篇 |
2000年 | 40篇 |
1999年 | 23篇 |
1998年 | 16篇 |
1997年 | 20篇 |
1996年 | 14篇 |
1995年 | 10篇 |
1994年 | 10篇 |
1993年 | 10篇 |
1992年 | 2篇 |
1991年 | 2篇 |
1990年 | 1篇 |
1986年 | 1篇 |
排序方式: 共有1619条查询结果,搜索用时 656 毫秒
471.
以实际生活污水为对象,研究了反硝化聚磷菌(DPB)的驯化培养以及A2N双污泥反硝化除磷系统的快速启动.采用先独立培养反硝化聚磷菌和好氧硝化生物膜再连续运行的方式成功地快速启动了A2N系统.采用污水处理厂除磷工艺中的活性污泥为种泥,在SBR系统中以先A/O(厌氧/好氧)后A/A(厌氧/缺氧)的方式运行,32 d成功地使反硝化聚磷菌成为优势菌属.在SBR反应器中,采用硝化效果较好的活性污泥为种泥,好氧硝化生物膜30 d挂膜成功,氨氮去除率稳定在99%以上.然后,A2N系统连续运行,11 d后系统反硝化除磷效果进入稳定状态,出水氨氮和正磷酸盐浓度均为0,硝态氮为10.26 mg/L ,出水COD为19.56 mg/L ,COD、氨氮、总氮和磷去除率分别为91%、100%、77%和100%,说明A2N系统具有很好的脱氮除磷效果,认为系统启动成功. 相似文献
472.
为克服难降解废水厌氧微生物反应器启动初期生物易流失和启动过程缓慢的缺点,将厌氧絮状污泥进行固定化包埋作为厌氧反应器的接种污泥处理有毒难降解的PTA废水,同时考察固定化细菌在厌氧反应器启动过程中的变化特性.结果表明,经过136 d的运行,反应器在COD有机负荷为3 kg.(m3.d)-1,水力停留时间为3~4 d的运行条件下,PTA废水的COD去除率可以达到75%~85%,且系统具有比较好的稳定性和生物量保持能力.另一方面,胞外聚合物(EPS)的变化、产甲烷菌DNA特异性扩增和包埋颗粒的扫描电镜观察结果表明,虽然包埋载体在一定程度上限制了传质速度,但包埋颗粒中的厌氧微生物在微生物相和数量上都仍有显著的变化和增长. 相似文献
473.
十二烷基磺酸钠(SDS)改性蒙脱石对Cu~(2+)、Cd~(2+)的吸附研究 总被引:10,自引:3,他引:7
以阴离子表面活性剂(十二烷基磺酸钠,SDS)为改性剂制备了有机蒙脱石,研究其对Cu2+、Cd2+的吸附行为,并用XRD、FTIR、SEM、XPS对有机蒙脱石进行表征.实验结果表明,有机蒙脱石对Cu2+、Cd2+的吸附基本上在20min内达到平衡,并随pH增大(1.0~7.0),吸附量增加,最佳pH约为6.0.有机蒙脱石对Cu2+、Cd2+的吸附等温线更符合Langmuir等温吸附方程,SDS改性蒙脱石对Cu2+、Cd2+的最大吸附量较纯蒙脱石分别增加15.7%、15.5%.XRD、FTIR、SEM、XPS及碳含量分析结果显示,SDS主要分布在蒙脱石表面且相对稳定,少量嵌入层间,有机蒙脱石对Cu2+、Cd2+的吸附机制为配位吸附和离子交换. 相似文献
474.
光催化技术因其较高的催化活性和低廉的价格已经被水处理业内广泛采用.但是粉末催化剂的明显缺点制约了其工业化应用,因此固定化光催化技术应运而生。通过收集国内外资料.对于光催化固定技术应用的两个关键因素——固定方法和适用的反应器的发展进行了介绍。当固定的同时催化剂活性不大幅下降.且采用适合于该种载体的反应器,固定化光催化技术在水处理领域有着广阔的应用前景。 相似文献
475.
F/M对ASBR中基质的吸收、储存和利用影响 总被引:1,自引:0,他引:1
研究了不同F/M(COD/VSS)下以葡萄糖为基质时厌氧序批式反应器(ASBR)中的微生物代谢规律.结果表明,在序批操作条件下,水解产酸菌对葡萄糖的代谢存在2条并列的途径,即直接代谢为VFA和首先转化为胞内储存物糖原,然后糖原再被转化为VFA.前者约占进水COD的34%~38%,而后者则高达41%~46%.F/M越高,糖原的储存量越大,当F/M分别为0.27、 0.20和0.14时,单位质量污泥糖原的最大储存量分别为116.8、 81.1和62.4 mg/g.糖原的储存减缓了VFA的积累,为ASBR反应器的高效和正常运行创造了条件. 相似文献
476.
A/A系统反硝化除磷的强化及其稳定性研究 总被引:3,自引:0,他引:3
利用厌氧/缺氧(A/A)SBR,试验研究了选择和富集反硝化除磷菌(DPB)的条件.结果表明,采用电子供体和电子受体充分分开的两段进水方式运行,当厌氧段进水COD与缺氧段投加硝酸盐质量浓度为300 mg.L-1、50 mg.L-1,pH值约为7.0时,DPB可快速成为系统中的优势菌群,系统可达到良好的反硝化聚磷效果;将前述系统改变为一段进水方式运行后,系统仍具有良好的反硝化聚磷效果.在进水磷浓度同为20 mg.L-1下,在缺氧段投加磷的运行方式比在厌氧段投加磷的运行方式更能提高系统的除磷能力. 相似文献
477.
Attempts have been made to generate euchlorine gas by chlorate-chloride process and to utilize it further to clean up SO2 and NOx from the flue gas in a lab scale bubbling reactor.Preliminary experiments were carried out to determine the gas and liquid phase mass transfer coefficients and their correlation equations have been established.Simultaneous removal of SO2 and NOx from the simulated flue gas using aqueous euchlorine scrubbing solution has been investigated.Euchlorine oxidized NO into NO2 completely and the later subsequently absorbed into the scrubbing solution in the form of nitrate.SO2 removal efficiency of around 100% and NOx removal efficiency of around 72 % were achieved under optimized conditions.Mass balance has been confirmed by analyzing the sulfate, nitrate, euchlorine and chloride ion using ion chromatograph/auto-titrator and comparing it with their corresponding calculated values. 相似文献
478.
Nitrogen removal via nitrite from municipal landfill leachate 总被引:2,自引:0,他引:2
A system consisting of a two-stage up-flow anaerobic sludge blanket (UASB), an anoxic/aerobic (A/O) reactor and a sequencing
batch reactor (SBR), was used to treat landfill leachate. During operation, denitrification and methanogenesis took place simultaneously
in the first stage UASB, and the e uent chemical oxygen demand (COD) was further removed in the second stage UASB. Then the
denitrification of nitrite and nitrate in the returned sludge by using the residual COD was accomplished in the A/O reactor, and ammonia
was removed via nitrite in it. Last but not least, the residual ammonia was removed in SBR as well as nitrite and nitrate which were
produced by nitrification. The results over 120 d (60 d for phase I and 60 d for phase II) were as follows: when the total nitrogen
(TN) concentration of influent leachate was about 2500 mg/L and the ammonia nitrogen concentration was about 2000 mg/L, the shortcut
nitrification with 85%–90% nitrite accumulation was achieved stably in the A/O reactor. The TN and ammonia nitrogen removal
e ciencies of the system were 98% and 97%, respectively. The residual ammonia, nitrite and nitrate produced during nitrification in
the A/O reactor could be washed out almost completely in SBR. The TN and ammonia nitrogen concentrations of final e uent were
about 39 mg/L and 12 mg/L, respectively. 相似文献
479.
The present study evaluated the potential of white-rot fungal strain Coriolus versicolor to decolorize five structurally di erent dyes
in sequential batch reactors under optimized conditions. The experiments were run continuously for seven cycles of 8 d each. High
decolorizing activity was observed even during the repeated reuse of the fungus, especially when the old medium was replaced with
fresh medium after every cycle. Biodegradation was the dominating factor as the fungus was able to produce the enzyme laccase mainly,
to mineralize synthetic dyes. The nutrients and composition of the medium played important roles in sustaining the decolorisation
potential of the fungus. Corncob was found be an easy and cheap substitute for carbon source for the fungus. Glucose consumption by
the fungus was in accordance to its decolorisation activity and chemical oxygen demand (COD) reduction. 相似文献
480.
Polyaluminum chloride was synthesized with a membrane reactor, and the process characteristics, membrane fouling and cleaning were investigated. 相似文献