全文获取类型
收费全文 | 78篇 |
免费 | 18篇 |
国内免费 | 62篇 |
专业分类
安全科学 | 9篇 |
废物处理 | 12篇 |
环保管理 | 6篇 |
综合类 | 85篇 |
基础理论 | 10篇 |
污染及防治 | 32篇 |
评价与监测 | 1篇 |
社会与环境 | 1篇 |
灾害及防治 | 2篇 |
出版年
2023年 | 2篇 |
2022年 | 2篇 |
2021年 | 3篇 |
2020年 | 5篇 |
2019年 | 4篇 |
2018年 | 2篇 |
2017年 | 2篇 |
2016年 | 7篇 |
2015年 | 5篇 |
2014年 | 7篇 |
2013年 | 13篇 |
2012年 | 18篇 |
2011年 | 10篇 |
2010年 | 6篇 |
2009年 | 4篇 |
2008年 | 7篇 |
2007年 | 6篇 |
2006年 | 10篇 |
2005年 | 5篇 |
2004年 | 9篇 |
2003年 | 9篇 |
2002年 | 7篇 |
2001年 | 5篇 |
2000年 | 3篇 |
1999年 | 2篇 |
1998年 | 1篇 |
1997年 | 2篇 |
1990年 | 2篇 |
排序方式: 共有158条查询结果,搜索用时 31 毫秒
91.
改性蜂窝陶瓷催化臭氧化降解水中微量硝基苯 总被引:5,自引:4,他引:5
以硝基苯为目标反应物,对改性蜂窝陶瓷、蜂窝陶瓷催化臭氧化和单独臭氧氧化去除水中微量有机污染物的效果进行了比较.发现与单独臭氧氧化相比,改性蜂窝陶瓷和蜂窝陶瓷催化臭氧化工艺可以提高水中硝基苯的去除率,分别为38.35%和15.46%.在本次实验条件下,随着改性蜂窝陶瓷催化剂的用量增加到5份,硝基苯的降解效率上升了30.55%;3种工艺对硝基苯的去除率都随着温度的升高而显著增加,随着pH值的升高越来越大,在pH=10.00左右时,臭氧/改性蜂窝陶瓷联用对硝基苯的去除优势消失;臭氧/改性蜂窝陶瓷催化氧化对硝基苯的去除遵循自由基机理;催化剂对硝基苯的吸附很小,对去除几乎没有影响;对于3个体系,将总量相同的O3多次投加可以获得明显优于一次性投加的去除效果;改性蜂窝陶瓷催化剂的使用寿命较长. 相似文献
92.
93.
94.
95.
陶瓷微滤膜深度处理炼油污水二级出水的效能及膜清洗研究 总被引:1,自引:0,他引:1
建立了炼油污水二级生化出水的陶瓷微滤膜深度处理系统,当膜孔径为0.2 mm、操作压力为0.12 MPa时,该系统对CODCr和SS的去除率分别达到79%以上和87%以上,出水达到生活杂用水水质标准.自动高压气体(0.5 MPa)反冲洗可有效地提高膜通量;反应系统中加入Al2(SO4)3絮凝剂(50 mg/(L d))与不加入时相比,可使膜通量提高近80%;采用NaOH、HNO3、NaClO溶液和家用洗涤灵进行化学清洗时,HNO3和NaClO先后使用的复合清洗方法效率最高. 相似文献
96.
97.
98.
Recently, various solid wastes from industry such as glass waste, fly ash, sewage sludge and slag have been recycled into various value-added products such as ceramic tile. The conventional solutions of dumping the wastes in landfills or incineration, including in Malaysia are getting obsolete as the annual huge amount of the solid wastes would boost-up disposal cost and may cause permanent damage to the flora and fauna. This recent waste recycling approach is much better and greener as it can resolve problems associated with over-limit storage of industrial wastes and reduce exploration of natural resources for ceramic tile to continuously sustain the nature. Therefore, in this project, an attempt was made to recycle electric arc furnace (EAF) slag waste, obtained from Malaysia’s steel making industry, into ceramic tile via conventional powder compaction method. The research work was divided into two stages. The first stage was to evaluate the suitability of EAF slag in ceramic tile by varying weight percentage of EAF slag (40 wt.%, 50 wt.% and 60 wt.%) and ball clay (40 wt.%, 50 wt.% and 60 wt.%), with no addition of silica and potash feldspar. In the second stage, the weight percentage of EAF slag was fixed at 40 wt.% and the percentage of ball clay (30 wt.% and 40 wt.%), feldspar (10 wt.% and 20 wt.%) and silica (10 wt.% and 20 wt.%) added was varied accordingly. Results obtained show that as weight percentage of EAF slag increased up to 60 wt.%, the percentage of apparent porosity and water absorption also rose, with a reduction in tile flexural strength and increased porosity. On the other hand, limiting the weight percentage of EAF slag to 40 wt.% while increasing the weight percentage of ball clay led to a higher total percentage of anorthite and wollastonite minerals, resulting in higher flexural strength. It was found that introduction of silica and feldspar further improved the flexural strength due to optimization of densification process. The highest flexural strength, lowest apparent porosity and water absorption of EAF slag based tile was attained at the composition of 40 wt.% EAF slag – 30 wt.% ball clay – 10 wt.% feldspar – 20 wt.% silica. The properties of ceramic tile made with EAF slag waste (up to 40 wt.%), especially flexural strength are comparable to those of commercial ceramic tile and are, therefore, suitable as high flexural strength and heavy-duty green ceramic floor tile. Continuous development is currently underway to improve the properties of tile so that this recycling approach could be one of the potential effective, efficient and sustainable solutions in sustaining our nature. 相似文献
99.
臭氧氧化对陶瓷膜超滤工艺降低饮用水中浊度的影响 总被引:3,自引:1,他引:2
利用臭氧陶瓷膜超滤集成工艺,研究了臭氧对陶瓷膜超滤工艺处理不同浊度原水的影响.实验用陶瓷膜平均孔径为100 nm.结果表明,与不投加臭氧的情况相比,投加3 mg·L-1臭氧可将浊度为14、52、108和510 NTU原水的膜通量提高18.2%~104.9%,投加5 mg·L-1臭氧可将此值提高至21.7% ~116.3%,而投加1~2 mg·L-1臭氧对膜通量的改善不明显.投加5mg·L-1臭氧可将CODMn的去除率提高至28.7% ~46.9%,投加1~3 mg·L-1臭氧对CODMn的去除率无显著影响,膜出水有机物浓度有所升高.臭氧氧化后原水中小分子量有机物增多,降低了膜的有机物污染程度,有利于膜通量改善.集成工艺出水中2~3 μm颗粒物数量为10 ~36个·mL-1.臭氧氧化导致陶瓷膜过滤初期出水中颗粒物数量略微升高.本研究对于水中颗粒物通过陶瓷超滤膜孔的探讨,以及改善膜对颗粒物的去除具有重要的指导意义. 相似文献
100.