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81.
采用厌氧酸化+二级光合细菌(PSB)流化床的组合工艺对植物压榨发酵废水进行降解实验,一级流化床(PSB1)中填料为轻质多孔炭渣,二级流化床(PSB2)为活性炭,扰动方式分别采用机械流化和机械气动组合流化,稳定运行40d。结果表明,进水酸化12h后CODCr由80000~120000mg/L降至63000~95000mg/L,进而由系统出水回流稀释至8000~12000mg/L,进入二级流化床反应器,PSB1白天厌氧光照、夜间微好氧,PSB2白天微好氧、夜间好氧,停留48h,CODCr降至295.8~384mg/L,稳定实现96.2%以上的CODCr去除率,TN去除率为71.3%。 相似文献
82.
Biological pretreatment of Yellow River water 总被引:1,自引:0,他引:1
XIE Shu-guang TANG Xiao-yan WU Wei-zhong WEN Dong-hui WANG Zhan-sheng 《环境科学学报(英文版)》2005,17(4):557-561
Bio-ceramic filter(BF) and moving-bed biofilm reactor(MBBR) were used for biological pretreatment of Yellow River water in this study. The BF only had slight advantage over MBBR for TOC and ammonia removal. However, like UV254, the average removal rate of THMFP in the BF was much higher than that in the MBBR. UV254 removal did not show obvious correlation with trihalomethane formation potential(THMFP) removal. Hexachlorocyclohexane could be effectively removed in both BF and MBBR. As for diatom and cyanobateria removal the MBBR had better performance than the BF, which was contrary to the average chlorophyll-a(Chl-a) removal rate. The proposal was made in this study that biological flocculation and sedimentation of sloughed biofilm should play a more important role on algae removal in the MBBR than in the BF. The BF and MBBR could effectively remove microcystins. Moreover, MBBR could be a promising technology for biological pretreatment. 相似文献
83.
IntroductionAs a promising advanced oxidation technology for watertreatment ,catalytic ozonation has received great attentionforthe efficient degradation of organic compoundsinrecent years(Legube , 1999) . Some studies showed that homogeneousand heterogen… 相似文献
84.
含硫酸盐高浓度有机废水预处理的试验研究 总被引:1,自引:0,他引:1
在含硫酸盐高浓度有机废水浸泡铁刨花的静态试验的基础上,进行了“铁床”处理高浓度糖厂生产废水的动态试验。通过稳定工况之后,“铁床”CODcr平均下降41.3%,SO4^2-平均下降56.2%,有利于后续厌氧生物处理,并达到以废治废的目的。 相似文献
85.
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87.
《环境科学学报(英文版)》2023,35(4):396-407
Based on the experimental and theoretical methods, the NO selective catalytic oxidation process was proposed. The experimental results indicated that lattice oxygen was the active site for NO oxide over the -MnO2(110) surface. In the theoretical study, DFT (density functional theory) and periodic slab modeling were performed on an -MnO2(110) surface, and two possible NO oxidation mechanisms over the surface were proposed. The non-defect -MnO2(110) surface showed the highest stability, and the surface Os (the second layer oxygen atoms) position was the most active and stable site. O2 molecule enhanced the joint adsorption process of two NO molecules. The reaction process, including O2 dissociation and O=N-O-O-N=O formation, was calculated to carry out the NO catalytic oxidation mechanism over -MnO2(110). The results showed that NO oxidation over the -MnO2(110) surface exhibited the greatest possibility following the route of O=N-O-O-N=O formation. Meanwhile, the formation of O=N-O-O-N=O was the rate-determining step. 相似文献
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89.
IntroductionChlorinatedorganiccompoundshavebeenusedonalargescaleinthechemical,petrochemical,andelectronicindustries.Inrecentyears ,worldwideattentionhasbeengiventotheenvironmentalandhealthimpactofthemasaclassofcontaminants .Severalareknowntocauseozonedepletion ,whileothersproduceadverseeffectsonthehumancentralnervoussystemandhavebeenlinkedtodiseasessuchascancer.Almostallofthechlorinatedaromaticcompoundsaretoxicandthermallystable .Oncereleasedintoenvironment,theywillaccumulateinthesurroundings… 相似文献
90.
The preparation of immobilizing-catalysts for decomposing ozone by using dipping method was studied. XRD, XPS and TEM were used to characterize the catalysts. The three kinds of catalysts were selected preferentially, and their catalytic activities were investigated. The results showed that the catalyst with activated carbon dipping acetate( active components are Mn:Cu = 3:2, active component proportion in catalyst is 15%, calcination temperature is 200℃ ) has the best catalytic activity for ozone decomposing. One gram of catalyst can decompose 17.6g ozone at initial ozone concentration of 2.5g/m^3 and the residence time in reactor of 0.1s. The experimental results also indicated that humidity of reaction system had negative effect on catalytic activity. 相似文献