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51.
络合-超滤耦合工艺去除水中镍离子的研究 总被引:1,自引:1,他引:0
以聚丙烯酸钠(PAANa)和聚乙烯亚胺(PEI)作为络合剂,将其与镍离子络合后的溶液转移至超滤杯中,在0.1 MPa压力下通过聚醚砜超滤膜进行分离,研究pH值和络合剂/Ni2+装载质量比(L)对Ni2+去除率的影响,并根据朗缪尔等温模型拟合络合反应平衡常数.同时研究超滤时间对膜通量和Ni2+去除率的影响.结果表明,选用PAANa为络合剂,在pH值为8、L=5时,Ni2+的去除率达到最大值99.5%.PEI为络合剂时,Ni2+去除率在pH值为7、L为5时达到最大值93.0%.不同pH值条件下拟合得到的络合平衡常数表明,pH为7时最有利于络合反应.另外,单个络合剂单体所能结合的Ni2+个数随着pH值的升高而增大.研究结果还表明,在长达12 h的超滤时间内,PAANa为络合剂时,膜通量的衰减<10%;PEI为络合剂时,膜通量基本保持不变;Ni2+的去除率都基本保持恒定.因此,在合适条件下,络合-超滤耦合工艺能有效去除水中的镍离子. 相似文献
52.
Oxidation inhibition of sulfite in dual alkali FGD system 总被引:1,自引:0,他引:1
MO Jian-song WU Zhong-biao CHENG Chang-jie GUAN Bao-hong ZHAO Wei-rong 《环境科学学报(英文版)》2007,19(2):226-231
A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization (FGD) system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4).55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results. 相似文献
53.
Ce(Ⅲ)对UV-B辐射胁迫下大豆幼苗光化学反应的影响 总被引:2,自引:0,他引:2
用水培法研究Ce(Ⅲ)对UV-B辐射胁迫下大豆幼苗光化学反应的影响.结果表明, 20 mg·L-1 CeCl3使大豆幼苗净光合速率(Pn)、Hill反应、Mg2+-ATPase活性与光合磷酸化活力4项指标较对照提高23.2%~14.3%; 有效抑制UV-B辐射(T1=0.15 W·m-2和T2=0.45 W·m-2)胁迫下4项指标下降, 4项指标降幅[Ce(Ⅲ)+T1为36.6%~15.9%,Ce(Ⅲ)+T2为65.6%~33.2%]小于对应的UV-B辐射组(T1为50.9%~23.3%,T2为77.3%~51.4%). 动态变化显示, Ce(Ⅲ)减缓了胁迫期4项指标的下降趋势,促进了恢复期4项指标上升幅度. 说明Ce(Ⅲ)通过减轻UV-B辐射对大豆幼苗光化学反应的伤害, 遏制UV-B辐射胁迫下大豆幼苗Pn下降. 相似文献
54.
The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3. 相似文献
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57.
随着印染工艺不断更新,大量化学分子结构复杂的化工染料应用到印染行业,使得常规的水处理工艺难以降解印染废水中的染料。本文以活性黑(RB5)染料为研究对象,采用液相高压放电产生强氧化性自由基来降解染料废水,考察反应时间、初始浓度和气体流量对RB5降解的影响,研究结果表明:在外部功率相同的情况下,浓度高染料其降解率相对较低;通入氧气量增加,产生的活性自由基和活性物质数量也增加,RB5的降解率也增大,但气流量不宜过大;高压放电产生的各种活性物质容易破坏染料发色基团的分子链,使其脱色。 相似文献
58.
Catalytic oxidation is widely used in pollution control technology to remove volatile organic compounds. In this study, Pd/ZSM-5 catalysts with different Pd contents and acidic sites were prepared via the impregnation method. All the catalysts were characterized by means of N2 adsorption- desorption, X-ray fluorescence (XRF), HE temperature programmed reduction (H2-TPR), and NH3 temperature programmed desorption (NH3-TPD). Their catalytic performance was investigated in the oxidation of butyl acetate experiments. The by-products of the reaction were collected in thermal desorption tubes and identified by gas chromatography/mass spectrometry. It was found that the increase of Pd content slightly changed the catalytic activity of butyl acetate oxidation according to the yield of CO2 achieved at 90%, but decreased the cracking by-products, whereas the enhancement of strong acidity over Pd-based catalysts enriched the by-product species. The butyl acetate oxidation process involves a series of reaction steps including protolysis, dehydrogenation, dehydration, cracking, and isomerization. Generally, butyl acetate was cracked to acetic acid and 2- methylpropene and the latter was an intermediate of the other by-products, and the oxidation routes of typical by-products were proposed. Trace amounts of 3-methylpentane, hexane, 2-methylpentane, pentane, and 2-methylbutane originated from iso4merization and protolysis reactions. 相似文献
59.
Fe2+和Fe3+对厌氧氨氧化污泥活性的影响 总被引:3,自引:2,他引:1
通过接种厌氧氨氧化污泥研究了Fe离子浓度及价态变化对厌氧氨氧化污泥活性的影响.短期浓度影响结果表明,当进水铁离子浓度由0升高到5 mg·L-1时,厌氧氨氧化污泥活性因受刺激而逐渐增强;当进水铁离子浓度大于5 mg·L-1时,因厌氧氨氧化反应产碱,铁离子形成氢氧化物沉淀,生物活性未受到影响.不同价态铁离子浓度变化对厌氧氨氧化污泥活性的影响无明显区别.长期价态影响结果表明,经过71个周期培养,含Fe2+进水的厌氧氨氧化反应器R1脱氮效能(以氮计)由0.28 kg·(m3·d)-1升高到0.65 kg·(m3·d)-1,是含Fe3+进水反应器R2的1.28倍.因此Fe2+更适合厌氧氨氧化菌生长的需求.实验结果进一步表明,Fe3+易导致厌氧氨氧化反应器R2内氨氮过量转化,亚硝氮与氨氮转化比(1.17)明显低于含Fe2+进水的反应器R1内亚硝氮与氨氮转化比(1.24). 相似文献
60.
双组分VOCs的催化氧化及动力学分析 总被引:1,自引:1,他引:0
考察了微波加热与管式炉加热下挥发性有机化合物(VOCs)甲苯与氯苯的催化氧化性能,并对双组分VOCs的反应动力学进行了分析.结果表明,VOCs的竞争吸附使得双组分中甲苯和氯苯的转化率比单组分降低3%~12%;微波的"热点效应"与"非热效应"使得VOCs转化效率明显优于管式炉加热,尤其是氯苯的转化率提高了31%~38%;微波加热降低了氧化反应温度和处理能耗.动力学分析表明,微波加热下甲苯和氯苯的反应活化能比管式炉加热下减少了2146 J·mol-1和1450J·mol-1,微波加热下氯苯的化学反应速率常数是管式炉加热的35倍,甲苯的反应速率常数提高了6倍. 相似文献