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991.
992.
采用本文(Ⅰ)报建立的LPG(liquefied petroleum gas)埋地储罐泄漏渗流扩散多相混合数值模型分别对气态和液态LPG在含水量不同的砂池中渗流扩散到外界环境的过程进行数值模拟,得到砂池中的流场、浓度场和LPG渗透到外界环境的质量流速。在数值模拟的基础上,对LPG气相、液相两种状态渗流扩散在砂池出口处LPG流速随时间的变化过程进行分析,总结出LPG渗透到外界的流速变化规律。模拟结果表明重力和出口位置对渗流扩散的方向影响很大,压力驱动是LPG渗流的重要影响因素;流体进出口处是流体流动活跃区域,非达西效应明显。数值模拟结果与LPG气体渗流扩散试验数据吻合较好,验证了理论模型和数值模拟的可靠性。 相似文献
993.
采用离子交换和配位合成方法,通过配位链将配体引入金属蒙脱土层间,制备了Co-Phen-HAA/MMT负载型催化材料,采用IR,XRD、SEM的现代分析测试技术,分析了催化材料的结构,XRD显示蒙脱土层间距增大0.577nm,表明配体进入金属蒙脱土的片层间;在分子氧的氧化作用下,考察了反应温度、时间、溶剂等因素对苯乙烯环氧化反应的影响.实验结果表明,最佳反应温度82℃,反应时间8 h,苯乙烯的转化率为93.9%,反应活化能41.35 kJ/mol. 相似文献
994.
995.
PTFE-F-PbO2 电极在H2SO4溶液中的析氧行为 总被引:1,自引:0,他引:1
F-PbO2 electrode and polytetrafluoroethylene (PTFE) doped F-PbO2 electrode (PTFE-F-PbO2) were prepared on a plexiglas sheet substrate by a series of procedure including chemical and electrochemical depositions. The electrochemical activities of these two electrodes for oxygen evolution (OE) reaction were examined by electrochemical tests. In comparison with F-PbO2, PTFE-F-PbO2 electrode exhibited larger active surface area and higher oxygen vacancy deficiency, which resulted in its higher electrocatalytic activity for OE. In addition, both exchange current density and activation energy of the electrodes for OE were calculated in terms of active surface area. The values of exchange current density and activation energy in 0.5 mol·L^-1 H2SO4 aqueous solution were 1.125×10^ -3 mA·cm^-2 and 18.62 kJ·mol^-1 for PTFE-F-PbO2, and 8.384×10^-4 mA·cm^- 2 and 28.98 kJ·mol^-1 for F-PbO2, respectively. Because these values are calculated on the basis of the active surface areas of the electrodes, the enhanced activity of PTFE-F-PbO2 can be attributed to an increase in oxygen vacancy deficiency of PbO2 due to doping by PTFE. The influence of PTFE adulteration on the activity of PbO2 film electrode for OE was investigated in detail in this study. 相似文献
996.
浅析相关参数对气流床粉煤加压气化的影响 总被引:2,自引:0,他引:2
介绍了气流床粉煤加压气化的原理及我国粉煤加压气化技术的研发过程、试车情况,分析了粉煤粒度、密相输送氮气量、氧煤比、蒸汽煤比、气化压力及气化炉温度等因素对粉煤加压气化的影响,为我国粉煤加压气化技术的产业化提供参考。 相似文献
997.
HDPE/PA6/MRP共混物阻燃性能研究 总被引:1,自引:1,他引:1
用微胶囊化红磷(MRP)作为阻燃剂,利用双螺杆挤出机制备了阻燃HDPE/MRP共混物,并首次使用点燃氧指数和燃烧氧指数来表征它们的阻燃性能。结果表明:添加少量的PA6可提高HDPE/MRP复合材料的阻燃效果,固定PA6与MRP的添加总量为15%,且在HDPE∶PA6∶MRP=85∶4∶11时,其极限氧指数最大,为22.1%;在固定MRP含量的情况下,随PA6含量的增加,HDPE/PA6/MRP复合材料的阻燃性增强。 相似文献
998.
999.
The results of an experimental study on electrochemical disinfection of water are presented. Attention was paid to the behaviour
of chlorine compounds during electrolysis of water containing chlorides, with particular regard to the selectivity of the
process towards the production of oxidising agents. Two reactor configurations were tested: a stirred tank cell and a filter
press cell inserted in a hydraulic circuit. Both cells were equipped with boron doped diamond (BDD) anodes. Experiments were
performed in batch and continuous mode. The effect of such operating parameters, current density, stirring rate or recirculating
flow rate, on the behaviour of the process was investigated. The results at BDD anodes show that low current densities and
perfect mixing of the system should be adopted in order to obtain high values of the concentration of oxidising agents avoiding
the formation of such undesired by-products as chlorite, chlorate and perchlorate ions. Runs were also performed in which
BDD was substituted by a commercial (Ti/RuO2) DSA anode and the results obtained with the two materials are compared. 相似文献
1000.
A. Katsaounis 《Journal of Applied Electrochemistry》2008,38(8):1097-1110
The origin of the effect of non-faradaic electrochemical modification of catalytic activity (NEMCA) or Electrochemical Promotion
was investigated via temperature-programmed-desorption (TPD) of oxygen, from polycrystalline Pd films deposited on 8 mol%Y2O3–stabilized–ZrO2 (YSZ), an O2− conductor, under high-vacuum conditions and temperatures between 50 and 250 °C. Oxygen was adsorbed both via the gas phase
and electrochemically, as O2−, via electrical current application between the Pd catalyst film and a Au counter electrode. Gaseous oxygen adsorption gives
two adsorbed atomic oxygen species desorbing at about 300 °C (state β1) and 340–500 °C (state β2). The creation of the low temperature peak is favored at high exposure times (exposure >1 kL) and low adsorption temperatures
(Tads < 200 °C). The decrease of the open circuit potential (or catalyst work function) during the adsorption at high exposure times,
indicates the formation of subsurface oxygen species which desorbs at higher temperatures (above 450 °C). The desorption peak
of this subsurface oxygen is not clear due to the wide peaks of the TPD spectra. The TPD spectra after electrochemical O2− pumping to the Pd catalyst film show two peaks (at 350 and 430 °C) corresponding to spillover Oads and
according to the reaction:
The formation of the spillover oxygen species is an intermediate stage before the formation of the atomic adsorbed oxygen, Oads. Mixed gaseous and electrochemical adsorption was carried out in order to simulate the Electrochemical Promotion conditions.
The initial surface coverage with oxygen from the gas phase plays a very important role on the high or low effect of polarization.
In general mixed adsorption leads to much higher oxygen coverages compare with that observed either under gaseous or electrochemical
adsorption. The binding strength of the atomic adsorbed oxygen (state β2) was investigated as a function of applied potential. It was found that the binding energy decreases linearly with increasing
catalyst potential and work function. Similar behavior has been observed for oxygen adsorption on Pt, Ag and Au deposited
on YSZ in previous studies. 相似文献