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931.
论述了尿素磷酸盐作为反刍动物新型饲料添加剂的饲效及国内外开发利用情况,对其性质和物性数据做了阐述;探索了生产工艺路线和最佳工艺条件,介绍了饲用效果。  相似文献   
932.
简要地介绍了化学清洗的分类及清洗方案的制定以实例论述了化学清洗技术在工厂的应用效果,实践说明了化学清洗技术是一项非常有效的企业节能增效新技术  相似文献   
933.
The reaction kinetics of alloys based on magnesium are known to be greatly improved by the partial substitution of Mg with rare earths and transition metals,particularly Ni.The enhanced superficial hydrogen dissociation rate,the weakened Mg-H bond and the lower activation energy following element replacement are thought to be related to the better performance.The experimental alloys Ce5Mg95-xNix(x=5,10,15)were smelted by the vacuum induction melting.The phase transformation and structural evolution of experimental alloys before and after reaction with hydrogen were char-acterized by X-ray diffraction,scanning electron microscopy and transmission electron microscopy.The cast specimens contain CeMg12,Mg and Mg2Ni phases,and the increase in Ni content results in an obvious growth of Mg2Ni phase.The isothermal and non-isothermal hydrogenation and dehydrogenation kinetics of the experimental specimens were investi-gated using the Sievert apparatus,differential scanning calorimetry and thermal gravimetric analyzer.The activation energy may be calculated using the Arrhenius and Kissinger equations.The experimental alloys have been shown to have good activation properties,with a reversible hydriding and dehydriding capacities of around 5.0 wt.%in the first cycle.The initial dehydrogenation temperature of MgH2 decreases from 557.5 to 537.7 K with changing Ni content from 5 to 15 at.%.The dehydrogenation activation energy also reduces from 77.09 to 62.96 kJ/mol,which explains the improved hydrogen storage performance caused by Ni substitution.It can be shown that the impact of Ni on the decomposition enthalpy of MgH2 is quite modest,with the absolute enthalpy(ΔHr)only decreasing from 78.48 to 76.15 kJ/mol.  相似文献   
934.
    
The potential of CO2 utilization through its injection into blast furnace (BF) tuyeres is studied using the 1D steady-state zonal model. Scenarios with the injection of CO2, hydrogen, and their co-injection at various H2/CO2 mass ratios are analyzed. The impacts on factors affecting vertical temperature patterns and the position of the cohesive zone in the BF are identified. A life cycle assessment for several scenarios with various carbon emissions intensities of hydrogen production, carbon capture, and grid electricity generation is performed. Injection of CO2 without the addition of hydrogen increases the coke rate, reduces productivity, and increases direct CO2 emissions; however, thanks to producing top gas with higher calorific value, injection of CO2 may reduce the global warming potential (GWP) if the electric grid carbon intensity is above 654 kg-CO2 kWh−1, while carbon capture is powered by green electricity. Although the injection of hydrogen alone would result in a more substantial reduction of GWP from the baseline than the injection of H2/CO2 mix at any mass ratio, considering the identified impacts on heat exchange and the position of the cohesive zone in the BF, co-injection might be an enabling solution for the adoption of hydrogen injection.  相似文献   
935.
    
Owing to the complexity of converter reactions and the inevitable fluctuations of raw materials, developing a universal smelting strategy suitable for all converter conditions is challenging. Therefore, this study introduces a multimode smelting strategy based on a novel classification method to categorize molten iron. In this method, the molten iron is classified into four regions based on the comprehensive effects of Si and P contents. Specific smelting strategies are recommended for the molten iron in each region. These strategies include adjustments to slag basicity, charging schemes, and the blowing mode of the lance. These multimode smelting strategies are implemented in actual production. The results indicate satisfactory optimization of production processes, including stable production, cost reduction, and increased efficiency. Consequently, the dephosphorization rate increases by 1.22%, the lime consumption per ton of steel decreases by 2.41 kg t−1, and the average basicity of steel slag decreases by 0.21. This strategy provides preliminary guidance before the initiation of the smelting process to improve efficiency, reduce consumption, and standardize the operations.  相似文献   
936.
    
In this article, oxidation processes of Ag-Bi-Sb-based phases were investigated. Synthesized AgBiS2 and AgSbS2-Sb2S3-Sb samples were thermally analyzed in synthetic air by applying the simultaneous DSC-TGA analysis technique. The oxidation processes at PO?=0.2 atm and T<1173 K were observed to take place in many-step sequence of various reactions with an overall reaction 2AgMeS2 + 5.5O2(g) ? 2Ag + Me2O3 + 4SO2(g), where Me=(Bi,Sb). Oxidations of AgBiS2, Sb2S3, and AgSbS2 were observed to begin above 549±2K, 610±2K, and 733±2K, respectively. Furthermore, oxidation processes of AgBi3S5 and Ag3SbS3 were estimated, and thermodynamic functions for the overall oxidation reactions were calculated and discussed.  相似文献   
937.
    
The extraction of precious metals from tellurides by cyanidation is more difficult than when they are in their native form, nevertheless the reason for their refractory nature has not been adequately supported. In this study, the mechanism of the cyanidation kinetics of silver telluride (Ag2Te) was investigated. For this purpose, cyanidation experiments were carried out to: (1) study the difference between the cyanidation kinetics of elemental silver and silver telluride; (2) study the effect of temperature (i.e. 20, 25, 27, 30, 35 and 40°C) on silver telluride dissolution; and (3) elucidate the kinetic mechanism of the silver telluride cyanidation. The results obtained showed that: (1) while 83.5% of elemental silver was dissolved in 8?h, only 13.2% of silver from silver telluride was dissolved in the same time; (2) temperature has an important effect on silver extraction from silver telluride, but a minor effect on tellurium dissolution; and (3) at temperatures between 20 and 27°C, the process was controlled by the chemical reaction with an apparent activation energy of 191.9?kJ?mol?1, whereas at temperatures between 30 and 40°C, the process was controlled by diffusion through a Ag5Te3 layer of products with an apparent activation energy of 25.2?kJ?mol?1.  相似文献   
938.
    
Z. Wang  Q. Liu  L. You  S. Wei  L. Cao 《钢铁冶炼》2018,45(4):379-385
Physical modelling of slag splashing practice of an 80 t combined blown converter was conducted in this paper. Through measuring the mass flux of splashed slag, the effect of different operating parameters on slag splashing was investigated. By means of variance analysis, the influence significance of different operating parameters on slag splashing was obtained, and the optimal combination of operating parameters were acquired as follows: lance height 600?mm, top gas flowrate 18000?Nm3?h?1, four nozzles lance, bottom nozzle configuration D4, bottom gas flowrate 100?Nm3?h?1, and amount of remained slag 10%. In addition, the relation between the agitation energy of top blow and mass flux of splashed slag was discussed, and the estimation model for mass flux of splashed slag during BOF slag splashing practice was proposed through data analysis.  相似文献   
939.
    
  相似文献   
940.
    
The hot metal full pretreatment and less-slag steelmaking process constituted a platform to produce clean steel with low cost and rapid pace and also realized a professional production line. The w[P] can be less than 0.030% at the end of De-P converter and 0.006% at the end of De-C converter. The w[N] in steel can be less than 15×10−6 at the stirring station. This production line can make clean steel steadily used for auto sheet or pipeline, for example X65MS. The De-C slag was left in the converter for the next heat and recycled to De-P converter to reduce lime consumption, which has a great benefit for the cost saving.  相似文献   
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