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351.
高参数小管径内煤油的传热特性研究 总被引:11,自引:0,他引:11
本文对酸碱水洗煤油在高热流密度、高流速、高压、小直径圆管条件下进行了试验及理论研究,试验参数为热流密度q=0.8-50 MW/m2、亚临界压力p=2 MPa、超临界压力p=5,15 MPa、质量流速pw=8500-51000 kg/m2·s、圆管内径φ=1.7 mm。通过试验研究,获得了酸碱水洗煤油在亚临界及超临界压力条件下的传热特性、拟沸腾发生的界限条件以及传热恶化时的临界热流密度值及相关影响因素。在对试验结果分析的基础上,建立了临界热流密度关联式,计算结果与试验结果吻合良好。 相似文献
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本文采用拍摄速度为10000帧/秒的高速摄影仪对不锈钢箔表面的过冷沸腾现象进行了可视化实验研究。实验结果与用微液层模型理论预测的结果一致。高过冷度区域的沸腾换热机理主要是由气泡生长、消失过程中温度边界层的强制排除(所谓强制对流)引起的。气泡周期主要由等待时间构成,这在过冷度高的情况下尤为显著。对等热流密度换热面,微液层模型预测的气泡周期与实验值比较吻合。 相似文献
356.
A theoretical estimation of the pre-breakdown-heating time in the underwater discharge acoustic source
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One of the common characteristics of the electrothermal breakdown in an underwater discharge acoustic source(UDAS) is the existence of a pre-breakdown-heating phase.In our experiment,two phenomena were observed:(1) the breakdown time that takes on high randomicity and obeys a "double-peak" stochastic distribution;(2) the higher salt concentration that reduces the residual voltage and causes 100% non-breakdown.The mechanism of electrothermal breakdown is analysed.To specify the end of the pre-breakdown-heating phase,a "border boiling" assumption is proposed,in which the breakdown time is assumed to be the time needed to heat the border water around the initial arc to 773 K.Based on this ’border boiling’ assumption,the numerical simulation is performed to evaluate the effects of two heating mechanisms:the Joule heating from the ionic current,and the radiation heating from the initial arc.The simulation results verify the theoretical explanations to these two experiment phenomena:(1) the stochastic distribution of the radius of the initial arc results in the randomicity of the breakdown time;(2) the difference in efficiency between the radiation heating and the Joule heating determines that,in the case of higher salt concentration,more energy will be consumed in the pre-breakdown-heating phase. 相似文献
357.
选择欧拉多相流模型和非平衡沸腾模型,用Fluent 软件对单边受热竖直向上平滑管进行了过冷流动沸腾换热的数值分析。研究了不同质量流速、进口温度和热流密度对对流换热系数和空泡份额的影响,并分析了它们对传热恶化的影响。 相似文献
358.
Boiling flow simulations are conducted on adaptive octree grids. A phase change model consistent with the mixture formulation, in conjunction with the Volume-of-Fluid (VOF) model, is used to track the liquid–vapor interface. Test cases including Rayleigh Taylor instability and bubble growth in a uniform superheat are conducted to validate the phase change model on adaptive grids. The validated model is then used to conduct film boiling simulations on both two-dimensional and three-dimensional adaptive grids. The average wall Nusselt number agrees well with the widely accepted correlations of Berenson (1961) and Klimenko (1981) and Klimenko and Shelepen (1982) for film boiling on a horizontal surface. For the test cases presented, the efficiency of the adaptive technique, as measured by the adaptive mesh refinement (AMR) efficiency, is mostly in the range of 50–80%. Although this efficiency is a function of the nature and dimensionality of the problem, this range of efficiency is comparable to those obtained in the simulations of primary jet atomization conducted by Fuster et al. (2009). This work opens the prospect of conducting more realistic (three-dimensional) multi-modal boiling flow simulations, and problems of similar complexity, in an efficient manner. 相似文献
359.
With the long-term objective of Critical Heat Flux (CHF) prediction, bubble dynamics in convective nucleate boiling flows has been studied using a Direct Numerical Simulation (DNS). A sharp-interface phase change model which was originally developed for pool boiling flows is extended to convective boiling flows. For physical scales smaller than the smallest flow scales (smaller than the grid size), a micro-scale model was used. After a grid dependency study and a parametric study for the contact angle, four cases of simulation were carried out with different wall superheat and degree of subcooling. The flow structures around the growing bubble were investigated together with the accompanying physics. The relation between the heat flux evolution and the bubble growth was studied, along with investigations of bubble diameter and bubble base diameter evolutions across the four cases. As a validation, the evolutions of bubble diameter and bubble base diameter were compared to experimental observations. The bubble departure period and the bubble shapes show good agreement between the experiment and the simulation, although the Reynolds number of the simulation cases is relatively low. 相似文献
360.
In this study, saturated flow boiling characteristics of deionized water in single rectangular minichannels are investigated experimentally. A special attention is paid to the effect of aspect ratio (channel width to depth, Wch/Hch) on the heat transfer and total pressure drop. Experiments are conducted for various values of the mass flux and the wall heat flux. Flow visualization is used as a complementary technique for a deeper physical understanding of flow phenomena. The results show that the channel aspect ratio has a significant effect on both the local two-phase heat transfer coefficient and the total pressure drop. In general manner, the aspect ratio of 1 presents the highest heat transfer coefficients, while the aspect ratio of 0.25 demonstrates the lowest ones. On the other hand, the lowest values of the pressure drop are obtained at the extreme values of the aspect ratio (0.25 and 4). 相似文献