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41.
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Jan‐Chan Huang 《应用聚合物科学杂志》2004,94(4):1547-1555
Experimental values of Flory–Huggins parameters, χ, between polymers and probes, are frequently used to determine the solubility parameters of the polymers by the method of DiPaola–Baranyi and Guillet. The solubility parameters of probes were usually estimated by using heat of vaporization. When χ is measured at a temperature near the critical temperature of the probes and used to determine the solubility parameter of polymers, the departure of enthalpy of the probe vapor from the ideal gas state should be considered. This study discussed the method to make the correction and its effect on the determination solubility parameter of polymers. Without correction in the vapor phase enthalpy, the solubility parameters of the probes and polymer tend to be underestimated and the error increases when the critical temperature is approaching. Analytical expressions for the effect of correction on the solubility parameter of probes and parameters of polymers were derived. By use of probes with a range of solubility parameters on both sides of the solubility parameter of polymers, the correlation between parameters of polymers was shown to be reduced. © 2004 Wiley Periodicals, Inc. J Appl Polym Sci 94: 1547–1555, 2004 相似文献
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In this work, entropic expressions of UNIFAC‐FV and Entropic‐FV models were evaluated by using an extensive database of infinite dilution vapor–liquid equilibrium (VLE) data of athermal systems containing polypropylene, polyethylene, and polyisobutylene. For the infinite dilution athermal systems, performance of the Entropic‐FV model was better than that of the UNIFAC‐FV model. Then, finite concentration VLE data of non‐athermal systems that consisted of 16 polymers and 36 solvents containing a large variety of solvent–polymer systems ranging from nonpolar to polar substances were considered to optimized 46 pairs of group interaction parameters of the Entropic‐FV model. For systems containing polar solvents of three types of solvents studied, revised group interaction parameters gave significant improvements from 17.9 to 13.0% average absolute deviation (AAD) of solvent activities. For overall results, improvements were achieved from 15.1 to 12.4% AAD. © 2005 Wiley Periodicals, Inc. J Appl Polym Sci 97: 1145–1153, 2005 相似文献
45.
Activities of NiO were measured in the oxide and spinel solutions of the system MnO–NiO–Al2 O3 at 1300° and 1400° C with the aim of deriving information on the thermodynamic properties of the spinel phases. Synthetic samples in selected phase assemblages of the system were equilibrated with metallic nickel and a gas phase of known oxygen partial pressures at a total pressure of 1 atm. The data on NiO activities and directions of conjugation lines between coexisting oxide and spinel phases were used to establish the activity–composition relations in spinel solid solutions at 1300° and 1400°C. The MnAl2 O4 –NiAl2 O4 solid solutions exhibit considerable negative deviations from ideality at these temperatures. The free energy of formation of MnAl2 O4 from its oxide components (MnO + Al2 O3 ) at 1300° and 1400°C is calculated to be −24.97 and −26.56 kJ. mol−1 , respectively. The activities determined in the stoichiometric spinel solid solutions are more negative as compared with those predicted from cation distribution models. 相似文献
46.
The solubility and activity–composition relations of chromium oxide in melts of the systems CaO–CrO x –SiO2 and CaO–Al2 O3 –CrO x –SiO2 have been determined at 1500°C by equilibrating melts with Pt–Cr alloys at known oxygen pressures. It is shown that the increase in the concentration of divalent chromium ions, as the oxygen pressure and the basicity of melt decrease, results in a dramatic increase in the solubility of chromium oxide in the liquid phase. An increase in the Al2 O3 content of the melt leads to a decrease in the solubility of chromium oxide over the whole composition range studied. The activity coefficient of CrO has been found to increase with increasing melt basicity and decreasing oxygen pressure whereas the activity coefficient of CrO1.5 decreases sharply with increasing melt basicity for siliceous melts but levels off at a basicity ratio (wt% CaO/wt% SiO2 ) of about 0.7. An increase in the Al2 O3 content of the melts results in an increase in the activity coefficient of CrO. 相似文献
47.
糠醛渣对染料甲基紫的吸附行为 总被引:4,自引:0,他引:4
以废弃物糠醛渣为原料制备吸附剂,研究了甲基紫溶液在糠醛渣上的吸附行为,并从热力学和动力学角度探讨了吸附作用机理。吸附平衡模型研究表明,糠醛渣对甲基紫的吸附符合Langmuir与Freundlich型的复合型吸附,即单层吸附和吸附剂表面非均质吸附同时存在;吸附动力学研究表明,糠醛渣对甲基紫的吸附符合准二级吸附动力学方程;热力学参数,ΔG0为-6.667 kJ.mol^-1--8.216kJ.mol^-1、ΔH0为16.866kJ.mol^-1、ΔS0为0.079 kJ.mol^-1.K^-1、为14.753 kJ.mol^-1,说明糠醛渣对甲基紫的吸附是自发进行的、吸热的,且主要为一物理吸附过程。糠醛渣作为吸附剂处理甲基紫废水,是一种有效的方法。该方法实现了以废治废的废物资源化目标,具有良好的社会效益和经济效益. 相似文献
48.
基于有限时间热力学理论,以供热率密度作为热力学优化目标,分析了恒温热源不可逆空气热泵循环的性能,导出了供热率密度与压比和换热器有效度等参数间的解析关系式,并由数值计算分析了热源温比、总热导率及压缩机和膨胀机效率等对热导率最优分配及供热率密度最优性能的影响特点。 相似文献
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基于非平衡态热力学的传递唯象研究 总被引:1,自引:0,他引:1
从广义力与流的角度,探讨了传递现象的共同本质,即各种强度量势场梯度作用下的能流和流。运用非平衡态热力学的相关理论,推导了多势场影响下的传递唯象方程。根据非平衡态热力学分析不可逆过程的一般步骤,提出确定传递唯象方程力与流的两种方法,体现了热力学和传输学在传递研究中的学科交叉。对热电耦合现象的应用分析表明,基于非平衡态热力学的传递唯象方程,能够完整、深入地揭示不可逆效应之间的耦合关系。 相似文献