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1.
2.
Shailesh J. Patil 《Chemical Engineering Communications》2019,206(5):605-618
Jatropha oil is a promising nonedible feedstock for producing renewable diesel. In this work, the hydrotreatment processing of jatropha oil was investigated. Instead of using conventional alumina-supported Co–Mo, Ni–Mo, and Ni–W catalysts that need sulfidation pretreatment, noble metals such as Pd and Ru were chosen. Trials were performed in an isothermal trickle-bed reactor and the reaction conditions were as follows: temperature 603–663?K, weight hourly space velocity (WHSV) 1 to 4/h, pressure 1.5–3?MPa, and H2/oil ratio 200–800 (v/v). Yield of n-C15 to n-C18 hydrocarbons was maximized (70.3 and 43.8% for Pd/Al2O3 and Ru/Al2O3, respectively) at the following conditions: T?=?663 K, WHSV?=?2/h, P?=?3?MPa, and H2/oil ratio?=?600 (v/v). Since Ru favored cracking reactions to a larger extent than Pd, the yield of C15 to C18 hydrocarbons over Ru/Al2O3 was lowered. Using simple first-order plots for oil conversion, activation energies for the hydrotreating process over Pd/Al2O3 and Ru/Al2O3 were found and they were equal to 109 and 121?kJ/mol, correspondingly. 相似文献
3.
研究了在超临界条件下甘油三乙酸酯与甲醇或乙醇的酯交换反应,分别考察了超临界状态下醇油摩尔比和温度对反应的影响。实验结果表明,甲醇或乙醇与甘油三乙酸酯的摩尔比为14、反应温度为350℃、反应时间为20m in时,乙酸甲酯或乙酸乙酯的收率分别达100%和60%。对超临界状态下动力学的研究结果表明,甘油三乙酸酯与甲醇或乙醇的酯交换反应为拟一级反应,在相同的反应条件下,采用甲醇时酯交换反应速率比用乙醇时快,相应的甘油三乙酸酯的转化率也高;甘油三乙酸酯在超临界甲醇或乙醇中酯交换反应的表观活化能分别为58.7 kJ/mol和75.1 kJ/mol,甘油三乙酸酯与甲醇酯交换反应的活化能低于与乙醇酯交换反应的活化能,表明碳链短的醇更易进行酯交换反应。 相似文献
4.
利用高酸值餐饮废油脂制备生物柴油 总被引:8,自引:0,他引:8
以高酸值餐饮废油脂为原料,在酯化反应后再经两步酯交换反应制备生物柴油。在酯化反应中添加吸水剂可降低油脂的酸值,经一次酯化反应即可将油脂的酸值降至2m g/g左右,满足酯交换反应的要求。考察了酯化反应中吸水剂的添加方式、种类及其用量对酯化反应的影响,以及酯交换催化剂的种类及用量对脂肪酸甲酯(FAME)收率和产物组成的影响。实验结果表明,以凹凸棒土为吸水剂(用量为餐饮废油脂中游离脂肪酸质量的3%),且在酯化反应30m in时加入,酯化效果较好;以质量比为1∶1的NaOH和KOH混合物为催化剂进行两步酯交换反应时,催化剂的最佳用量依次为1.00%和0.75%(质量分数,基于油脂的质量),FAME收率最高达到96.33%。 相似文献
5.
The present work is focusing on the synthesization and physico-chemical properties of Jatropha curcas biodiesel with diesel and alcohols.The densities of binary diesel (2)+1-alkanols (C_3 or C_4)(3) and ternary Jatropha curcas biodiesel (1)+diesel (2)+1-alkanols (C_3or C_4)(3) blends have been reported over full range of composition at temperatures within range 288.15 to 313.15 K.Also densities of Jatropha curcas biodiesel (1)+diesel or 1-alkanols (C_3 or C_4)(2) blends have been measured at 313.15 K.Excess molar volumes,V~E,V~E_(123)of binary and ternary blends were calculated from the measured data and the derived properties were correlated to composition using Redlich–Kister equation.A reasonable agreement was found between the measured and estimated values.Further,densities and excess molar volumes data were reasoned to discuss molecular interactions taking into consideration effect of composition and temperature. 相似文献
6.
Biodiesel was produced by transesterification of soybean oil with methanol using ZnO loaded with KF as a solid base catalyst.
It was found that the catalyst with 15 wt.% KF loading and calcined at 873 K showed the optimum activity. XRD, IR and Hammett
indicator method were employed for the catalyst characterization. The results showed the activity of the catalysts was correlated
with their basicity. The influence of various reaction variables on the conversion was also discussed. 相似文献
7.
8.
Robert O. Dunn 《Journal of the American Oil Chemists' Society》2005,82(5):381-387
Biodiesel, an alternative diesel fuel derived from transesterification of vegetable oils or animal fats, is composed of saturated
and unsaturated long-chain FA alkyl esters. During long-term storage, oxidation caused by contact with air (autoxidation)
presents a legitimate concern with respect to monitoring and maintaining fuel quality. Extensive oxidative degradation may
compromise quality by adversely affecting kinematic viscosity, acid value, or PV. This work examines the oil stability index
(OSI) as a parameter for monitoring the oxidative stability of soybean oil FAME (SME). SME samples from five separate sources
and with varying storage and handling histories were analyzed for OSI at 60°C using an oxidative stability instrument. Results
showed that OSI may be used to measure relative oxidative stability of SME samples as well as to differentiate between samples
from different producers. Although addition of α-tocopherol or TBHQ increased OSI, responses to these antioxidants varied
with respect to SME sample. Variations in response to added antioxidant were attributed to aging and other effects that may
have caused oxidative degradation in samples prior to acquisition for this study. Results showed that OSI was more sensitive
than iodine value in detecting the effects of oxidative degradation in its early stages when monitoring SME during storage. 相似文献
9.
Vinnie?Mao Samir?K.?Konar David?G.?B.?BoocockEmail author 《Journal of the American Oil Chemists' Society》2004,81(8):803-808
The base-catalyzed transmethylation of soybean oil has been studied under conditions whereby the reaction starts as a single
phase, but later becomes two phases as glycerol separates. Methanol/oil molar ratios of 6∶1 were used at 23°C. The catalysts
were sodium hydroxide (0.5, 1.0, and 2.0 wt%), potassium hydroxide (1.0 and 1.4 wt%), and sodium methoxide (0.5, 1.0, and
1.35 wt%), all concentrations being with respect to the oil. Oxolane (tetrahydrofuran) was used to form a single reaction
phase. The reactions deviated from homogeneous kinetics as glycerol separated, taking with it most of the catalyst. When 1.0
wt% sodium hydroxide was used, the methyl ester content reached 97.5 wt% after 4 h, compared with 85–90 wt% in the two-phase
reaction. Sodium hydroxide (1.0 wt%), sodium methoxide (1.35 wt%), and potassium hydroxide (1.4 wt%) gave similar results,
presumably because the same number of moles was used. The ASTM biodiesel specification for chemically bound glycerol was achieved
after only 3 min when 2.0 wt% sodium hydroxide was used. However, the standard was not achieved after 4 h when 1.0 wt% sodium
hydroxide was used, the MG content being 1.1–1.6 wt%. The use of 2.0 wt% catalyst is commercially impractical. 相似文献
10.