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61.
62.
The kinetics of the rearrangement of cyclohexanone-oxime has been studied in a fixed bed, glass tubular reactor at atmospheric pressure and temperatures of 240, 270, 300 and 335°C, using ultrastable HY zeolite catalyst. Several kinetic models, including the Langmuir-Hinshelwood type, have been derived and the best statistical fit has been obtained with a pseudo-first order kinetic equation. The rate constants and activation energies for the formation of the products caprolactam, cyclohexanone and 5-cyanopent-l-ene have been calculated. Based on the evolution of the selectivity with temperature, and the I.R. spectra of the poisoned catalyst, different decay models have been deduced and discussed. 相似文献
63.
64.
The O-methylation of phenol with dimethyl carbonate proceeds selectively in the vapor phase over alkali ion exchanged X-zeolites. Thus, a 76% yield of anisole was obtained with a 93% selectivity over NaX at 553 K. The participation of basic sites in the O-methylation is suggested. 相似文献
65.
The adsorption of nitrogen oxides on Cu-ZSM-5 was studied by infrared spectroscopy to elucidate the species associated with the band at 2133 cm–1. The band was found for both NO and NO2 adsorption. Labeling experiments with15NO revealed that the associated surface species contained nitrogen and, most likely, an N-O bond. Co-adsorption experiments of NO and oxygen produced adsorbed nitronium, NO
2
+
, as the principal, associated species. Adsorption of nitrogen oxides on dispersed CuO and the HZSM-5 support demonstrated that the 2133 cm–1 band was not necessarily associated with copper ions. A relatively strong correlation between the bands at 2133 and 3615 cm–1 indicates that the primary adsorption sites of NO
2
+
are the strongly protic, bridging Si(OH)Al framework hydroxyls. Once these were filled, other, weaker acid sites began to adsorb NO
2
O
. 相似文献
66.
Seung-Min Oh Hyun-Ha Kim Atsushi Ogata Hisahiro Einaga Shigeru Futamura Dong-Wha Park 《Catalysis Letters》2005,99(1-2):101-104
Toluene was decomposed in a surface discharge plasma reactor packed with various zeolites. The positioning effect of the zeolite bed was also investigated Reactor-B, in which the zeolite bed was located upstream, performed much better than Reactor-A, in which the zeolite bed was located downstream. Furthermore, the decomposition efficiency in Reactor-B increased with the capacity for toluene adsorption on zeolite, while that in Reactor-A did not. The toluene adsorbed in micropores was not decomposed effectively by direct electron impact, but was decomposed by active oxygen species generated in the plasma zone on the zeolite surface. A good correlation was also observed between toluene decomposition and ozone consumption in the downward-type reactor. 相似文献
67.
HZSM-5分子筛催化合成1,3-苯并二嗯茂烷类化合物 总被引:2,自引:0,他引:2
研究了HZSM-5分子筛催化邻苯二酚与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、异戊醛、正己醛、正辛醛、苯甲醛、二苯甲酮等10余种醛(酮)的缩合反应。考察了反应时间、酚与醛(酮)的配比、HZSM-5分子筛用量等因素对邻苯二酚与醛(酮)反应的影响。结果表明,当n(邻苯二酚):n(醛(酮)]=1:1.4,催化剂用量为3.5g/mol邻苯二酚,反应5h,选择性一般在99.2%以上,转化率也一般在30%以上,表明,HZSM-5分子筛对邻苯二酚与醛(酮)的反应有较好的催化性能。 相似文献
68.
Effectiveness of microwave heating in an activation treatment of zeolites was studied and utilization of zeolites for reusable desiccant was examined. X zeolite was chosen as a target material for its large adsorption capacity. Na-X zeolite easily caused a thermal runaway by microwave radiation of 500 W but Ca contained X zeolite merely reached ca. 573 K under the same conditions. Mixtures of Na-X and Ca-X with suitably mixed ratios did not cause the thermal runaway and their heating temperatures were controlled (>573 K) at will. Under the most suitable conditions, the mixture reached a dehydration degree of 92%. A degradation degree of adsorptive capacity of the mixture for water was examined after three treatments. The average degradation degree was 1.5% per treatment. The heating method is promising as a quick and easy technique to activate zeolite. By applying the method, the zeolites with suitable mixing ratios are usable as a reusable desiccant for home use. 相似文献
69.
The adsorption of molecular hydrogen on model zeolites has been simulated employing Grand Canonical Monte Carlo (GCMC) procedure. The effects of cation type, available volume, surface area, temperature, pressure and pre-adsorbed organics such as benzene on the hydrogen uptake are analyzed. The hydrogen adsorption can be affected mainly by the available volume and surface area per g-zeolite at the same temperature and pressure. Increase of temperature results in the decrease of sorption intensity and capacity. The adsorption capacity correlates well with the pressure with high linearity at room temperature. Adsorption is lowered by the pre-adsorbed benzene molecule. The orientation and the number of benzene molecule in zeolite affect the adsorption capacity. The organic zeolite with larger available volume shows larger adsorption capacity. 相似文献
70.
This paper reports the development of a method for simultaneously measuring zeolite, silicate, and phosphate in laundry detergent
products by inductively coupled plasma atomic emission spectrometry. A sample is decomposed under alkaline oxidative conditions
to decompose zeolite, silicate, phosphate, and organic substances. Then hydrochloric acid is added to the decomposed solution
to dissolve aluminum hydroxide precipitate before analysis. This sample preparation procedure was investigated by using a
total organic carbon analyzer and was confirmed to be applicable to simultaneous measurements of zeolite, silicate, and phosphate.
Relative standard deviation for the analysis is less than 2.1%, recovery is more than 99.0%, and the calibration curve gives
a correlation coefficient ofR=1.000. The detection limit of this method for aluminum and silicon is 0.1%, and for phosphorus, 0.2% by weight in the product.
This method is applicable to various laundry detergent products that contain zeolite, silicate, or phosphate and is five times
faster than the three wet chemical methods. 相似文献