全文获取类型
收费全文 | 275篇 |
免费 | 1篇 |
专业分类
电工技术 | 3篇 |
化学工业 | 23篇 |
金属工艺 | 11篇 |
机械仪表 | 4篇 |
建筑科学 | 5篇 |
矿业工程 | 6篇 |
石油天然气 | 54篇 |
无线电 | 2篇 |
一般工业技术 | 75篇 |
冶金工业 | 25篇 |
原子能技术 | 62篇 |
自动化技术 | 6篇 |
出版年
2021年 | 6篇 |
2018年 | 7篇 |
2016年 | 8篇 |
2014年 | 7篇 |
2013年 | 3篇 |
2012年 | 4篇 |
2011年 | 8篇 |
2010年 | 5篇 |
2008年 | 10篇 |
2007年 | 11篇 |
2006年 | 4篇 |
2005年 | 8篇 |
2004年 | 6篇 |
2003年 | 7篇 |
2002年 | 9篇 |
2001年 | 4篇 |
2000年 | 5篇 |
1998年 | 3篇 |
1997年 | 6篇 |
1995年 | 3篇 |
1994年 | 3篇 |
1993年 | 4篇 |
1992年 | 3篇 |
1991年 | 2篇 |
1990年 | 3篇 |
1989年 | 7篇 |
1988年 | 6篇 |
1987年 | 5篇 |
1986年 | 3篇 |
1984年 | 5篇 |
1983年 | 9篇 |
1982年 | 6篇 |
1981年 | 4篇 |
1978年 | 2篇 |
1977年 | 7篇 |
1976年 | 8篇 |
1975年 | 8篇 |
1974年 | 12篇 |
1973年 | 4篇 |
1972年 | 5篇 |
1971年 | 3篇 |
1970年 | 5篇 |
1969年 | 4篇 |
1967年 | 3篇 |
1966年 | 7篇 |
1965年 | 3篇 |
1964年 | 5篇 |
1961年 | 2篇 |
1959年 | 2篇 |
1958年 | 2篇 |
排序方式: 共有276条查询结果,搜索用时 15 毫秒
91.
92.
A. B. Sazonov É. P. Magomedbekov G. V. Veretennikova S. A. Samoilov A. V. Zharkov 《Atomic Energy》2005,98(2):127-134
The reactions resulting in the tritium contamination of mineral oils in pumps during transfer of tritium-containing gas mixtures are examined. The basic chemical forms of tritium dissolved in oils are established. The adsorption of tritium-containing impurities of spent oils and the chemical isotopic exchange of adsorbed impurities with concentrated sulfuric acid are studied. A method for handling tritium-containing waste oils that permits decreasing the radiation hazard due to storage of these oils and recycling tritium gas is proposed on the basis of these investigations.__________Translated from Atomnaya Énergiya, Vol. 98, No. 2, pp. 134–143, February, 2005. 相似文献
93.
V. A. Kirillov A. B. Shigarov A. V. Samoilov N. A. Kuzin V. V. Kireenkov D. A. Ivanov 《Theoretical Foundations of Chemical Engineering》2016,50(1):1-14
A catalytic heater design was proposed for an external combustion engine. This design is based on the partial oxidation or autothermal conversion of hydrocarbon fuel to syngas and its further oxidation with heat generation in a radial catalytic reactor integrated with a tubular heat exchanger. The theoretical analysis of operational regimes for a catalytic heater with a thermal power of 25–50 kW was performed with regard to the distribution of gas and the mathematical modeling of processes in a catalyst bed integrated with a heat exchanger, and some estimates were given for the performance of an external combustion engine. The conditions providing a uniform distribution of gas along the length of a radial reactor with suction of a reaction mixture into the catalyst bed were determined. A design of catalytic heating system elements was developed, and some layout solutions that provide a rational mutual arrangement of system components were created. 相似文献
94.
95.
N. A. Samoilov 《Chemistry and Technology of Fuels and Oils》2002,38(4):237-244
It is theoretically substantiated and experimentally demonstrated that sectioning of a stationary bed of adsorbent with walls parallel to flow of the treated feedstock increases the efficiency of the adsorbent. Mathematical modeling of sectioned adsorbers with a mobile bed of adsorbent demonstrated the possibility of increasing the quality of the sampled narrow fractions and decreasing the power consumption for regeneration of the adsorbent. 相似文献
96.
R. A. Peskov V. I. Alekseev L. V. Levanov O. B. Samoilov E. F. Mitenkova N. V. Novikov 《Atomic Energy》1995,79(3):579-583
Special Office of Machine Design Institute of Fast Reactors, Russian Academy of Sciences. Translated from Atomnaya énergiya,
Vol. 79, No. 3, pp. 171–174, September, 1995. 相似文献
97.
98.
99.
100.