Zobrazeno 1 - 10
of 15
pro vyhledávání: '"M. Yu. Savinov"'
Autor:
A.M. Konovalov, D. G. Rudik, A. Shakirov, G. S. Taer, T. D. Krakhmalova, G. Simakov, Yu.A. Melikyan, A K Berdnikova, A. V. Kumpan, E. Kozlova, A. G. Dolgolenko, D. V. Guss, Yu. V. Gusakov, A. V. Sidorenko, O. E. Nepochataya, Pavel Dzhumaev, V.V. Sosnovtsev, D. Yu. Akimov, M. Yu. Kolpakov, A. G. Kovalenko, V. Belov, A.V. Khromov, A. V. Lukyashin, M. Yu. Savinov, S. V. Bobkov, Alexander Bolozdynya
Publikováno v:
Instruments and Experimental Techniques. 60:782-788
A procedure for spark-discharge purification of a liquid xenon sample with a mass of 55 kg is described. The average lifetime of ionization electrons before capture by electronegative impurities in liquid xenon increased from ≤ 0.1 μs to ≥ 50 μ
Autor:
E. Kozlova, A. V. Kumpan, Pavel Dzhumaev, G. Simakov, D. E. Kdib, V.V. Sosnovtsev, V. Belov, M. Yu. Savinov, A.V. Khromov, M. Yu. Kolpakov, A. V. Galavanov, Yu.A. Melikyan, A. Shakirov, Yu. V. Gusakov, D. Yu. Akimov, A. V. Lukyashin, A.M. Konovalov, N. V. Volkov, D. G. Rudik, A. A. Vasin, S. V. Bobkov, A. G. Kovalenko, O. E. Nepochataya, Alexander Bolozdynya
Publikováno v:
Technical Physics Letters. 44:637-639
The formation of titanium nanoparticles (NPs) in a high-voltage electric discharge between titanium electrodes in liquid xenon at a temperature of –105°C has been observed. It has been shown that these titanium nanoparticles have a spherical shape
Autor:
V. E. Poznyak, M. Yu. Savinov
Publikováno v:
Chemical and Petroleum Engineering. 44:709-714
Nitrogen is used with a tubular apparatus to organize rectification in an industrial plant for producing krypton and xenon. Experimental results are given with experimental and industrial condenser-evaporators. The problem of choking in the upper tub
Autor:
M. Yu. Savinov
Publikováno v:
Chemical and Petroleum Engineering. 44:452-458
A solution is provided for obtaining especial-purity products subject to the need to obtain simultaneously the maximum possible extraction coefficients. Schemes are given for basic units for isolating one component from an n-component mixture. Three
Autor:
M. Yu. Savinov
Publikováno v:
Chemical and Petroleum Engineering. 44:459-463
Experiments are reported for an industrial plant type X-0.06 for producing xenon-nitrogen mixtures in order to examine the adsorption replacement of hazardous oxygen by nitrogen. The equation previously used for the replacement has been shown to be i
Publikováno v:
Chemical and Petroleum Engineering. 44:131-137
Results are provided for a study in a laboratory test unit of the adsorption dynamics for krypton, xenon, ethane and nitrogen hemioxide (lower oxide) from air in two-layer equipment simulating an industrial adsorber of a combined purification unit (C
Publikováno v:
Chemical and Petroleum Engineering. 43:474-480
Results of laboratory bench studies of the dynamics of low-temperature adsorption of xenon from the starting mixture resembling what is called “dirty oxygen” on four types of domestic industrial sorbents are reported. The purpose of these studies
Publikováno v:
Chemical and Petroleum Engineering. 43:259-269
Questions are considered for creating industrial technology for processing a primary krypton concentrate of krypton and xenon in the form of a krypton-xenon mixture. New progressive engineering solutions, protected by patents, are used in a Khrom-3 u
Autor:
M. Yu. Kolpakov, M. Yu. Savinov, A. M. Arkharov, V. L. Bondarenko, V. N. Kazushchik, V. B. Vorotyntsev
Publikováno v:
Chemical and Petroleum Engineering. 40:666-671
Hardware has been developed as a standard instrument, known as the automated analysis system (AAS), which works in conjunction with a newly developed software that runs on an IBM-compatible PC. In this document, we cover the communication method of t
Publikováno v:
Chemical and Petroleum Engineering. 40:595-599
A schematic diagram of the plant for getting nitrogen-xenon mixture from “dirty” oxygen of air-fractionating plant (AFP) is shown and described. Industrial plant test data are presented in the form of relationship of the adsorber operation time w