Zobrazeno 1 - 10
of 23
pro vyhledávání: '"A. I. Elshin"'
Autor:
I. E. Kuzora, A. I. Elshin, Vladimir Z. Mordkovich, A. R. Karaev, A. A. Kamenev, E. Yu. Kharitonova, E. Mitberg, I. A. Maslov
Publikováno v:
Petroleum Chemistry. 47:288-298
Investigation of the optimization of the feedstock composition on delayed coking units (UZK 21-10/3M) at the Angarsk Petrochemical Company using the introduction of different heavy oil residues and by-products of petroleum chemistry was carried out.
Autor:
A. A. Rytsev, Zh. Yu. Gusakova, A. A. Osintsev, S. V. Kuznetsov, K. G. Ziganshin, O. A. Chekenev, S. Yu. Tvorogov, A. V. Pastukhov, A. L. Samoshkin, L. A. Ponyaev, S. P. Yanbaev, I. V. Pavlov, A. I. Elshin, G. K. Ziganshin
Publikováno v:
Chemistry and Technology of Fuels and Oils. 43:17-21
0009-3092/07/4301–0017 © 2007 Springer Science+Business Media, Inc. Deasphalting of vacuum resid with liquefied propane is usually conducted in extraction towers of the gravity type. Standard towers (Fig. 1a) have a small (~7 m) height of the prop
Autor:
I. E. Sidorov, I. V. Kuks, S. L. Kryachek, A. I. Elshin, V. M. Moiseev, L. Sh. Glazov, I. M. Liberzon, B. Z. Solyar
Publikováno v:
Chemistry and Technology of Fuels and Oils. 40:222-226
The final stage of revamping of the GK–3 cat cracker reactor block with introduction of new technology is described. The elements of implantation are: combined external riser reactor; high–efficiency feedstock and slurry nozzles; crude treatment
Autor:
V. M. Moiseev, A. V. Pereladov, G. S. Vulisanova, Yu. N. Lebedev, Ya. P. Lozhkin, V. G. Chekmenev, A. I. Elshin
Publikováno v:
Chemistry and Technology of Fuels and Oils. 38:13-16
In 1999, Angarsk Petrochemical Company issued a bid for revamping the EDU—AVT—6 Plant for the purpose of simultaneously producing four oil cuts in the vacuum unit — transformer oil base (viscosity of 7—9 mm2/sec at 50°C), low—viscosity, me
Publikováno v:
Chemistry and Technology of Fuels and Oils. 37:90-93
A method for assessing the efficiency of a catalyst for hydrotreating of petroleum feedstock in industrial conditions, selected with consideration of the strength properties, stable activity, and cost, is proposed. This evaluation will ensure that th
Publikováno v:
Chemistry and Technology of Fuels and Oils. 36:191-194
Autor:
A. V. Zyuzin, V. N. Kostyukov, A. I. Elshin, A. N. Aktuganov, B. N. Makhon’kin, S. V. Mukhin, F. I. Serdyuk, A. A. Shatalov, Al. V. Kostyukov, V. B. Mailer
Publikováno v:
Chemistry and Technology of Fuels and Oils. 36:153-159
Autor:
I. M. Liberzon, V. M. Zarubin, A. I. Elshin, V. M. Moiseev, V. A. Kiselev, B. Z. Solyar, F. I. Serdyuk, L. Sh. Glazov, D. V. Shekera, I. E. Sidorov, T. Kh. Melik-Akhnazarov
Publikováno v:
Chemistry and Technology of Fuels and Oils. 36:182-187
Reconstruction of the reactor unit (RU) on the cat cracker in the GK-3 complex at Angarsk Refinery is being carried out in three stages. The first was conducted in 1993–1994, the second in 1998–1999, and the third stage will be executed in 2000
Autor:
D. A. Sergeev, I. M. Liberzon, B. Z. Solyar, A. I. Elshin, V. M. Moiseev, V. M. Zarubin, A. S. Gribok, I. E. Sidorov, L. Sh. Glazov, I. V. Kuks, I. E. Kuzora
Publikováno v:
Chemistry and Technology of Fuels and Oils. 44:92-94
The results of operation of the cat cracker after revamping with introduction of cracking technology in a once-through reactor in two basic regimes: “mild”-for maximum refining of light petroleum products at a low cracking temperature, and “sev
Publikováno v:
Chemistry and Technology of Fuels and Oils. 34:359-362
In the separation of the vapor-phase products of cracking from spent microbead catalyst at the outlet from a riser reactor, improvements in separation efficiency and curtailment of the separation time will reduce the extent of secondary reactions in