Zobrazeno 1 - 10
of 17
pro vyhledávání: '"K. V. Baklashov"'
Publikováno v:
Chemistry and Technology of Fuels and Oils. 42:317-321
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::836c59ace0ef920d85231f64642543c1
https://doi.org/10.1007/s10553-006-0080-5
https://doi.org/10.1007/s10553-006-0080-5
Autor:
V. V. Ezhov, A. S. Levandovskii, V. G. Zaitsev, K. V. Baklashov, V. V. Melekhin, Yu. N. Lebedev, V. V. Napadovskii
Publikováno v:
Chemistry and Technology of Fuels and Oils. 42:325-331
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ef15061879d2536a1eb2ca8061b8e76a
https://doi.org/10.1007/s10553-006-0082-3
https://doi.org/10.1007/s10553-006-0082-3
Autor:
E. V. Karmanov, A. V. Prokopenko, I. A. Zil'berberg, M. N. Rogov, S. I. Myachin, K. V. Baklashov, Yu. N. Lebedev
Publikováno v:
Chemistry and Technology of Fuels and Oils. 42:345-351
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::90da176a8a7fc00357159d99e648b66a
https://doi.org/10.1007/s10553-006-0085-0
https://doi.org/10.1007/s10553-006-0085-0
Autor:
A. S. Levandovskii, Yu. N. Lebedev, K. V. Baklashov, V. V. Ezhov, V. V. Napadovskii, V. G. Chekmenev, V. G. Zaitsev
Publikováno v:
Chemistry and Technology of Fuels and Oils. 40:1-7
A single–tower scheme for atmospheric distillation of crude oil with preliminary separation of naphtha vapors after heating the crude with heat from waste streams is implemented. The unit's equipment corresponds to the current world level. The spec
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f139af42c68885c760527c0c3572b33e
https://doi.org/10.1023/b:cafo.0000021585.44775.1b
https://doi.org/10.1023/b:cafo.0000021585.44775.1b
Autor:
L. L. Man'kovskaya, Yu. N. Lebedev, N. Yu. Krymov, A. G. Sypin, V. S. Lutsik, N. M. Dyurik, K. V. Baklashov, T. M. Zaitseva, S. A. Kotov
Publikováno v:
Chemistry and Technology of Fuels and Oils. 40:14-18
A naphtha cut hydrotreating unit with output of 750,000 tons/year was started up in October 2003 at Slavneft'—Yaroslavnefteorgsintez OJSC. The unit was “turnkey” designed and built by Kedr–89 SIC on order of YaRVAZ CJSC — a subsidiary of Sl
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::68d7a1c2c2813f3d7c7ed647498d93c5
https://doi.org/10.1023/b:cafo.0000021587.54116.5f
https://doi.org/10.1023/b:cafo.0000021587.54116.5f
Autor:
A. A. Melkumyants, Yu. N. Lebedev, K. V. Baklashov, B. S. Zats, M. B. Vikhorev, Ya. P. Lozhkin
Publikováno v:
Chemistry and Technology of Fuels and Oils. 40:19-23
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1ca77133d8c4372ebbc9beb84f7e0cc9
https://doi.org/10.1023/b:cafo.0000021588.30215.d6
https://doi.org/10.1023/b:cafo.0000021588.30215.d6
Autor:
B. A. Isaev, Yu. M. Lebedev, V. N. Nikolaenko, Yu. A. Boiko, V. A. Gnatenko, A. S. Levandovskii, S. P. Leiter, V. A. Gorshkov, K. V. Baklashov
Publikováno v:
Chemistry and Technology of Fuels and Oils. 38:154-157
Acceptance tests were successfully conducted and the unit for production of a high—octane, environmentally clean gasoline additive — methyl tert—butyl ether (MTBE) — with output of 60,000 tons/year in feedstock — the C4 catalytic cut — wa
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::252da38108f0ac1672c148f67fffefae
https://doi.org/10.1023/a:1016200316961
https://doi.org/10.1023/a:1016200316961
Autor:
V. G. Zaitsev, I. A. Ershova, Yu. N. Lebedev, I. N. Lapin, A. S. Fomin, L. P. Razvozzhaev, K. V. Baklashov, V. V. Napadovskii, V. V. Ezhov
Publikováno v:
Chemistry and Technology of Fuels and Oils. 38:8-12
In April 2001, a new naphtha reforming unit with output of 450,000 tons/year having a preliminary hydrotreating unit with output of 600,000 tons/year was started up at Rosneft@apos; Oil Company's Komsomol'sk Refinery.
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::893d496be2a94ff6b1d0a69e5f0f1e12
https://doi.org/10.1023/a:1014952419824
https://doi.org/10.1023/a:1014952419824
Autor:
M. B. Vikhorev, G. P. Strelikov, A. I. Lugovskoi, K. V. Baklashov, Ya. P. Lozhkin, V. M. Kapustin, Yu. N. Lebedev, G. G. Musienko
Publikováno v:
Chemistry and Technology of Fuels and Oils. 38:21-26
The 1A/1M cat cracker at the Ryazan' Refinery OJSC (Tyumen' Oil Company) was exhaustively revamped. This cat cracker, designed by Grozgiproneftekhim in 1960, was started up in 1967. According to the plan, its capacity would be 750,000 tons/year. Afte
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3610d7d92431b9963b6181c2fb533d45
https://doi.org/10.1023/a:1014908604802
https://doi.org/10.1023/a:1014908604802
Autor:
V. V. Melekhin, V. V. Ezhov, A. B. Nikolaev, A. S. Levandovskii, V. V. Napadovskii, V. N. Nikolaenko, K. V. Baklashov, I. N. Lapin, Yu. N. Lebedev, S. A. Oganesyan, V. G. Zaitsev
Publikováno v:
Chemistry and Technology of Fuels and Oils. 38:287-292
TThe first plant in Russia for low—temperature isomerization of pentane—hexane naphtha cuts with a capacity of 100,000 tons/year was started up in May, 2002. Due to the close collaboration of Rosneft' Oil Company — Komsomol'sk Oil Refinery, Ked
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e6825ddcb9133cd20a1a6986a5bc0aba
https://doi.org/10.1023/a:1021253829031
https://doi.org/10.1023/a:1021253829031