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S.S. Zabrodskii (1971)
Vysokotemperaturnye ustanovki s psevdoozhizhennym sloem
(2013)
Energy and resource saving tech nology for batch preparation and coke cooling in Rus sia
S.S. Kutateladze (1990)
Teploperedacha i gidrodinamicheskoe soprotivlenie: spravochnoe posobie
(2005)
New energy saving technologies in coke production
N.P. Shamanov, A.N. Dyadik, A.Yu. Labinskii (1988)
Dvukhfaznye struinye apparaty
L. Zabezhinskiy (2013)
Energy- and resource-saving technology for batch preparation and coke cooling in RussiaCoke and Chemistry, 56
(1968)
Influence of a rough surface on the radiant properties, Teplofiz
Kuppan Thulukkanam (2013)
Heat Exchanger Design Handbook
(2005)
New energy saving technologies in coke production, Prom
(1971)
Vysokotemperaturnye ustanovki s psev doozhizhennym sloem (High Temperature Fluidized Bed System)
S.G. Agababov (1968)
Influence of a rough surface on the radiant propertiesTeplofiz. Vys. Temp., 8
M.N. Ivanovskii, V.P. Sorokin, I.V. Yagodkin (1978)
Fizicheskie osnovy teplovykh trub
A.F. Chudnovskii (1962)
Teplofizicheskie kharakteristiki dispersnykh materialov
(1992)
Research on systems for combined thermal preparation of coal batch and coke slaking
(1962)
Teplofizicheskie kharakteristiki dis persnykh materialov (Thermophysical Characteristics of Disperse Materials)
A.A. Agroskin, V.B. Gleibman (1980)
Teplofizika tverdogo topliva
(1978)
Fizicheskie osnovy teplovykh trub (Physical Principles of Thermal Tubes)
R. Siegel, J. Howell, M. Mengüç (2020)
Thermal Radiation Heat Transfer
(1997)
Computer analysis of the heat transfer in an ETK boiler with a moving bed of disperse material, Inzh
(1964)
Teploperedacha (Heat Transfer)
A.G. Z. Yu.A. Blokh, L.N. Ryzhkov (1991)
Teploobmen izlucheniem: spravochnik
S.N. Shorin (1964)
Teploperedacha
A.V. Lykov (1967)
Teoriya teploprovodnosti
(1992)
Yu.N., Research on systems for combined thermal preparation of coal batch and coke slaking
(1991)
Teploobmen izlucheniem: spravochnik (Radiant Heat Transfer: A Handbook)
Heat transfer within hybrid boilers for preliminary batch heating and radiant cooling of coke is considered. On the basis of experiments on an industrial prototype and model calculations, reliable values are obtained for the heat-transfer coefficients between the free-flowing material and thermal tubes. From the heat balance, the final temperature of the batch and coke is determined. In a flow-through heat exchanger, the excess heat from the coke is transmitted to water (steam) that is sent to a steam turbine for power generation. Recommendations are made regarding the heat-exchanger structure.
Coke and Chemistry – Springer Journals
Published: Nov 12, 2015
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