Zobrazeno 1 - 10
of 27
pro vyhledávání: '"Zhongxi Chao"'
Publikováno v:
14754-14765
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research
In this work, a computational fluid dynamics simulator has been developed for a novel double-loop circulating fluidized bed reactor which is used for a chemical looping combustion process. The simulator is implemented in an in-house code including th
Publikováno v:
In Chemical Engineering Journal 2005 106(1):43-52
Modelling of binary fluidized bed reactors for the sorption-enhanced steam methane reforming process
Publikováno v:
The Canadian Journal of Chemical Engineering. 95:157-169
Publikováno v:
Advances in Engineering Software. 80:156-173
A dynamic one-dimensional multicomponent model for two-phase flows which includes heat- and mass transfer processes are studied in the Euler framework. The model is intended for reactive gas-solid flows in bubbling fluidized bed reactors. A model is
Publikováno v:
Powder Technology
A multiphase CFD model has been developed and implemented in an in-house code for a coupled double loop circulation fluidized bed (DLCFB) reactor which can be utilized for the chemical looping combustion process. The air reactor and the fuel reactor
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::413369838ff22b31df210e754ccb754d
http://hdl.handle.net/11250/2492441
http://hdl.handle.net/11250/2492441
Publikováno v:
Chemical Engineering Journal
A reactive CFD model has been developed and implemented numerically in an in-house code for a coupled double loop circulation fluidized bed reactor. In the current work it is utilized for the chemical looping combustion (CLC) process but the model ca
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::40dceb24fcb24a06aaea36272d37eee2
http://hdl.handle.net/11250/2492439
http://hdl.handle.net/11250/2492439
Publikováno v:
Fuel Processing Technology. 125:290-300
The aim of the present study is to investigate the performance of a dynamic one-dimensional multi-component model for two-phase flows which includes heat- and mass transfer processes. The model is intended for reactive gas–solid flows in bubbling f
Publikováno v:
The Canadian Journal of Chemical Engineering. 92:401-420
Computational demanding two- and three-dimensional two-fluid models are frequently adopted simulating gas–solid flows in fluidised beds. Reduced computational cost is favourable for efficient numerical studies of technologies such as the novel chem
Publikováno v:
Powder Technology. 224:311-322
The behavior of seven binary particle drag closures from the literatures which have been derived based on the kinetic theory of granular flows (KTGF) for the application to fluidized beds are investigated using a binary KTGF model. The dynamic size s
Publikováno v:
Particuology. 10:62-71
This paper presents simulation results of the density segregation in a dense binary gas fluidized bed using a multi-fluid model from Chao et al. (2011). The segregation behavior of two types of particles with approximately same particle diameters and