Zobrazeno 1 - 10
of 14
pro vyhledávání: '"Haidar Taofeeq"'
Publikováno v:
Chemical Engineering & Technology. 45:220-229
Autor:
A. Al-Farraji, Haidar Taofeeq
Publikováno v:
Chinese Journal of Chemical Engineering. 28:2985-2992
The impact of temperature and particle size on minimum fluidizing velocity was studied and analyzed in a small pilot scale of bubbling fluidized bed reactor. This study was devoted to providing some data about fluidization to the literature under hig
Autor:
Muthanna H. Al-Dahhan, Haidar Taofeeq
Publikováno v:
International Journal of Thermal Sciences. 135:546-558
In this work, the influence of the vertical tube diameter on the performance of the heat transfer is conducted in a gas-solid fluidized bed of 0.14 m inside diameter. The heat transfer coefficient is measured using an advanced fast-response heat tran
Publikováno v:
The Canadian Journal of Chemical Engineering. 100
Publikováno v:
Flow Measurement and Instrumentation. 85:102169
Autor:
Muthanna H. Al-Dahhan, Haidar Taofeeq
Publikováno v:
Chemical Engineering Research and Design. 138:87-104
In this work, the impact of the vertical internals on the flow regimes and their transition velocities has been studied in a 0.14 m inside diameter gas–solid fluidized bed. The identification of the flow regimes was accomplished statistically (stan
Publikováno v:
Flow Measurement and Instrumentation. 63:18-32
Advanced gas-solid optical fiber probe technique that can measure simultaneously solids velocity, solids concentration related quantity, and their time series fluctuations has been implemented with simple and new calibration methods for both solids h
Autor:
Haidar Taofeeq, Muthanna H. Al-Dahhan
Publikováno v:
Advanced Powder Technology. 29:2548-2567
The effect of a circular configuration of intense vertical immersed tubes on the hydrodynamic parameters has been investigated in a gas-solid fluidized bed of 0.14 m inside diameter. The experiments were performed using glass beads solid particles of
Autor:
Haidar Taofeeq, Muthanna H. Al-Dahhan
Publikováno v:
International Journal of Heat and Mass Transfer. 122:229-251
An investigation of the influence of a bundle of intense vertical immersed tubes on the local heat transfer coefficients and related gas hydrodynamics of bubble frequency and gas holdup was conducted in a gas-solid fluidized bed of 0.14 m inside diam