By Jiatao Zhang
Chemical Engineering III contains the lawsuits of the third SREE convention on Chemical Engineering (CCE 2013, Hong Kong, 28-29 December 2013) and the second SREE Workshop on power, atmosphere and Engineering (WEEE 2013, which used to be part of CCE 2013).
The contributions speak about present useful demanding situations and strategies in Chemical Engineering, and canopy quite a lot of topics:
Chemical engineering and environment
Oil and fuel engineering
Chemical Engineering III can be useful to engineers and lecturers concerned or drawn to those components.
Read Online or Download Chemical Engineering III PDF
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Additional info for Chemical Engineering III
B. J Hoebink, J. R. H. Ross, TAP investigations of the CO2 reforming of CH4 over Pt/ZrO2 , J. Catal. 166: 306, 1997. I. M. Bodrov, L. O. Apel’baum, M. L. Temkin, Kinetics of the reaction of methane with water vapor, catalysed by nickel on a porous carrier, Kinet. Katal. 8: 821, 1967. J. H. Bitter, K. Seshan, J. A. Lercher, Mono and Bifunctional pathways of CO2 /CH4 reformng over Pt and Rh based catalysts, J. Catal. 176: 293, 1998. V. A. Tsipouriari, X. E. Verykios, Carbon and oxygen reaction pathways of CO2 reforming of methane over Ni/La2 O3 and Ni/Al2 O3 catalysts studied by isotopic tracing techniques, J.
Hangzhou: Zhejiang University Press. Jayakumar, N. S. & Farouq, S. M. 2008. The Dynamics of Liquid Cooling in Half-coil Jackets. Chemical Product and Process Modeling 3(1): 1–16. Li, Y. X. & Wu, J. H. 2010. Numerical Research on Fluid Turbulent Flow and Heat Transfer in the Half-coil Jackets. The Chin. J. of Process Eng. 10(4): 644–649. Li, Y. X. & Wu, J. H. 2011. Flow Characteristics of Turbulent Fluid in the Inner Half-coil Jackets of an Autoclave. The Chin. J. of Process Eng. 11(6): 913–918.
Mesh model of the separator. 2 Subsea gas-liquid hydrocyclone separator grid model By three-dimensional modeling software (UG) to complete simplifies 3D model of the separator, use an intermediate format file into CFD pre-processing analysis software in GAMBIT. The mesh model id shown in Figure 2. 3 Turbulence model of the subsea gas-liquid hydrocyclone separator Currently the widely used turbulence models are standard K-ε model, RNG K-ε model and the Reynolds stress model (RSM). Standard K-ε model is based on isotropic turbulence model, its simulation result error of separator flow field is large (Shan Yongbo, 2005).
Chemical Engineering III by Jiatao Zhang