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Carotenoids Particle Formation by Supercritical Fluid Technologies 被引量:7
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作者 全灿 Johan Carlfors Charlotta Turner 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2009年第2期344-349,共6页
Based on the solubility in supercritical CO2,two strategies in which CO2 plays different roles are used to make quercetine and astaxanthin particles by supercritical fluid technologies.The experimental results showed ... Based on the solubility in supercritical CO2,two strategies in which CO2 plays different roles are used to make quercetine and astaxanthin particles by supercritical fluid technologies.The experimental results showed that micronized quercetine particles with mean particle size of 1.0-1.5 μm can be made via solution enhanced dispersion by supercritical fluids(SEDS) process,in which CO2 worked as turbulent anti-solvent;while for astaxanthin,micronized particles with mean particle size of 0.3-0.8 μm were also made successfully by rapid expansion supercritical solution(RESS) process. 展开更多
关键词 quercetine ASTAXANTHIN rapid expansion of supercritical solution solution enhanced dispersion by supercritical fluids particle formation
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Experimental study and characteristic finite element simulation of solute transport in a cross-fracture 被引量:1
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作者 Long-fei Chen yong Huang 《Geoscience Frontiers》 SCIE CAS CSCD 2016年第6期963-967,共5页
A new method, the characteristic finite element method (CFEM), was developed to simulate solute transport in a cross-fracture. The solution of this mathematical model for solute transport considered that the contrib... A new method, the characteristic finite element method (CFEM), was developed to simulate solute transport in a cross-fracture. The solution of this mathematical model for solute transport considered that the contribution of convection and dispersion terms was deduced using the single-step, trace-back method and routine finite element method (FEM). Also, experimental models were designed to verify the reliability and validity of the CFEM. Results showed that experimental data from a single fracture model agreed with numerical simulations obtained from the use of the CFEM. However, routine FEM caused numerical oscillation and dispersion during the calculation of solute concentration. Furthermore, in this cross-fracture model, CFEM simulation results predicted that the arrival time of concentration peak values decreased with increasing flux. Also, the second concentration peak value was obvious with the decrease of flux, which may have resulted from the convergence of solute concentrations from main, and branch, fractures. 展开更多
关键词 Solute transport Cross-fracture CFEM Dispersion
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