Author:
Blyton Christopher A.J.,Bryant Steven L.
Funder
University of Texas at Austin (BP, Chevron, ExxonMobil, Foundation CMG, Statoil and the USGS)
Subject
Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Reference43 articles.
1. High-pressure (vapor+liquid) equilibrium in binary mixtures of (carbon dioxide+water or acetic acid) at temperatures from 313 to 353K;Bamberger;J. Supercritical Fluids,2000
2. Air entrainment in baffled stirred tanks;Bhattacharya;Chem. Eng. Res. Des.,2007
3. Blyton, C. 2012. Kinetics of CO2 Dissolution in Brine: Experimental Measurement and Application to Geologic Storage. MS Thesis, The University of Texas at Austin.
4. Blyton, C., Bryant, S. 2012. Mass transfer coefficient for carbon dioxide dissolution into brine. Presented at the 11th Greenhouse Gas Control Technologies Conference, Kyoto, Japan, November 10–12.
5. Boogerd, F.C., Bos, P., Kuenen, J.G., Heijnen, J.J., R.G. van der Lans, 1990. Oxygen and carbon dioxide mass transfer and the aerobic, autotrophic cultivation of moderate and extreme thermophiles: a case study related to the microbial desulfurization of coal. Biotechnology and Bioengineering, 35, 1111–1119.
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