| 1 |
Novel system configuration with activated sludge like-geometry to develop aerobic granular biomass under continuous flow
Cofre C, Campos JL, Valenzuela-Heredia D, Pavissich JP, Camus N, Belmonte M, Pedrouso A, Carrera P, Mosquera-Corral A, Val del Rio A
Bioresource Technology, 267, 778, 2018 |
| 2 |
Solugas - Comprehensive analysis of the solar hybrid Brayton plant
Korzynietz R, Brioso JA, del Rio A, Quero M, Gallas M, Uhlig R, Ebert M, Buck R, Teraji D
Solar Energy, 135, 578, 2016 |
| 3 |
Vapor-liquid equilibria for the binary system 2,2-dimethylbutane plus 1,1-dimethylpropyl methyl ether (TAME) at 298.15, 318.15, and 338.15 K
del Rio A, Coto B, Renuncio JAR, Pando C
Fluid Phase Equilibria, 221(1-2), 1, 2004 |
| 4 |
Vapor-liquid equilibria for the binary system hexan-1-ol plus tert-butyl methyl ether (MTBE) at 298.15, 318.15, and 338.15 K
de Llano JJ, Segade L, Jimenez E, del Rio A, Renuncio JAR, Pando C
Fluid Phase Equilibria, 208(1-2), 115, 2003 |
| 5 |
Vapor-liquid equilibria and excess properties of octane+1,1-dimethylpropyl methyl ether (TAME) mixtures
del Rio A, Coto B, Pando C, Renuncio JAR
Fluid Phase Equilibria, 200(1), 41, 2002 |
| 6 |
Vapor-liquid equilibria for the binary system hexane+1,1-dimethylpropyl methyl ether at 298.15, 308.15, 318.15, and 328.15 K
del Rio A, Coto B, Pando C, Renuncio JAR
Industrial & Engineering Chemistry Research, 41(5), 1364, 2002 |
| 7 |
Vapor-liquid equilibria for the binary systems decane+1, 1-dimethylethyl methyl ether (MTBE) and decane+1, 1-dimethylpropyl methyl ether (TAME) at 308.15, 318.15 and 328.15 K
del Rio A, Coto B, Pando C, Renuncio JAR
Fluid Phase Equilibria, 187-188, 299, 2001 |
| 8 |
Vapor-liquid equilibria and excess properties of cyclohexane-1,1-dimethylpropyl methyl ether (TAME) mixtures
del Rio A, Coto B, Pando C, Renuncio JAR
Industrial & Engineering Chemistry Research, 40(2), 689, 2001 |
