| 1 |
High-pressure C-H-O diagrams: Fuel composition, carbon deposition, and open circuit voltage of pressurized SOFCs
Muramoto A, Kikuchi Y, Tachikawa Y, Lyth SM, Shiratori Y, Taniguchi S, Sasaki K
International Journal of Hydrogen Energy, 42(52), 30769, 2017 |
| 2 |
Pressure dependence of equilibrium melting temperature of poly (lactic acid)
Rohindra D, Kuboyama K, Ougizawa T
Polymer, 118, 297, 2017 |
| 3 |
High pressure vapor-liquid equilibria for binary methane and protic ionic liquid based on propionate anions
Oliveira LMC, Ribeiro FRG, Alcantara ML, Pisoni GO, Cabral VF, Cardozo-Filho L, Mattedi S
Fluid Phase Equilibria, 426, 65, 2016 |
| 4 |
Quantitative Raman spectroscopic investigation of geo-fluids high-pressure phase equilibria: Part II. Accurate determination of CH4 solubility in water from 273 to 603 K and from 5 to 140 MPa and refining the parameters of the thermodynamic model
Ou WJ, Geng LT, Lu WJ, Guo HR, Qu K, Mao PX
Fluid Phase Equilibria, 391, 18, 2015 |
| 5 |
Quantitative Raman spectroscopic investigation of geo-fluids high-pressure phase equilibria: Part I. Accurate calibration and determination of CO2 solubility in water from 273.15 to 573.15 K and from 10 to 120 MPa
Guo HR, Chen Y, Hu QC, Lu WJ, Ou WJ, Geng LT
Fluid Phase Equilibria, 382, 70, 2014 |
| 6 |
Exploration of the effect of process variables on the production of high-value fuel gas from glucose via supercritical water gasification
Hendry D, Venkitasamy C, Wilkinson N, Jacoby W
Bioresource Technology, 102(3), 3480, 2011 |
| 7 |
High-pressure phase equilibrium of the ternary system carbon dioxide plus water plus acetic acid at temperatures from 313 to 353 K
Bamberger A, Sieder G, Maurer G
Journal of Supercritical Fluids, 32(1-3), 15, 2004 |
