1 |
Optimal Operation of Simulated Moving Bed Technology on Utilization of Naphtha Resource Cao J, Shen BX, Liu JC Separation Science and Technology, 48(2), 246, 2012 |
2 |
Suitable catalysts for hydroisomerization of long-chain normal paraffins Deldari H Applied Catalysis A: General, 293, 1, 2005 |
3 |
Hybrid zirconia catalysts for conversion of Fischer-Tropsch waxy products to transportation fuels Zhou Z, Zhang YL, Tierney JW, Wender I Fuel Processing Technology, 83(1-3), 67, 2003 |
4 |
Anion-modified zirconia: effect of metal promotion and hydrogen reduction on hydroisomerization of n-hexadecane and Fischer-Tropsch waxes Zhang SG, Zhang YL, Tierney JW, Wender I Fuel Processing Technology, 69(1), 59, 2001 |
5 |
In situ observation of the two-dimensional crystals of alkanes on a reconstructed Au(100)) surface in neat liquid by scanning tunneling microscopy Yamada R, Uosaki K Langmuir, 16(10), 4413, 2000 |
6 |
Correlation for gas-liquid equilibrium prediction in Fischer-Tropsch synthesis Wang YN, Li YW, Bai L, Zhao YL, Zhang BJ Fuel, 78(8), 911, 1999 |
7 |
High-pressure solubilities of hydrogen, nitrogen, and carbon monoxide iu dodecane from 344 to 410 K at pressures to 13.2 MPa Gao W, Robinson RL, Gasem KAM Journal of Chemical and Engineering Data, 44(1), 130, 1999 |
8 |
Crystalline bilayers in the very long chain n-alkanoic acid C191H383COOH Ungar G, Zeng XB Macromolecules, 32(10), 3543, 1999 |
9 |
Prediction of vapor-liquid equilibria for asymmetric systems at low and high pressures with the PSRK model Li JD, Fischer K, Gmehling J Fluid Phase Equilibria, 143(1-2), 71, 1998 |
10 |
Solubility of carbon dioxide in eicosane, docosane, tetracosane, and octacosane at temperatures from 323 to 473 K and pressures up to 40 MPa Sato Y, Tagashira Y, Maruyama D, Takishima S, Masuoka H Fluid Phase Equilibria, 147(1-2), 181, 1998 |