1 |
Liquid-Liquid Equilibria for the n-Pentyl acetate, n-Hexyl acetate, n-Pentanol, or n-Hexanol plus Furfural plus Water Systems at 298 and 323 K Mikola M, Kangas J, Pokki JP, Mannisto M, Ahola J, Tanskanen J, Alopaeus V Journal of Chemical and Engineering Data, 66(1), 210, 2021 |
2 |
A discretized model for enzymatic hydrolysis of cellulose in a fed-batch process Tervasmaki P, Sotaniemi V, Kangas J, Taskila S, Ojamo H, Tanskanen J Bioresource Technology, 227, 112, 2017 |
3 |
Mixture adsorption on zeolites applying the p(i)(sat) temperature-dependency approach Leppajarvi T, Kangas J, Malinen I, Tanskanen J Chemical Engineering Science, 89, 89, 2013 |
4 |
Maxwell-Stefan modeling of the separation of H-2 and CO2 at high pressure in an MFI membrane Kangas J, Sandstrom L, Malinen I, Hedlund J, Tanskanen J Journal of Membrane Science, 435, 186, 2013 |
5 |
Utilization of P-i(sat) temperature-dependency in modelling adsorption on zeolites Leppajarvi T, Malinen I, Kangas J, Tanskanen J Chemical Engineering Science, 69(1), 503, 2012 |
6 |
A new Newton homotopy based method for the robust determination of all the stationary points of the tangent plane distance function Malinen I, Kangas J, Tanskanen J Chemical Engineering Science, 84, 266, 2012 |
7 |
Modified Bounded Homotopies in the Solving of Phase Stability Problems for Liquid-Liquid Phase-Splitting Calculations Kangas J, Malinen I, Tanskanen J Industrial & Engineering Chemistry Research, 50(11), 7003, 2011 |