793 - 804 |
Estimation of boundary layer thickness at side wall of a fully turbulent agitated vessel without baffles Shiobara K, Hiraoka S, Kato Y, Iwata S, Tada Y, Yamaguchi T, Yamamura M |
805 - 807 |
Mass transfer improvement on double-pass laminar counterflow concentric circular mass exchangers with external recycle Ho CD, Ho CL, Tu W |
808 - 816 |
Effect of the composition and coating condition on the structure and performance of catalyst layer of PEFC Komoda Y, Ikeda Y, Suzuki H, Usui H, Ioroi T, Kobayashi T |
817 - 823 |
Dynamic determination of the effluent concentrations of the acetates in an adsorption column packed with zeolite 13X using a gas phase FT-IR Wu CY, Chung CC, Chung TW |
824 - 831 |
Multiple steady-states in a heat integrated distillation column (HIDiC) Kano M, Fukushima T, Makita H, Hasebe S |
832 - 839 |
Nonlinear control design using VRFT Sakamoto M, Hamaguchi T, Ota Y, Hashimoto Y |
840 - 846 |
Prediction of the melt index in a high-density polyethylene process Lee EH, Kim TY, Yeo YK |
847 - 853 |
Sonochemical preparation of gold nanoparticles: Comparison with the thermal reduction system Shimazaki Y, Ando C, Saeki S, Kobayashi Y, Konno M |
854 - 859 |
A continuous production method of nano-particles of leucine by controlled nucleation and growth in ternary systems Marui Y, Funakoshi K, Sawada T, Matsuoka M |
860 - 868 |
New nickel-based catalyst for tar reforming, with superior resistance to coking and sulfur poisoning in biomass gasification processes Sato K, Shinoda T, Fujimoto K |
869 - 873 |
Emission behavior of condensable suspended particulate matter from a laboratory scale RDF fluidized bed combustor Tsukada M, Horikawa A, Sugimoto K, Abe K, Wada M, Liu YY, Kamiya H |
874 - 878 |
Hydrothermal dechlorination of a reclaimed oil in a continuous packed-bed reactor Akimoto M, Iida T, Sato S |