| 937 - 944 |
The potential of energy saving by gas-phase adsorption processes
Mersmann A, Fill B, Hartmann R, Maurer S |
| 945 - 949 |
Modeling of coagulation processes with the aid of population balances
Schuetz S, Piesche M |
| 949 - 952 |
On the solubility of sour gases in aqueous electrolyte solutions: New experimental data and correlation
Xia JZ, Kamps APS, Rumpf B, Maurer G |
| 952 - 955 |
Telomerization of carbon dioxide and 1,3-butadiene: Process development in a miniplant
Behr A, Heite M |
| 956 - 959 |
Chemisorption of N2O and H-2 for the surface determination of copper catalysts
Hinrichsen O, Genger T, Muhler M |
| 959 - 964 |
Development of ceramic membranes and adsorbents from silicon-organic precursors
Schmidt H, Koch D, Grathwohl G |
| 964 - 967 |
Chemical modification of poly(styrene-co-acrylonitrile) in a melt
Becker H, Merayo N, Schmidt-Naake G |
| 967 - 971 |
Biological nitrogen removal from wastewater of the metal-working industry
Buchheister F, Schuch R, Winter J |
| 973 - 983 |
3-D finite element analysis of a hydrogenation reactor
Holzl R |
| 985 - 995 |
Modeling flow distribution for internally manifolded direct methanol fuel cell stacks
Argyropoulos P, Scott K, Taama WM |
| 997 - 999 |
Emission of high-quality pipework flange gaskets
Bathen D, Hummelt C, Meisel J, Hofmann S |
| 1001 - 1005 |
Identical feed drops in a flow vessel may not always be desirable
Das PK |
| 1007 - 1012 |
Heavy metal adsorption to a chelating resin in a binary solid fluidized bed
Yang JZ, Renken A |
| 1013 - 1020 |
Wood hydrolysis and hydrolysate detoxification for subsequent xylitol production
Converti A, Dominguez JM, Perego P, da Silva SS, Zilli M |
| 1021 - 1026 |
Systems with structured packing: Fluid-dynamics and liquid-solid mass transfer
Cavatorta ON, Bohm U |
