Publication Details (including relevant citation information):
The publication describes results of an extension of the research of new compact type of Fischer-Tropsch reactor. A catalytic bed of the reactor had been named plug-through contactor membranes (PCM). Geometry of the bed had been chosen in favour of radial.
The Fischer-Tropsch synthesis using a contactor membrane reactor was studied varying pore size distribution parameters and membrane geometry. These parameters are responsible for the magnitude of the diffusion constrains and, therefore, correlate with the FTS process productivity and selectivity. The nature of the observed correlations is discussed.
Address (URL): http://www.springerlink.com/content/ltp72xv545291661/