Abstract
The dependence of the selectivity and output capacity of the Fischer Tropsch process with respect to liquid and solid hydrocarbons on pore structure parameters of a catalyst was determined for the example of a cobalt catalyst produced by impregnation of a preformed aluminosilicate support. The results obtained are analyzed in terms of the diffusion-kinetic theory.
Full Text 
Sign-in/Register to access full text options
Sign-in/Register to access full text options 
Published version (
Free)
Free) 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a call
