Sergio P.Bressa; Nestor O.Ardiaca; Osvaldo M.Martinez; Guillermo F.Barreto
Sergio P.Bressa; Nestor O.Ardiaca; Osvaldo M.Martinez; Guillermo F.Barreto
摘要: A mathematical model for analyzing and simulating selective hydrogenation of butyne-1 and 1,3-bu-tadiene in industrial
trickle bed reactors operated to obtain high purity butene-1 is presented in this work.From the analysis of typical operating
conditions,only the relevant phenomena are finally retained in the model formulation.The model is then employed to analyze
the effect of operating variables and catalyst selectivity in process performance.In particular,the search for the minimum
hydrogen flow rate necessary to fulfil butene-1 purity specifications is undertaken.