Chenical engineering questionethane is chlorinate in a continuous reactor: c2h6 + cl2 c2h5cl + hcl some of the product monochloroethane is further chlorinated in an undesired side reaction: c2h5cl + cl2 c2h4cl2 + hcl suppose your principal objective is to maximize the selectivity of monochloroethane production relative to dichloroethane. would you design a reactor for a high or low conversion of ethane? explain your answer. (hint: if the reactor contents remained in the reactor long enough for most of the ethane in the feed to be consumed, what would be the main product) what additional processing steps would almost certainly be carried out to make the process economically sound?