Abstract
The paper considers the possibility of involving additional butane-butylene feedstock in the MTBE synthesis and oligomerization unit. An important factor is the content of diene hydrocarbons in BBF, which negatively affects the activity of the catalyst and accordingly the product yield of the unit. In this connection possibility of implementation of selective hydrogenation process was analyzed in order to improve quality of feedstock in terms of target components of MTBE and oligomerizate synthesis. Calculations of process in specialized software were carried out.
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