Abstract
A promising direction in processes of general organic synthesis is use of bioethanol as a raw material for production of ethylacetate. The article is devoted to the development and modeling of the reaction-rectification process to produce ethyl acetate by dehydrogenation of ethanol, which will allow combining in one apparatus the chemical conversion and separation of the resulting reaction mixture by rectification, reducing the cost of carrying out the process and increasing the main parameters of the process. As part of the work, the collection and processing of physicochemical information about the components of the reaction mixture was carried out, a mathematical model of the process was developed, based on which the development and modeling of the technological scheme were carried out, the parameters and indicators of the process were determined
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