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Economic trade-offs in acrylic acid reactor design
Affiliation:1. Faculty of Chemistry, Nicolaus Copernicus University in Torun, 87-100, Torun, Poland;2. Chem. Dept. University of Copenhagen. Universitetsparken 5, 2100 Copenhagen, Denmark;1. Instituto de Química, UNESP - Universidade Estadual Paulista, Prof. Francisco Degni 55, 14800-060, Araraquara-SP, Brazil;2. Instituto de Investigaciones en Catálisis y Petroquímica, Santiago del Estero 2654, Santa Fé, Argentina
Abstract:The acrylic acid process using air oxidation of propylene presents many interesting design trade-offs, particularly in the design of the reactor. The desired and undesired reactions are highly exothermic and very temperature dependent (large activation energies), so a large flowrate of inert water is also fed to the reactor to act as a thermal sink. Propylene conversion increases with temperature and reactor size, but acrylic acid yield decreases with increasing temperature. The heat of reaction is removed by generaing steam, and the steam pressure is an important design optimization variable since it sets low limits on reactor temperature. Using low-pressure steam gives high acrylic acid yield and lower carbon dioxide generation but requires large reactors. Larger air flowrates increase reactor oxygen concentrations, which reduce reactor volume but increase air compression costs.This paper explores the effects of the many design trade-offs on capital investment, energy cost and product selectivity.
Keywords:Acrylic acid  Reactor design  Reactor design trade-offs
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