Question: 3-8. Develop the recycle structure for the butadiene sulfone process (see Exercise 5.4-9). Assume that HR=48,000Btu/mol,Keq=(6.8461011)exp[36,940/(T(=R)]. k1=(8.1721015)exp[52,200/T(R)], and k1=k1Keq[mol/(ft3hr)] : that the reaction rate corresponds

3-8. Develop the recycle structure for the butadiene sulfone process (see

3-8. Develop the recycle structure for the butadiene sulfone process (see Exercise 5.4-9). Assume that HR=48,000Btu/mol,Keq=(6.8461011)exp[36,940/(T(=R)]. k1=(8.1721015)exp[52,200/T(R)], and k1=k1Keq[mol/(ft3hr)] : that the reaction rate corresponds to the stoichiometry; and that we use a CSTR for the reactor. Consider variable densit y effects and assume that the annualized, installed reactor cost is given by 3150VR0.558[S/(ft3yr)]. Plot the economic potential versus the significant design variables

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