The following reaction occurs in an isothermal constant-volume batch reactor: A → R A → S A → T A → U with k₁ = 0.05 min¯¹, k₂ = = 0.025 min-¹, k3 = 0.015 min¯¹, and k = 0.008 min¹ are the kinetic constants of the first, second, third, and fourth reaction, respectively. Pure A is charged mol

Summarize your answers in the table provided. Attach a legible and answer sheet upon submission. Points may not be given to any item without a clea unless it is not necessary. Answers with erasures will not be considered. PROBLEM 6.1. Production of Trichloroethylene Trichloroethylene, a widely used degreasing solvent for machine parts, is produced in a two-step reaction sequence. Ethylene is first chlorinated to yield terachloroethane, which is dehydrochlorinated to form trichloroethyle. C₂H4(g) + 2 Cl2(g) → C₂H₂C14(1) + H₂(g) (AH)1=-385.76 kJ/mol C₂H2C14(1)→ C2HCl3(1) + HCl(g) gladins The standard heat of formation of liquid trichloroethylene is -276.2 kJ/mol. Reaction 1: Reaction 2: (W) Enthalpy Values and Standard Heats of Reaction Component AH (kJ/mol) C₂H4(g) Cl₂(g) H₂(g) HCl(g) C₂H₂C14(1) C₂HCl3 (1) Q (kW) Reaction Reaction 1 Reaction 2 (VD) TUO Hn lato T (WA) veisdial (lom\34) H dom) a Assuming W, APE, and AKE are negligible, determine the amount of heat (Q) evolved if 300 mol/h…

Determine the number of trays that is required in a distilling column to separate a benzene- toluene binary mixture. The theoretical no. of stages is 8.2. The equipment was designed with a partial condenser and a reboiler. The optimum feed location is at 5.2, and the theoretical feed location is at 2.8 from the partial condenser at the top.

Thank you for you reply I appreciate it. Would you be able to expand on what you did for the integration at the for Part A please?