For this exercise, the application of a multiple recycle gas compression multistage process is studied. The configuration process together with the main operating conditions of each one of the equipment is shown in the Fig. P1.2. The input stream corresponds to a mole flow rate of 2500 lb mol/ h, at 50 F and 80 psia. The molar composition of the inlet gas is shown in Table P1.1. The goal is to run the simulation and observe the tear streams that the simulator uses to develop the calculation (in the case of Aspen Plus®). Then, select new tear streams, reset the simulation and verify t
For this exercise, the application of a multiple recycle gas compression multistage process is studied. The configuration process together with the main operating conditions of each one of the equipment is shown in the Fig. P1.2. The input stream corresponds to a mole flow rate of 2500 lb mol/ h, at 50 F and 80 psia. The molar composition of the inlet gas is shown in Table P1.1. The goal is to run the simulation and observe the tear streams that the simulator uses to develop the calculation (in the case of Aspen Plus®). Then, select new tear streams, reset the simulation and verify t
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