The benzene compound was chosen for use in the aspen plus program. Chemical compound Y $($which is in the vapor phase$)$ is required to be cooled with two coolants between stages according to the following specifications: The stream from the first refrigerant should be in the vapor phase but the temperature should be reduced. In the second stage, the outgoing stream is expected to be in liquid phase only. more details The feed enters the first coolant at a pressure of $10$ bar and a temperature $40\backslash$deg C higher than its boiling point at the specified pressure. Pressure must be maintained at $10$ bar for all refrigerants. Feed mass flow rate is $500$ kg$/$hour$.$ Questions: $1.$ Use Aspen Plus to obtain photovoltaic, TV$,$ and PT diagrams and explain each of them using Excel. I want a diagram for this process. $2.$ Using the chart you obtained above, determine the inlet and outlet temperatures for each of the three coolers. $3.$ Simulating the process in the Aspen Plus environment and a screenshot of the benzene process simulation. $4.$ What are the power requirements for each stage? $5.$ How can you verify the results obtained from your Aspen Plus simulation. $6.$ Explain the effect of increasing the pressure in both coolers to $20$ bar.The benzene compound was chosen for use in the aspen plus program. Chemical compound Y $($which is in the vapor phase$)$ is required to be cooled with two coolants between stages according to the following specifications: The stream from the first refrigerant should be in the vapor phase but the temperature should be reduced. In the second stage, the outgoing stream is expected to be in liquid phase only. more details The feed enters the first coolant at a pressure of $10$ bar and a temperature $40\backslash$deg C higher than its boiling point at the specified pressure. Pressure must be maintained at $10$ bar for all refrigerants. Feed mass flow rate is $500$ kg$/$hour$.$ Questions: $1.$ Use Aspen Plus to obtain photovoltaic, TV$,$ and PT diagrams and explain each of them using Excel. I want a diagram for this process. $2.$ Using the chart you obtained above, determine the inlet and outlet temperatures for each of the three coolers. $3.$ Simulating the process in the Aspen Plus environment and a screenshot of the benzene process simulation. $4.$ What are the power requirements for each stage? $5.$ How can you verify the results obtained from your Aspen Plus simulation. $6.$ Explain the effect of increasing the press

ure

Problem Statement

It is required to cool a chemical compound $Y($which is in vapor phase$)$ with $2$ interstage coolers according to the following specification:

The outlet stream from the first cooler should be in vapor phase but the temperature should be reduced.

In the second stage, the outlet stream is expected to be in liquid only phase.

Further details

The feed enters the first cooler at a pressure of $\frac{10}{b}ar$ and a temperature, which is $40C$ above its boiling point at the given pressure.

The pressure should be maintained at $10$ bar for all the coolers.

The mass flowrate of the feed is $500k\frac{g}{h}.$

Questions:

Use Aspen Plus to obtain PV$,$ TV and PT diagrams and explain each of them.

Using the diagram you obtained above, determine the entry and exit temperature in each of the three coolers.

Simulate the process in Aspen Plus environment.

What is the power requirement for each of the stages.

How would you verify the results obtained from your Aspen Plus simulation.

Explain the effect of increasing the pressure in each of the cooler to $20$ bar. in both coolers to $20$ bar.$($

Notes I want all answers to contain screenshots from the program...And use Excel to create charts$)$