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Problem: A feed mixture with a flow rate of 2 0 0 0 kmo l h , containing components A , B , C ,

Problem:
A feed mixture with a flow rate of 2000kmolh, containing components A,B,C, and D, is provided. The objective for the selected system is to achieve a minimum recovery of 90% of the most volatile component from the feed in the top product. The composition of the mixture, in order of decreasing volatility, is xA=0.40,xB=0.25,xC=0.20, and xD=0.15.
*In the case where the proposed mixture could not lead to the desired minimum recovery of 90%, you may adjust the value(s) accordingly.
The column operates under a pressure of 1 atm absolute, and the feed is in a liquid state at its boiling point at this pressure. Your task is to determine the appropriate operating reflux ratio for the column and provide a justification for your choice.
Assigned alcohol mixture -3,7,11 and 12
\table[[I,Component,Boiling point )],[A,2-methyl-2-propanol,82.0],[B,n-Butanol,117.7],[C,Hexanol,157.0],[D,1-Heptanol,175.8]]Part A (60 marks)
a) Determine the flow rates and compositions of the distillate and bottoms product, indicating the selection of the light key and heavy key components. Specify the source of the utilized K values. (8 marks)
b) Determine the temperatures at the top (dew point) and bottoms product (boiling point).
marks)
c) Calculate the minimum number of stages required. (5 marks)
d) Validate the component distribution using the minimum number of stages obtained in part c).(7 marks)
e) Assess if the obtained dew point, boiling point, and minimum number of stages from part b) need to be revised based on the composition obtained in part d).(7 marks)
f) Calculate the minimum reflux ratio. (5 marks)
g) Determine the operating reflux ratio and justify the chosen value. (8 marks)
h) Calculate the number of theoretical stages and indicate the method used (e.g., ErbarMaddox, Gilliland, or Molokanov).(5 marks)
i) Determine the location of the feed tray. (5 marks)
Part B (40 marks)
To propose a preliminary design of the distillation column, the following elements should be considered:
a) Estimate the column efficiency by taking into account the fluid viscosity and the selected tray type. Provide a justification for the chosen tray type. (6 marks)
b) Calculate the actual number of trays based on the theoretical number of trays and the overall column efficiency. (3 marks)
c) Determine the precise location of the feed tray. (4 marks)
d) Estimate the height of the column. (5 marks)
e) Calculate the diameter of the column based on the ratio of vapor to liquid flow rates. Use a design velocity for the vapor phase that is within the range of 75-85% of the flooding velocity. (10 marks)
2
f) Check for the possibility of weeping. (6 marks)
g) Verify the ratio of column height to diameter. (3 marks)
h) Propose the suitable material for constructing the column and trays, providing a justification for the selection. (3 marks)
Optional (for bonus points):
a) Calculate the reboiler duty and the flow rate of heating element required. Propose the heating element and the condition at which it will be supplied. (10 marks)
b) Calculate the condenser duty and the flow rate of cooling element required. Propose the cooling element and the condition at which it will be supplied. (10 marks)
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