
Concept explainers
(a)
Interpretation:
The temperature at which the first drop of condensate forms along with its composition is to be determined.
Concept introduction:
Dew-point temperature is the temperature at which the first drop of liquid appears when a vapor is cooled slowly at the constant pressure. At this point the condensation starts.
Using a
(b)
Interpretation:
The vapor and liquid phase mole fractions of benzene and toluene are to be determined. Also, the ratio of total moles in vapor to the total moles in liquid is to be calculated.
Concept introduction:
Dew-point temperature is the temperature at which the first drop of liquid appears when a vapor is cooled slowly at the constant pressure. At this point the condensation starts.
Using a
A flowchart is the complete representation of a process through boxes or other shapes which represents process units and arrows that represents the input and output of the process. The flowchart must be fully labelled to infer important data about the process involved.
In a system, a conserved quantity (total mass, mass of a particular species, energy or momentum) is balanced and can be written as:
Here, ‘input’ is the stream which enters the system. ‘generation’ is the term used for the quantity that is produced within the system. ‘output’ is the stream which leaves the system. ‘consumption’ is the term used for the quantity that is consumed within the system. ‘accumulation’ is used for the quantity which is builds up within the system.
All the equations which are formed are then solved simultaneously to calculate the values of the unknown variables.
(c)
Interpretation:
The temperature at which the last bubble of the vapor condense is to be determined. Also, it composition is to be calculated.
Concept introduction:
Dew-point temperature is the temperature at which the first drop of liquid appears when a vapor is cooled slowly at the constant pressure. At this point the condensation starts.
Using a

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Chapter 6 Solutions
ELEM.PRIN.OF CHEMICAL...ABRIDGED (LL)
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- Bioprocessing/ Protein isolation and purification. Develop a purification train for a facility where first process is a perfusion upstream bioreactors 500L producing low cell culture titer of approx. 0.5 g/L perfusing at 2 VVD over 30 days. The current facility has a secondary clarification process for the perfusate coming from the bioreactor. Secondary depth filtration clarification capacity of 200 L/m2. Identify the correct filter area, and system (pump) requirements for the process scale. Also identify optimal flowrates for flushing and processing, total process time, buffer volumes required. Assume 10 L/m2 holdup of the depth filters identify the size of the tank required to collect the filtrate. Average yield of overall clarification is 80% estimate the titer in the clarified pool.arrow_forwardsolve for both a stripper and absorber. take the equilibrium data given to just be a y=x linearrow_forwardsolve all parts plsarrow_forward
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