Q. The point where A and B rich solubility curve merge is known as _________

View solution

Q. Justify that X represents heterogeneity of the solution.

View solution

Q. Find LPM in the below one pair partially miscible ternary diagram.
Where, A,B,C are the pure components

View solution

Q. Find the sum of R and E if the sum of F and S is 80 kmol.

View solution

Q. Find the process.

View solution

Q. Find the rate of extract in mol/hr if

View solution

Q. If the pure solvent is used, find the value of “ys” by analysing the below single stage extractor.
Where, F,S are feed and solvent

View solution

Q. By analysing this extraction equilibrium triangle, find the solvent requirement range.

View solution

Q. Find the mixture M in kg if R is 4 kg and E is 10 kg, where E is extract and R is raffinate.

View solution

Q. Find the representation A for extraction process.

View solution

Q. Find the representation X.

View solution

Q. Differential contractors are continuous extractor.

View solution

Q. The high density difference among the liquid in the extractor cause ________

View solution

Q. Motivational force in a differential contractor is

View solution

Q. Packed tower with ________ packing preferable for liquid extraction.

View solution

Q. _____________ mixing is applicable for differential contractors.

View solution

Q. If a system has low interfacial tension _________ extractor is preferred.

View solution

Q. The extractor preferred for getting immediate dispersion after piping is ___________________

View solution

Q. More than three stages of mixer settler attached to get _____________

View solution

Q. If the holding time is more in a mixer then _______ will be poor.

View solution