User provided internal flows are generally for(a) Reflux in high purity(b) Overhead liquid products(c) Narrow building columns(d) NOR relationI have been asked this question in class test.Question is from Rigorous Computational Methods in division Rigorous Distillation Calculations of Distillation Design

User provided internal flows are generally for(a) Reflux in high purit

1.	User provided internal flows are generally for(a) Reflux in high purity(b) Overhead liquid products(c) Narrow building columns(d) NOR relationI have been asked this question in class test.Question is from Rigorous Computational Methods in division Rigorous Distillation Calculations of Distillation Design
Answer» Right OPTION is (d) NOR relation The explanation is: User provided internal flows are generally for REFLUX in high PURITY, overhead liquid products and NARROW building columns also called as NOR relation.

Discussion

No Comment Found

Related InterviewSolutions

The K in the below equation holds for(a) Distribution Factor(b) Henry Factor(c) Vapor Factor(d) Dew factorThis question was posed to me in an interview for internship.The query is from Bubble Point Method in division Rigorous Distillation Calculations of Distillation Design
For a reboiler stage N, the middle diagonal is(a) -(1+L1/KI1D)(b) KIf and LiF(c) L1/KI1D(d) -(1+B1/KI1VN)The question was asked in an online interview.The origin of the question is Tridiagonal Matrix Method for Material Balances in portion Rigorous Distillation Calculations of Distillation Design
Bubble point is at?(a) A(b) B(c) C(d) Wrong interpretationThis question was posed to me in exam.My question is taken from Recovery from Failure and Analyze Results in portion Rigorous Distillation Calculations of Distillation Design
C is the?(a) Heat capacity(b) Coefficient(c) Total component(d) Final componentI have been asked this question during an interview for a job.Query is from Recovery from Failure and Analyze Results topic in portion Rigorous Distillation Calculations of Distillation Design
When this condition satisfies(a) Mass transfer at interface should cancel(b) Mass transfer at interface should unite(c) Mass transfer at interface should maximum(d) Mass transfer at interface should minimumI had been asked this question in my homework.The question is from Non Equilibrium Rate Based Methods topic in portion Rigorous Distillation Calculations of Distillation Design
The Homotomy parameter, t travels between(a) 0 and 1(b) 0 and infinity(c) 1 and infinity(d) 1 and -1This question was posed to me during an interview.I would like to ask this question from Relaxation Method topic in division Rigorous Distillation Calculations of Distillation Design
In global Newton method, all equations are solved together in(a) Regula falsi technique(b) 2N technique(c) Newton Raphsontechnique(d) False techniqueI got this question during an interview.My enquiry is from Global Newton Method topic in portion Rigorous Distillation Calculations of Distillation Design
Newton’s method is a fixed point iteration method, As Pn(a) g(Pn-1)(b) (Pn-1)(c) g(d) PnThis question was posed to me during a job interview.My question comes from 2N Newton Method in portion Rigorous Distillation Calculations of Distillation Design
The BP Method generally work best for(a) Narrow Boiling systems(b) Ideal systems(c) Nearly ideal systems(d) Any systemsThe question was posed to me in an online quiz.My question is from Bubble Point Method topic in division Rigorous Distillation Calculations of Distillation Design
When Raoult’s law and Dalton’s law hold for the mixture, the K factor is(a) Pi/P(b) Yi/Xi(c) Y*/X(d) X*/XI had been asked this question during an online interview.This is a very interesting question from Bubble Point Method topic in chapter Rigorous Distillation Calculations of Distillation Design

Discussion

No Comment Found

Related InterviewSolutions

Reply to Comment