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Q#1
GATE CH 2013
NAT
+2 marks
-0 marks
The vapor-liquid equilibrium curve of a binary mixture A-B, may be approximated by a linear equation over a narrow range of liquid mole fractions ( 
) as follows
Here 
is the mole fraction of A in the vapor. 100 moles of a feed ( 
) is batch distilled to a final residue 
. Using the Rayleigh equation, the number of moles of the residue left behind in the distillation unit, up to 2 digits after the decimal point, is 
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| Topic | Questions | Attempted | Correct | |
|---|---|---|---|---|
| Heat Transfer | 26 | 0 | 0 | |
| Chemical Technology | 17 | 0 | 0 | |
| Mechanical Operations | 12 | 0 | 0 | |
| Mass Transfer | 42 | 0 | 0 | |
| Instrumentation and Process Control | 26 | 0 | 0 | |
| Fluid Mechanics | 24 | 0 | 0 | |
| Engineering Mathematics | 41 | 0 | 0 | |
| General Aptitude | 60 | 0 | 0 | |
| Chemical Reaction Engineering | 26 | 0 | 0 | |
| Process Calculation | 9 | 0 | 0 | |
| Plant Design Economics | 10 | 0 | 0 | |
| Thermodynamics | 24 | 0 | 0 |
Distillation
17 Qs
0 Att
0 Cor
Relative Volatility
Continuous Distillation
Designing of Distillation Column
Dimensionless No.
Film Theory
Tray Tower
Designing Part of Distillation Column
Dimensionless Numbers
Batch Distillation
Mcabe-Thiele Method
Topic-wide
Numerical Ability
21 Qs
0 Att
0 Cor
Permutation and Combination
Set Theory
Geometry/Mensuration
Infinite Series
Number System
Number Series
Data Interpretation
Mixtures and Allegations
Binomial Theorem
Maxima and Minima
Pipe and Cistern
Probability
Topic-wide