Title | Tutorial sheet 1 Solution |
---|---|
Author | Li Feng Chang |
Course | Reaction Engineering |
Institution | University of Queensland |
Pages | 5 |
File Size | 177.9 KB |
File Type | |
Total Downloads | 86 |
Total Views | 156 |
Download Tutorial sheet 1 Solution PDF
CHEE3005 Tutorial Sheet 1: Solutions Q1. Determine the equilibrium conversion of the following reaction: C2 H4 ( g ) H2 O( g ) C2 H5 OH ( g ) as a function of the temperature, at 30 atm, and steam/ethylene molar ratio equals to 10.
Given that H 298 50 kJ/mol 0
K =6.8x10 atm at 145C P 30 atm. 2
1
C pC2 H4 11.85 0.12T 36.6x 106 T 2 , J/mol/K CPH2O 30.4 9.63x103 T 1.17x106 T 2 , J/mol/K CPC2 H5OH 29.27 0.17T 49.95x106 T 2 , J/mol/K Solution T
H o (T ) H o (298)
C p ( T ') dT '
298
C p C pC2 H5 OH C pC2 H4 C pH2 O (29.27 30.4 11.85) (0.17 9.63 x10 3 0.12) T (49.95 1.17 36.6) x10 6 T 2
-12.98 0.04T -14.52 x10 6 T 2 Calculation of H o ( T ) T
H o ( T ) H o (298)
C ( T ') dT ' p
298 T
50,000+ (-12.98 0.04T -14.52x 106 T 2 )dT ' 298 T T T2 T3 = 50,000 12.98(T 298) 0.04 14.52x106 2 298 3 298 2 2 6 3 3 50,000 12.98( T 298) 0.02( T 298 ) 4.84 x10 ( T 298 )
Calculation of the equilibrium constant: o d ln( K ) H ( T ) dT RT 2
K (T ) ln K (418)
T
H o (T ') dT ' RT ' 2 418
T 1 50, 000 2982 2983 1 298 6 x T 12.98 0.02 1 4.84 10 ' dT ' T '2 2 R 418 T '2 T '2 T' T'
T T T T 2 1 1 1 6 T ' 2 1 3 1 298 0.02 ' 298 4.84 10 298 T x T 50,000 12.98 ln( ') R T ' 418 T ' 418 T ' 418 T ' 418 2 K T 1 1 1 1 1 2 1 8.4136 xln T 50, 000 12.98 ln 298 0.02 (T 418) 298 T 418 T 418 T 418 418 K418
T 2 4182 1 1 4.84 x10 2983 2 T 418 6
From equilibrium thermodynamics K P (T ) K y P
( c d ) ( a b)
yC2H 5OH yC2 H4 yH2 O
yC 2H 5OH y C2 H4 y H2 O
P
(1 1 1)
P 1
Assume 1 mole of C2H4 and 10 moles of steam initially. After n moles of C2H4 have reacted C2 H 4 ( g ) H 2O ( g ) C2 H 5OH ( g ) 1-n 10-n n Total number of moles = 1-n+10-n+n = 11-n 1 n Mole fraction C2H4 = 11 n 10 n Mole fraction H2O = 11 n n Mole fraction C2H5OH = 11 n KT
yC2 H5 OH PyC 2H 4 yH 2O
n (11 n ) 30(1 n )(10 n )
This gives a quadratic equation for n:
(30 KT 1)n2 (330KT 11)n 300KT 0 The solution for n represents the conversion at temperature T.
1.0 0.8
0.1 conversion
equilibrium constant, K (atm.)
1
0.01
0.6 0.4
0.001
0.2 0.0
0.0001 400
500
600
400
700
500
600
700
temperature (K)
temperature (K)
Q2. A gas phase reaction, 2A + 3B C, is conducted with several starting ratios, r = nbo/nao. The equilibrium constant Ky = 10.
(a) Show that the equilibrium conversion of A for any value of the ratio r follows the relation
K y 10
X 1 r 2 X 2 1 X
4 3
2
3 r 2 X
(b) At what value of the ratio r is the conversion of substance A maximum, and what is this maximum conversion? (c) What is the maximum possible conversion for an equimolar mixture (i.e. r = 1), and at what value of Ky is this obtained? Solution
(a) Assume: - Pressure is constant - Isothermal Starting with one mole of A perform a mole balance, assuming X moles of A are reacted. 2A + 3B C 3 X N : 1 X r X 2 2 total N , NT 1 r 2 X
Ky
yC 2 3 yA yB
XN T2 N T3 3 2 NT 1 X r X 2
3
2
X 1 r 2 X
4
3 2 2 1 X r X 2
3
(b) As shown in the hint, for maximum conversion:
f 0 r X where,
K y 10 f X , r
X 1 r 2 X
4
3 2 2 1 X r X 2
3
The derivative of f with respect to r is zero because f is constant (=10). On differentiating f(X,r)
3 4 X f 4 1 r 2 X 3 1 r 2 X 0 2 3 4 2(1 X ) r X 3 3 r X r X 2 2 This yields
4 1 r 2 X
3
r 3X 2
3
3 1 r 2 X r 3X 2
4
4
whose solution is r = 3, and upon substitution in Eq. (1), with Ky=10, we obtain
X m 4 2X m 2 1 X m
2
4
3 3 X m 2
3
10
(1)
This has the solution: Xm = 0.563. This is the maximum conversion for the reaction, and is obtained when r = 3, for the value of Ky = 10. (c) For the reaction 2A + 3B C
3 moles of B are required for every 2 moles of A converted. When r = 1, only one mole of B is available for every mole of A, and species B is limiting. To convert this one mole of B only 2/3 moles of A are reacted from the one mole of A available. Thus, the maximum conversion of A is 2/3, or 0.67. From the equation for Ky, we have
Ky
X 1 r 2 X
3
3 2 2 1 X r X 2
For r = 1 this yields
Ky
and for X → 2/3, Ky → ∞.
4
8 X 1 X
2
3
3 X 1 2 ...