IB Chemistry on Equilibrium Constant, Kc and Equilibrium Law.
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Transcript of IB Chemistry on Equilibrium Constant, Kc and Equilibrium Law.
http://lawrencekok.blogspot.com
Prepared by
Lawrence Kok
Tutorial on Equilibrium Law, Equilibrium constant
Kc and Reaction quotient Qc.
Dynamic Equilibrium
Reversible (closed system)
Forward Rate, K1 Reverse Rate, K-1
Kc = ratio of molar conc of product (raised to power of their respective stoichiometry coefficient) to molar conc of reactant (raised to power of their respective stoichiometry coefficient)
Conc of product and reactantat equilibrium
At Equilibrium
Forward rate = Backward rateConc reactants and products remain
CONSTANT/UNCHANGE
Equilibrium Constant Kc
aA(aq) + bB(aq) cC(aq) + dD(aq)
coefficient
Solid/liq not included in Kc
Conc represented by [ ]
K1
K-1
ba
dc
cBA
DCK
1
1
K
KKc
Equilibrium Constant Kc
express in
Conc vs time Rate vs time
A + B
C + D
Conc
Time
Click here notes on dynamic equilibrium
Excellent Notes
reversetconsrate
forwardtconsrate
K
K
..tan..
..tan..
1
1
Large Kc
• Position equilibrium shift to right• More products > reactants
Magnitude of Kc
ba
dc
cBA
DCK
Extend of reaction
How far rxn shift to right or left?
Not how fast
ba
dc
cBA
DCK
Small Kc
• Position equilibrium shift to left• More reactants > products
cKcK
Position of equilibrium
2CO2(g) ↔ 2CO(g) + O2(g)
92103 cK
2H2(g) + O2(g) ↔ 2H2O(g)
81103cK
H2(g) + I2(g) ↔ 2HI(g)
2107.8 cK
1
Kc
• Position equilibrium lies slightly right• Reactants and products equal amount
Reaction completion
Product favouredReactant favoured Reactant/Product equal
cK
Temp dependent
Extend of rxn
Not how fast
Equilibrium Constant Kc
ba
dc
cBA
DCK
aA(aq) + bB(aq) cC(aq) + dD(aq)
Conc of product and reactant at equilibrium
Equilibrium expression HOMOGENEOUS gaseous rxn
4NH3(g) + 5O2(g) ↔ 4NO(g) + 6H2O(g) N2(g) + 3H2(g) ↔ 2NH3(g)
NH4CI(s) ↔ NH3(g) + HCI(g)
2SO2(g) + O2(g) ↔ 2SO3(g)
52
4
3
6
2
4
ONH
OHNOKc
32
1
2
2
3
HN
NHKc
11
3 HCINHKc
04
11
3
CINH
HCINHKc
12
2
2
2
3
OSO
SOKc
Equilibrium expression HETEROGENOUS rxn
CaCO3(s) ↔ CaO(g) + CO2(g)
03
1
2
1
CaCO
COCaOK c
12
1COCaOKc
CH3COOH(l) + C2H5OH(l) ↔ CH3COOC2H5(l) + H2O(l)
152
1
3
1
2
1
523
OHHCCOOHCH
OHHCOOCCHKc
Equilibrium expression HOMOGENEOUS liquid rxn
Cu2+(aq) + 4NH3(aq) ↔ [Cu(NH3)4]
2+
43
12
2
43 )(
NHCu
NHCuKc
Reactant/product same phase
Reactant/product diff phase
aA bB
2aA 2bB
bB aA
aA bB
aA bB
a
b
cA
BK
aA bB
Equilibrium Constant Kc Equilibrium Constant Kc
b
a
cB
AK
'
c
cK
K1'
inverse
X2 coefficient
2'
cc KK
coefficient
2
1
a
b
c
A
BK
21
21
'
ccc KKK 21'
a
b
cA
BK
a
b
cA
BK
a
b
cA
BK
2
2'
2
1
aA bB bB cC
a
b
ciA
BK
b
c
ciiB
CK
+ 2 reactions+ aA cC
a
c
a
b
b
c
cA
C
A
B
B
CK
'
ciciic KKK '
Effect on Kc
Inverse Kc
Square Kc
Square root cK
Multiply both Kc
2
1
ciiK ciK
N2(g) + O2(g) ↔ 2NO(g)
2NO(g) + O2(g) ↔ 2NO2(g)
19103.2 ciK
6103ciiK
2NO2(g) ↔ N2(g) + 2O2(g)
13
619
107
103103.2
c
c
ciicic
K
K
KKKN2(g) + 2O2(g) ↔ 2NO2(g)
13107 cK
12'
13
'
1042.1
107
11
c
c
c
K
KK
HF(ag) ↔H+(aq) + F -(aq)
H2C2O4(ag) ↔ 2H+(aq) + C2O4
2 -(aq)
4108.6 ciK
6108.3 ciiK
2HF(ag) + C2O42- ↔ 2F -(aq) + H2C2O4(aq)
2HF(ag) ↔ 2H+(aq) + 2F -(aq)
2H+(ag) + C2O4
2- ↔H2C2O4(aq)
7242'106.4108.6 cic KK
5
6
''106.2
108.3
11
cii
cK
K
12.0106.2106.4 57
'''
c
ccc
K
KKK
Kc for diff rxnAdding 2 rxns
+
Inverse rxn
Adding 2 rxns
2HF(ag) + C2O42- ↔ 2F -(aq) + H2C2O4(aq)
+
HF(ag) ↔H+(aq) + F -(aq)
4108.6 ciK
x2 coefficient
H2C2O4(ag) ↔ 2H+(aq) + C2O4
2 -
Inverse rxn
6108.3 ciiK
2HF(ag) ↔ 2H+(aq) + 2F -(aq)
2H+(ag) + C2O4
2- ↔H2C2O4(aq)
Add 2 rxn
7'106.4 cK
5''106.2 cK+
Effect on Kc Effect on Kc
Inverse rxn Inverts expression
Doubling rxn coefficient Squares expression
Tripling rxn coefficient Cubes expression
Halving rxn coefficient Square root expression
Adding 2 reactions Multiplies 2 expression
cK
1
2
cK
3
cK
cK
ii
c
i
c KK
Square Kc
Invert Kc
Multiply Kc
1
2
3
N2(g) + 2O2(g) ↔ 2NO2(g)
H2 + I2 ↔ 2HI
50cK
12
1
2
2
IH
HIKc
2HI ↔ H2 + I2
2
1
2
1
2'
HI
IHKc
02.050
11'
c
cK
K
2SO2 + O2 ↔ 2SO3
12
2
2
2
3
OSO
SOKc
200cK
SO2 + O2 ↔ SO3
1.14200'
cc KK
2
1
4SO2 + 2O2 ↔ 4SO3
40000
200
,
22'
c
cc
K
KK
N2(g) + 3H2(g) ↔ 2NH3(g)
32
1
2
2
3
HN
NHKc
Kc is 170 at 500K Determine if rxn is at equilibrium when conc are at:[N2] =1.50, [H2] = 1.00, [NH3] = 8.00
00.150.1
00.8
3
2
1
2
2
3
c
c
Q
HN
NHQ
• Rxn not at equilibrium
• Shift to right, favour product
• Qc must increase, till equal to Kc
IB Questions
Determine Kc for inversing rxn
inverse
Determine Kc for halving rxn
2
1
1
2
2
2
2
3
OSO
SOK c
halving
Determine Kc for doubling rxn
2SO2 + O2 ↔ 2SO3
doubling
12
2
2
2
3
OSO
SOKc
200cK
2
1
2
2
2
2
3
OSO
SOK c
21
34
170cK7.42cQ
cc KQ
Kc and Qc
H2(g) + I2(g) ↔ 2HI(g)
cK
Constant at fixed Temp
12
1
2
2
IH
HIKc
At equilibrium
Independent of initial conc
Initial conc of H2 , I2 and HI
00.4cQ
12
1
2
2
IH
HIQc
4.461012.01014.1
1052.21212
22
cK 4.46cK
Expt InitialConc H2
InitialConc I2
Initial Conc HI
1 0.0500 0.0500 0.100
Initial conc of H2 , I2 and HI
Expt InitialConc H2
InitialConc I2
Initial Conc HI
1 2.40 x 10-2 1.38 x 10-2 0
Expt EquilibriumConc H2
EquilibriumConc I2
EquilibriumConc HI
1 1.14 x 10-2 0.12 x 10-2 2.52 x 10-2
At equilibrium conc
Not at equilibrium
H2(g) + I2(g) ↔ 2HI(g)
00.4050.0050.0
100.02
cQ
Predict the direction of rxn
Difference between
cQ
Conc of product/reactant
at equilibruim conc
Reaction quotient at particular time
Not at equilibrium conc
Varies NOT constant
Kc and Qc
H2(g) + I2(g) ↔ 2HI(g)
12
1
2
2
IH
HIKc
4.461012.01014.1
1052.21212
22
cK 4.46cK
At equilibrium conc
cc KQ cc KQ
cc KQ
Reaction at equilibrium
More product > reactant
Rxn shift left more reactant
→
cc KQ
cQ
Bring Qc down
More reactant > product
Rxn shift right → more product
Bring Qc up cQ
cc KQ
cQ
Expt InitialConc H2
InitialConc I2
Initial Conc HI
1 0.0500 0.0500 0.100
Initial conc of H2 , I2 and HI
12
1
2
2
IH
HIQc
00.4050.0050.0
100.02
cQ
cQ
Expt InitialConc H2
InitialConc I2
Initial Conc HI
1 0.0250 0.0350 0.300
Initial conc of H2 , I2 and HI
12
1
2
2
IH
HIQc
1030350.00250.0
300.02
cQ
Click here to view notes
Kc from reaction stoichiometry
H2(g) + I2(g) ↔ 2HI(g)
4.46 sameK c
12
1
2
2
IH
HIKc
Kc = 46.4 ( 730K)At equilibrium 4 diff initial conc of H2 , I2 and HI
4.461012.01014.1
1052.21212
22
cKRxn 1
same
Qc = Kc - rxn at equilibrium, no side/shift occurQc < Kc– rxn shift right, favour product Qc > Kc – rxn shift left, favour reactant
Rxn 2, 3, 4diff initial conc
more products
H2(g) + I2(g) ↔ 2HI(g)
cQ
Rxn shift to right
Rxn shift to leftmore reactants
treac
productQc
tan
treac
productQc
tan
cQ
cc KQ cc KQ cc KQ
12
1
2
2
IH
HIKc
How dynamic equilibrium is shifted when H2 is added ?
• Add H2 , Qc decrease• Position equilibrium shift to right• Rate forward and reverse increase• New equilibrium conc achieved when
Rate forward Kf = Rate reverse Kr
• More product NH3 ,but Kc unchanged
N2(g) + 3H2(g) ↔ 2NH3(g) 07.4cK
Equilibrium disturbedH2 added. More reactant
At equilibrium Conc reactant/product no change
At new equilibrium Conc reactant/product no change
24.2cQ
Equilibrium Conc H2 = 0.82MEquilibrium Conc N2 = 0.20MEquilibrium Conc NH3 = 0.67M
32
1
2
2
3
HN
NHKc
31
2
82.020.0
67.0cK
New Conc H2 = 1.00MConc N2 = 0.20MConc NH3 = 0.67M
32
1
2
2
3
HN
NHQc
31
2
00.120.0
67.0cQ
07.4cK
New Equilibrium Conc H2 = 0.90MNew Equilibrium Conc N2 = 0.19MNew Equilibrium Conc NH3 = 0.75M
31
2
90.019.0
75.0cK
32
1
2
2
3
HN
NHKc
07.4cK
Shift to the right - Increase product - New Conc achieve- Qc = Kc again
cc KQ
How dynamic equilibrium shift when H2 added ?
• Add H2 , Qc decrease• Position equilibrium shift to right• Rate forward and reverse increase• New equilibrium conc achieved when
Rate forward Kf = Rate reverse Kr
• More product NH3 ,but Kc unchanged
Rate forward Kf = Rate reverse Kr
N2(g) + 3H2(g) ↔ 2NH3(g) 07.4cK
07.4 cc KQ
Equilibrium disturbedH2 added. More reactant
cc KQ
Equilibrium shift to right Rate forward Kf > Rate reverse Kr
cQ
At equilibrium Conc reactant/product no change
At new equilibrium Conc reactant/product no change
Qc increase until Qc = Kc
cQ
Rate forward Kf = Rate reverse Kr
cc KQ cc KQ cc KQ
Equilibrium Law (Using ICE Method)
Reactants species present Product species present
2HI 1H2 1I2
Initial 0.8 0.0 0.0
Change -2x +x +x
Equilibrium 0.8 – 2x +x +x
2HI ↔ H2 + I2Mol ratio 2↔ 1:1
↔
CO + H2O ↔ CO2 + H2
CO H2O I2 H2
Initial 3 3 0 0
Change -x -x +x +x
Equilibrium 3 - x 3 - x +x +x
Mol ratio 1:1↔ 1:1
2NO + 1O2 ↔ 2CO2
2NO 1O2 2CO2
Initial 0.3 0.3 0.0
Change -x -1/2x +x
Equilibrium 0.3 - x 0.3 – 1/2x +x
Mol ratio 2:1 ↔ 1
↔
↔
2NO2 2NO 1O2
Initial 0 1 1
Change +2x -2x -x
Equilibrium +2x 1 – 2x 1 - x
2NO2 ↔ 2NO + 1O2Mol ratio 2↔ 2:1
↔
2HI 1H2 1I2
Initial 0 3 1
Change +4x -2x -2x
Equilibrium +4x 3 – 2x 1 - 2x
2HI ↔ 1H2 + 1I2Mol ratio 2↔ 1:1
↔
2NO 1O2 2CO2
Initial 0 0 1
Change +2x +1x -2x
Equilibrium +2x +1x 1 - 2x
2NO + 1O2 ↔ 2CO2Mol ratio 2:1 ↔ 2
↔
ICE method"I" - initial conc for each species rxn mixture."C" – change in conc for each species as system move toward eq."E" - equilibrium conc of each species in equilibrium.
Change
React and Produce
x amtreact
x amtproduce
Equilibrium Law (Using ICE Method)
H2 added to system
2HI 1H2 1I2
Equilibrium 0.8 0.6 0.8
2HI ↔ 1H2 + 1I2Mol ratio 2↔ 1:1
↔
2HI 1H2 1I2
Initial 0.8 1.0 0.8
Change +2x -x -x
Equilibrium 0.8 + 2x 1 - x 0.8 - x
2H
Rxn shift to left
2NO2 2NO 1O2
Equilibrium 3 1 2
2NO2 ↔ 2NO + 1O2Mol ratio 2↔ 2:1
↔ NO2NO2 2NO 1O2
Initial 3 1.5 2
Change +2x -2x -x
Equilibrium 3 + 2x 1.5 – 2x 2 - x
CO H2O I2 H2
Equilibrium 3 3 2 2
CO + H2O ↔ I2 + H2Mol ratio 1:1↔ 1:1
CO1CO 1H2O 1I2 1H2
Initial 4 3 2 2
Change -x -x +x +x
Equilibrium 4 - x 3 - x 2 + x 2 + x
↔↔
Rxn shift to left
Rxn shift to right
cc KQ
cc KQ
cc KQ
At equilibrium
cQ cc QK
↔
At equilibrium NO added to system
cQ cc QK
↔cc KQ
At equilibrium CO added to system
cQ cc QK
Equilibrium Constant Kc
ba
dc
cBA
DCK
aA(aq) + bB(aq) cC(aq) + dD(aq)
Conc of product and reactant at equilibrium
Equilibrium Law Expression - Law of Mass Action
Cal Kc. (Vol vessel - 1 dm3 )Eq Conc : [CO] = 8.78 x 10-3 M
[Br2] = 4.90 x 10-3M[COBr2] = 3.40 x 10-3M
CO + Br2 ↔ COBr2
CO + Br2 ↔ COBr2
Eq conc 8.78 x 10-3 4.90 x 10-3 3.40 x 10-3
Eq Conc = Moles/Vol
12
1
1
2
BrCO
COBrKc
1313
3
1090.41078.8
1040.3
cK 79cK
Ex 1
Cal eq conc CI2
Kc = 0.19. (Vol vessel - 1 dm3 ) Eq Conc : [PCI5] = 0.20M
[PCI3] = 0.01M
PCI5 ↔ PCI3 + CI2Ex 2
PCI5 ↔ PCI3 + CI2
Eq conc 0.20 0.01 x
13
1
2
1
3
PCI
CIPCIK c
1
11
20.0
01.019.0
x 8.3x
Ex 3 N2O4 ↔ 2NO2
Cal eq conc N2O4
Kc = 1.06 x 10-5. (Vol vessel - 1 dm3 ) Eq Conc : [NO2] = 1.85 x 10-3M
N2O4 ↔ 2NO2
Eq conc x 1.85 x 10-3
142
2
2
ON
NOKc
1
235 1085.1
1006.1x
323.0cK
Cal Kc
Cal Eq Conc
Cal Eq Conc
All homogeneous gaseous
Equilibrium Law (Using ICE Method)
1 mol ethanoic acid add to 1 mol ethanol, at equilibrium, 0.67 mol ester produced.Cal Kc. (Vol vessel - 1 dm3)
CH3COOH + C2H5OH ↔ CH3COOC2H5 + H2O
Initial mole 1.0 1.0 0 0
Change (1 - 0.67) (1 - 0.67) 0.67 0.67
Mole at eq 0.33 0.33 0.67 0.67
Eq Conc 0.33/1 0.33/1 0.67/1 0.67/1
In esterification, 2 mol ethanoic acid, 3 mol ethanol and 2 mol H2O mixed.Cal eq conc, Kc - 4.0 (Vol vessel – 1 dm3 )
CH3COOH + C2H5OH ↔ CH3COOC2H5 + H2O
Initial mole 2 3 0 2
Change (2 - x ) (3 - x) +x 2 + x
Mole at eq (2 – x ) (3 – x) +x 2 + x
Eq Conc (2 – x )/1 (3 -x)/1 x/1 (2 + x)/1
Conc CH3COOC2H5 = 1.33MConc H2O = 3.33MConc CH3COOH = 0.67MConc C2H5OH = 1.67M
Change = React and ProduceEx 4
Ex 5
Mole ratio 1:1 ↔ 1:1
152
1
3
1
2
1
523
OHHCCOOHCH
OHHCOOCCHKc
11
11
33.033.0
67.067.0cK 12.4cK
- x amt reacted + x amt produced
152
1
3
1
2
1
523
OHHCCOOHCH
OHHCOOCCHKc
11
11
32
24
xx
xx
33.1x
I
C
E
Eq Conc = Mole/Vol
-0.67 +0.67
Eq Conc = Mole/Vol
Mole ratio 1:1 ↔ 1:1
Change = Reacted and Produced
I
C
E
Click here notes equilibrium law
Initial amt X (0.02) and Y (0.01). At eq conc – 0.009 Z produced Cal Kc. (Vol vessel – 600 cm3 )
X + Y ↔ Z
Initial mole 0.02 0.01 0
Change (0.02 – 0.009) (0.01 – 0.009) 0.009
Mole at eq 0.011 0.001 0.009
Eq Conc 0.011/0.6 0.001/0.6 0.009/0.6
Mixture 1.9 mol H2 and 1.9 mol I2 was added to vessel . At eq conc, 3mol HI formCal Kc . (Vol vessel – 1 dm3 )
H2 + I2 ↔ 2HI
Initial mole 1.9 1.9 0
Change (1.9 – 1.5) (1.9 – 1.5) 3
Mole at eq 0.4 0.4 3
Eq Conc 0.4/1 0.4/1 3/1
0.05 mol SO2CI2 was used, at equilibrium 0.0345 mol CI2 formedCal Kc. (Vol vessel – 2 dm3 )
SO2CI2 ↔ SO2 + CI2
Initial mole 0.05 0 0
Change (0.05 – 0.0345) 0.0345 0.0345
Mole at eq 0.0155 0.0345 0.0345
Eq Conc 0.0155/2 0.0345/2 0.0345/2
Ex 6
Ex 8
Equilibrium Law (Using ICE Method)
X + Y ↔ Z
11
1
YX
ZKc
11
1
0016.00183.0
015.0cK 491cK
12
1
2
2
IH
HIKc
11
2
4.04.0
3cK 56cK
SO2CI2 ↔ SO2 + CI2
122
1
2
1
2
CISO
CISOKc
1
11
00775.0
0173.00173.0cK
0386.0cK
H2 + I2 ↔ 2HI Ex 7
I
C
E
I
C
E
I
C
E
Mole ratio 1:1 ↔ 1
Mole ratio 1:1 ↔ 2
Mole ratio 1 ↔ 1:1
Change = React and Produce
-0.009 +0.009
Change = React and Produce
-1.5 +3
Change = React and Produce
-0.0345 +0.0345
Initial amt, 3 mol CO and H2O were used.Cal eq conc H2, Kc - 4.0 (Vol vessel - 1 dm3 )
Initial amt PCI5 - 0.01 mol. Kc = 0.19. (Vol vessel - 0.5 dm3 ) Cal eq conc PCI5, PCI3 and CI2
[PCI5] = (0.01 – 0.0091)/0.5 = 0.0018M[PCI3] = 0.0091/0.5 = 0.018M[CI2] = 0.0091/0.5 = 0.018M
Ex 9
Equilibrium Law (Using ICE Method)
12
1
1
2
1
2
OHCO
HCOKc
CO + H2O ↔ CO2 + H2
11
11
334
xx
xx
Mx 2
PCI5 ↔ PCI3 + CI2
15
1
2
1
3
PCI
CIPCIK c 1
2
5.0
01.0
5.0
x
x
Kc 1
2
5.0
01.0
5.019.0
x
x
0091.0x
CO + H2O ↔ CO2 + H2
Initial mole 3 3 0 0
Change (3 - x) (3 - x) +x +x
Eq Conc (3 - x)/1 (3 - x)/1 x/1 x/1
I
C
E
Ex 10
I
C
E
PCI5 ↔ PCI3 + CI2
Initial mole 0.01 0 0
Change 0.01 - x +x +x
Eq Conc (0.01 – x)/0.5 x/0.5 x/0.5
1 mol HI was used initially, and 0.78 mol of HI remain at equilibrium.Cal Kc. (Vol - 1 dm3 )
Ex 11
2HI ↔ H2 + I2
2HI ↔ H2 + I2
Initial mole 1 0 0
Change (1 - 0. 22) 0.11 0.11
Eq Conc 0.78/1 0.11/1 0.11/1
I
C
E
2
1
2
1
2
HI
IHKc
2
11
78.0
11.011.0cK 02.0cK
Mole ratio 1:1 ↔ 1:1
Change = React and Produce
- x amt reacted + x amt produced
Change = React and Produce
Mole ratio 2↔ 1:1
-0.22 +0.11
Quadratic eqn
Quadratic eqn
H2 + I2 ↔ 2HI
Eq conc reactant/product given.Cal Kc using vol vessel - 1 dm3 /2 dm3
Ex 12
Equilibrium Law (Using ICE Method)
H2 + I2 ↔ 2HI
H2 + I2 ↔ 2HI Mole at eq 0.4 0.4 3
Eq Conc 0.4/1 0.4 /1 3/1
Using approximation and assumption
Eqn with equal number molecule both sideEq expression – Independent of volume
12
1
2
2
IH
HIKc
12
1
2
2
IH
HIKc
11
2
4.04.0
3cK
11
2
24.0
24.0
23
cK
56cK
H2 + I2 ↔ 2HI Mole at eq 0.4 0.4 3
Eq Conc 0.4/2 0.4 /2 3/2
56cK
SO2CI2 ↔ SO2 + CI2
Mole at eq 0.011 0.001 0.009
Eq Conc 0.011/1 0.001/1 0.009/1
SO2CI2 ↔ SO2 + CI2
122
1
2
1
2
CISO
CISOKc
1
11
011.0
009.0001.0cK
41018.8 cK
1
11
2011.0
2009.0
2001.0
cK
111
0055.0
00045.00005.0cK
51009.4 cK
1 dm3 2 dm3
1 dm3 2 dm3
SO2CI2 ↔ SO2 + CI2
Ex 13
Eqn with diff number molecule both sideEq expression – Dependent of volume
Eq conc reactant/product given.Cal Kc using vol vessel - 1 dm3 /2 dm3
SO2CI2 ↔ SO2 + CI2
Mole at eq 0.011 0.001 0.009
Eq Conc 0.011/2 0.001/2 0.009/2
Eq amt used instead of eq conc
Eq amt used instead of eq conc
Equilibrium Law (Using ICE Method) Using approximation and assumption
2H2O ↔ 2H2 + O2
2H2O ↔ 2H2 + O2
Initial mole 0.1 0 0
Change - x +x +x/2
Eq Conc 0.1 - x +x +x/2
22
1
2
2
2
OH
OHK c
2
12
5
1.0
2/104
x
xx
Solve cubic eqn difficult !
523 1041.02 xx
2
12
5
1.0
2/104
xx
523 1041.02 x
0093.0x
PCI5 ↔ PCI3 + CI2
15
1
2
1
3
PCI
CIPCIK c
Eq conc reactant/product given.Cal eq conc, Kc - 1. Vol vessel - 1 dm3
Solve quadratic eqn difficult !
Kc very small < 10-3
Not much change in reactant concApproximation is VALID
SMALLKc BIGKc
Eq conc reactant/product given.Cal eq conc, Kc - 4 x 10-5. Vol vessel - 1 dm3
- Little product form
- Initial Conc reactant
unchanged
Using
approximation
0.1 – x ≈ 0.1
[reactant]initial ≈[reactant]eq
Cannot use
approximation
1 – x ≠ 1
Kc very BIG > 10-3
Change in reactant concApproximation NOT VALID
[reactant]initial ≠ [reactant]eq
- Lots product form
- Initial Conc reactant
changed
PCI5 ↔ PCI3 + CI2
Initial mole 1 0 0
Change 1 - x +x +x
Eq Conc 1 – x x x
1
2
11
x
x
012 xx
62.0x
Equilibrium Law (Using ICE Method) Using approximation and assumption
PCI5 ↔ PCI3 + CI2
PCI5 ↔ PCI3 + CI2
Initial mole 1 0 0
Change 1 - x +x +x
Eq Conc 1 – x x x
15
1
2
1
3
PCI
CIPCIK c
1
2
11
x
x
62.0x
Eq conc reactant/product given.Cal eq conc, Kc - 1. Vol vessel - 1 dm3
Solve quadratic eqn 012 xxKc very small < 10-3
Not much change reactant concApproximation is VALID
SMALLKc BIGKc
Eq conc reactant/product given.Cal eq conc, Kc - 1 x 10-10. Vol vessel - 1 dm3
- Little product form
- Initial conc reactant
unchanged
Using
approximation
1 – x ≈ 1
Cannot use
approximation
1 – x ≠ 1
Kc very BIG > 10-3
Change in reactant conc, BIG
[reactant]initial ≠ [reactant]eq
[ 1 ]initial ≠ [ 0.38 ]eq
- Lots product form
- Initial conc reactant
changed
[PCI5] = (1 – 0.62) = 0.38M[PCI3] = 0.62M[CI2] = 0.62M
Change in x - big
PCI5 ↔ PCI3 + CI2
Initial mole 1 0 0
Change 1 - x +x +x
Eq Conc 1 – x x x
PCI5 ↔ PCI3 + CI2
15
1
2
1
3
PCI
CIPCIK c
1
2
10
1101
x
x
1
2
10
1101
x
5101 x
[PCI5] = (1 – 0.00001) = 0.99999M
[PCI3] = 0.00001M[CI2] = 0.00001M
[reactant]initial ≈ [reactant]eq
[ 1 ]initial ≈ [0.99999]eq
Eqn with equal number molecule both sideEq expression – Independent of volume
Initial amt, 1 mol CO and H2O were used.Cal eq conc all component, Kc - 4.0 (Vol vessel - 1 dm3 )
Ex 14
Equilibrium Law (Using ICE Method)
12
1
1
2
1
2
OHCO
HCOKc
CO + H2O ↔ CO2 + H2
11
11
114
xx
xx
667.0x
CO + H2O ↔ CO2 + H2
Initial mole 1 1 0 0
Change - x - x +x +x
Eq Amt (1 - x) (1 - x) x x
I
C
E
0.05 mol SO2CI2 added to 2 dm3 vessel. At equilibrium, 0.0345 mol CI2 form. Cal Kc
I
C
E
0386.0cK
2
2
14
x
x
[CO] = 1 – 0.667 = 0.333 [H2O] = 1 – 0.667 = 0.333[CO2] = 0.667[H2O] = 0.667
Using square root method
SO2CI2 ↔ SO2 + CI2
SO2CI2 ↔ SO2 + CI2
Initial mole 0.05 0 0
Change -0.0345 +0.0345 + 0.0345
Mole at eq (0.05 – 0.0345) 0.0345 0.0345
Eq Conc 0.0155/2 0.0345/2 0.0345/2
122
1
2
1
2
CISO
CISOKc
1
11
00775.0
0173.00173.0cK
Using approximation and assumption
Cannot use
approximation
[1 – x] ≠ 1
BIGKc
1 dm3
2 dm3
Eqn with diff number molecule both sideEq expression – Dependent of volume
Ex 15
Eq amt used instead of eq conc
Eq amt cannot be used
Equilibrium Law (Using ICE Method)
H2 + I2 ↔ 2HI
H2 + I2 ↔ 2HI
Initial mole 2 2 0
Change -x -x +2x
Mole at eq 2 - x 2 - x +2x
Eq Conc 2 – x 2 – x +2x
12
1
2
2
IH
HIKc
11
2
22
249
xx
x
x
x
2
249
Initial amt, 2 mol H2 and I2 were used.Cal eq conc all component, Kc - 49 (Vol vessel - 2 dm3 )
56.1x
I
C
EEqn with equal number molecule both sideEq expression – Independent of volume
[H2] = (2 – 1.56) = 0.44M[I2] = (2 – 1.56) = 0.44M[HI] = 2 x 1.56 = 3.12M
Click here simulation equilibrium Click here simulation
Equilibrium was investigated in two expt at diff tempResult shown table below. Cal Kc for expt 1 and 2.
2HI ↔ H2 + I22HI ↔ H2 + I2
Initial mole 0.06 0 0
Change -0.02 +0.01 +0.01
Mole at eq (0.06 – 0.02) +0.01 +0.01
Eq Conc 0.04 0.01 0.01
EXPT 1
2HI ↔ H2 + I2
Initial mole 0 0.04 0.04
Change +0.04 -0.02 - 0.02
Mole at eq +0.04 0.04 – 0.02 0.04 - 0.02
Eq Conc 0.04 0.02 0.02
2
1
2
1
2
HI
IHKc
2
11
04.0
01.001.0cK21025.6 cK
2
11
04.0
02.002.0cK 25.0cK
EXPT 2
Ex 16
66% N2O4 reacted
Mol ratio N2O4 : NO2, = 1 : 2
66% N2O4 react – 66% x 1 = 0.66 mol N2O4 react
0.66 mol N2O4 react - 1.32 mol NO2 produced
Amt N2O4 left = 1 – 0.66 = 0.34 mol
Initial amt -2 mol SO2 and O2 were used.Cal eq amt, if 90% of SO3 formed .
Equilibrium Law)
2SO2 + 1O2 ↔ 2SO3
Initial mole 2 2 0
Change - 1.8 -0.9 +1.8
Eq Amt (2 – 1.8) (2 – 0.9) +1.8
Eq Amt 0.2 1.1 1.8
15100
2331
2%
xxx
xNitrogen
90% SO3 produce
Mol ratio SO2 : SO3, = 1 : 1
90% SO2 react – 90% SO3 produced
90% SO2 react - 90% x 2 = 1.8 mol SO3 produced
Amt SO2 = (2 – 1.8) = 0.2 mol left
Mol ratio SO2 : O2. = 2 : 1
1.8 mol SO2 react with 0.9 mol O2
Amt O2 = (2 – 0.9) = 1.1 mol left
Initial amt, 2 mol SO2 and O2 were used.Cal eq amt, if 20% of SO2 react.
20% SO3 react
Mol ratio SO2 : SO3, = 1 : 1
20% SO2 react – 20% SO3 produced
20% SO2 react - 20% x 2 = 0.4 molSO3 produced
Amt SO2 left = 2 – 0.4 = 1.6 mol left
Mol ratio SO2 : O2. = 2 : 1
0.4 mol SO2 react with 0.2 mol O2
Amt O2 left = 2 – 0.2 = 1.8 mol
Initial amt, 1 mol N2O4 used. 66% dissociated.Cal eq amt.
1N2O4 ↔ 2NO2
Initial mole 1 0
Change -0.66 +1.32
Eq Amt (1 – 0.66) +1.32
Eq Amt 0.34 1.32
N2 + H2 react ratio 1 : 3 to produce NH3. Equilibrium mixture contain 15% NH3. Cal eq amt for each species.
N2 + 3H2 ↔ 2NH3
Initial mole 1 3 0
Change -x -3x 2x
Eq Amt 1 – x 3 – 3x 2x
Eq Amt 0.74 2.22 0.52
Let x N2 reacted
X = 0.26
[N5] = 0.74, [H2] = 2.22, [NH3] = 0.52
2SO2 + 1O2 ↔ 2SO3
Initial mole 2 2 0
Change -0.4 -0.2 +0.4
Eq Amt (2 – 0.4) (2 – 0.2) +0.4
Eq Amt 1.6 1.8 0.4
Change
React and Produce
x amtreact
x amtproduce
Ex 17 Ex 18
Ex 19Ex 20
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Click here on reversible rxn
Simulation on Dynamic equilibrium
Click here equilibrium constant
Click here simulation equilibrium Click here simulation
Acknowledgements
Thanks to source of pictures and video used in this presentation
Thanks to Creative Commons for excellent contribution on licenseshttp://creativecommons.org/licenses/
Prepared by Lawrence Kok
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