3.1.6 Chemical equilibria, Le Chatelier’s principle and Kc Flashcards

1
Q

Le Chatelier’s principle

A

If external condition is changed, the equilibrium will shift to
oppose the change and try to reverse it.

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2
Q

Position of equilibrium

A

Composition of the equilibrium mixture
If position of equilibrium favours reactants = equilibrium
mixture contains mostly reactants.

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3
Q

Dynamic equilibrium state

A
  1. Forward and backward reactions occur at equal states

2. Concentrations of reactants and products stay constant

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4
Q

Position of equilibrium- Temperature

Temp increase:

A

equilibrium shifts to oppose this and moves in the
endothermic direction to try and reduce the temp by
absorbing heat

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5
Q

Position of equilibrium- Temperature

Temp decrease:

A

equilibrium shifts to oppose this and moves in the
exothermic direction to try and increase the temp by giving
out heat

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6
Q

Compromise temp in industry

A

Low temp= high yield but slow rate
Compromise temp used to give a reasonable yield and rate to
make best possible yield.

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7
Q

Position of equilibrium- Pressure

Pressure increase:

A

equilibrium shifts towards the side with fewer moles of gas

to oppose the change so reduces the pressure.

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8
Q

Position of equilibrium- Pressure

Pressure decrease:

A

equilibrium shifts towards the side with more moles of gas to
oppose the change therefore increasing the pressure.

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9
Q

Advantage and disadvantages of increasing pressure

industrially

A

Adv: higher yield of product and faster rate of reaction
Disadv: Expensive: equipment to contain high pressures and
high electricity costs for pumping gases to make high
pressures.

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10
Q

Position of equilibrium- Catalyst

A

No affect apart from speeding up rate at which equilibrium is
achieved.
Speed up rates of forward and backward reactions by the
same amounts

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11
Q

Haber process

A

N2 + 3H2 2NH3 ΔH = -ve (exo)

Temp: 450*C (low temp: good yield, slow rate- compromise
temp used)
Pressure: 200-1000 atm (high pressure = good yield and high
rate)
Catalyst: iron
Expensive: equipment required and electricity needed
Use of ammonia: fertiliser

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12
Q

Contact process

A

Stage 1:
S (s) + O2 (g) –> SO2 (g)
Stage 2:
SO2 (g) + 1/2O2(g) SO3 (g) ΔH = -98kJ mol-1
Temp: 450*C (low temp: good yield, slow rate-
compromise temp used)
Pressure: 10 atm (high pressure = slightly better yield and high rate; too high temp = high energy costs to produce the pressure)
Catalyst: V2O5 (vanadium (v) oxide)

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13
Q

Producing methanol from carbon monoxide:

A

CO (g) + 2H2(g) CH3OH (g) ΔH = -ve (exo)
CO (g) + 2H2(g) CH3OH (g) ΔH = -ve (exo)
Temp: 400*C
Pressure: 50 atm
Catalyst: Chromium and
ZnOx

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14
Q

Hydrating ethene to produce ethanol

A

CH2=CH2 (g) + H2O(g) CH3CH2 (l) ΔH = -ve (exo)
Temp: 300*C
Pressure: 70 atm - too high pressures = polymerisation of ethene to poly(ethene)
Catalyst: concentrated H3PO4- phosphoric acid

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15
Q

Catalysts in industry

A

Catalysts: speed up rate of reaction allowing lower temps to be used so lower energy costs
No affect on position of equilibrium

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16
Q

Unreacted products in industry

A

Recycling- reactants put back into reactor. Improving overall yield of all processes.
-Methanol and Ethanol can be used as fuelds
Disadv- recycling costly