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The 'Haber process' (also known as 'Haber–Bosch process') is the reaction of nitrogen and hydrogen, over an iron-substrate, to produce ammonia. The Haber process is important due to the fact that ammonia is difficult to produce, on an industrial scale. Even though 78.1% of the air we breathe is nitrogen, the gas is relatively inert due to the strength of the triple bond that keeps the molecule together. It was not until the start of the twentieth century that this method was developed to harness the atmospheric abundance of nitrogen to create ammonia, which can then be oxidised to make the nitrates and nitrites essential for the production of nitrate fertilizer and munitions.

Contents

Description

History

The process

Synthesis gas preparation

Ammonia synthesis

Reaction Rate and Equilibrium

Catalysts

Conclusion

See also

References

External links

Description

In the 'Haber Process', nitrogen (N₂) and hydrogen (H₂) gases are reacted over an iron catalyst (Fe³⁺) in which aluminium oxide (Al₂O₃) and potassium oxide (K₂O) are used as promoters. The reaction is carried out under conditions of 250 atmospheres (atm), 450-500 °C; resulting in a yield of 10-20%:
:N₂(g) + 3H₂(g) → 2NH₃(g) ΔH^o = -92.4 kJ/mol
(Where ΔH^o is the standard heat of reaction or standard enthalpy change)
These conditions are chosen due to the high reaction rate which they foster despite the poor relative amount of ammonia produced.

History

The process was first patented by Fritz Haber. In 1910 Carl Bosch, while working for chemical company BASF, successfully commercialized the process and secured further patents. It was first used on an industrial scale by the Germans during World War I: Germany had previously imported 'Chilean saltpeter' from Chile, but the demand for munitions and the uncertainty of this supply in the war prompted the adoption of the process. Without this process, Germany would almost certainly have run out of munitions by 1916, thereby ending the war. The ammonia produced was oxidized for the production of nitric acid in the Ostwald process, and the nitric acid for the production of various explosive nitro compounds used in munitions.

The process

The bulk of the chemical technology consists in getting the hydrogen from methane or natural gas using heterogeneous catalysis and then react it with the atmospheric nitrogen.

Synthesis gas preparation

First, the methane is cleaned, mainly to remove sulphur impurities that would poison the catalysts. This is done by turning sulphur into hydrogen sulphide:
:CH₃SH + H₂ → CH₄ + H₂S
and then reacting with zinc oxide to form zinc sulphide:
: H₂S + ZnO → ZnS + H₂O
The clean methane is then reacted with steam over a catalyst of nickel oxide. This is called steam reforming and occurs in two steps:
First step:
(one mole of methane in)
:CH₄ + H₂O → CO + 3H₂ (3 moles of hydrogen out)
:CO + H₂O → CO₂ + H₂ (1 extra mole of hydrogen out)
''Note that 4 moles of hydrogen are produced per mole of methane''
Secondary reforming then takes place with the addition of air:
:2 H₂ + O₂ + N₂ → 2H₂O + N₂
''This now gives a ratio of nitrogen to hydrogen of'' '1:5'
Then occur two’’shifts’’ which take CO to CO₂ again by reaction with steam, one at high temperature, then one at low temperature:
:CO + H₂O → CO₂ + H₂ high temperature '1:6'
:→ the catalyst here is a mixture of iron, chromium and copper
:CO + H₂O → CO₂ + H₂ low temperature '1:7'
:→ the catalyst here is a mixture of copper, zinc and aluminum
The removal of carbon dioxide is easily done by reaction with potassium carbonate.
:K₂CO₃ + H₂O + CO₂→ 2KHCO₃
The gas mixture is now passed into a methanator which converts any remaining CO₂ into methane for recycling:
: CO₂ + 4H₂ → CH₄ + 2H₂O '1:3'
We now have a gas mixture containing nitrogen and hydrogen in the correct ratio of 1:3. This is called synthesis gas.

Ammonia synthesis

The final stage is the crucial synthesis of ammonia using promoted magnetite, iron oxide, as the catalyst:
:N₂(g) + 3H₂(g) → 2NH₃(g) + ΔH^o = -92.4 kJ/mol
This is done at 100 - 250 atmospheres (atm) and between 300 and 550 °C, passing the gases over four beds of catalyst, with cooling between each pass to maintain a reasonable equilibrium constant. On each pass only about 15% conversion occurs, but any un-reacted gases will be recycled, so that eventually an overall yield of 98% can be achieved.

Reaction Rate and Equilibrium

There are two main opposing factors in this synthesis: the temperature and the rate of reaction. At room temperature, the reaction is painfully slow and the obvious solution is to raise the temperature. This may increase the rate of the reaction but, since the reaction is exothermic, it also has the effect, according to Le Chatelier's Principle, of favouring the reverse reaction and thus reducing equilibrium constant, given by:

As the temperature increases, the equilibrium is shifted and hence, the constant drops dramatically according to the Van't Hoff equation.

Temp. (°C)	Keq
25	6.4 x 102
200	4.4 x 10-1
300	4.3 x 10-3
400	1.6 x 10-4
500	1.5 x 10-5

Thus one might suppose that a low temperature is to be used and some other means to increase rate. However, the catalyst itself requires a temperature of at least 400 °C to be efficient.
Pressure is the obvious choice to favour the forward reaction because there are 4 moles of reactant for every 2 moles of product, and the pressure used (around 200 atm) alters the equilibrium concentrations to give a profitable yield.
Economically, though, pressure is an expensive commodity. Pipes and reaction vessels need to be strengthened, valves more rigorous, and there are safety considerations of working at 200 atm. In addition, running pumps and compressors takes considerable energy. Thus the compromise used gives a single pass yield of around 15%.
An additional way to force the reaction to the right is to remove the product from the system. This is done by lowering the temperature of the product gases that are still under high pressure and effectively freezing out the liquid ammonia, while the hydrogen and nitrogen remain as gases.

Catalysts

The catalyst has no effect on the position of equilibrium, rather, it provides an alternative pathway with lower activation energy and hence increases the reaction rate, while remaining chemically unchanged at the end of the reaction. The first Haber–Bosch reaction chambers used osmium and uranium catalysts. However, today a much less expensive iron catalyst is used almost exclusively.
In industrial practice, the iron catalyst is prepared by exposing a mass of magnetite, an iron oxide, to the hot hydrogen feedstock. This reduces some of the magnetite to metallic iron, removing oxygen in the process. However, the catalyst maintains most of its bulk volume during the reduction, and so the result is a highly porous material whose large surface area aids its effectiveness as a catalyst. Other minor components of the catalyst include calcium and aluminum oxides, which support the porous iron catalyst and help it maintain its surface area over time, and potassium, which increases the electron density of the catalyst and so improves its reactivity.
The reaction mechanism, involving the heterogeneous catalyst, is believed to be as follows:
# N₂(g) → N₂(adsorbed)
#' N₂(adsorbed) → 2N(adsorbed)'
# H₂(g) → H₂(adsorbed)
# H₂(adsorbed) → 2H(adsorbed)
# N(adsorbed) + 3H(adsorbed)→ NH₃(adsorbed)
# NH₃(adsorbed) → NH₃(g)
Reaction 5 occurs in three steps, forming NH, NH₂, and then NH₃. Experimental evidence points to reaction 2 as being the slow, rate-determining step.

Conclusion

The Haber process now produces 100 million tons of nitrogen fertilizer per year, mostly in the form of anhydrous ammonia, ammonium nitrate, and urea. 1% of the world's annual energy supply is consumed in the Haber process.^[1] That fertilizer is responsible for sustaining 40% of the Earth's population, as well as various deleterious environmental consequences. .

See also

★ Chemical kinetics

★ Reaction rate

★ Rate equation

References

1. Science, 6 September 2002: Vol. 297. no. 5587, pp. 1654 - 1655 DOI: 10.1126/science.1076659


★ ''Enriching the Earth: Fritz Haber, Carl Bosch, and the Transformation of World Food Production'' by Vaclav Smil (2001) ISBN 0-262-19449-X

★ ''Fertilizer Industry: Processes, Pollution Control and Energy Conservation'' by Marshall Sittig (1979) Noyes Data Corp., N.J. ISBN 0-8155-0734-8

★ “Heterogeneous Catalysts: A study Guide”,

★ ”CIEC Catalysis”, [1]

★ Haber Process for Ammonia Synthesis

External links

★ What is the Haber-Bosch Process?

★ Haber-Bosch process

★ Fertilizer,agriculture and the production of food

★ Food Crises and the Role of Agriculture: Past and Current

★ Britannica guide to Nobel Prizes: Fritz Haber

★ Nobel e-Museum - Biography of Fritz Haber

★ Uses and Production of Ammonia