This goal was realized by Fritz Haber in 1908[4, 5] when he was able to
produce ammonia in a substantial yield from nitrogen and hydrogen by the use of an
osmium catalyst at a pressure of about 175 bar and at 550 °C. Haber’s apparatus
produced about 90 grams of ammonia per hour with about 98 grams of the osmium
catalyst[1, 3, 6, 7]. Due to the cost of osmium, research into more economically
feasible catalysts was conducted. Then Alwin Mittasch of BASF in 1910 found that
adding alumina, Al2O3, and potash, K2O, to iron was a suitable catalyst for ammonia
synthesis.
At this point, there was a sizable gap between Fritz Haber’s apparatus and a
full-sized plant that would be able to mass-produce ammonia. The largest part of this
problem was the high pressure of reactant gasses that was needed to produce
ammonia. The technology to perform this high pressure reaction was developed by
Carl Bosch of BASF in 1913 who oversaw the first factory dedicated to ammonia
synthesis in Oppau, Germany[1, 8, 9]. This factory was able to produce 30 tons of
ammonia per day with 300 Kg of the doubly promoted iron catalyst with a total
pressure of 200 atmospheres of the nitrogen and hydrogen reactant gasses.
[1] Jennings, J.R., Catalytic Ammonia Synthesis Fundamentals and Practice.
[3] Topham, S.A., Catalysis, Science and Technology, ed. M.B. John R. Anderson. Vol. 7. 1985, Berlin: Springer-Verlag.
[4] Crookes, W., Report of the 68th meeting of the British Association for the Advancement of Science, Bristol, 1898. 1898, London: John Murray.
[5] Goran, M., The Story of Fritz Haber. 1967, Oklahoma: University of Oaklahoma Press.
[6] Haber, F., Z. Elek., 1910. 16: p. 244.
[7] Haber, F. and R.L. Rossignol, Z. Elek., 1913. 19: p. 53.
[8] Mittasch, A., Geschichte der Ammoniaksynthese. 1951, Weinheim: Verlag Chemie.
[9] Partington, J.R. and L.H. Parker, The Nitrogen Industry. 1922, London: Constable.
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