Agriculture Reference
In-Depth Information
Table 5. The energy input for production of ammonia
Region
GJ/ton NH 3
Reference
sources
min
max
World average
36.9
27.6
53.0
a
36.6
27.0
58.2
b
41.5
28.0
c
Europe
34.7
d
32.1
28.4
e
35.0
28.0
c
Russia + Central Europe
40.7
c
North America
37.9
28.0
c
China and India
47.6
c
Rest of the world 36.4
References: a = Williams & Al-Ansari, 2007; b = IFA, 2009; c = IEA, 2007; d = Haas & van Dijk, 2010
and e = Kongshaug, 1998.
Thus, due to consumption of natural gas or other hydrocarbons both for feedstock and for
fuel, CO 2 emissions are the major component of GHG budgets for ammonia manufacture.
Table 6. The GHGs emissions, expressed as CO 2 equivalent, for production of ammonia
Region
ton CO 2 eq./ton NH 3
Reference
Sources min max
World average 2.1 1.5 3.1 a
Europe 1.9 b
1.8 1.6 c
References: a = Williams & Al-Ansari, 2007 b = Haas & van Dijk, 2010; c = Kongshaug, 1998.
Nitric Acid
Nitric acid is used in the manufacture of ammonium nitrate, calcium nitrate and
potassium nitrate. For fertilizer purposes, the acid strength is in the range of 50-65%.
Ammonia is vaporized, mixed with air and burned over a platinum/rhodium alloy catalyst to
form nitrogen monoxide and water (eq. 1) according the following reactions (UNEP/UNIDO,
1998):
4NH 3 + 5O 2 4NO + 6H 2 O
(1)
Simultaneously, some nitrogen and nitrous oxide are formed (eq. 2 and 3):
4NH 3 + 3O 2 2N 2 + 6H 2 O
(2)
4NH 3 + 4O 2 2N 2 O + 6H 2 O
(3)
The nitric oxide is oxidized to nitrogen dioxide, and the latter is absorbed in water to give
nitric acid (eq. 4 and 5):
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