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Large Volume Inorganic Chemicals - Ammonia ... - ammk-rks.net

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Chapter 11.1.2 Environmental issues1.1.2.1 Energy consumption and emission of greenhouse gasesFor emissions of N 2 O from the production of nitric acid, see Section 3.1 and Table 3.7.Energy consumption has become an environmental issue because of the ecological impact ofenergy production and transport, and because of the emission of greenhouse gases from fuelburning. Fertiliser production currently accounts for about 2 – 3 % of the total global energyconsumption. For Western Europe, the corresponding figure is about 1 %. Nitrogen fertilisersaccount for a large majority of this consumption. Most of the energy for fertiliser production isrequired by the fixation of atmospheric nitrogen to manufacture ammonia. Considerableenergy is also required for the conversion of ammonia to urea. For the manufacture ofammonium nitrate, the conversion of ammonia to nitric acid provides a <strong>net</strong> energy gain whichcan be used, for example, to produce electrical energy via a steam turbine. The neutralisation ofammonia with nitric acid to produce ammonium nitrate also releases energy. In the case ofphosphate fertilisers, energy is required for the mining of the ore, for the production ofphosphoric acid, for the further processing into finished products and for pollution control [27,UNEP, 1998].Although fertiliser production will always consume large amounts of energy in processesrequiring high temperatures and pressures, the industry has become more energy efficientthrough improved design. <strong>Ammonia</strong> factories built in 1990 used some 30 per cent less energyper tonne of nitrogen than those designed around 1970. Energy use in a new plant, using naturalgas in a reforming process, including raw materials, can now be lower than 30 GJ/tonne NH 3 ,compared with 75 GJ/tonne for the processes prevalent in the early 1960s. Partial oxidationprocesses use considerably more energy than reforming processes. In 1995, the average for allplants in the US fertiliser industry was about 40 GJ/tonne [27, UNEP, 1998].1.1.2.2 Energy exportAmongst the AAF industries the production of sulphuric acid and nitric acid are candidatesfor exporting energy as high, medium, or low pressure steam or as hot water. If all thermalenergy is converted to electrical power via a steam turbine, the <strong>net</strong> energy export will bereduced by approximately 65 %.See also Sections 2.3.1.1, 3.2.6 and 4.4.15, Table 4.17, Table 4.18, Table 4.19 and Table 4.20.Production of Export as Rema<strong>rks</strong>HNO 3H 2 SO 4HP steamHP steamLP steamHot waterPlants optimised for maximum energy export tend to have lowtemperatures in tail gases.1. This might entail a safety issue, due to the potential for formationof AN in the expander turbine and the stack, see Section 3.4.102. This might interfere with the selection and applicability of tail gastreatment systems, see Section 3.4.10 and 3.4.6The potential for energy export depends on the combination of the SO 2source, the SO 2 level in the inlet gas and the applied conversion process.The energy export can be increased significantly, if the waste heat fromthe acid cooling can be recovered and used<strong>Ammonia</strong> plants can be designed to export energy and at the same timeNH 3HP steamimproving the <strong>net</strong> energy consumptionTable 1.3: Considerations on energy exportThis table is based on the referenced sections<strong>Large</strong> <strong>Volume</strong> <strong>Inorganic</strong> <strong>Chemicals</strong> – <strong>Ammonia</strong>, Acids and Fertilisers 3

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