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

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

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Chapter 4Achieved environmental benefitsNote: Conversion rates, tail gas SO 2 concentrations and specific SO 2 load in tail gases arecorrelated, see Figure 4.7, Figure 4.8 and Figure 4.9.Average daily conversion rates of at least 99.7 – 99.9 % with double contact processes [154,TWG on LVIC-AAF]. Conversion rates of 99.8 % are achievable with four catalyst beds andinlet gas of low variabilility. With four catalyst beds and inlet gases from non-ferrous metalproduction (higher variability), 99.7 % are achievable [57, Austrian UBA, 2001]. For examplesof degree of variation of the SO 2 inlet concentration and the variation of the conversion rate, seeFigure 4.12 and Figure 4.13.For energy recovery and export, see Section 4.4.15.99,914Conversion rate in %99,8599,899,75Conversionrate in %SO 2 inlet concentrationin % v/v131211109SO2 inlet cioncentration in % v/v99,724 hours of operation8Figure 4.12: SO 2 inlet concentration and conversion rate of production based on sulphur burning[154, TWG on LVIC-AAF, 2006]99,8012,099,7511,5Conversion rate in %99,7099,6599,6099,5599,5099,4599,4099,3599,30Conversionrate in %SO 2 inletconcentrationin % v/v11,010,510,09,59,08,58,07,57,0SO2 inlet concentration in % v/v24 hours of operationFigure 4.13: SO 2 inlet concentration and conversion rate of production based on Zn roasting[154, TWG on LVIC-AAF, 2006]174 Large Volume Inorganic ChemicalsAmmonia, Acids and Fertilisers

Chapter 4Cross-media effectsNone believed likely.Operational dataIn general, the process uses gases with an SO 2 content of 10 to 11 % [58, TAK-S, 2003]. Theinlet gas temperature is about 400 ºC. Gases with lower temperatures, e.g. metallurgical gasesafter purification, require reheating from 50 to 400 ºC. This is usually carried out with recoveredheat from the conversion process [57, Austrian UBA, 2001].Applicability• applicable for SO 2 inlet content of 5 – 12 % v/v [58, TAK-S, 2003]• applicable for SO 2 inlet content of >4.5 up to 14 % v/v. Below 4.5 % v/v, double contactprocesses do not work autothermally [59, Outukumpu, 2005].Pressure contact process. One plant is known to operate a double contact process at an elevatedpressure of 5 bar. This increases the conversion rate by shifting the conversion equilibrium andfavouring the formation of SO 3 . The pressure double contact process achieves 99.8 – 99.85 %conversion; here, the tail gas contains 200 – 250 ppm SO 2 . The disadvantages are higherelectricity consumption and, at the same time, less steam production. Higher NO x emissions arecaused by higher sulphur combustion temperatures (1800 ºC). In comparison, savings of 10 – 17% on investment costs are gained. However, the benefits from building a plant for smaller gasvolumes (at higher pressure) are offset by more stringent safety regulations and additional costsfor pressure resistant materials.EconomicsThe double contact/double absorption process is considered as the baseline for inlet gas SO 2concentrations >4.5 % v/v.Driving force for implementationDevelopment of the single contact/single absorption process.References to literature and example plants[57, Austrian UBA, 2001, 58, TAK-S, 2003], Donau Chemie AG, Lenzing AG, Degussa AGLarge Volume Inorganic ChemicalsAmmonia, Acids and Fertilisers 175

Chapter 4Cross-media effectsNone believed likely.Operational dataIn general, the process uses gases with an SO 2 content of 10 to 11 % [58, TAK-S, 2003]. Theinlet gas temperature is about 400 ºC. Gases with lower temperatures, e.g. metallurgical gasesafter purification, require reheating from 50 to 400 ºC. This is usually carried out with recoveredheat from the conversion process [57, Austrian UBA, 2001].Applicability• applicable for SO 2 inlet content of 5 – 12 % v/v [58, TAK-S, 2003]• applicable for SO 2 inlet content of >4.5 up to 14 % v/v. Below 4.5 % v/v, double contactprocesses do not work autothermally [59, Outukumpu, 2005].Pressure contact process. One plant is known to operate a double contact process at an elevatedpressure of 5 bar. This increases the conversion rate by shifting the conversion equilibrium andfavouring the formation of SO 3 . The pressure double contact process achieves 99.8 – 99.85 %conversion; here, the tail gas contains 200 – 250 ppm SO 2 . The disadvantages are higherelectricity consumption and, at the same time, less steam production. Higher NO x emissions arecaused by higher sulphur combustion temperatures (1800 ºC). In comparison, savings of 10 – 17% on investment costs are gained. However, the benefits from building a plant for smaller gasvolumes (at higher pressure) are offset by more stringent safety regulations and additional costsfor pressure resistant materials.EconomicsThe double contact/double absorption process is considered as the baseline for inlet gas SO 2concentrations >4.5 % v/v.Driving force for implementationDevelopment of the single contact/single absorption process.References to literature and example plants[57, Austrian UBA, 2001, 58, TAK-S, 2003], Donau Chemie AG, Lenzing AG, Degussa AG<strong>Large</strong> <strong>Volume</strong> <strong>Inorganic</strong> <strong>Chemicals</strong> – <strong>Ammonia</strong>, Acids and Fertilisers 175

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