Large Volume Inorganic Chemicals - Ammonia ... - ammk-rks.net
Large Volume Inorganic Chemicals - Ammonia ... - ammk-rks.net Large Volume Inorganic Chemicals - Ammonia ... - ammk-rks.net
Chapter 22.4 Techniques to consider in the determination of BATConventional steam reforming is described in Section 2.2.3.Partial oxidation is described in Section 2.2.4.2.4.1 Advanced conventional processesDescriptionThe different process steps for the conventional steam reforming process are integrated withrespect to mass and energy flow. During the years of development, a considerable reduction inenergy consumption has been achieved by improving the existing components in the process. Inaddition, today’s equipment and machinery can achieve a considerable thermodynamicefficiency and a high degree of reliability. Online availability exceeding 93 % is not uncommonin such plants. Advanced conventional process plants are usually characterised by the followingfeatures:• high duty primary reformer using high pressures of up to 40 bar• equipped with low NO x burners• stoichiometric air in secondary reforming (stoichiometric H/N ratio)• low energy CO 2 removal system.Differences in the configurations offered by the various engineering contractors generally resultfrom the optimised arrangements that they utilise and from using different well developedequipment designs. Specific examples of some applied techniques are:• increasing the temperatures of the mixed feed and process air in line with the current limitsfor metallurgical standards for construction. This, in turn, allows for a reduced reformerfiring and an increase in the reformer operating pressure, which also saves in the energyneeded for compression of the synthesis gas• utilising the recovered heat after the secondary reformer to raise and superheat steam• applying improved designs of high temperature shift reactors for lower steam to carbon ratio• utilising ammonia converter designs which use small size catalysts for higher conversions• ensuring the efficient recovery of a large proportion of reaction heat energy from theammonia synthesis. This is achieved by extracting the heat from the ammonia synthesisloop and using it to raise high pressure steam• applying a highly efficient ammonia condensation and refrigeration system.The high levels of NO x emissions of the conventional process are mainly due to the particularfiring conditions in the primary reformer. The use of low NO x burner techniques minimises thelevel, but relatively high NO x emissions still remain.Achieved environmental benefitsIn comparison with conventional processes, the following environmental benefits are achieved:• reduced reformer firing, lower NO x emissions• energy savings.For achievable emission and consumption levels, see:• Table 2.6 for energy consumption• Table 2.7 for NO x emissions• and Table 2.8 and Table 2.9 for other levels.58 Large Volume Inorganic Chemicals – Ammonia, Acids and Fertilisers
Chapter 2Cross-media effects• still relatively high NO x emissions.Operational dataSee Description.ApplicabilityApplicable in new and existing plants. The applicability in existing plants requires anassessment of the specific case.EconomicsCost benefits can be presumed.Driving force for implementationPlant optimisation and cost benefits.References to literature and example plants[1, EFMA, 2000, 3, European Commission, 1997]Large Volume Inorganic Chemicals – Ammonia, Acids and Fertilisers 59
- Page 36 and 37: Chapter 11,8Relative production cap
- Page 38 and 39: Chapter 11.2.3 Supply of steam and
- Page 40 and 41: Chapter 11.3 Overview of emissions
- Page 42 and 43: Chapter 1ApplicabilityGenerally app
- Page 44 and 45: Chapter 11.4.3 Handling excess stea
- Page 46 and 47: Chapter 11.4.5 Optimisation/mainten
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- Page 52 and 53: Chapter 11.4.9 Environmental manage
- Page 54 and 55: Chapter 1(v) Documentation- establi
- Page 56 and 57: Chapter 1iv. allow for comparison w
- Page 58 and 59: Chapter 1A number of studies show t
- Page 60 and 61: Chapter 11.5 Common BATIn understan
- Page 62 and 63: Chapter 11.5.2 BAT for environmenta
- Page 64 and 65: Chapter 2Location CompanyCapacity F
- Page 66 and 67: Chapter 22.2.2 Output from ammonia
- Page 68 and 69: Chapter 22.2.3.2 Primary reformingT
- Page 70 and 71: Chapter 2Process name Solvent/reage
- Page 72 and 73: Chapter 22.2.4 Partial oxidationThe
- Page 74 and 75: Chapter 2In the moving bed process,
- Page 76 and 77: Chapter 22.2.6 Storage and transfer
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- Page 80 and 81: Chapter 22.3.2 NO x emissionsTable
- Page 82 and 83: Chapter 22.3.3 Other consumption le
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- Page 90 and 91: Chapter 22.4.3 Heat exchange autoth
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- Page 100 and 101: Chapter 22.4.9 Combined Claus unit
- Page 102 and 103: Chapter 2Operational dataSee Descri
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- Page 108 and 109: Chapter 22.4.16 Stripping and recyc
- Page 110 and 111: Chapter 22.4.18 Use of sulphur resi
- Page 112 and 113: Chapter 22.4.20 Indirect cooling of
- Page 114 and 115: Chapter 22.4.22 Ammonia removal fro
- Page 116 and 117: Chapter 22.4.24 Metal recovery and
- Page 118 and 119: Chapter 2Driving force for implemen
- Page 120 and 121: Chapter 22.5 BAT for ammoniaBAT is
- Page 123 and 124: Chapter 33 NITRIC ACID3.1 General i
- Page 125 and 126: Chapter 3Pressure in bar Temperatur
- Page 127 and 128: Chapter 33.2.5 Tail gas properties
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- Page 135 and 136: Chapter 3Process typeNO x emission
Chapter 22.4 Techniques to consider in the determination of BATConventional steam reforming is described in Section 2.2.3.Partial oxidation is described in Section 2.2.4.2.4.1 Advanced conventional processesDescriptionThe different process steps for the conventional steam reforming process are integrated withrespect to mass and energy flow. During the years of development, a considerable reduction inenergy consumption has been achieved by improving the existing components in the process. Inaddition, today’s equipment and machinery can achieve a considerable thermodynamicefficiency and a high degree of reliability. Online availability exceeding 93 % is not uncommonin such plants. Advanced conventional process plants are usually characterised by the followingfeatures:• high duty primary reformer using high pressures of up to 40 bar• equipped with low NO x burners• stoichiometric air in secondary reforming (stoichiometric H/N ratio)• low energy CO 2 removal system.Differences in the configurations offered by the various engineering contractors generally resultfrom the optimised arrangements that they utilise and from using different well developedequipment designs. Specific examples of some applied techniques are:• increasing the temperatures of the mixed feed and process air in line with the current limitsfor metallurgical standards for construction. This, in turn, allows for a reduced reformerfiring and an increase in the reformer operating pressure, which also saves in the energyneeded for compression of the synthesis gas• utilising the recovered heat after the secondary reformer to raise and superheat steam• applying improved designs of high temperature shift reactors for lower steam to carbon ratio• utilising ammonia converter designs which use small size catalysts for higher conversions• ensuring the efficient recovery of a large proportion of reaction heat energy from theammonia synthesis. This is achieved by extracting the heat from the ammonia synthesisloop and using it to raise high pressure steam• applying a highly efficient ammonia condensation and refrigeration system.The high levels of NO x emissions of the conventional process are mainly due to the particularfiring conditions in the primary reformer. The use of low NO x burner techniques minimises thelevel, but relatively high NO x emissions still remain.Achieved environmental benefitsIn comparison with conventional processes, the following environmental benefits are achieved:• reduced reformer firing, lower NO x emissions• energy savings.For achievable emission and consumption levels, see:• Table 2.6 for energy consumption• Table 2.7 for NO x emissions• and Table 2.8 and Table 2.9 for other levels.58 <strong>Large</strong> <strong>Volume</strong> <strong>Inorganic</strong> <strong>Chemicals</strong> – <strong>Ammonia</strong>, Acids and Fertilisers