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EUROPEAN COMMISSIONIntegrated Pollu
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Executive SummaryEXECUTIVE SUMMARYT
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Executive SummaryII.Production and
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Executive Summarybed, using a cesiu
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Executive SummaryConversion process
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Executive SummaryBAT is to treat al
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PrefacePREFACE1. Status of this doc
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Preface5. How to understand and use
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2.2.4.2 Gasification of heavy hydro
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5.4.2 Hemihydrate process (HH) ....
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10.4.3 Fluoride recovery and abatem
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Figure 8.1: Overview of the product
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Table 4.20: Energy balance of a dou
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ScopeSCOPEThis document on Large Vo
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Chapter 197 % of nitrogen fertilise
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Chapter 11.1.2.3 High exhaust gas v
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Chapter 1the SSD of NPK does not le
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Chapter 11,8Relative production cap
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Chapter 11.2.3 Supply of steam and
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Chapter 11.3 Overview of emissions
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Chapter 1ApplicabilityGenerally app
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Chapter 11.4.3 Handling excess stea
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Chapter 11.4.5 Optimisation/mainten
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Chapter 1Operational dataNo informa
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Chapter 1ApplicabilityEspecially ap
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Chapter 11.4.9 Environmental manage
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Chapter 1(v) Documentation- establi
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Chapter 1iv. allow for comparison w
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Chapter 1A number of studies show t
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Chapter 11.5 Common BATIn understan
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Chapter 11.5.2 BAT for environmenta
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Chapter 2Location CompanyCapacity F
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Chapter 22.2.2 Output from ammonia
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Chapter 22.2.3.2 Primary reformingT
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Chapter 2Process name Solvent/reage
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Chapter 22.2.4 Partial oxidationThe
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Chapter 2In the moving bed process,
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Chapter 22.2.6 Storage and transfer
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Chapter 2Production process Feedsto
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Chapter 22.3.2 NO x emissionsTable
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Chapter 22.3.3 Other consumption le
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Chapter 2ParameterProcessEmission l
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Chapter 22.4 Techniques to consider
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Chapter 22.4.2 Processes with reduc
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Chapter 22.4.3 Heat exchange autoth
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Chapter 22.4.4 Revamp: increase cap
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Chapter 22.4.5 Pre-reformingDescrip
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Chapter 2ApplicabilityGenerally app
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Chapter 22.4.7 Advanced process con
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Chapter 22.4.9 Combined Claus unit
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Chapter 2Operational dataSee Descri
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Chapter 22.4.12 Preheating of combu
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Chapter 22.4.14 Isothermal shift co
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Chapter 22.4.16 Stripping and recyc
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Chapter 22.4.18 Use of sulphur resi
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Chapter 22.4.20 Indirect cooling of
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Chapter 22.4.22 Ammonia removal fro
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Chapter 22.4.24 Metal recovery and
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Chapter 2Driving force for implemen
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Chapter 22.5 BAT for ammoniaBAT is
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Chapter 33 NITRIC ACID3.1 General i
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Chapter 3Pressure in bar Temperatur
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Chapter 33.2.5 Tail gas properties
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Chapter 33.3 Current emission and c
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Chapter 3N 2 O emission levelProces
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Chapter 3N 2 O emission levelProces
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Chapter 3Process typeNO x emission
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Chapter 3Process typeNO x emission
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Chapter 3140120Generation factor %1
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Chapter 33.4.2 Optimisation of the
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Chapter 33.4.3 Alternative oxidatio
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Chapter 33.4.4 Optimisation of the
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Chapter 3Achieved environmental ben
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Chapter 33.4.5 N 2 O decomposition
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Chapter 33.4.6 Catalytic N 2 O deco
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Chapter 3According to [89, Kuiper,
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Chapter 33.4.7 Combined NO x and N
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Chapter 3EconomicsInvestment costs.
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Chapter 3Operational dataSee descri
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Chapter 3NOx removal efficiency in
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Chapter 33.4.10 Addition of H 2 O 2
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Chapter 33.4.11 NO X reduction duri
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Chapter 3Installing a low temperatu
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Chapter 3NO x emission level as NO
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Chapter 3Operational dataNo specifi
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Chapter 4Country Company Location C
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Chapter 4Country Company Location C
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Chapter 4Figure 4.2 gives an overvi
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Chapter 4Two general converter type
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Chapter 4Figure 4.6 gives an impres
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Chapter 44.2.3 Sulphur sources and
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Chapter 44.2.3.5 Non-ferrous metal
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Chapter 4Sulphur source/SO 2 produc
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Chapter 44.3 Current emission and c
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Chapter 410Tail gas specific SO2 lo
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Chapter 4Capacity in tonnesof 100 %
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Chapter 4Capacity in tonnesof 100 %
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Chapter 4SO 2 sourceSpent acid and
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Chapter 4Cross-media effectsWithout
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Chapter 4Achieved environmental ben
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Chapter 44.4.3 Addition of a 5 th b
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Chapter 44.4.4 Application of a Cs-
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Chapter 4EUR/yearWaste gas volume (
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Chapter 44.4.6 Replacement of brick
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Chapter 4EUR/yearWaste gas volume (
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Chapter 4PlantSO 2 sourceInlet SO 2
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Chapter 44.4.10 Combination of SCR
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Chapter 4Achieved environmental ben
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Chapter 4Driving force for implemen
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Chapter 44.4.14 Monitoring of SO 2
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Chapter 4EconomicsCost benefits can
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Chapter 4Energy inputRecovery and l
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Chapter 44.4.16 Minimisation and ab
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Chapter 44.4.17 Minimisation of NO
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Chapter 44.4.19 Tail gas scrubbing
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Chapter 7- the product drops slowly
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Chapter 7• recovered heat from wa
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Chapter 7.7.4.8 Conversion of Ca(NO
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Chapter 77.4.9 Multistage scrubbing
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Chapter 77.4.10 Combined treatment
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Chapter 7Driving force for implemen
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Chapter 7[79, Carillo, 2002] descri
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Chapter 77.5 BAT for NPK fertiliser
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Chapter 88 UREA AND UAN8.1 General
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Chapter 8Various strategies have be
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Chapter 88.3 Current emission and c
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Chapter 8ConsumptionofPer tonne ure
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Chapter 8Per tonneurea in GJRemarks
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Chapter 8Process water after treatm
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Chapter 8Pollutant Source g/tonne u
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8.4 Techniques to consider in the d
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Chapter 88.4.2 CO 2 stripping proce
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Chapter 88.4.3 NH 3 stripping proce
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Chapter 88.4.4 Isobaric double recy
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Chapter 88.4.5 Safe NH 3 washing fr
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8.4.7 Revamping conventional plants
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Chapter 8References to literature a
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Chapter 8ApplicabilityGenerally app
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Chapter 8Achieved environmental ben
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Chapter 88.4.11 Treatment of exhaus
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Chapter 88.4.12 Process water treat
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Chapter 88.4.13 Monitoring of key p
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Chapter 88.4.14 UAN: partial recycl
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Chapter 99 AN AND CAN9.1 General in
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Chapter 99.2 Applied processes and
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Chapter 9automatically adjusted by
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Chapter 9Some examples of granulato
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Chapter 9Pollutant mg/Nm 3 g/tonne
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Chapter 9ParameterWaste water emiss
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Chapter 9Cross-media effectsProcess
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Chapter 9Fertiberia S.A. in Cartage
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Chapter 9Cross-media effectsNone be
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Chapter 9Cross-media effectsNone be
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Chapter 99.4.6 Exhaust gas treatmen
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Chapter 99.5 BAT for AN/CANBAT is t
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Chapter 1010.2 Applied processes an
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Chapter 1010.3 Current emission and
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Chapter 10DustAMFERT, Rock grinding
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Chapter 1010.4 Techniques to consid
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Chapter 1010.4.3 Fluoride recovery
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Chapter 1010.5 BAT for superphospha
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Chapter 1111.2 Recommendations for
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References12 REFERENCES1 EFMA (2000
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References64 Kristiansen and Jensen
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References112 Gry (2001). "Program
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Glossary13 GLOSSARYMolecular weight
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GlossaryDDAP Diammonium Phosphate (
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GlossaryPSAPTFEPressure Swing Adsor
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GlossaryMoS 2N 2N 2 ONH 2 CONHCONH
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AnnexesCapacity Inlet SO 2 Processt