December 2011 - SIMA
December 2011 - SIMA December 2011 - SIMA
Syngas options include a coal gasifier, coke ovengas, or BOF gas. The big advantage of coalgasification is that lower grade, inexpensive domesticcoals can be used to produce a high quality reducinggas for the MIDREX Shaft Furnace.Coal GasificationThere are three general types of coal gasifiers: fixedbed, entrained flow, and fluidized bed. All threetechnologies are based on partial oxidation(gasification) of a carbonaceous (carbon containing)feed material.The general partial oxidation reaction is:2 CH + O ———> 2 CO + n H2n 2In addition to the desired CO and H , the syngas2exiting a gasifier also contains CO , H O, CH , H S,2 2 4 2NH , and particulates. If a fixed bed gasification3technology is utilized, the syngas will also containaromatic organic compounds.While each of the gasifier types can make anacceptable reducing gas for a MIDREX DR Plant,the fixed bed and fluidized bed technologies will bethe preferred choices for many locations becausethey can accommodate the high ash domestic coals.Countries of interest include India, China, and theCIS. The leading fixed bed process is the LurgiGasification process; it is well-proven, with over 102gasifiers in commercial operation worldwide, theearliest of these built in 1955. Figure 2 shows Lurgigasifiers at the Sasol Plant in Secunda, South Africa.There are a number of fluidized bed processes,including the KBR Transport Gasifier, known asTRIG, and the U-Gas Process, which is licensedby Synthesis Energy Systems. These processes arein the early stages of commercialization, but showgood promise.The Coal Gasification ProcessFigure 3 shows a simplified MXCOL processflowsheet. In the gasification processes, coal isgasified at elevated pressures by reacting with highpressure steam and high purity oxygen to produce asyngas suitable for the production of fuels andchemicals, power generation or the reduction of ironore. The fixed bed and fluidized bed gasifiers operateFigure 2Lurgi Gasifiers in Secunda, South Africaat a temperature below the ash melting point so thecoal ash is discharged from the gasifier as a solid.Because of this low operating temperature, thesetechnologies require significantly lower quantities ofoxygen than the entrained flow gasification processeswhich melt the ash.The syngas exiting the gasifier is hot, dirty, andcontains a significant amount of non reducing gascomponents. Downstream of the gasifier, the syngasis cleaned and conditioned to remove most of theundesired components and produce saleablecommodities such as sulfur and petrochemical plantfeedstocks.Figure 3MXCOL FlowsheetDECEMBER-2011/8
MIDREX ® Direct Reduction PlantThe cleaned, high pressure syngas (reducing gas)exiting the gasification plant contains approximately85 percent H +CO, 2.5 percent CO , and 10-1222percent CH . Table I shows the syngas quality4required for MXCOL.Syngas CharacteristicTable IMXCOL Syngas QualityMIDREX RequirementCO content 2.0-3.0%2Gas Quality* > 10Gas RequirementPressure~ 2.2 net Gcal / t DRI> 3 bargH /CO ratio 1.0-2.02Sulfur content< 5 ppmvParticulates content < 10 mg / Nm 3N + Ar content < 0.5 %2* Gas Quality is defined as ( % H+ % CO2)2+ % CO ) / ( % H O2In the MIDREX Plant, the cold syngas isdepressurized to about 3 barg in a turboexpander,which generates electricity. The low pressure syngasis mixed with recycled gas to produce the requiredreducing gas. The mixed gas is then heated to over900º C and enters the MIDREX ® Shaft Furnace,where it reacts with the iron oxide to produce DRI.The reduction reactions are shown below:Fe O2 3Fe O2 3+ 3H2—> 2Fe + 3H O2+ 3CO —> 2Fe + 3CO2The spent reducing gas (top gas) exiting the shaftfurnace is scrubbed and cooled, then passed througha CO removal system. This reduces the CO content22to 2-3 percent or less, which ensures that the mixedreducing gas (syngas from the gasification plant andrecycled top gas from the MIDREX Plant) has anacceptably high reductants (H +CO) to oxidants2(H O+CO )ratio for efficient iron oxide reduction. The2 2CO removal system will also remove the sulfur gases2contained in the recycled top gas. The recycling ofthe top gas makes MXCOL a very efficient process.The CO removed from the gasification plant gas2cleaning and conditioning plant and the CO removal2system in the MIDREX Plant are high purity. Thesestreams could be sequestered or sold for enhancedoil recovery or use in a petrochemical or otheroperation.Emissions from MXCOL are shown in Table II.Table IIMXCOL EmissionsPM10 SO NOx COmg/Nm 3 mg/Nm 3 mg/Nm 3 2kg/t DRIReheater
- Page 3 and 4: CHAIRMAN’S MESSAGEI am happy that
- Page 5 and 6: Target Setting:The methodology for
- Page 7 and 8: Energy conservation Opportunities i
- Page 9: MXCOL ® : A BREAKTHROUGH IN COAL-B
- Page 14 and 15: IRON ORE PELLETS AS THE FUTURE META
- Page 16 and 17: Raw material availability:Basic raw
- Page 18 and 19: ore also could be intended to gener
- Page 20 and 21: AVERAGE PERFORMANCE PARAMETERS:Sl.
- Page 22 and 23: CONCLUSION:The salient features of
- Page 24 and 25: HARI MACHINES JOINS HANDS WITH RAFA
- Page 26 and 27: Indian Reference of RafakoSA - Pola
- Page 28 and 29: DECEMBER-2011/26
- Page 30 and 31: e maintained while taking advantage
- Page 32 and 33: Plant Upgrades Reference ListPlant
- Page 34 and 35: TRI-FLO ® :-THE NEW GENERATION MUL
- Page 36 and 37: The ability of the Tri-Flo ® to be
- Page 38 and 39: Rejects re-cleaning with a 700 mm I
- Page 40 and 41: GREEN FIELD STEEL PROJECT OF JSPLJS
- Page 42: DECEMBER-2011/40
Syngas options include a coal gasifier, coke ovengas, or BOF gas. The big advantage of coalgasification is that lower grade, inexpensive domesticcoals can be used to produce a high quality reducinggas for the MIDREX Shaft Furnace.Coal GasificationThere are three general types of coal gasifiers: fixedbed, entrained flow, and fluidized bed. All threetechnologies are based on partial oxidation(gasification) of a carbonaceous (carbon containing)feed material.The general partial oxidation reaction is:2 CH + O ———> 2 CO + n H2n 2In addition to the desired CO and H , the syngas2exiting a gasifier also contains CO , H O, CH , H S,2 2 4 2NH , and particulates. If a fixed bed gasification3technology is utilized, the syngas will also containaromatic organic compounds.While each of the gasifier types can make anacceptable reducing gas for a MIDREX DR Plant,the fixed bed and fluidized bed technologies will bethe preferred choices for many locations becausethey can accommodate the high ash domestic coals.Countries of interest include India, China, and theCIS. The leading fixed bed process is the LurgiGasification process; it is well-proven, with over 102gasifiers in commercial operation worldwide, theearliest of these built in 1955. Figure 2 shows Lurgigasifiers at the Sasol Plant in Secunda, South Africa.There are a number of fluidized bed processes,including the KBR Transport Gasifier, known asTRIG, and the U-Gas Process, which is licensedby Synthesis Energy Systems. These processes arein the early stages of commercialization, but showgood promise.The Coal Gasification ProcessFigure 3 shows a simplified MXCOL processflowsheet. In the gasification processes, coal isgasified at elevated pressures by reacting with highpressure steam and high purity oxygen to produce asyngas suitable for the production of fuels andchemicals, power generation or the reduction of ironore. The fixed bed and fluidized bed gasifiers operateFigure 2Lurgi Gasifiers in Secunda, South Africaat a temperature below the ash melting point so thecoal ash is discharged from the gasifier as a solid.Because of this low operating temperature, thesetechnologies require significantly lower quantities ofoxygen than the entrained flow gasification processeswhich melt the ash.The syngas exiting the gasifier is hot, dirty, andcontains a significant amount of non reducing gascomponents. Downstream of the gasifier, the syngasis cleaned and conditioned to remove most of theundesired components and produce saleablecommodities such as sulfur and petrochemical plantfeedstocks.Figure 3MXCOL FlowsheetDECEMBER-<strong>2011</strong>/8