Netherlands, with alternative fuels - ALF-CEMIND at ENCI Maastricht.pdfBenelux Alternative fuels at...
Transcript of Netherlands, with alternative fuels - ALF-CEMIND at ENCI Maastricht.pdfBenelux Alternative fuels at...
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Benelux
Alternative fuels at ENCI Maastricht
ALF-CEMIND study tour, aug 29 & 30, 2007
Practical experiences from the Maastricht Cement works , the Netherlands, with alternative fuels
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PROGRAM 30.08.2007
1. General introduction ENCI Maastricht cement works / A F
2. BioMill (dried sewage sludge grinding)
3. SBI (coarse fuels handling installation)
4. Plant visit
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Cement grinding
Clinker production
Cement grinding
IJMUIDEN
ROTTERDAM
MAASTRICHT
DEN BOSCH
ENCI production locations
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PLANT MAASTRICHT* New organisation per 01.07.2005* 3 hierarchical levels (MT – Teamleaders – Teams)
(Year end) Real Real Real Target2004 2005 2006 2007
ClinkerRegular FTE's 159,4 88,8 86,1 88,5Future pre pension 16 7 -
CementRegular FTE's 159,4 94,8 91,8 96,0Future pre pension 17,5 9,4 -
Plant Maastricht 318,8 217,1 194,3 184,5
Real Real Real Target2004 2005 2006 2007
Cement equivalent in Kton 1.215 1.226 1.349 1.334
Productivity Tons/Fte 3.692 5.635 6.906 7.230
Overview Manpower
Productivity
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•Long dry kiln, 1968 (L: 180 m, Ø: 5,5 m)•2 stage preheater•Max capacity 950.000 tpy•Heat consumption 3,6 GJ/t cli•Planetary cooler•No precalcining, No midkiln firing
ENCI Maastricht cement works kiln 8
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AF target for Europe
Target 2007 : Group: 25,0 %T.E.A.M.: 14,1 %
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ENCI Policy
Sustainabledevelopment
AlternativeMaterials
Energy Emissions
100
100
0
100 100
0 0 0
Is according to HC AFR policy commitment
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Limitations / constraints
Important limitations and constraints for ENCI Maastricht:
� Permit (sludges, paper, plastics, rubber, manure, animal
meal, all non-hazardous with exception for glycolbottom)
� Kiln layout (no precalcining, only main burner)
� Emissions
� Feeder availability & capacity
� Quality (P2O5)
� Production capacity
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Fuel package history ENCI kiln-8
GJ/t cli from prim., alt.-biomass and alt.-other
0,0
0,5
1,0
1,5
2,0
2,5
3,0
3,5
4,0
4,5
5,0
1968
1970
1972
1974
1976
1978
1980
1982
1984
1986
1988
1990
1992
1994
1996
1998
2000
2002
2004
2006
GJ/
t cli
% alternative other
% alternative biomass
% primary
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Realisation 2006
ktpy GJ/t cli Biomass %kiln Finecokes 5,3 0,22 0
PPDF40 SBI 10,8 0,31 60PPDF40 DS5 0,0 0,00 60Paper sludge Smurfit Kappa 1,2 0,01 100Anode dust 25,8 1,01 0Glycolbottom 11,8 0,23 0Dewatered sludge 0,0 0,00 100Natural gas 0,2 0,01 0Lignite 10,3 0,29 0Animal Meal 13,0 0,31 100Sewage Sludge BioMill 73,4 1,20 100Paper sludge Sappi 6,2 0,05 100Rubbergranulate 0,0 0,00 0Sewage sluge SC Heer. 0,0 0,00 100PPDF90 6,3 0,13 80
dryer Natural gas 0,9 0,04 0Lignite 2,5 0,07 0Total kiln 3,75
Fossil 8 %Biomass 49 %
Alternative 43 %Total 100 %
Fossil = % fossil fuels in fuel packageBiomass =% biomass alternative fuels in fuelpackageAlternative % non biomass alternative fuels in fuelpackage
Fossil8%
Biomass49%
Altern.43%
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Kiln-8 specific fuel cost development
0,00
0,50
1,00
1,50
2,00
2,50
3,00
3,50
4,00
4,50
1999 2000 2001 2002 2003 2004 2005 2006
Fue
l cos
t [eu
ro p
er to
n cl
i]
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Dosing equipment for Fuels
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Coarse AF :PPDF
Papersludge
Glycolbottom
Solid fuel mix:Cokes
Lignite Sewage sludge,
Animal meal
IR-Flame detection
Natural gas
Cooling air
Concrete
Swirl air
Axial air
Axial air
Solid mixSwirl air
Natural gas
Glycolbottom
Side view burner head Kiln-8 Front view burner head Kiln-8
Alt. fuels
Cooling air
Burner : FLS-Swirlax burner + ENCI-overfire lance
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BioMill (dried sewage sludge grinding)
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• First trials with Sewage Sludge in 1996
• Sewage Sludge/Cokes mixture ground in ball mill at a low O2-content (1996 - jan. 2000).
• “BioMill” a vertical roller mill for grinding Sewage Sludge commisioned in feb. 2000 (joint venture, ENCI / ZL)
• Sewage Sludge consumption : 1997 : <1 tph2000 : 3,5 tph (BioMill 1) 2004 : >6 tph (BioMill 2)2007 : 11 tph
Sewage sludge at ENCI; history
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Bio Mill
joint venture
WBL35 kton unground sludge 80 kton ground sludge
operation +capital costs
profit share 50% profit share 50%
Other suppliers
45 kton unground sludge
Joint venture ENCI / WBL
WIN-WIN: solving a waste problem together with the Government
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Vertical roller mill - BMH
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Day stock silos for ground sludge
Storage silos for unground sludge
Filter
Vertical Mill110 kW
BioMill
Wim Heldens
Explosion valve
Filter
Filter
DosingequipmentCoriolis
Pump
Fan
Explosion valveExplosion valve
Kiln
Tm
Tm
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Sewage sludge consumption history
Sewage sludge consumption (kg/t cli)
0
20
40
60
80
100
120
1996 1997 1998 1999 2000 2001 2002 2003 2004 2005 2006
kg/t
cli
BioMill 2
BioMill 1
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Sewage sludge limits and constraints
Ash : Av. Ash conc. 33% => raw meal quality adjusted accordingly(LSF raw meal >> 100)
Hg :Hg-limit 0,05 mg/Nm3 => ESP dust purge to break Hg-cycle
Cl : Build up of Cl in kiln system => ESP dust purge to break Cl-cycle
P2O5 :P2O5 in cli >0,8% => LSF cli increased to compensate for drop in early strength.
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SBI (coarse fuels handling installation)
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Motivation for waste fuel burner
Lowering fuel costs
Introduction of coarse fuels (rubber)
No preca., no midkiln.
Limited possibilities at coal channel (width : 57 mm)
Burner adjustment !
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1993 : Waste fuel burner, overfire lance
Considerations :� Burnout characteristics� Experience elsewhere (proven tech.)� Low cost solution
Solution :� Overfire lance, mounted on main burner � Costs : appr. 20 k€� Not required to make big adjustments to swirlax
burner (e.g. reinforcement of trolly)
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Waste fuel burner
� Outer diam. : 219 mm� Fuel feed channel : 125 mm� Cooling air : not in use.� Transport air : 2100 Nm3/h� Air velocity : 50 m/s� Burner weight : + 25 % (appr.)� Capacity : appr. 5 tph
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Schematic overview coarse fuels handling/firing
• Simple lay out• Low inv. cost : appr. 150 k€
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History firing through waste fuel burner
� 1993 : erection of waste fuel burner & waste fuel h andling installation for coarse fuels (simple lay out)
� 1994 : first trials with shredded rubber (< 2cm)
� 1995 : trials with plastic chips
� 1998 : trials with Rofire
� 1999 : introduction of Paper sludge (dry)
� 2000 : introduction of Rofire
� 2001 : replacement of first waste fuel handling ins tallation by definite installation (SBI)
� 2006 : introduction of Paper sludge (wet), PPDF40 a nd PPDF 90
� 2007 : addition of extra feeder for introduction of low calorific coarse fuels (TBI).
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SBI
Main burner
Overfire lance
FLS-swirlax + overfire lance
Fuel 1 Fuel 2
Belt weigh feeders
inv. cost : appr. 2.700 k€
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TBI, simple feeder for low calorific fuels
� Increase in feedingflexibility
� Releave of unloading &handling load at SBI
� Inv. appr. 100 k €
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Heat input through waste fuel burner
0
2
4
6
8
10
12
14
16
18
20
1968
1970
1972
1974
1976
1978
1980
1982
1984
1986
1988
1990
1992
1994
1996
1998
2000
2002
2004
2006
% o
f tot
al h
eat i
nput
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SBI limits and constraints
Fuel handling capacity : Truck unloading capacity / crane capacity / AF bulk density=> Strict logistics planning, crane software improvement, quality specs regarding bulk density
Burnout :Coarse fuels burnout vs fine fuels burnout => Heat-% fromcoarse fuels limited to 20 %.
Equipment availability :SBI “MTBF“ not good => change in rotary valve size and type, crane software improvement, no rubber anymore.
Cl : Build up of Cl in kiln system => ESP dust purge to break Cl-cycle, Cl limit in quality specs for AF.