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Maximizing solid alternative fuels
With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria
HANOI / 22nd August 2018. Dr Stefan Kern
LOESCHE Symposium Hanoi 2018 22.08.2018
Maximising solid alternative fuels
With the A TEC Rocket Mill® at Wietersdorfer & Peggauer
Cement, Austria
W & P Zement Wietersdorf
A TEC Rocket Mill®
Operational results Rocket Mill® for main burner fuel
01
03
02
LOESCHE Symposium Hanoi 2018 22.08.2018
Maximising solid alternative fuels
With the A TEC Rocket Mill® at Wietersdorfer & Peggauer
Cement, Austria
W & P Zement Wietersdorf
A TEC Rocket Mill®
Operational results Rocket Mill® for main burner fuel
01
03
02
LOESCHE Symposium Hanoi 2018 22.08.2018
W&P Zement
4
Location of cement plant Wietersdorf
LOESCHE Symposium Hanoi 2018 22.08.2018
W&P Zement
5
▪ Headquarters: Klagenfurt / Austria
▪ Founded in 1893
▪ Turnover: approx. € 600 million
▪ Employees: approx. 3,000
▪ Locations: in 30 countries
▪ Cement Plant Wietersdorf / Austria
– Wietersdorf kiln line: max. 2.200 tpd
– approx. 100.000 t/y RDF
– TSR (RDF) rate 80-85%
– 50% RDF is processed at plant site
LOESCHE Symposium Hanoi 2018 22.08.2018
W&P Zement
6
Projects developed by A TEC together with W&P Zement
First Project - Cyclones
Cement Mill Dedusting
1992
01
Dedusting system
Cyclones for Clonker cooler dedusting
1993
02
1990
Study on preheater
Implementation study Precalciner/Preheater
2003
03
2000
Sewage sludge drying
Gas handling system
2011
04
Kiln conversion from Lepol to precalciner
New preheater, calciner and Chlorine Bypass
2006
05
2010
06
A TEC XMercury
Mercury emission reduction, first installation worldwide
2014
A TEC Rocket Mill®
RDF preparation for main burner
2014
07
Today
TSR > 80 %
2018
12 14 16 1802 04 06 0892 94 96 98
LOESCHE Symposium Hanoi 2018 22.08.2018
W&P Zement
7
System diagramme SAF preparation in Wietersdorf
Pre-shredder Shredder
Fine shredding,
A TEC Rocket Mill®Fe separatorHeavies
separation
< 300 mm < 80 mm
< 15 mm
Main burner
Impurities
Truck delivery
< 80 mm
Storage
LOESCHE Symposium Hanoi 2018 22.08.2018
W&P Zement
8
RDF preparation with the A TEC Rocket Mill®
▪ In operation since 2014
▪ Drive power: 250/315 kW
▪ Single chamber pilot mill
▪ Throughput: approx. 2.5 t / h (finished product)
▪ Size reduction from 80 mm to <15 mm
▪ Specific energy requirements: approx. 65 kWh / t
▪ Moisture reduction: around 8-10%
LOESCHE Symposium Hanoi 2018 22.08.2018
Maximising solid alternative fuels
With the A TEC Rocket Mill® at Wietersdorfer & Peggauer
Cement, Austria
W & P Zement Wietersdorf
A TEC Rocket Mill®
Operational results Rocket Mill® for main burner fuel
01
03
02
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
10
General information
▪ Two grinding chambers
▪ Power controlled
▪ Direct drive
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
11
Grinding tools
▪ Horizontally rotating chains
▪ Special chain links
▪ Screen for final product size
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
12
Discharge of organics
▪ Automatic discharge during operation
▪ Slide gate releases the impurities
▪ Impurities do not enter product
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
13
Final product
▪ Size defined with screen size
− E.g. ø 15 mm screen -> max. 15 mm,
approx. 50% < 5 mm.
▪ Increased specific surface (‘fluffy’ like
cotton)
▪ Drying effect during the grinding
process up to 10 %
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
14
Quality improvement of the fuel
Ash reduction Moisture reduction
Size reduction Specific surface increase
SAF Quality
• Separation of inorganics
• Easy discharge of impurities
• Max. output defined by
sieve
• Simultaneous drying effect
• Release of approx. 10 % (rel.) of
the moisture content
• Very fibrous after shredding
• Size reduction by crushing, not
cutting
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
15
Final product size < 15 mm < 30 mm
Screen size Ø 15 mm Ø 30mm
Output size < 15 mm / ~ 50 % < 5 mm < 30 mm / ~ 40% < 10 mm
Throughput 8 - 10 t/h 15-17 t/h
Specific power consumption 50 - 60 kWh/t < 15 mm final 30 - 35 kWh/t < 30 mm final
Dimension 8.530 x 4.160 x 6.000 l x b x h (mm)
Weight 62.000 kg
Drive unit 2 x 315 kW
Rotor speed ~ 580 min-1
Discharge 2 x conveyor screws
Key performance data
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
16
Possible new treatment line
< 15 mm
Existing treatment line
pre-shredder shredder
fine shredder
(cutting)
screen (opt.)
Fe separator opt. heavy
separation
< 250 mm < 80 mm < 15 mm
> 250 mm
pre-shredder
Rocket Mill®
screen (opt.)
Fe separator opt. heavy
separation
< 250 mm
< 15 mm> 250 mm
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill®
17
Advantages
▪ Size reduction from < 300mm to 15 mm in one
grinding step
▪ Saving of one shredding step
▪ Easy to operate
▪ Easy to maintain
▪ Robust construction
▪ Drying effect during operation
▪ Separation of FE and non-FE materials
▪ Different output fuel particle sizes for main
burner and calciner possible
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.0 Mobile
18
Advantages
▪ Compact design
▪ Small footprint
▪ Easy installation
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.0 Mobile
19
Basic data
Basic data of Rocket Mill® RM 2.00 single
▪ Drive unit: 1 x 315 kW
▪ Rotor speed: 750 rpm
RDF 90% < 30 mm
▪ Throughput: 6 - 7 t/h
▪ Specific power consumption: 30 - 35 kWh/t
LOESCHE Symposium Hanoi 2018 22.08.2018
Maximising solid alternative fuels
With the A TEC Rocket Mill® at Wietersdorfer & Peggauer
Cement, Austria
W & P Zement Wietersdorf
A TEC Rocket Mill®
Operational results Rocket Mill® for main burner fuel
01
03
02
LOESCHE Symposium Hanoi 2018 22.08.2018
Results W&P Zement
21
Comparison of operating costs old system vs. Rocket Mill®
Shredder Cutting mill Rocket Mill®
Wear 18,1 %
Man power 26,3 %
Electricity 26,7 %
Total costs 22,4 %
Wear 10,4 %
Man power 6,6 %
Electricity 85,3 %
Total costs 28,5 %
Wear 81,9 %
Man power 73,7 %
Electricity 73,3 %
Total costs 77,6 %
Shredder & cutting mill vs. A TEC Rocket Mill® in % of total preparation costs
Saving in operating costs - 71,5 %
LOESCHE Symposium Hanoi 2018 22.08.2018
Results W&P Zement
22
▪ Due to the higher quality of AF produced with the rocket mill, the coal amount could be reduced.
▪ Comparison of clinker production with same clinker quality and roughly same kiln feed:
▪ This allows savings in coal consumption of around 200 kg/h with 120 t/h kiln feed.
Coal savings on the existing system W&P with AF from the Rocket Mill®
Kiln feed [t/h] Coal at main burner [t/h]Coal per kiln feed [kg/t]
April 122,11 1,91 15,6
July 115,01 1,61 14,0
LOESCHE Symposium Hanoi 2018 22.08.2018
A TEC Rocket Mill® RM 2.5 Double
23
▪ Better burnout of AF in kiln due to improved physically properties
▪ High clinker quality due to reducing reduction atmospheres
– Reduction of Fe2+ content (brown clinker)
– Less sulphure circulation
▪ Less water content in system
▪ Higher substitution rates and higher capacity
▪ Stable condition due to more homogenized product
Positiveimpact onpyroprocess
THANK YOU
for your attention
Dr Stefan Kern
Email: s.kern@atec-ltd.com

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Maximizing Solid Alternative Fuels

  • 1. Maximizing solid alternative fuels With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria HANOI / 22nd August 2018. Dr Stefan Kern
  • 2. LOESCHE Symposium Hanoi 2018 22.08.2018 Maximising solid alternative fuels With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria W & P Zement Wietersdorf A TEC Rocket Mill® Operational results Rocket Mill® for main burner fuel 01 03 02
  • 3. LOESCHE Symposium Hanoi 2018 22.08.2018 Maximising solid alternative fuels With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria W & P Zement Wietersdorf A TEC Rocket Mill® Operational results Rocket Mill® for main burner fuel 01 03 02
  • 4. LOESCHE Symposium Hanoi 2018 22.08.2018 W&P Zement 4 Location of cement plant Wietersdorf
  • 5. LOESCHE Symposium Hanoi 2018 22.08.2018 W&P Zement 5 ▪ Headquarters: Klagenfurt / Austria ▪ Founded in 1893 ▪ Turnover: approx. € 600 million ▪ Employees: approx. 3,000 ▪ Locations: in 30 countries ▪ Cement Plant Wietersdorf / Austria – Wietersdorf kiln line: max. 2.200 tpd – approx. 100.000 t/y RDF – TSR (RDF) rate 80-85% – 50% RDF is processed at plant site
  • 6. LOESCHE Symposium Hanoi 2018 22.08.2018 W&P Zement 6 Projects developed by A TEC together with W&P Zement First Project - Cyclones Cement Mill Dedusting 1992 01 Dedusting system Cyclones for Clonker cooler dedusting 1993 02 1990 Study on preheater Implementation study Precalciner/Preheater 2003 03 2000 Sewage sludge drying Gas handling system 2011 04 Kiln conversion from Lepol to precalciner New preheater, calciner and Chlorine Bypass 2006 05 2010 06 A TEC XMercury Mercury emission reduction, first installation worldwide 2014 A TEC Rocket Mill® RDF preparation for main burner 2014 07 Today TSR > 80 % 2018 12 14 16 1802 04 06 0892 94 96 98
  • 7. LOESCHE Symposium Hanoi 2018 22.08.2018 W&P Zement 7 System diagramme SAF preparation in Wietersdorf Pre-shredder Shredder Fine shredding, A TEC Rocket Mill®Fe separatorHeavies separation < 300 mm < 80 mm < 15 mm Main burner Impurities Truck delivery < 80 mm Storage
  • 8. LOESCHE Symposium Hanoi 2018 22.08.2018 W&P Zement 8 RDF preparation with the A TEC Rocket Mill® ▪ In operation since 2014 ▪ Drive power: 250/315 kW ▪ Single chamber pilot mill ▪ Throughput: approx. 2.5 t / h (finished product) ▪ Size reduction from 80 mm to <15 mm ▪ Specific energy requirements: approx. 65 kWh / t ▪ Moisture reduction: around 8-10%
  • 9. LOESCHE Symposium Hanoi 2018 22.08.2018 Maximising solid alternative fuels With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria W & P Zement Wietersdorf A TEC Rocket Mill® Operational results Rocket Mill® for main burner fuel 01 03 02
  • 10. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 10 General information ▪ Two grinding chambers ▪ Power controlled ▪ Direct drive
  • 11. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 11 Grinding tools ▪ Horizontally rotating chains ▪ Special chain links ▪ Screen for final product size
  • 12. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 12 Discharge of organics ▪ Automatic discharge during operation ▪ Slide gate releases the impurities ▪ Impurities do not enter product
  • 13. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 13 Final product ▪ Size defined with screen size − E.g. ø 15 mm screen -> max. 15 mm, approx. 50% < 5 mm. ▪ Increased specific surface (‘fluffy’ like cotton) ▪ Drying effect during the grinding process up to 10 %
  • 14. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 14 Quality improvement of the fuel Ash reduction Moisture reduction Size reduction Specific surface increase SAF Quality • Separation of inorganics • Easy discharge of impurities • Max. output defined by sieve • Simultaneous drying effect • Release of approx. 10 % (rel.) of the moisture content • Very fibrous after shredding • Size reduction by crushing, not cutting
  • 15. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 15 Final product size < 15 mm < 30 mm Screen size Ø 15 mm Ø 30mm Output size < 15 mm / ~ 50 % < 5 mm < 30 mm / ~ 40% < 10 mm Throughput 8 - 10 t/h 15-17 t/h Specific power consumption 50 - 60 kWh/t < 15 mm final 30 - 35 kWh/t < 30 mm final Dimension 8.530 x 4.160 x 6.000 l x b x h (mm) Weight 62.000 kg Drive unit 2 x 315 kW Rotor speed ~ 580 min-1 Discharge 2 x conveyor screws Key performance data
  • 16. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 16 Possible new treatment line < 15 mm Existing treatment line pre-shredder shredder fine shredder (cutting) screen (opt.) Fe separator opt. heavy separation < 250 mm < 80 mm < 15 mm > 250 mm pre-shredder Rocket Mill® screen (opt.) Fe separator opt. heavy separation < 250 mm < 15 mm> 250 mm
  • 17. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® 17 Advantages ▪ Size reduction from < 300mm to 15 mm in one grinding step ▪ Saving of one shredding step ▪ Easy to operate ▪ Easy to maintain ▪ Robust construction ▪ Drying effect during operation ▪ Separation of FE and non-FE materials ▪ Different output fuel particle sizes for main burner and calciner possible
  • 18. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.0 Mobile 18 Advantages ▪ Compact design ▪ Small footprint ▪ Easy installation
  • 19. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.0 Mobile 19 Basic data Basic data of Rocket Mill® RM 2.00 single ▪ Drive unit: 1 x 315 kW ▪ Rotor speed: 750 rpm RDF 90% < 30 mm ▪ Throughput: 6 - 7 t/h ▪ Specific power consumption: 30 - 35 kWh/t
  • 20. LOESCHE Symposium Hanoi 2018 22.08.2018 Maximising solid alternative fuels With the A TEC Rocket Mill® at Wietersdorfer & Peggauer Cement, Austria W & P Zement Wietersdorf A TEC Rocket Mill® Operational results Rocket Mill® for main burner fuel 01 03 02
  • 21. LOESCHE Symposium Hanoi 2018 22.08.2018 Results W&P Zement 21 Comparison of operating costs old system vs. Rocket Mill® Shredder Cutting mill Rocket Mill® Wear 18,1 % Man power 26,3 % Electricity 26,7 % Total costs 22,4 % Wear 10,4 % Man power 6,6 % Electricity 85,3 % Total costs 28,5 % Wear 81,9 % Man power 73,7 % Electricity 73,3 % Total costs 77,6 % Shredder & cutting mill vs. A TEC Rocket Mill® in % of total preparation costs Saving in operating costs - 71,5 %
  • 22. LOESCHE Symposium Hanoi 2018 22.08.2018 Results W&P Zement 22 ▪ Due to the higher quality of AF produced with the rocket mill, the coal amount could be reduced. ▪ Comparison of clinker production with same clinker quality and roughly same kiln feed: ▪ This allows savings in coal consumption of around 200 kg/h with 120 t/h kiln feed. Coal savings on the existing system W&P with AF from the Rocket Mill® Kiln feed [t/h] Coal at main burner [t/h]Coal per kiln feed [kg/t] April 122,11 1,91 15,6 July 115,01 1,61 14,0
  • 23. LOESCHE Symposium Hanoi 2018 22.08.2018 A TEC Rocket Mill® RM 2.5 Double 23 ▪ Better burnout of AF in kiln due to improved physically properties ▪ High clinker quality due to reducing reduction atmospheres – Reduction of Fe2+ content (brown clinker) – Less sulphure circulation ▪ Less water content in system ▪ Higher substitution rates and higher capacity ▪ Stable condition due to more homogenized product Positiveimpact onpyroprocess
  • 24. THANK YOU for your attention Dr Stefan Kern Email: s.kern@atec-ltd.com