Contents
Innovation and optimisation
in cement grinding
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Electrical energy demand for cement production
• Extraction and blending 5 %
• Raw material grinding 24 %
• Raw material homogenisation 6 %
• Clinker production 22 %
• Cement grinding 38 %
• Conveying, packing, loading 5 %
100 %
total demand ~ 110 kWh/tcement
more than 60 % for grinding processes! *all*
Grinding and its impact on quality
Cement grinding as an example:
quality parameters:
• workability
• water demand
• strength
• durability of concrete
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Particle size distribution in RRSB-diagram
Description of cement fineness with RRSB position parameter
and slope:
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Specific energy consumption of different grinding systems
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Evolution of comminution technologies Chronology:
Manual comminution
Hammer mechanism (ca. 1512)
Edge runner (ca. 1800)
Ball mill (ca. 1890)
Vertical roller mill (ca. 1930)
High pressure grinding rolls (ca. 1985)
Horomill®
Manual comminution (16th century)
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Hammer mechanism (16/17th century)
from:
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Edge runner (18/19th century)
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Evolution of comminution technologies
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Comminution mechanisms in different
grinding systems
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Comminution mechanisms in the ball mill
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Ball mill for dry grinding
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Ball mill
Advantages
• combined drying and grinding
• reliable – long service life
• widePSD
• high fineness
• good for abrasive materials
Disadvantages
• for high moisture
external drying
necessary
• high energy demand
• no explicit stress area
still widely used in cement plants
Potentials for ball mills
Exact adjustment of grinding media and linings to requirement
separator adjustment
–> optimisation of mill and separator
Grinding systems for efficient comminution
Objectives
• Lower grinding energy demand than ball mills
• Comminution to a large extent by using the
compression
• Comminution in an explicit “compression zone”
Principle design of vertical roller mills
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Vertical roller mills for raw material grinding
• Combined drying, grinding and separation
• Energy consumption 60 – 70 % compared
to a ball mill
• Moisture contents up to 25 %
• Compared to a ball mill 10 to 20 % higher
capital costs
• Used in 90 % of all new plants as raw mill
• Throughput up to 840 t/h, feed size up
to 200 mm
• Installed power up to 7 000 kW, grinding
table diameter up to 6 700 mm
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Vertical roller mill for cement and slag grinding
• Energy consumption:
70 % of a ball mill for cement
50 % of a ball mill for slag
• Fineness:
max. 4 500 cm²/g for cement
max. 6 000 cm²/g for slag
• Moisture required for stabilising the
grinding bed – less influence on
cement quality
• Lowwearcosts
• Throughput up to 300 t/h
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High pressure grinding rolls
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• Defined grinding area
• Feed up to 60 mm
• Grinding pressure from
50 to 400 MPa
• Compacted cakes up
to 40% fines and
coarse particles
High pressure grinding rolls – main features
• First application 1984
• Today worldwide more than
600 mills in operation
• Throughput rates up to 1 300 t/h
• Grinding force from
2 to 20 Mega-Newton
• Efficiency
1.8 to 3.5 times higher than ball mill
1.1 to 1.4 times higher than vertical roller mill
• cement finish grinding limited by PSD
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Example:
High pressure grinding rolls for raw material grinding
• Advantages:
– Energy consumption 50 % lower than ball mill
– Extremely low roller wear (min 0.25 g/t)
• Disadvantages:
– Drying capacity is limited to 4 % feed moisture
– Application only for non-abrasive raw materials, due to
wear of deglomerator
Application of high pressure grinding rolls for cement grinding
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Comminution by compression: operating principles
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Operating principle of Horomill®
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Horizontal roller mill (Horomill®)
For wet materials external dryer necessary
Wear costs comparable to build-up welded high pressure
grinding rolls
Raw material grinding
• Energy consumption 50 % compared to a ball mill
Cement grinding
• Max. cement fineness 4 000 cm²/g
• Energy consumption 70 % compared to a ball mill
Slag grinding
• Max. cement fineness 4 800 cm²/g
• Energy consumption 60 % compared to a ball mill
Comparison of different systems for cement grinding
Technological parameters for different grinding systems
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Comparison of different systems for slag grinding
Comparison of service lives of the grinding elements from different
grinding systems when grinding granulated blastfurnace slag
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Influence of grinding system on cement properties
Grinding the same clinker in a ball mill, a VRM and a HPGR
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Slag grinding and properties of slag cement
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Size reduction energy
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Energy utilisation of compression and impact
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Throughput-speed-behaviour of different mill types
• VRM: depends on grindingtable-
diameter and number of
rollers
• HPGR: linear correlation only
for low circumferential speed of
rolls
• Modified horizontal roller mill:
linear correlation also for high
circumferential speed (limit not
yet known)
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Direction of new developments
HPGR:
• Operation point
not adjustable
• Independent
adjustment of
grinding force and
thickness of
grinding bed not
possible
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Objectives for future developments
• Comminution only by compression
• Compression of a grinding bed with defined thickness
• Independent adjustment of grinding force and thickness of
grinding bed
• Low specific energy demand
Modified horizontal roller mill
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Other comminution technologies for cement grinding?
• HEM High Energy Milling: very small particles high reactivity
mechanical activation of particles (< 2μm); tested for cement
grinding
• Ultrasonic-comminution (Patent DE 102 59 456 B4)
energy-transfer by acoustic pulse; tested for slag grinding
• Plasma comminution (European Patent EP0976457)
comminution in a liquid by shock waves; tested for semiconductor
material
• Low temperature comminution (Internat. Application No.
PCT/EP2007/010159)
reducing particle size by rapidly reduction of energy level
Summary (1)
Ball mill
• High energy consumption
• Reliable – long service life of the wearing parts
• Limitation in feed moisture – at high feed moisture external
drying necessary
High pressure grinding rolls
• High energy savings
• Limitation in feed moisture – with external drying no
limitation in material moisture
• Maximum achievable fineness 4 000 cm²/g (clinker)
Summary (2)
Vertical roller mill
• High energy savings
• Very high material moisture contents (up to 25 %) can be
processed
• Lowwearcosts
• Maximum achievable fineness 4 500 Blaine for OPC
Summary (3)
Horizontal roller mill (Horomill)
• Energy savings of 30 to 40 %
• Maximum achievable fineness 4 000 Blaine for OPC and
4 800 Blaine for slag
No comminution without energy input
Highest efficiency of comminution by compression
Objectives
• Optimisation of known grinding processes necessary
• Development of new comminution processes:
comminution by compression in an explicit stress area
• Comminution in one process without postrefining
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