Observational procedures and data reduction Lecture 2: Sampling images
Lecture 3_Size Reduction
-
Upload
muhammad-ahmad -
Category
Documents
-
view
29 -
download
1
description
Transcript of Lecture 3_Size Reduction
![Page 1: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/1.jpg)
“SIZE
REDUCTION”
By
Engr. SHAHID MIRZA
Dated: 7th December, 2012
![Page 2: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/2.jpg)
Size Reduction
Definition :
“Size reduction is applied to all the ways in which solids are cut or broken into smaller pieces.”
or
“Disintegration of the solid substance by mechanical forces without altering their state.”
![Page 3: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/3.jpg)
Fundamentals
![Page 4: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/4.jpg)
Methods of Size Reduction
Impact• For coarse, medium or fine particles,
• Example: hammer
Compression• For coarse type materials,
• Example: nut cracker
Attrition• Very fine articles of soft non abrasive
materials
• Example: file
Cutting• To attain definite particle shape or size
• Example: knife cutters
![Page 5: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/5.jpg)
Different ways to attain Size Reduction
![Page 6: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/6.jpg)
Factors effecting Size Reduction
Manner in which load is applied
Magnitude of the load
Nature of the material
Nature of the force
Rate of application of a force
![Page 7: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/7.jpg)
Stringent market specificationEasy transport and handling of solid particles Increases the reactivity of solids especially in catalytic
reactions It permits separation of unwanted ingredients by
mechanical separationsCreate appropriate particle sizes for subsequent processingCreate a free-flowing material. Improve material blending & prevent segregation by
making different sized products with similar particle size distributions.
Why to Reduce Size
![Page 8: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/8.jpg)
Energy Consumed In Crushing
Elastic deformation of the particles before fracture occur;
Inelastic deformation which results in size reduction;
Elastic distortion of the equipment;Friction between particles and the machine;In noise, heat & vibration in the plants;Friction losses in the plant itself:
![Page 9: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/9.jpg)
Characteristics of Ideal Crusher
Have a large capacity
Require a small power input per unit of product
Yield a product of the single size or the size distribution required
![Page 10: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/10.jpg)
Energy Requirement
Three laws governing Energy requirements are as given below:
Kick’s law
Rittenger’s law
Bond’s lawThe basic differential equation which states that the energy “dE” require to affect a small change “dL” in the size of the unit mass of the material is simple power function of the size.
PdE CLdL
![Page 11: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/11.jpg)
RITTINGER’S Law
Rittinger, assumed that the energy required for size reduction is directly proportional, to the change in surface area. This leads to a value of -2 for p in equation as area is proportional to length squared. If we put:
C = KRfC and so
dE / dL = KR fC L-2
where KR is called Rittinger's constant, and integrate the resulting form of we obtain:
E = KR fC (1/L2– 1/L1)
where, KR is the Rittenger’s Constant (m4/kg) fC is the Crushing strength of material (N/m2) L1 is the feed size (m) L2 is the product size (m)
![Page 12: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/12.jpg)
KICK’S Law
Kick assumed that the energy required to reduce a material in size was directly proportional to the size reduction ratio L1/L2 .This implies that p is equal to -1 in equation 1.
Hence on integrating C = KRfC
and putting the limits we get
E = KK fC ln (L1/L2)
where, KK is the Kick’s law constant (m3/kg) fC is the crushing strength of the material (N/m2) L1 is the feed size (m) L2 is the product size (m)
![Page 13: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/13.jpg)
BOND’S Law
Bond defines the quantity Ei the work index: The amount of energy required to reduce unit mass of the material from an infinitely large particle size down to such a size that 80% of the product passes a 100µm .Bond’s crushing equation would be
where,Ei is the work index (J/kg)q is the reduction ratio (L1/L2) (-)L1 is the feed size (m)L2 is the product size (m)
2
100 11iE E
L q
![Page 14: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/14.jpg)
Work Index for different materials
Material Work IndexkWatts h/Ton
Material Work IndexkWatts h/Ton
Bauxite 8.78 Phosphorus Rock
2.74
Clinker 3.15 Quartz 2.65
Clay 2.51 Slate 2.57
Coal 1.40 Trap Rock 2.87
Gravel 2.66 Granite 1.31
Gypsum 2.69 Shale 2.63
Iron Ore 3.53 Coke 1.31
Lime stone 2.66
![Page 15: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/15.jpg)
Crushing Efficiency
Crushing efficiency is defined as the ratio of the surface energy created by crushing to the energy absorbed by the material.
ή = Es (Awb – Awa)
Wn
where
ή is the crushing efficiency
Es is the energy per unit area Awb
Awb is the surface area per unit mass of product
Awa is the surface area per unit mass of feed
Wn is the power input to the crusher
Most of the energy is lost in Friction while the rest is available for crushing.
![Page 16: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/16.jpg)
Comparing the laws
It is common practice to assume thatKick’s proposal is applicable for large particle size
(coarse crushing and crushing).Rittinger’s for very small particle size (ultrafine
grinding).Bond formula being suitable for intermediate
particle size–the most common range for many industrial grinding processes.
![Page 17: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/17.jpg)
Comparing the laws
![Page 18: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/18.jpg)
It is generally advisable to rely on the past experience of equipment manufacturers and on tests in order to predict energy requirements for the milling of a particular material.
![Page 19: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/19.jpg)
Problem 1
A material is crushed in a Blake Jaw Crusher such that the average size of the particle is reduced from 50mm to 10mm with the consumption of energy at the rate of 13.0 kW / (kg/s). What will be the consumption of energy needed to; crushed the same material of average size 75mm to an average size of 25mm:
(a) Assuming Rittinger’s law applies ?(b) Assuming Kick’s law applies ?
Which of these results would be regarded as being more reliable and why ?
![Page 20: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/20.jpg)
Food is grinded from 6 mm to 0.12 mm particle diameter using a mill with a 7.5 kW motor. What reduction in throughput rate would you expect if the material was reduced to 0.08mm instead of 0.12 mm?
Problem 2
![Page 21: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/21.jpg)
Methods of Crushing
Choke Crushing: The machine is kept full of
the material The discharge of the product
is impeded to stay for longer period.
Free Crushing: It involves the feeding of the
material at a comparatively low rate so that the product
can escape, readily. The time of stay in the
machine is short.
Suitable for small amount When entire size reduction is
completed in one step
Large feed is there Energy consumption is
optimized Low degree of crushing is
required
![Page 22: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/22.jpg)
WET & DRY CRUSHING
Power consumption.Capacity.Removal of the Product.Dust formation.Solid handling.
![Page 23: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/23.jpg)
Open & Closed Circuit Grinding
Open Circuit Grinding When the plant is operated such that the feed is
passed into the equipment once only. No Attempt is made to return the oversize
particles to the machine for further reduction.
![Page 24: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/24.jpg)
Open & Closed Circuit Grinding
Closed Circuit Grinding When the plant is operated such that the
oversize particles are refluxed into the equipment until the desired size is attained.
Low power consumption is there and thus is preferred in industry.
Product
![Page 25: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/25.jpg)
CHOICE OF EQUIPMENT
![Page 26: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/26.jpg)
Factor Effecting Choice of Machinefor Crushing
HardnessStructureCrushing StrengthStickinessSoapinessExplosive MaterialHarmful Material
![Page 27: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/27.jpg)
Factors Influencing Choice of Size Reduction Equipment
Feed Size Product Size
Coarse Crushers 60 – 1.5 inch 2 – 0.75 inch
Intermediate Crushers 2 – 0.75 inch 0.75 inch – 200 mesh
Fine Crushers / Grinders
0.75 inch – 200 mesh
About 275 mesh
Ultra Fine Crushers 275 mesh Upto 325 mesh
![Page 28: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/28.jpg)
Type of Equipments
Coarse Crushers
Intermediate Crushers
Blake Jaw Crusher Dodge Jaw Crusher Gyratory Crusher
Crushing Rolls Disc Crushers Edge Runner Mill Hammer Mill Single Roll Crusher
![Page 29: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/29.jpg)
Continuing...
Fine Crushers
Ultra Fine Crushers
Roll mill Net Pendulum Mill Griffin Mill Ring Roll Mill Ball Mill
High Speed Hammer Mill Agitated Mill Fluid Energy Mill
![Page 30: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/30.jpg)
Jaw Crushers Working Principle
They are coarse size reduction machines.They basically works under the influence of
Compression & Rubbing Force.One jaw is fixed called the anvil and the other is
moving jaw.Two types
Blake Jaw crusher Dodge Crusher
![Page 31: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/31.jpg)
Mechanical Construction of Blake Jaw Crusher
Two jaws (anvil and the moving one)Crushing plates are made up of manganese steel.Max. space is at the top so max. pressure for large
particle is exerted at the top.One to the toggle plates is made weaker so as to
protect the equipment.Heavy flywheel is used as the load is intermittent.Power requirement depends upon the size &
capacity thus varying from 7 to 70 kW (feed rate of 10kg/s)
![Page 32: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/32.jpg)
![Page 33: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/33.jpg)
Diagram of Blake Jaw crusher
![Page 34: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/34.jpg)
![Page 35: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/35.jpg)
Difference Between Blake Jaw Crusher &Dodge Crusher
Blake Jaw Crusher Moving jaw is pivoted at the
top. Uniform product is not
obtained Max movement at the
bottom. More widely used. Little tendency to clog. Takes in small feed due to
small opening at the top.
Dodge Crusher Moving jaw is pivoted at the
bottom. More uniform product. Min movement at the
bottom. Less widely used Tendency to clog Takes in large feed due to
larger opening at the top.
![Page 36: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/36.jpg)
Dodge Jaw Crusher
![Page 37: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/37.jpg)
Jaw Crusher
Advantages Little head room required. Easy replacement of worn parts. Easy adjustment of set opening.
Disadvantages Expensive, heavy foundations necessary due to
intermittent crushing action. Emergency stopping impossible due to fly wheels. Re-start with choked crushing chamber impossible. Flat objects may pass uncrushed. A special feeder for constant feed rate is needed to
prevent choking.
![Page 38: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/38.jpg)
BALL MILL
![Page 39: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/39.jpg)
Mechanical Construction
Simplest of the size reducing machinesRotating hollow cylinderAxis could be horizontal or at a small angle to the
horizontalOutlet is covered with a coarse screen to prevent
ball escapeInner surface is lined with manganese steel
(abrasion-resistant), stoneware or rubber.Coefficient of frictionLift bars
![Page 40: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/40.jpg)
Continuing...
Feed intake is of 50mm sizeEfficiency increment with hold up timeBalls occupy 30% - 50% of the volumeOptimum diameter proportional to the square root of
the feed sizeLarge / small ballsPebblesCompound mill
![Page 41: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/41.jpg)
Figure
![Page 42: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/42.jpg)
Compound mill
![Page 43: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/43.jpg)
Terminology of Zone
![Page 44: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/44.jpg)
Motion with in a ball mill
![Page 45: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/45.jpg)
Factors Influencing the Size of the Product
Rate of the feedProperties of the feedWeight of the ballsDiameter of the ballsSlope of the millSpeed of the rotation of the millLevel of the material in the mill
![Page 46: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/46.jpg)
Usage of the ball mill
Wet or dryCost of insulationInert atmosphereGrinding mediumAll degrees of hardnessBatch or continuousOpen or closed circuit grinding
![Page 47: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/47.jpg)
Critical Speed of the ball mill
A rotational speed at which a ball fails to loose contact with the wall of the mill is known to be the critical speed.
It is denoted by
where,
nc = critical speed of the Ball mill
g = gravitational acceleration
R = inner radius of the ball mill
r = radius of the balls
1
2 ( )c
gn
R r
![Page 48: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/48.jpg)
Figure
r
O
A
R - r
R
c
mgg
cosc
mgg
2( )
c
m R r wg
r
![Page 49: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/49.jpg)
Derivation
Consider a single ball in operation reached at a point “A” on the periphery of the mill.
Let radius of the mill = R radius of the ball = r
The distance from the centre of the mill “O” and the centre of the ball (R – r) while α is the angle between the vertical and the radius AO.At “A” two forces are acting on the ball
(1) Force of gravity(2) Centrifugal force
![Page 50: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/50.jpg)
(1) Force of gravity
As we know that F = mg for horizontal plane but here it is angled (α). So reviving it into rectangular components, we get
• mg cos α• mg sin α
As F = mg is not dimensionally consistent so we introduce gc . Hence we get
• mg cos α / gc
• mg sin α / gc
The component that keeps the ball in circular motion is the centripetal component of the force of gravity i.e.
-------- (i)cos
c
mg
g
![Page 51: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/51.jpg)
(2) Centrifugal force
Centrifugal force = mv2 / r1
where v = r1 ω when (ω being = 2n)
Now centrifugal force becomes
where r1 = ( R – r )
introducing the conversion factor gc
------------- (ii)
2 21 1
1
( )mv m r
r r
2
2
( )
( )c
m R r
m R rg
![Page 52: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/52.jpg)
Operating speed should be 60% to 80% of the Critical speed.
1
2 ( )c
gn
R r
![Page 53: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/53.jpg)
Differentiate between Ball mill & Tube mill
Ball Mills Length to Diameter ratio
• Close to 1
Usage• Batch & Continous
Holding time• Less
Compartments• Usually 1
• Compound mill
Product size• Usually fine
Tube Mills
• Usually 4,3 – 1
• Usually batch
• High
• Usually 2 or more
• Compartment mill
• Fine or ultra fine
![Page 54: Lecture 3_Size Reduction](https://reader035.fdocuments.net/reader035/viewer/2022062321/55cf991b550346d0339b9ced/html5/thumbnails/54.jpg)
Differentiate between Ball mill & Rod mill
Ball Mills Length to Diameter ratio
• Close to 1 Usage
• Batch & Continous Holding time
• Less Compartments
• Usually 1• Compound mill
Product size• Usually fine
Product Quality • Not uniform
Rod Mills
• Usually 3,2 – 1
• Usually batch
• High
• Only one
• Ultra fine
• Uniform