GOVERNMENT ENGINEERING COLLEGE,
BHARUCH
• SUBJECT : SOLID-FLUID OPERATION
• Topic: Static mixers, intensive mixers, heating
and cooling mixers
SEM:-8, Group:-2, Year:-2018
Prepared by:
• VAGADIA HARDIK (140140105018)
• PATEL RASHMIN (140140105045)
• PATEL RONAK (140140105046)
• RAJ PRIYANK (140140105050)
• MODI SAGAR (140140105057)
Contents
•Static Mixers: Helical Element Mixers and
Turbulent Vortex Mixer or High Shear Mixers(HSM)
•Intensive Mixers: Change-can mixers, Kneaders:
Double-arm kneader (Sigma mixer) and Banbury mixer,
Mixer extruder and Muller mixer
•Heating and Cooling Mixers
Static Mixers
• What are static mixers?
• These are the mixers which are applicable to gases or low
viscosity liquids which are blended by passing them together
through a length of a open pipe or a pipe containing orifice
plates or segmental baffles.
• So the mixing is done by the flow of the gases or liquids inside
the pipe only.
• Under appropriate conditions the pipe length may be as short as
5 to 10 pipe diameters, but 50 to 100 pipe diameters is
recommended.
• More difficult mixing tasks are accomplished by static mixers,
commercial devices which consist of a series of metal inserts
placed in the pipe.
• Types of Static Mixers:
• Helical element mixer
• Turbulent vortex mixer
Helical Element Mixers
• Helical-element mixer is mainly used with viscous liquids
and pastes.
• This mixers provide continuous in- line mixing of fluids,
gases, or powders using no moving components. That’s
why also known as motionless mixers.
• Alternating helical mixing elements provide thorough
radial and axial blending in a short length by dividing the
main flow into two equal streams as material passes each
element.
• Each element 1 to 1.5 pipe diameters in length, divides the
stream into two, gives it a 180 degree twist, and delivers it
to the next element.
• Figure (a):
Elements of a helical-element mixer;
• The second element divides the already divided stream and
twists it 180 degree in the opposite direction.
• Successive elements further subdivide the stream until the
striations are so thin that the blending process can be finished
by molecular diffusion.
• The number of divisions increases by 2^n, where “n” is the
number of elements.
• These mixers are custom-designed for each application. The
number of elements is determined by the specific application.
• Mixers can be jacketed or electrically heated, and supplied with
fixed or removable mixer elements.
• Sizes range from 2mm to 2m in diameter.
• The recommended number of helical elements is 6 for Re = 100
to 1000, 12 for Re = 10 to 100, and 18 for Re less than 10.
• More elements are needed for very viscous liquids because of
the lower molecular diffusivity.
• The pressure drop per unit length is about 6 times that in the
empty pipe when Re less than 10, but increases to about 50 to
100 times that in the empty pipe when Re = 2000.
Advantages
• Provide excellent mixing or blending of two liquids, a liquid
and gas, two gases, or two powders
• Plug flow device (first in, first out)
• Short, uniform residence time
• Uniform temperature, no “hot spots”
• Smooth shape and edge sealing of elements allows no dead
spaces for product to hangup of degrade
• Can be used for materials with low to high viscosities, upto
20000 poise or more
• No maintenance since no moving parts
• Can process highly corrosive materials
• Can be used in high viscosity heat exchangers to increase heat
transfer coefficients three to four times standard open tube
designs
Turbulent Vortex Mixer or High Shear
Mixer
• This is also used for gases and low-viscosity liquids as shown in
figure (b).
• This also provide continuous in-line mixing of fluids, gases, or
powders using no moving components.
• Each element of this mixer has four tabs protruding at an angle
into the pipe.
• Counter-rotating longitudinal vortices are formed in the wakes
of the tabs, providing efficient blending of the liquids or gases
after only two to four elements.
• The unique, intermeshing element design provides high levels of
mixing in a very short overall length and product residence time.
• The pressure drop per unit length is 25 to 40 times the value
for the empty pipe at Re = 10^4 to 10^5, but since only a few
elements are needed, the overall pressure drop is not large.
• The design is also adaptable to many types of applications.
• Figure (b) :
Turbulent Vortex Mixer;
• These mixers are custom-designed for each application. The
number of elements and design specifics are determined by
the specific application.
• Mixers can be jacketed or electrically heated, and supplied
with fixed or removable mixer elements.
• Sizes range from 2mm to 2m and larger in diameter.
Advantages
• Provide excellent mixing or blending of two liquids, a liquid and
gas, two gases, or two powders
• Plug flow device (first in, first out)
• Short, uniform residence time
• Uniform temperature, no “hot spots”
• Can be used for materials with low to high viscosities, upto
20000 poise or more
• No maintenance since no moving parts
• Can process highly corrosive materials
• High degree of mixing in short overall length
Applications
Processes: Industries:
Mixing Powder mixing Polymer processing
Injection molding
Reacting Liquid mixing Fiber production Fine
films
Coloring Laminar and turbul- Plastics extrusion
Polymerzation ent mixing applications Foods including edible
Heat exchange Obtaining product tem- oil, ice cream, mayonnai
pH control perature uniformity -se, chocolate, beverage,
Neutralization Extrusion milk, yogurt, and cheese
Diffusion Compounding Pharmaceutical
Gas mixing
Materials
Elements can be constructed of :
• Stainless steel
• Hastelloy
• Teflon
• Carbon steel
• PVC
• PP (polypropylene)
• PE (polyethylene)
• FRP (fiber reinforced plastics)
• Tantalum
• Kynar
• Inconell and many other materials
Intensive Mixers
Intensive mixers includes: change-can mixers, kneader (
dispersor or masticator ), mixer extruder and muller mixers.
Change-can mixer:
• blend viscous liquids or light pastes as in food processing or
paint manufacture.
• a small removable can 5-100 gal in size holds the material
to be mixed.
• In pony mixer, the agitator consists of several vertical
blades held on a rotating head and positioned near the
walls of the can.
• The blades are slightly twisted.
• The agitator is mounted eccentrically wrt the axis of the can.
• The can rests on a turntable driven in a direction opposite to
that of the agitator.
• When mixing is complete, the agitator head is raised, lifting the
blades put of the can, the blades are wiped clean, and the can is
replaced with another containing a new batch.
• In beater mixer, the can or vessel is stationary, the agitator has
a planetary motion, are shaped to pass with close clearance
over the side and bottom of the mixing vessel.
KNEADERS:
General Information:
• Kneaders are high intensive mixers for cohesive solid systems.
• Some kneaders achieve their mixing action by squashing the
mass flat, holding it and squashing it again.
• Others tear the mass apart and shear it between a moving blade
and a stationary surface. There are two main types of kneaders:
• There are two main types of kneaders:
1. Double arm kneader
2. Banbury Mixers
Double arm Kneader
• A two arm kneader handles suspensions, paste and light
plastic masses.
• All double arm kneader mixers are equipped with two mixing
blades placed in W-shaped horizontal trough.
• The commonly used blades are sigma blade, spiral blade,
masticator blade and naben blade.
• The blades rotate towards each other at the same or
differential speed.
• The rotation of blade is either tangential to each other or the
blade may overlap within trough.
• The blades pass the container walls and each other at a close
clearance 2-3 mm resulting in homogeneous mixture.
• The close clearance produce very high shearing action
thereby reducing any large particles.
• Homogeneous mixing is achieved within 10-15 minutes and
mixing homogeneity is 99%.
• The power consumption is very high compared to other types
of mixers.
• A disperser is heavier in construction and draws more power
than a kneader, it works additives and coloring agents into
stiff materials.
• A masticator is still heavier and draws even more power. It
can disintegrate scrap rubber and compound the toughest
plastic masses.
• Are often called intensive mixers.
SIGMA MIXER:
• The sigma blade mixer is a commonly used and most popular
mixer for high viscosity materials.
• It belongs to the family of double arm kneader mixers.
• It consist of a short rectangular trough with a saddle shaped
bottom. Two counter rotating blades are incorporated in the
trough.
• The blades are so placed and shaped that the material turned
up by one blade is immediately turned under the adjacent
one.
• The blades are driven through a gear mechanisam provided at
either or both ends.
• The trough may be open or closed and may be jacketed for
heating or cooling. The machine is operated in a batch wise
fashion.
• The machine can be emptied through a bottom valve where
100% discharge or thorough cleaning, between batches, is not
as essential.
• The material to be kneaded is dropped into the trough and
mixed for a period of about 5-20 minutes or longer.
• The trough is then unloaded by tilting it.
Blades for Double Arm Kneader
• Various designs of mixing blades are in following figure. The
sigma blade is most widely used.
• The mixer employing sigma blades is capable of starting and
operating with either liquids or solids or a combination of both.
• The sigma blade has good mixing action and is relatively easy to
clean when sticky materials are being handled.
• The dispersion blade builds up high shear forces required to
disperse powder or liquids into plastic or to rubbery masses.
• The double-naben blade is useful for heavy plastic materials.
Banbury Mixer
• A banbury mixer is the most common internal mixer. It is a heavy
duty machine with two blades each rotating in a cylindrical
sheet, but these cylinders partly intersect with each other.
• The blade is pear shaped, but the projection is spiral along the
axis and the two spirals interlock.
• The machine operates at a speed of 40 rpm or lower.
• The clearance between the blades and the walls is extremely
small, and it is here that the mixing action takes place.
• The material is fed from above and held in the trough during
mixing by an air-operated piston under a pressure of 1-10
kgf/cm^2.
• Mixed material is discharged through a heavy sliding door
which is provided at the bottom of the trough.
• The heat generated is taken out by spraying cooling water on
the walls of the mixing chamber and circulating through the
hollow agitator shafts during operation.
• Used mainly in plastic and rubber industries.
Figure :- Banbury Mixer
Muller Mixers
• A muller mixer consists of a pan incorporating muller wheels.
• In one of the designs of muller mixer , the pan is stationary and
wheels rotate; while in the other design, the pan is rotated and
the axis of the wheels is held stationary.
• In the stationary pan muller mixer, the central vertical shaft is
driven, causing the muller wheels to roll in a circular path over a
layer solids on the pan floor.
• Plows direct the solids under the muller wheels during mixing or
to an opening in the pan floor for the discharge of the mixer at
the end of the cycle.
• The muller wheels crush the material, breaking down lumps
and agglomerates.
• Capacity of the muller mixer ranges from a fraction of cubic
meter to more than 1.6 m^3 and the corresponding power
requirements ranges from 1/3 to 75hp.
• Mullers are used for handling batches of heavy solids and
pastes.
• These are also effective in uniformly coating the particles of
granular solids with a small amount of liquid.
Mixer Extruders
• Extruders are used to mix liquid-solid systems and to extrude
molten or plasticized polymers to semi-final and final product
forms.
• The feed to an extruder usually contains the base polymer in
granular or powder form, together with additives such as
stabilizers, plasticizers, and coloring pigments.
• The base polymer and additive are combined in a feed tunnel,
providing a relatively homogeneous mass that is then extruded
in the main working chamber.
• During processing in the extruder, the polymer is melted and the
additives are mixed.
• The feed enters a channel where it is mixed by one or two
rotating screws.
• The extrudate product is delivered at high pressure and at a
controlled rate from the extruder for shaping by a die or mold.
Applications:
• Plastic industry
• Preparation of additives such as pigments and resins
• Used to process cat and dog foods
• Floating and sinking fish feeds for the aquaculture and fish
farming
Heating and Cooling Mixers
High Speed Mixer:
• Bigger vessel with double wall jacket construction and perfect
height to dia ratio.
• Inside vessel is made from S.S 304 and mirror polished to avoid
depositing of material.
• Adjustable baffle plate is provided to achieve rapid and better
dispersion.
• Efficient production without cross- contamination and free from
moisture.
• Lower scrap rates in the extrusion due to consistence quality of
the dry blend.
• Excellent dispersion of the additives even with higher calcium
loading.
• Precise peripheral speed of mixing tool.
• Special S.S. blades having abrasive and wear resistance,
balanced with proper design for excellent mixing and higher
blade life.
• Heavy duty bearing housing with best quality bearings for
trouble free working.
• Best quality material of all key components.
Cooling Mixer
• Bigger S.S. 304 Vessel mirror polished with mild steel jacket
for water circulation insures better and efficient cooling of
compounds.
• Mirror polished S.S 304 cone is provided for water circulation
and to increasing the cooling surface area and efficient
cooling cycle in least time.
• Shovel type S.S blades for efficient movement of compound
for shorter cooling time and discharge of material.
Thanks for attention

Types of solid fluid mixers

  • 1.
    GOVERNMENT ENGINEERING COLLEGE, BHARUCH •SUBJECT : SOLID-FLUID OPERATION • Topic: Static mixers, intensive mixers, heating and cooling mixers SEM:-8, Group:-2, Year:-2018 Prepared by: • VAGADIA HARDIK (140140105018) • PATEL RASHMIN (140140105045) • PATEL RONAK (140140105046) • RAJ PRIYANK (140140105050) • MODI SAGAR (140140105057)
  • 2.
    Contents •Static Mixers: HelicalElement Mixers and Turbulent Vortex Mixer or High Shear Mixers(HSM) •Intensive Mixers: Change-can mixers, Kneaders: Double-arm kneader (Sigma mixer) and Banbury mixer, Mixer extruder and Muller mixer •Heating and Cooling Mixers
  • 3.
    Static Mixers • Whatare static mixers? • These are the mixers which are applicable to gases or low viscosity liquids which are blended by passing them together through a length of a open pipe or a pipe containing orifice plates or segmental baffles. • So the mixing is done by the flow of the gases or liquids inside the pipe only. • Under appropriate conditions the pipe length may be as short as 5 to 10 pipe diameters, but 50 to 100 pipe diameters is recommended. • More difficult mixing tasks are accomplished by static mixers, commercial devices which consist of a series of metal inserts placed in the pipe.
  • 4.
    • Types ofStatic Mixers: • Helical element mixer • Turbulent vortex mixer
  • 5.
    Helical Element Mixers •Helical-element mixer is mainly used with viscous liquids and pastes. • This mixers provide continuous in- line mixing of fluids, gases, or powders using no moving components. That’s why also known as motionless mixers. • Alternating helical mixing elements provide thorough radial and axial blending in a short length by dividing the main flow into two equal streams as material passes each element. • Each element 1 to 1.5 pipe diameters in length, divides the stream into two, gives it a 180 degree twist, and delivers it to the next element.
  • 6.
    • Figure (a): Elementsof a helical-element mixer;
  • 7.
    • The secondelement divides the already divided stream and twists it 180 degree in the opposite direction. • Successive elements further subdivide the stream until the striations are so thin that the blending process can be finished by molecular diffusion. • The number of divisions increases by 2^n, where “n” is the number of elements. • These mixers are custom-designed for each application. The number of elements is determined by the specific application. • Mixers can be jacketed or electrically heated, and supplied with fixed or removable mixer elements. • Sizes range from 2mm to 2m in diameter. • The recommended number of helical elements is 6 for Re = 100 to 1000, 12 for Re = 10 to 100, and 18 for Re less than 10.
  • 8.
    • More elementsare needed for very viscous liquids because of the lower molecular diffusivity. • The pressure drop per unit length is about 6 times that in the empty pipe when Re less than 10, but increases to about 50 to 100 times that in the empty pipe when Re = 2000.
  • 10.
    Advantages • Provide excellentmixing or blending of two liquids, a liquid and gas, two gases, or two powders • Plug flow device (first in, first out) • Short, uniform residence time • Uniform temperature, no “hot spots” • Smooth shape and edge sealing of elements allows no dead spaces for product to hangup of degrade • Can be used for materials with low to high viscosities, upto 20000 poise or more • No maintenance since no moving parts • Can process highly corrosive materials • Can be used in high viscosity heat exchangers to increase heat transfer coefficients three to four times standard open tube designs
  • 11.
    Turbulent Vortex Mixeror High Shear Mixer • This is also used for gases and low-viscosity liquids as shown in figure (b). • This also provide continuous in-line mixing of fluids, gases, or powders using no moving components. • Each element of this mixer has four tabs protruding at an angle into the pipe. • Counter-rotating longitudinal vortices are formed in the wakes of the tabs, providing efficient blending of the liquids or gases after only two to four elements. • The unique, intermeshing element design provides high levels of mixing in a very short overall length and product residence time.
  • 12.
    • The pressuredrop per unit length is 25 to 40 times the value for the empty pipe at Re = 10^4 to 10^5, but since only a few elements are needed, the overall pressure drop is not large. • The design is also adaptable to many types of applications. • Figure (b) : Turbulent Vortex Mixer;
  • 14.
    • These mixersare custom-designed for each application. The number of elements and design specifics are determined by the specific application. • Mixers can be jacketed or electrically heated, and supplied with fixed or removable mixer elements. • Sizes range from 2mm to 2m and larger in diameter.
  • 15.
    Advantages • Provide excellentmixing or blending of two liquids, a liquid and gas, two gases, or two powders • Plug flow device (first in, first out) • Short, uniform residence time • Uniform temperature, no “hot spots” • Can be used for materials with low to high viscosities, upto 20000 poise or more • No maintenance since no moving parts • Can process highly corrosive materials • High degree of mixing in short overall length
  • 16.
    Applications Processes: Industries: Mixing Powdermixing Polymer processing Injection molding Reacting Liquid mixing Fiber production Fine films Coloring Laminar and turbul- Plastics extrusion Polymerzation ent mixing applications Foods including edible Heat exchange Obtaining product tem- oil, ice cream, mayonnai pH control perature uniformity -se, chocolate, beverage, Neutralization Extrusion milk, yogurt, and cheese Diffusion Compounding Pharmaceutical Gas mixing
  • 17.
    Materials Elements can beconstructed of : • Stainless steel • Hastelloy • Teflon • Carbon steel • PVC • PP (polypropylene) • PE (polyethylene) • FRP (fiber reinforced plastics) • Tantalum • Kynar • Inconell and many other materials
  • 18.
    Intensive Mixers Intensive mixersincludes: change-can mixers, kneader ( dispersor or masticator ), mixer extruder and muller mixers. Change-can mixer: • blend viscous liquids or light pastes as in food processing or paint manufacture. • a small removable can 5-100 gal in size holds the material to be mixed. • In pony mixer, the agitator consists of several vertical blades held on a rotating head and positioned near the walls of the can. • The blades are slightly twisted.
  • 19.
    • The agitatoris mounted eccentrically wrt the axis of the can. • The can rests on a turntable driven in a direction opposite to that of the agitator. • When mixing is complete, the agitator head is raised, lifting the blades put of the can, the blades are wiped clean, and the can is replaced with another containing a new batch. • In beater mixer, the can or vessel is stationary, the agitator has a planetary motion, are shaped to pass with close clearance over the side and bottom of the mixing vessel.
  • 21.
    KNEADERS: General Information: • Kneadersare high intensive mixers for cohesive solid systems. • Some kneaders achieve their mixing action by squashing the mass flat, holding it and squashing it again. • Others tear the mass apart and shear it between a moving blade and a stationary surface. There are two main types of kneaders: • There are two main types of kneaders: 1. Double arm kneader 2. Banbury Mixers
  • 22.
    Double arm Kneader •A two arm kneader handles suspensions, paste and light plastic masses. • All double arm kneader mixers are equipped with two mixing blades placed in W-shaped horizontal trough. • The commonly used blades are sigma blade, spiral blade, masticator blade and naben blade. • The blades rotate towards each other at the same or differential speed. • The rotation of blade is either tangential to each other or the blade may overlap within trough.
  • 24.
    • The bladespass the container walls and each other at a close clearance 2-3 mm resulting in homogeneous mixture. • The close clearance produce very high shearing action thereby reducing any large particles. • Homogeneous mixing is achieved within 10-15 minutes and mixing homogeneity is 99%. • The power consumption is very high compared to other types of mixers.
  • 25.
    • A disperseris heavier in construction and draws more power than a kneader, it works additives and coloring agents into stiff materials. • A masticator is still heavier and draws even more power. It can disintegrate scrap rubber and compound the toughest plastic masses. • Are often called intensive mixers.
  • 26.
    SIGMA MIXER: • Thesigma blade mixer is a commonly used and most popular mixer for high viscosity materials. • It belongs to the family of double arm kneader mixers. • It consist of a short rectangular trough with a saddle shaped bottom. Two counter rotating blades are incorporated in the trough. • The blades are so placed and shaped that the material turned up by one blade is immediately turned under the adjacent one. • The blades are driven through a gear mechanisam provided at either or both ends.
  • 27.
    • The troughmay be open or closed and may be jacketed for heating or cooling. The machine is operated in a batch wise fashion. • The machine can be emptied through a bottom valve where 100% discharge or thorough cleaning, between batches, is not as essential. • The material to be kneaded is dropped into the trough and mixed for a period of about 5-20 minutes or longer. • The trough is then unloaded by tilting it.
  • 29.
    Blades for DoubleArm Kneader • Various designs of mixing blades are in following figure. The sigma blade is most widely used. • The mixer employing sigma blades is capable of starting and operating with either liquids or solids or a combination of both. • The sigma blade has good mixing action and is relatively easy to clean when sticky materials are being handled. • The dispersion blade builds up high shear forces required to disperse powder or liquids into plastic or to rubbery masses. • The double-naben blade is useful for heavy plastic materials.
  • 32.
    Banbury Mixer • Abanbury mixer is the most common internal mixer. It is a heavy duty machine with two blades each rotating in a cylindrical sheet, but these cylinders partly intersect with each other. • The blade is pear shaped, but the projection is spiral along the axis and the two spirals interlock. • The machine operates at a speed of 40 rpm or lower. • The clearance between the blades and the walls is extremely small, and it is here that the mixing action takes place. • The material is fed from above and held in the trough during mixing by an air-operated piston under a pressure of 1-10 kgf/cm^2.
  • 33.
    • Mixed materialis discharged through a heavy sliding door which is provided at the bottom of the trough. • The heat generated is taken out by spraying cooling water on the walls of the mixing chamber and circulating through the hollow agitator shafts during operation. • Used mainly in plastic and rubber industries.
  • 34.
  • 35.
    Muller Mixers • Amuller mixer consists of a pan incorporating muller wheels. • In one of the designs of muller mixer , the pan is stationary and wheels rotate; while in the other design, the pan is rotated and the axis of the wheels is held stationary. • In the stationary pan muller mixer, the central vertical shaft is driven, causing the muller wheels to roll in a circular path over a layer solids on the pan floor. • Plows direct the solids under the muller wheels during mixing or to an opening in the pan floor for the discharge of the mixer at the end of the cycle.
  • 36.
    • The mullerwheels crush the material, breaking down lumps and agglomerates. • Capacity of the muller mixer ranges from a fraction of cubic meter to more than 1.6 m^3 and the corresponding power requirements ranges from 1/3 to 75hp. • Mullers are used for handling batches of heavy solids and pastes. • These are also effective in uniformly coating the particles of granular solids with a small amount of liquid.
  • 37.
    Mixer Extruders • Extrudersare used to mix liquid-solid systems and to extrude molten or plasticized polymers to semi-final and final product forms. • The feed to an extruder usually contains the base polymer in granular or powder form, together with additives such as stabilizers, plasticizers, and coloring pigments. • The base polymer and additive are combined in a feed tunnel, providing a relatively homogeneous mass that is then extruded in the main working chamber. • During processing in the extruder, the polymer is melted and the additives are mixed.
  • 38.
    • The feedenters a channel where it is mixed by one or two rotating screws. • The extrudate product is delivered at high pressure and at a controlled rate from the extruder for shaping by a die or mold.
  • 39.
    Applications: • Plastic industry •Preparation of additives such as pigments and resins • Used to process cat and dog foods • Floating and sinking fish feeds for the aquaculture and fish farming
  • 40.
    Heating and CoolingMixers High Speed Mixer: • Bigger vessel with double wall jacket construction and perfect height to dia ratio. • Inside vessel is made from S.S 304 and mirror polished to avoid depositing of material. • Adjustable baffle plate is provided to achieve rapid and better dispersion. • Efficient production without cross- contamination and free from moisture. • Lower scrap rates in the extrusion due to consistence quality of the dry blend.
  • 41.
    • Excellent dispersionof the additives even with higher calcium loading. • Precise peripheral speed of mixing tool. • Special S.S. blades having abrasive and wear resistance, balanced with proper design for excellent mixing and higher blade life. • Heavy duty bearing housing with best quality bearings for trouble free working. • Best quality material of all key components.
  • 43.
    Cooling Mixer • BiggerS.S. 304 Vessel mirror polished with mild steel jacket for water circulation insures better and efficient cooling of compounds. • Mirror polished S.S 304 cone is provided for water circulation and to increasing the cooling surface area and efficient cooling cycle in least time. • Shovel type S.S blades for efficient movement of compound for shorter cooling time and discharge of material.
  • 44.