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Shaping.

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Presentation on theme: "Shaping."— Presentation transcript:

1 Shaping

2 increasing liquid content
Shaping Overview of shaping technologies method product geometry Starting material mold costs product examples axial die pressing simple- complex granulate high ferrite cores, piezo ceramics isostatic pressing simple medium tubes, spark plug, pistons tape casting simple (tape) conc. suspension very low condensator substrates extrusion plastic mass low tubes pressure slip casting sanitary ceramics slip casting complex injection molding turbine blades Liquid content of the starting material for the different shaping processes Compaction of granulates ca. 5% Extrusion, injection molding ca Casting ca % increasing liquid content

3 Pressing Pressure forming methods
Shaping Pressing Pressure forming methods Compaction of powders is used for shaping simple forms. pump oil rubber bag Density (%) 20 40 60 80 100 Pressure(Mpa) alumina granules tile body KBr powder uniaxial pressing isostatic pressing Compaction process: 1. sliding and rearrangement of particles/granules 2. Deformation (elastic and plastic) of particles/granules (3. Densification of granules) Problems: - Unhomogeneous density distribution - Residual large pores (hollow granules) - Ejection problems Yanagida et al.: p

4 Isostating pressing Green body Pressure vessel with liquid
Shaping Isostating pressing Green body Pressure vessel with liquid Elastic, shape stable form The advantage of isostatic compaction is a more homogeneous density distribution. The complexity of the mold is, however, limited.

5 Die pressing: flow chart
Shaping Die pressing: flow chart Process flow diagram for shaping by die pressing.

6 Compaction of granules
Shaping Compaction of granules End stage I End stage II End stage III density pressure stage 1 stage 2 stage 3 Compaction behavior of granulated powders stage I granule flow and rearrangement stage II granule deformation stage III granule densification Evolution of the green-body microstructure during compaction of granules

7 Densification defects
Shaping Densification defects Pressure distribution in a die at the beginning and at the end of the second compaction stage. The spring back behavior after pressure is released is directly proportional to the pressure in a certain area. The differential pressure is mainly due to friction of the punch. Densification defects occurring on die pressed green bodies.

8 Die pressing additives
Shaping Die pressing additives Reed, 1995

9 Shaping Die pressing powders Reed, 1995

10 Products shaped by axial die pressing
Shaping Products shaped by axial die pressing

11 Shaping Slip casting I a) The slurry is poored into the mold made of plaster of Paris (CaSO4  0.5H2O). b) The mold absorbs the liquid, while the powder particles are deposited on the walls of the mold. c) The surplus suspension is drained and d) the greenbody is removed from the mold. Steps in slip casting of ceramics. (Source: From Modern Ceramic Engineering, by D.W. Richerson, p. 462, Fig Copyright © 1992 Marcel Dekker. Reprinted by permission.)

12 Shaping Hollow molds The holding time will dictate the wall thickness of the greenbody. Typical holding times are between 5 and 30 minutes.

13 Slip casting of sanitary ceramics
Shaping Slip casting of sanitary ceramics

14 Rheology in slip casting
Shaping Rheology in slip casting Slip casting of porcellaine 250 500 750 1000 1250 1500 Viscosity (mPa sec) 20 40 60 80 100 spindle speed (rpm) V The rheology of the cast is shear thinning. Before mixing, pumping and pouring the slurry has to be stirred % sodium silicate Influence of the viscosity on the shape of the slip casted white ware part

15 Kinetics of slip casting
Shaping Kinetics of slip casting The thickness of the cake deposited on the mold walls depend on mold and suspension characteristics. The wall thicknes growth is a parabolic.

16 Shaping Slip casting examples Slip casted silicon nitride turbine (Allied Signal)

17 Tape casting I Compositions of a alumina and titanate tape cast (vol%)
Shaping Tape casting I slurry doctor blade green body in form of a film liquid absorbing, porous film Compositions of a alumina and titanate tape cast (vol%) Powder Al2O BaTiO Solvent Trichlorethylene Methylethylketone Ethylalcohol Ethylalcolhol 16.0 Deflocculant Menhaden oil Menhaden oil Binder Polyvinylbutiral Acryllic emulsion Plasticizer Polyethylene glycol Polyethylene glycol Octyl phthalate Butylbenzlphtalate Wetting agent Cyclohexanone Such slurries exhibit also shear thinning. The quality and thickness of the tape is controlled by the size of the blade oppening, the speed of the tape, the rheology of the slurry and the shrinkage during drying. Industrial tape casting machines are up to 25m long, several meters wide and run with speeds. Up to 1.5m/min to produce tapes with thicknesses between 25 and 1250mm.

18 Shaping Tape casting II A doctor blade assembly. The ceramic slurry is held in the reservoir behind the blade [middle of the micrograph]. The twin micrometers [right] control the blade height above the carrier film. More sophisticated versions feature double blades and pumped metered slurry flow to keep the height of the slurry reservoir constant. Example of a tape drying on the Mistler laboratory-scale batch tape caster. Industrially the process is often continuous with the tape being force dried prior to removal from the carrier, dicing and further processing.

19 Pressurized slip casting I
Shaping Pressurized slip casting I 1. Closing of the mold 2. Injection of the slurry into the mold

20 Pressurized slip casting II
Shaping Pressurized slip casting II 3. Pressurizing the slurry 4. Draining of surplus slurry

21 Pressurized slip casting III
Shaping Pressurized slip casting III 5.Opening of the mold 6. Removal of the component

22 Pressurized slip casting examples
Shaping Pressurized slip casting examples Pressurized slip casting mold for sinks Finished products

23 Injection molding Process flow diagram
Shaping Injection molding Process flow diagram for shaping by injection molding

24 Injection molding products
Shaping Injection molding products Most products shown in the picture are guiding elements used in thread manufacturing

25 Extrusion casting cylindric greenbody slurry
Shaping Extrusion casting cylindric greenbody slurry Industrial pug mill ith deairing chamber and extrusion auger Yanagida et al.: p. 160

26 Drying of greenbodies I
Shaping Drying of greenbodies I Drying geometry moving drying air Boundary layer (air + vapour) Particles Suspension liquid Drying kinetics will depend on the rate of heat transfer into the body and mass (liquid) transport out of the body. Four rate determining processes can be distinguished: 1. Boundary layer mass transfer 2. Pore mass transfer 3. Boundary layer heat transfer 4. Pore heat transfer Each of the above steps are rate determining for some time during drying, the boundary layer process at the beginning, the pore processes towards the end. Mass and heat transfer rates are obviously coupled and equal to the evaporation rate E:

27 Drying of greenbodies II
Shaping Drying of greenbodies II as cast Shrinkage and deformation Moisture content at the surface const. Rate determining step: heat and mass transport through boundary layer No further shrinkage, all particles are in contact, leatherhard greenbody Moisture cont. constant rate Partially filled pores. Rate determining step: pore mass and heat transfer completely dry decreasingt rate time Typincal drying curve The boundary processes are linear functions of the greenbody size (radius for spheres, cylinders, thickness for plates), whereas the pore processes go with the square of the greenbody dimension. The overall rate is ± a square function of the greenbody size. Example for a spherical ZrO2 greenbody: Diameter: drying time 1cm h 10cm days

28 Shaping Drying shrinkage Linear and volume shrinkage of a greenbody can be defined by: The shrinkage can be influenced by the moisture content (Dl) amd the particle dimensions (N) shrinkage defects due to 1. Unhomogeneous drying of a homogeneous greenbody 2. Homogeneous drying of unhomogeneous green body moisture content drying rate shrinkage critical moist. cont. warping cracking delamination Unhomogeneities: - uneven moisture distribution - preferred orientation of particles


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