A Novel Micro- -Batch Mixer Batch Mixer A Novel Micro That Scales - - PowerPoint PPT Presentation

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A Novel Micro- -Batch Mixer Batch Mixer A Novel Micro That Scales - - PowerPoint PPT Presentation

A Novel Micro- -Batch Mixer Batch Mixer A Novel Micro That Scales To That Scales To The Single Screw Extruder The Single Screw Extruder By By Keith Luker, Randcastle Extrusion Keith Luker, Randcastle Extrusion Systems, Inc., Cedar Grove,


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SLIDE 1

A Novel Micro A Novel Micro-

  • Batch Mixer

Batch Mixer That Scales To That Scales To The Single Screw Extruder The Single Screw Extruder

By By Keith Luker, Randcastle Extrusion Keith Luker, Randcastle Extrusion Systems, Inc., Cedar Grove, NJ Systems, Inc., Cedar Grove, NJ Jennifer K. Lynch, Rutgers University Jennifer K. Lynch, Rutgers University Thomas J. Thomas J. Nosker Nosker, Rutgers University , Rutgers University

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SLIDE 2

Co Co-

  • Authors

Authors

  • Jennifer Lynch, of Rutgers

Jennifer Lynch, of Rutgers

  • Tom

Tom Nosker Nosker, of Rutgers , of Rutgers

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SLIDE 3

Background Background

  • Batch mixers mix.

Batch mixers mix.

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SLIDE 4

Background Background

  • Batch mixers mix.

Batch mixers mix.

  • Single Screw Extruders (SSE) do not

Single Screw Extruders (SSE) do not mix. mix.

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SLIDE 5

Background Background

  • Batch mixers mix.

Batch mixers mix.

  • Single Screw Extruders (SSE) do not

Single Screw Extruders (SSE) do not mix. mix.

  • Therefore, to suggest making a batch

Therefore, to suggest making a batch mixer to scale to a single screw mixer to scale to a single screw extruder, is an oxymoron. extruder, is an oxymoron.

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SLIDE 6

Background Background

  • Until Antec 07, few took the SSE as a

Until Antec 07, few took the SSE as a serious compounder. serious compounder.

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SLIDE 7

Background Background

  • Until Antec 07, few took the SSE as a

Until Antec 07, few took the SSE as a serious compounder. serious compounder.

  • At Antec 07, an SSE was described that:

At Antec 07, an SSE was described that:

  • Compounded to the 500 nm scale.

Compounded to the 500 nm scale.

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SLIDE 8

Background Background

  • Until Antec 07, no one took the SSE as a

Until Antec 07, no one took the SSE as a serious compounder. serious compounder.

  • At Antec 07, an SSE was described that:

At Antec 07, an SSE was described that:

  • Compounded to the 500 nm scale.

Compounded to the 500 nm scale.

  • Vented over a thin film.

Vented over a thin film.

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SLIDE 9

Background Background

  • Until Antec 07, no one took the SSE as a

Until Antec 07, no one took the SSE as a serious compounder. serious compounder.

  • At Antec 07, an SSE was described that:

At Antec 07, an SSE was described that:

  • Compounded to the 500 nm scale.

Compounded to the 500 nm scale.

  • Vented over a thin film.

Vented over a thin film.

  • Used 3 vents in a 36/1 L/D

Used 3 vents in a 36/1 L/D

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SLIDE 10

Background Background

  • Until Antec 07, no one took the SSE as a

Until Antec 07, no one took the SSE as a serious compounder. serious compounder.

  • At Antec 07, an SSE was described that:

At Antec 07, an SSE was described that:

  • Compounded to the 500 nm scale.

Compounded to the 500 nm scale.

  • Vented over a thin film.

Vented over a thin film.

  • Used 3 vents in a 36/1 L/D

Used 3 vents in a 36/1 L/D

  • Created multiple elongational flow fields

Created multiple elongational flow fields— —the the same mechanism as the parallel twin same mechanism as the parallel twin compounder. compounder.

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SLIDE 11

Background: Yesterday Antec 08 Background: Yesterday Antec 08

  • A variant of this 07 SSE reported the

A variant of this 07 SSE reported the ability to compound thermally sensitive ability to compound thermally sensitive materials: materials:

  • EVOH in multilayer regrind.

EVOH in multilayer regrind.

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SLIDE 12

Background: Yesterday Antec 08 Background: Yesterday Antec 08

  • A variant of this 07 SSE reported the

A variant of this 07 SSE reported the ability to compound thermally sensitive ability to compound thermally sensitive materials: materials:

  • EVOH in multilayer regrind.

EVOH in multilayer regrind.

  • Cellulose and oil

Cellulose and oil

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SLIDE 13

Background: Yesterday Antec 08 Background: Yesterday Antec 08

  • A variant of this 07 SSE reported the ability

A variant of this 07 SSE reported the ability to compound thermally sensitive materials: to compound thermally sensitive materials:

  • EVOH in multilayer regrind.

EVOH in multilayer regrind.

  • Cellulose and oil

Cellulose and oil

  • RPVC Pellets

RPVC Pellets— —at unheard of high screw speeds. at unheard of high screw speeds.

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SLIDE 14

Output RPVC Pellets Output RPVC Pellets

1 Inch 36/1 Extruder 1 Inch 36/1 Extruder

40 60 80 100 120 140 25 30 35 40 45 50 55 60 65 70 75 80 85 90 95

8.5 kg/ h Grams/ Minute Screw RPM

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SLIDE 15

Stock Temperature Stock Temperature

RPVC Pellets 25 mm, 36/1 Extruder RPVC Pellets 25 mm, 36/1 Extruder

192 194 195 196 187 189 192 194 184 186 187 188 181 182 183 184 176 178 179 184 175 185 195 0 (Flush) 0.1 0.2 0.3 96 rpm 81 rpm 60 rpm 46 rpm 30 rpm

Degrees C I mmersion Depth (mm)

(Through a 25 mm bore)

0 2.5 5 8

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SLIDE 16

Background: Yesterday Antec 08 Background: Yesterday Antec 08

  • A variant of this 07 SSE reported the ability to

A variant of this 07 SSE reported the ability to compound thermally sensitive materials: compound thermally sensitive materials:

  • EVOH in multilayer regrind.

EVOH in multilayer regrind.

  • Cellulose and oil

Cellulose and oil

  • RPVC Pellets

RPVC Pellets— —at unheard of high screw speeds. at unheard of high screw speeds.

  • RPVC Powder

RPVC Powder— —currently dominated by the conical currently dominated by the conical twin twin— —now processed easily at even higher screw now processed easily at even higher screw speed and scaled up to production! speed and scaled up to production!

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SLIDE 17
  • RPVC Powder:

RPVC Powder:

  • 25 mm:

25 mm:

  • 180 RPM

180 RPM

  • Melt 177C

Melt 177C

  • 13.2 kg/hr

13.2 kg/hr

Background: Yesterday Antec 08 Background: Yesterday Antec 08

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SLIDE 18
  • RPVC Powder:

RPVC Powder:

  • 25 mm:

25 mm:

  • 180 RPM

180 RPM

  • Melt 177C

Melt 177C

  • 13.2 kg/hr

13.2 kg/hr

  • 63 mm:

63 mm:

  • 70 RPM

70 RPM

  • Melt 191

Melt 191

  • 70 kg/hr

70 kg/hr

Background: Yesterday Antec 08 Background: Yesterday Antec 08

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SLIDE 19

UC Mixer UC Mixer SFEM SFEM Flexible PVC pellets/0.5% red/0.5% yellow concentrate Flexible PVC pellets/0.5% red/0.5% yellow concentrate

Coloring Vinyl Film Coloring Vinyl Film

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 20

Single Screw Mixer Comparison Single Screw Mixer Comparison 10% Elastomer & LDPE 10% Elastomer & LDPE

UC Mixer Double Wave SFEM

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 21

Advanced Materials via Immiscible Polymer Processing

A Cooperative Center for Research, Development and Commercialization

SFEM Single Screw Twin Screw SFEM Single Screw Twin Screw

RUTGERS

THE STATE UNIVERSITY OF NEW JERSEY

Single Screw Single Screw vs vs Twin Screw Twin Screw Continuous: 20PS/80PE Continuous: 20PS/80PE

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 22

Advanced Materials via Immiscible Polymer Processing

A Cooperative Center for Research, Development and Commercialization

RUTGERS

THE STATE UNIVERSITY OF NEW JERSEY

10 microns

Right picture, Antec 95, “CO-CONTINUITY AND PHASE INVERSION IN HDPE/PS BLENDS: THE ROLE OF INTERFACIAL MODIFICATION” by Daniel Bourry and Basis D. Favis

Twin @ 2,000 X Single Screw SFEM

10 microns

Picture courtesy Rutgers.

@ 2,000 X

Note: Material viscosity different.

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 23

Ceramic Nano Ceramic Nano-

  • Composites

Composites

PMMA Pellets & 5% Nano Ceramic 30 to 60 nm PMMA Pellets & 5% Nano Ceramic 30 to 60 nm

5,000 X 10,000X 50,000X

Advanced Materials via Immiscible Polymer Processing

A Cooperative Center for Research, Development and Commercialization

RUTGERS

THE STATE UNIVERSITY OF NEW JERSEY

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 24

This picture shows untangled CNT’s

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

Single Wall Carbon Nano Tubes Single Wall Carbon Nano Tubes

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SLIDE 25

2% Carbon Nano 2% Carbon Nano-

  • Tubes & PC

Tubes & PC

100,000 X 100,000 X (Enhanced)

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 26

Multi-wall CNT’s tested IEC 60093:

35 to 85 Ohms/ sq

5% Carbon Nano 5% Carbon Nano-

  • Tubes In

Tubes In Acetal Acetal

Conductive to Conductive to Dissapative Dissapative Range Range

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 27

Wood Flour & LDPE Pellets Wood Flour & LDPE Pellets

25% Flour 40% Flour

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 28

Wood Flour & RPVC Powder Wood Flour & RPVC Powder

100% RPVC Powder 60% RPVC 40% Woodflour Before Degassing 1” x 0.125 Tensile Bar 1” x 0.062 Tensile Bar

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 29

RPVC Pellets & RPVC Pellets & 15% Calcium Carbonate 15% Calcium Carbonate

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 30

35% Calcium Carbonate Powder 35% Calcium Carbonate Powder With PP Pellets: Two Vents With PP Pellets: Two Vents

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 31
  • The

The “ “Elongator Elongator” ” is a is a S

Spiral

piral F

Fluted

luted

E Elongational

longational M

  • Mixer. Generically: SFEM.
  • ixer. Generically: SFEM.

Background: Background: SSE Compounding SFEM SSE Compounding SFEM

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SLIDE 32

Background Background

  • Micro

Micro-

  • batch mixers useful for rare or

batch mixers useful for rare or expensive ingredients. expensive ingredients.

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SLIDE 33

Background Background

  • Micro

Micro-

  • batch mixers useful for rare or

batch mixers useful for rare or expensive ingredients. expensive ingredients.

  • Several types are known:

Several types are known:

  • A miniature conical twin screw with a

A miniature conical twin screw with a recirculation loop. recirculation loop.

  • A cup and rotor mixer.

A cup and rotor mixer.

  • An internal batch mixer with roller blades.

An internal batch mixer with roller blades.

  • Miniature dual pistons driving material back

Miniature dual pistons driving material back and forth. and forth.

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SLIDE 34

Purpose of This Study Purpose of This Study

  • Find out how well the SFEM SSE

Find out how well the SFEM SSE compares to the new micro batch mixer. compares to the new micro batch mixer.

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SLIDE 35

Experimental: Experimental:

  • Macroscopic: Extrude samples with SFEM

Macroscopic: Extrude samples with SFEM and compare to the micro and compare to the micro-

  • batch mixer.

batch mixer.

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SLIDE 36

Experimental: Experimental:

  • Macroscopic: Extrude samples with SFEM

Macroscopic: Extrude samples with SFEM and compare to the micro and compare to the micro-

  • batch mixer.

batch mixer.

  • Microscopic: Look at the immiscible

Microscopic: Look at the immiscible blends of polystyrene and blends of polystyrene and polyethelene polyethelene and see if the domains compare. and see if the domains compare.

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SLIDE 37

Historically Historically Single Screw Mixers Push! Single Screw Mixers Push!

Push to create melting. Push to create melting. Then push Then push after after melting for mixing as shear. melting for mixing as shear.

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SLIDE 38

Resistance Zone

C1 C2

Union Carbide Mixer Union Carbide Mixer (aka (aka Maddocks Maddocks Mixer) Mixer)

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SLIDE 39

Twisted UC Mixer Is An Egan Mixer Twisted UC Mixer Is An Egan Mixer

With Shaded Resistance Zone And Channels With Shaded Resistance Zone And Channels

C1 dead ends into B causing resistance. Pressure, generated upstream and by the spiral geometry forces material over the shaded resistance zone (RZ) where the material is sheared. C2 RZ C1 Flighted Barrier (B)

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SLIDE 40

Pushing Is Bad For Mixing Pushing Is Bad For Mixing

A-B-B-B-B-A

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SLIDE 41

A-B-B-B-B-A A-

  • A

B

Pushing Is Bad For Mixing Pushing Is Bad For Mixing

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SLIDE 42

Since Pushing Equals Bad Since Pushing Equals Bad… …

A-B-B-B-B-A A-

  • A

B

We must need a new force!

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SLIDE 43

Suppose We Suppose We Pull Pull ? ?

A-B-B-B-B-A

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SLIDE 44

Then Then… …

A-B-B-B-B-A

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SLIDE 45

Then Then… …

A – B – B – B –B - A

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SLIDE 46

Then Then… …

A – B – B – B – B - A

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SLIDE 47

Pulling Is Good For Mixing! Pulling Is Good For Mixing!

A – B – B – B – B - A

The smaller the domains, the better The smaller the domains, the better the mixing. the mixing.

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SLIDE 48

Suppose We Only Want To Melt? Suppose We Only Want To Melt?

A-A-A-A-A-A

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SLIDE 49

Pulling Pulling Is Good For Melting Too!

Is Good For Melting Too!

A – A – A – A – A - A

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SLIDE 50

New Generation of Mixers New Generation of Mixers Pull Pull And And Pull Pull Right Away Right Away

AFEM

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SLIDE 51

How Does the SFEM Work? How Does the SFEM Work?

P = Pump P = Pump C = Channel C = Channel

C1 C2 C3 P2 P1

AFEM

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SLIDE 52

Imagine A Screw Imagine A Screw Without A Flight At The End Without A Flight At The End

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SLIDE 53

In The Smooth Section, In The Smooth Section, What Path Will A Particle Take? What Path Will A Particle Take?

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SLIDE 54

A Spiral A Spiral

Pressure Flow Drag Flow

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SLIDE 55

If You Stop The Feed If You Stop The Feed… …

Drag Flow Pressure Flow

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SLIDE 56

Material Is Pumped In A Circle Material Is Pumped In A Circle

Drag Flow Pressure Flow

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SLIDE 57

So, A Smooth Section So, A Smooth Section Is A Radial Pump Is A Radial Pump

Drag Flow Pressure Flow

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SLIDE 58

End View Of Radial Pump End View Of Radial Pump’ ’s s Particle Path Particle Path

Drag Flow

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SLIDE 59

Suppose You Put Two Channels Suppose You Put Two Channels Into The Smooth Section Into The Smooth Section

Drag Flow P1 P2 C1 C2 P = Pump C = Channel

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SLIDE 60

Cross Section of AFEM or SFEM Cross Section of AFEM or SFEM

C1 C2 C3 P2 P1

P = Pump P = Pump C = Channel C = Channel

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SLIDE 61

Fine Elongation Fine Elongation

Region Of Fine Elongation

C1 P1

  • In the approach to the first pump, material

experiences fine elongation at low pressure

  • Lowest pressure means the lowest possible heat

rise! Zero is the lowest.

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SLIDE 62

Bi Bi-

  • Lobal Kneading Disc

Lobal Kneading Disc

Outline of twin’s Bi-lobal kneading disc

In the approach to the pump, the polymer cannot “know” whether it is in a single or a twin screw.

C1 P1 P2 C2 C3 Q092205.WLG

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SLIDE 63

C1 C2 V=0

Shear In P1 Is Shear In P1 Is “ “Pure Pure” ”

There is no pressure flow pushing material into P1—only drag flow . Shear mixing is

  • maximized. Heat rise is minimized.

Barrel Velocity is high

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SLIDE 64

C1 C2 V=0

Two Dimensional Elongation Two Dimensional Elongation

Exiting P1, material is released from P1 but still stuck to the barrel surface. Material extends two dimensionally.

Barrel Velocity is high

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SLIDE 65

C1 C2 C3 P1 P2

Thin Film Created For Venting Thin Film Created For Venting

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SLIDE 66

SFEM SFEM

Vent positions

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SLIDE 67

SFEM SFEM

End of Second C2 Beginning of First C1 End of Second C3 End of Second C1

P = Pump P = Pump C = Channel C = Channel

C1 C2 C3 P1 P2 P1 P2 Flight

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SLIDE 68

Batch Mixer Element Batch Mixer Element

C1 C2 C3 P2 P1

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SLIDE 69

Batch Mixer Element Batch Mixer Element

Pellets/Powder Plus

Die hole is covered during compounding then exposed during extrusion

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SLIDE 70

Batch Mixer Element: Flat View Batch Mixer Element: Flat View

C1 C2 C3 P2 P1

Seal

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SLIDE 71

Micro Batch Mixer Micro Batch Mixer

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SLIDE 72

Mixed for 2.5 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 73

Mixed for 2.5 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

slide-74
SLIDE 74

Mixed for 2.5 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 75

Mixed for 2.5 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 76

Mixed for 3.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

slide-77
SLIDE 77

Mixed for 3.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 78

Mixed for 3.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 79

2.5 Minutes 3.0 Minutes At 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

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SLIDE 80

Mixed for 4.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

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SLIDE 81

Mixed for 4.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

slide-82
SLIDE 82

Mixed for 4.0 minutes at 4.3 rpm

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

Polypropylene + 1% Red

slide-83
SLIDE 83

Batch Mixer Cooling Experiments Batch Mixer Cooling Experiments

2.5 Minutes 3.0 Minutes 4.0 Minutes At 4.3 rpm ~14 Revolutions Total

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SLIDE 84

1% Red Film and 1% Red Rod 1% Red Film and 1% Red Rod From Micro From Micro-

  • Batch Mixer

Batch Mixer

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SLIDE 85

10% Elastomer & LDPE 10% Elastomer & LDPE

SFEM SFEM Double Wave Batch Mixer Extruder Extruder

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SLIDE 86

Batch Mixer: Batch Mixer: Multiple Batch Test: RPVC Multiple Batch Test: RPVC

1.

  • 1. Process 15 Grams

Process 15 Grams

2.

  • 2. Extrude 5 grams

Extrude 5 grams

3.

  • 3. Close die door.

Close die door.

4.

  • 4. Repeat # 2 and # 3 five more times

Repeat # 2 and # 3 five more times for a 30 grams total. for a 30 grams total.

5.

  • 5. RPVC still not yellowed.

RPVC still not yellowed.

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SLIDE 87

35% Calcium Carbonate & PP 35% Calcium Carbonate & PP

SFEM Extruder SFEM Batch Mixer

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SLIDE 88

Continuous: 20PS/80HDPE Globules Continuous: 20PS/80HDPE Globules Domains: 0.2 to 2 Micron Domains: 0.2 to 2 Micron

(A) (B) (C ) (D)

Batch Mixer 24/1 Extruder, 2 SFEM

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SLIDE 89

(G ) (H) (E ) (F )

Batch Mixer 24/1 Extruder, 2 SFEM

Co Co-

  • continuous:30PS/70HDPE 3D Puzzle

continuous:30PS/70HDPE 3D Puzzle Domains: 02 to 20 Domains: 02 to 20+

+ Micron

Micron

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SLIDE 90
  • The SFEM Mixer and Extruder:

The SFEM Mixer and Extruder:

  • Have very similar physical geometry

Have very similar physical geometry yielding very similar levels of yielding very similar levels of mixedness mixedness. .

  • The micro

The micro-

  • batch mixer works on a time

batch mixer works on a time scale similar to extrusion. scale similar to extrusion.

Discussion/Conclusions: Discussion/Conclusions:

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SLIDE 91

Discussion/Conclusions: Discussion/Conclusions:

  • The SFEM comparisons represent

The SFEM comparisons represent major scenarios in single screw major scenarios in single screw extrusion. extrusion.

  • Color

Color

  • Thermally sensitive materials

Thermally sensitive materials

  • High filler levels

High filler levels

  • Melt Blending

Melt Blending

slide-92
SLIDE 92

Discussion/Conclusions: Discussion/Conclusions:

  • The SFEM mixer:

The SFEM mixer:

  • Extrudes a strand!

Extrudes a strand!

  • Strands are easy to pelletize.

Strands are easy to pelletize.

  • Pellets are the proper feed stock for

Pellets are the proper feed stock for processing equipment. processing equipment.

  • Avoids degradation.

Avoids degradation.

  • Is really fast so R & D mixtures prepared

Is really fast so R & D mixtures prepared in the Micro batch mixer will speed in the Micro batch mixer will speed results and scale to extrusion. results and scale to extrusion.

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SLIDE 93

Thanks To: Thanks To:

  • Jennifer Lynch and Tom

Jennifer Lynch and Tom Nosker Nosker of

  • f

Rutgers for the pictures of the PS/PE Rutgers for the pictures of the PS/PE blends and the ceramic nano particles. blends and the ceramic nano particles.

  • Very special thanks to Jennifer Lynch

Very special thanks to Jennifer Lynch for her effort, patience, advise and for her effort, patience, advise and gracious style. gracious style.

Advanced Materials via Immiscible Polymer Processing

A Cooperative Center for Research, Development and Commercialization

RUTGERS

THE STATE UNIVERSITY OF NEW JERSEY

slide-94
SLIDE 94

Thank You Thank You

PRESENTED BY

Keith Luker

President

Randcastle Extrusion Systems, Inc.

keithluker@randcastle.com

Questions?