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The State of the
Powder Handling
Industry
Presented by:
Joe Marinelli of Solids Handling Technologies
Karl Jacob of The Dow Chemical Company
Joe Florkowski of Powder & Bulk Solids
About Joe and Karl
 Joe Marinelli –President of Solids
Handling Technologies with 42
years in solids handling
 Karl Jacob – 32 years with Dow,
founder of Solids Processing Lab
Context of today’s
presentation
 Will focus primarily on bulk
solids handling – hoppers & bins,
chutes, pneumatic conveying
Brief History
 Coulomb and Rankine (1773 & 1857
 Janssen (1895)
 Jenike (1960’s)
Flowability measurements
• Jenike Shear Tester
 Standard in Europe and US
• Rotational Shear Testers
 Schulze RST, Brookfield,
Freeman, Peschl
• Rotational testers have increased
productivity and reproducibility
Direct Shear Testers
Ring
Jenike
Peschl
Freeman
Brookfield
Need for understanding of
shear testing measurements
• How to use flow properties test
results
• Practical designs to ensure
reliable flow
• Need to consider special designs
for difficult materials like elastic
solids, stick-slip, flaky, etc.
Current situation in bulk
solids handling
• Power plants shutting down
• Recognition by pharma sector of the
importance of solids handling
• Alternative energy strategy
bringing new solids handling
problems like batteries, biomass,
etc.
• New polymeric materials are
different than previous materials
like PS, PE, PC, Nylon, etc.
Economic Trends
• Recovering slowly from recession
• Aging equipment will have to be
upgraded
• Provides opportunities for reliable
vendors to help their customers
Education – still a
problem!
• Solids handling not consistently
taught at university level
• Most new engineers not aware of the
science of solids handling
• International universities involved
with solids handling applications –
Australia and Germany for example
• Lack of familiarity with Bulletin 123
Education
 Only a few institutions teach an
elective course in particle technology
– Akron, Purdue, Texas A&M, CCNY,
Cooper Union, Colorado, Florida
 Industry needs to push for this topic
to taught and seen as equal as other
mechanical and chemical operations
 Students need to understand the
importance of the area and how they
can add value by knowing about
solids
Research
• Fundamental research in bulk solids
handling still lacking in the USA
• Research tends to focus on the
“new” ideas – making and using
nanoparticles for example.
• Recent AIChE Plenary Session
underscored the industrial need for
particle technology expertise in both
research and manufacturing
Future Directions
Computational Tools
• Considerable progress in the last decade
for a variety of computational tools –
DEM, DEM/CFD, Solids Flowsheeting
tools
• Allow examination of geometries not
solved analytically
• Combination of computer science and
engineering science will only make
these tools better
• Validation essential!!!!
Pneumatic Conveying
 Still a lot more work to do in dense
phase to move from empirical
approach to more fundamental
approach
 Is there a way to correlate pickup
velocity or line pressure drop to
flow properties?
 Helpful values are: particle density,
particle size distribution and shape
Retrofits vs. New Equipment
• More companies fixing existing
equipment
• May be more practical to replace
with new equipment
• Requires knowledge of solids
handling and a practical approach
Biomass Handling
• Alternative and renewable energy
critical
• Wood pellets or chips for heat
• Soy, animal fats for biofuels
• Sugarcane, corn starch, switchgrass,
bamboo, palm
• Agricultural and municipal waste
• Estimated at 146 billion tons/yr used
Most folks forget about the “messy front end”
of biomass and grossly underestimate the
complexities of the situation.
A Better Understanding of flow
Promoting Devices
• Need much more understand of the
transmission of pressure and
vibrational waves in bulk solid as
function of solids properties
• Vibration
 Vibrators, bin dischargers, etc
• Aeration
 Aeration nozzles, air blasters
Segregation Problems
 Segregation problems are common
 Several mechanisms that cause it
 Excellent work done by Lueptow at
Northwestern and McCarthy at Pitt
beginning to shed fundamental
light on the problem
Northwestern Work
Stratified Segregated Mixed
W = 69 cm
Q = 1 cm3/s Q = 24 cm3/s Q = 420 cm3/s
q = Q/T
vr
Large
Particles
Small
Particles
Mixed
ParticlesStratified
Rathole Calculations
 Rathole calculations are too conservative
 Jenike found conservative approach
necessary
 An approach to determine stresses acting
on solids in funnel flow is required
Ratholing
“Dead” or non-
flowing region
Very simple
question: how big
should the hole be to
prevent the
formation of a stable
rathole?
• Approaches thus far
• Jenike ff=1.7
• Johanson, JR,
effective head approach
• Arnold and Roberts,
average the above
• Schwedes
•So what do we do?
• experienced practitioners
know what bound to choose
• consider the economic
consequence of a 6 ft outlet
size
Testing Flaky Materials
 How to test elastic or flaky products
 These materials do not shear well
 Shear cells too small for large
particle flakes
Silo Quaking Issues
 Flow of certain materials cause
serious vibrations
 Typically occurs with
incompressible materials
 Some possible solutions
Final Thoughts
 Still lots of good problems to address
 Will need academic/industrial
collaboration
 Venues like this powder show are a
necessity
Find Joe’s Powder Perspectives column online at:
http://www.powderbulksolids.com/powder-perspectives

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State of the Powder Bulk Solids Industry

  • 1. The State of the Powder Handling Industry Presented by: Joe Marinelli of Solids Handling Technologies Karl Jacob of The Dow Chemical Company Joe Florkowski of Powder & Bulk Solids
  • 2. About Joe and Karl  Joe Marinelli –President of Solids Handling Technologies with 42 years in solids handling  Karl Jacob – 32 years with Dow, founder of Solids Processing Lab
  • 3. Context of today’s presentation  Will focus primarily on bulk solids handling – hoppers & bins, chutes, pneumatic conveying
  • 4. Brief History  Coulomb and Rankine (1773 & 1857  Janssen (1895)  Jenike (1960’s)
  • 5. Flowability measurements • Jenike Shear Tester  Standard in Europe and US • Rotational Shear Testers  Schulze RST, Brookfield, Freeman, Peschl • Rotational testers have increased productivity and reproducibility
  • 7. Need for understanding of shear testing measurements • How to use flow properties test results • Practical designs to ensure reliable flow • Need to consider special designs for difficult materials like elastic solids, stick-slip, flaky, etc.
  • 8. Current situation in bulk solids handling • Power plants shutting down • Recognition by pharma sector of the importance of solids handling • Alternative energy strategy bringing new solids handling problems like batteries, biomass, etc. • New polymeric materials are different than previous materials like PS, PE, PC, Nylon, etc.
  • 9. Economic Trends • Recovering slowly from recession • Aging equipment will have to be upgraded • Provides opportunities for reliable vendors to help their customers
  • 10. Education – still a problem! • Solids handling not consistently taught at university level • Most new engineers not aware of the science of solids handling • International universities involved with solids handling applications – Australia and Germany for example • Lack of familiarity with Bulletin 123
  • 11. Education  Only a few institutions teach an elective course in particle technology – Akron, Purdue, Texas A&M, CCNY, Cooper Union, Colorado, Florida  Industry needs to push for this topic to taught and seen as equal as other mechanical and chemical operations  Students need to understand the importance of the area and how they can add value by knowing about solids
  • 12. Research • Fundamental research in bulk solids handling still lacking in the USA • Research tends to focus on the “new” ideas – making and using nanoparticles for example. • Recent AIChE Plenary Session underscored the industrial need for particle technology expertise in both research and manufacturing
  • 14. Computational Tools • Considerable progress in the last decade for a variety of computational tools – DEM, DEM/CFD, Solids Flowsheeting tools • Allow examination of geometries not solved analytically • Combination of computer science and engineering science will only make these tools better • Validation essential!!!!
  • 15.
  • 16. Pneumatic Conveying  Still a lot more work to do in dense phase to move from empirical approach to more fundamental approach  Is there a way to correlate pickup velocity or line pressure drop to flow properties?  Helpful values are: particle density, particle size distribution and shape
  • 17. Retrofits vs. New Equipment • More companies fixing existing equipment • May be more practical to replace with new equipment • Requires knowledge of solids handling and a practical approach
  • 18. Biomass Handling • Alternative and renewable energy critical • Wood pellets or chips for heat • Soy, animal fats for biofuels • Sugarcane, corn starch, switchgrass, bamboo, palm • Agricultural and municipal waste • Estimated at 146 billion tons/yr used Most folks forget about the “messy front end” of biomass and grossly underestimate the complexities of the situation.
  • 19. A Better Understanding of flow Promoting Devices • Need much more understand of the transmission of pressure and vibrational waves in bulk solid as function of solids properties • Vibration  Vibrators, bin dischargers, etc • Aeration  Aeration nozzles, air blasters
  • 20. Segregation Problems  Segregation problems are common  Several mechanisms that cause it  Excellent work done by Lueptow at Northwestern and McCarthy at Pitt beginning to shed fundamental light on the problem
  • 21. Northwestern Work Stratified Segregated Mixed W = 69 cm Q = 1 cm3/s Q = 24 cm3/s Q = 420 cm3/s q = Q/T vr Large Particles Small Particles Mixed ParticlesStratified
  • 22. Rathole Calculations  Rathole calculations are too conservative  Jenike found conservative approach necessary  An approach to determine stresses acting on solids in funnel flow is required
  • 23. Ratholing “Dead” or non- flowing region Very simple question: how big should the hole be to prevent the formation of a stable rathole? • Approaches thus far • Jenike ff=1.7 • Johanson, JR, effective head approach • Arnold and Roberts, average the above • Schwedes •So what do we do? • experienced practitioners know what bound to choose • consider the economic consequence of a 6 ft outlet size
  • 24. Testing Flaky Materials  How to test elastic or flaky products  These materials do not shear well  Shear cells too small for large particle flakes
  • 25. Silo Quaking Issues  Flow of certain materials cause serious vibrations  Typically occurs with incompressible materials  Some possible solutions
  • 26. Final Thoughts  Still lots of good problems to address  Will need academic/industrial collaboration  Venues like this powder show are a necessity
  • 27. Find Joe’s Powder Perspectives column online at: http://www.powderbulksolids.com/powder-perspectives