Rheology of powders and nanopowders through the use of a Couette four-bladed vane rheometer: flowability, cohesion energy, agglomerates and dustiness
Source abstract
Abstract
A new four-vane powder rheometer is proposed to study powder and nanopowder rheology at low and high shear rates. As shear rates increase, the powder flow will evolve from a Newtonian regime (low shear rates) to a Coulombic regime (moderate shear rates) and then to a kinetic regime (high shearrates) at which the powder may become self-fluidized because of intense particles collisions. Viscosity measurements of non cohesive glass beads at low shear rates (Coulombic regime) do not strongly depend upon the particle size and can reach values much larger than commonly used viscosities in CFDs models. Since, in the kinetic regime, the shear stress is a strong function of the particle size, agglomerate particle size of cohesive powders can be directly inferred from rheograms. Cohesive carbon black and silica nanopowders have been tested and compared to non-cohesive glass beads microparticles, chosen as reference. For non-cohesive glass bead micropowders, the "agglomerate" diameter average values found from rheological measurements are of the same order of magnitude as the primary diameters of the powder. This indicates that the kinetic theory of granular flows describes well these high shear-rate regimes and that such theory can be used to estimate agglomerate diameters. It is also found that estimated agglomerate sizes of nanometric cohesive materials can reach sizes of hundred micrometers depending upon their cohesion strength. Such agglomerate size measurements have been corroborated with those made by microscopy.
Source: openaire · Quality: candidate unverified · Source record ↗
Research context
OpenAlex topics: Granular flow and fluidized beds · Particle Dynamics in Fluid Flows · Rheology and Fluid Dynamics Studies
SciVX discovery tags are terminology-based. OpenAlex topics are source-provided classifications.
References (34)
Show source-provided references
1. 2011/696/EU (2011) RECOMMENDATIONS COMMISSION RECOMMENDATION of 18 October 2011 on the definition of nanomaterial (Text with EEA relevance). Off J Eur Union L 275/238
2. Abbott M (1966) An introduction to the method of characteristics. American Elsevier, New york
3. Andreotti B, Forterre Y, Pouliquen O (2011) Les milieux granulaires: entre fluide et solide. EDP Sciences
4. Bakhtiyarov SI, Overfelt RA, Reddy S (1996) Study of the apparent viscosity of fluidized sand. In: Siginer DAA, Advani SG (eds) 1996. Proceedings in Rheology and Fluid Mechanics of Nonlinear Materials. ASME International Mechanical Engineering Congress, New York, United Engineering Center, pp 243–24910.1115/IMECE1996-0248 ↗
5. Barnes HA, Nguyen QD (2001) Rotating vane rheometry—a review. J Non Newton Fluid Mech 98(1):1–1410.1016/S0377-0257(01)00095-7 ↗
6. Barois-Cazenave A, Marchal P, Falk V, Choplin L (1999) Experimental study of powder rheological behaviour. Powder Technol 103(1):58–6410.1016/S0032-5910(99)00013-3 ↗
7. Bouillard JX, Gidaspow D (1991) On the origin of bubbles and Geldart’s classification. Powder Technol 68(1):13–2210.1016/0032-5910(91)80059-R ↗
8. Bouillard JX, Lyczkowski RW, Gidaspow D (1989) Porosity distribution in a fluidized bed with an immersed obstacle. AIChE 35:908–97210.1002/aic.690350604 ↗
9. Bouillard J, Vignes A, Dufaud O, Perrin L, Thomas D (2010) Ignition and explosion risks of nanopowders. J Hazard Mater 181(1–3):873–88010.1016/j.jhazmat.2010.05.094 ↗
10. Bruni G, Colafigli A, Lettieri P, Elson T (2005) Torque measurements in aerated powders using a mechanically stirred fluidized bed rheometer (msFBR). Chem Eng Res Des 83(11):1311–131810.1205/cherd.05092 ↗
11. Bruni G, Barletta D, Poletto M, Lettieri P (2007) A rheological model for the flowability of aerated fine powders. Chem Eng Sci 62:397–40710.1016/j.ces.2006.08.060 ↗
12. Daniel RC, Poloski AP, Sáez AE (2008) Vane rheology of cohesionless glass beads. Powder Technol 181(3):237–24810.1016/j.powtec.2007.05.003 ↗
13. ECHA (2012a) Guidance on Information requirements and chemical safety assessment—Appendix R8-15: recommendations for nanomaterials applicable to chapter R8 Characterisation of dose (concentration) response for human health
14. ECHA (2012b) Guidance on information requirements and chemical safety assessment: Appendix R14-4: recommendations for nanomaterials applicable to chapter R.14: Occupational Exposure estimation
15. Geldart D (1973) Types of gas fluidization. Powder Technol 7:285–29210.1016/0032-5910(73)80037-3 ↗
16. Gidaspow D (1994) Multiphase flow and fluidization: continuum and kinetic theory descriptions. Academic Press, New York
17. Heirman G, Hendrickx R, Vandewalle L, Van Gemert D, Feys D, De Schutter G, Desmet B, Vantomme J (2009) Integration approach of the Couette inverse problem of powder type self-compacting concrete in a wide-gap concentric cylinder rheometer: Part II. Influence of mineral additions and chemical admixtures on the shear thickening flow behaviour. Cem Concr Res 39(3):171–18110.1016/j.cemconres.2008.12.006 ↗
18. Henry F (2013) Dynamique des systèmes nanodispersés: application au cas de l’agglomération des nanoparticules. Thesis in Chemical Engineering, Institut Polytechnique de Loraine, France, Nancy
19. Henry F, Bouillard J, Marchal P, Vignes A, Dufaud O, Perrin L (2013) Exploring a new method to study the agglomeration of powders: application to nanopowders. Powder Technol 250:13–20. doi: 10.1016/j.powtec.2013.08.01010.1016/j.powtec.2013.08.010 ↗
20. ISO/TS-27687 (2008) International standards organization, nanotechnologies—terminology and definitions for nano-objects: nanoparticle, nanofibre and nanoplate
21. Jenike AW (1987) A theory of flow of particulate solids in converging and diverging channels based on a conical yield function. Powder Technol 50(3):229–236. doi: 10.1016/0032-5910(87)80068-210.1016/0032-5910(87)80068-2 ↗
22. Johanson JR (1964) Stress and velocity fields in the gravity flow of bulk solids. J Appl Mech 31(3):499–506. doi: 10.1115/1.36296610.1115/1.3629668 ↗
23. Linsinger TR, Guilland D, Calzolai L, Rossi F, Gibson N, Klein C (2012) JRC reference report: requirement on measurements for the implementation of the European Commission definition on the term “Nanomaterial”. Institute o = for reference materials and measurements
24. Lochmann KOL, Stoyan D (2006) Statistical analysis of random sphere packings with variable radius distribution. Solid States Sci 8:1397–141310.1016/j.solidstatesciences.2006.07.011 ↗
25. Lun CKK, Savage SB, Jeffrey DJ, Chepurnity N (1984) Kinetic theory for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flow field. J Fluid Mech 140:223–23510.1017/S0022112084000586 ↗
26. Makkawi YW, Ocone R (2004) Comparative analysis of experimental and modelling of gas-solid flow hydrodynamics: effect of friction and interparticle cohesion forces. In: AICHE Proceedings, 2004
27. Marchal PCL (2004) Eléments de physique statistique appliqués à la rhéologie des milieu granulaires non cohésifs: le modèle du château de sables mouvants. Rhéologie 5:10–26
28. Marchal PSN, Choplin L (2009) Rheology of dense-phase vibrated powders and molecular analogies. J Rheol 53:1–2910.1122/1.3037266 ↗
29. Marchal PC, Choplin L, Smirani N (2005) System and method for rheological characterization of granular materials. USA Patent
30. Mewis J, Wagner NJ (2012) Colloidal suspension rheology. Cambridge University Press, Cambridge
31. REACH (2006) REGULATION (EC) No 1907/2006 OF THE EUROPEAN PARLIAMENT AND OF THE COUNCIL of 18 December 2006 concerning the Registration, Evaluation, Authorisation and Restriction of Chemicals (REACH), establishing a European Chemicals Agency, amending Directive 1999/45/EC and repealing Council Regulation (EEC) No 793/93 and Commission Regulation (EC) No 1488/94 as well as Council Directive 76/769/EEC and Commission Directives 91/155/EEC, 93/67/EEC, 93/105/EC and 2000/21/EC
32. Savage SB, Jeffrey DJ (1981) The stress tensor in a granular flow at high shear rates. J Fluid Mech 110:255–27210.1017/S0022112081000736 ↗
33. Sokolovskii SB (1965) Statitics of granular media. Pergamon Press, Oxford, UK
34. Tsardaka KDJER (1993) Apparent viscosity of particulate solids determined using creep analysis. Powder Technol 76:221–22410.1016/S0032-5910(05)80030-0 ↗