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Journal articles on the topic 'Rheology of suspensions'

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Published: 4 June 2021
Last updated: 13 February 2022

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1

WATANABE, Hiroshi. "Rheology of Suspensions." Journal of the Japan Society of Colour Material 70, no. 7 (1997): 468–75. http://dx.doi.org/10.4011/shikizai1937.70.468.

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2

Kerekes, Richard J. "Rheology of suspensions." Nordic Pulp & Paper Research Journal 21, no. 5 (December 1, 2006): 598–612. http://dx.doi.org/10.3183/npprj-2006-21-05-p598-612.

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3

Bustamante Rúa, Moisés Oswaldo, Nestor Ricardo Rojas Reyes, and Gali Ronel Quitian Chila. "Fine material effect on kaolin suspensions rheology." DYNA 83, no. 195 (February 23, 2016): 105–11. http://dx.doi.org/10.15446/dyna.v83n195.48855.

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A good rheological characterization can be used as a control parameter within the industrial processing of kaolin. The kaolin used was characterized by SEM, XRD, XRF and particle size. Also it was classified and separated in three sizes of fine material, which was introduced in suspensions with three different size distributions. The analysis was based on a rheological study of the fine particles influence, on the suspension viscosity. The results show that it is possible to modify the viscosity by altering the fines content without changing the solid fraction of the suspension. Suspensions of kaolin with 40% content of fines tend to decrease its viscosity value. Suspensions with quantities of fine greater than 60 %, increase the value of its viscosity. In the research are also presented the proposed mechanisms by which the presence of fine increases or decreases the value of the viscosity of a suspension.
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4

Butler, Jason E. "Suspension dynamics: moving beyond steady." Journal of Fluid Mechanics 752 (July 4, 2014): 1–4. http://dx.doi.org/10.1017/jfm.2014.278.

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AbstractThe dynamics of flowing, concentrated suspensions of non-colloidal particles continues to surprise, despite decades of work and the widespread importance of suspension transport properties to industrial processes and natural phenomena. Blanc, Lemaire & Peters (J. Fluid Mech., 2014, vol. 746, R4) report a striking example. They probed the time-dependent dynamics of concentrated suspensions of rigid and neutrally buoyant spheres by simultaneously measuring the oscillatory rheology and the sedimentation rate of a falling ball. The sedimentation velocity of the ball through the suspension depends strongly on the frequency of oscillation, though the rheology was found to be independent of frequency. The results demonstrate the complexities of suspension flows and highlight opportunities for improving models by exploring suspension dynamics and rheology over a wide range of conditions, beyond steady and unidirectional ones.
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5

Savarmand, Saeid, Mohammad-Reza Golkar-Narenji, and Kourosh Saedi. "Rheology of Glaze Suspensions." Canadian Journal of Chemical Engineering 81, no. 5 (May 19, 2008): 1062–66. http://dx.doi.org/10.1002/cjce.5450810518.

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6

Sung, Sang Hoon, Sunhyung Kim, Jeong Hoon Park, Jun Dong Park, and Kyung Hyun Ahn. "Role of PVDF in Rheology and Microstructure of NCM Cathode Slurries for Lithium-Ion Battery." Materials 13, no. 20 (October 13, 2020): 4544. http://dx.doi.org/10.3390/ma13204544.

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A binder plays a critical role in dispersion of coating liquids and the quality of coating. Poly(vinylidene fluoride) (PVDF) is widely used as a binder in cathode slurries; however, its role as a binder is still under debate. In this paper, we study the role of PVDF on the rheology of cathode battery slurries consisting of Li(Ni1/3Mn1/3Co1/3)O2 (NCM), carbon black (CB) and N-methyl-2-pyrrolidone (NMP). Rheology and microstructure of cathode slurries are systemically investigated with three model suspensions: CB/PVDF/NMP, NCM/PVDF/NMP and NCM/CB/PVDF/NMP. To highlight the role of PVDF in cathode slurries, we prepare the same model suspensions by replacing PVDF with PVP, and we compare the role of PVDF to PVP in the suspension rheology. We find that PVDF adsorbs neither onto NCM nor CB surface, which can be attributed to its poor affinity to NCM and CB. Rheological measurements suggest that PVDF mainly increases matrix viscosity in the suspension without affecting the microstructure formed by CB and NCM particles. In contrast to PVDF, PVP stabilizes the structure of CB and NCM in the model suspensions, as it is adsorbed on the CB surface. This study will provide a useful insight to fundamentally understand the rheology of cathode slurries.
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7

Puisto, Antti, Xavier Illa, Mikael Mohtaschemi, and Mikko Alava. "Modeling the rheology of nanocellulose suspensions." Nordic Pulp & Paper Research Journal 27, no. 2 (May 1, 2012): 277–81. http://dx.doi.org/10.3183/npprj-2012-27-02-p277-281.

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Abstract The transient response of a Population Balance based colloidal rheology model is studied in the context of nanofiber suspension rheology research. The model is calibrated against experimental rheology data for cellulose nano-whisker suspension and then subjected to transient shears. The non-equilibrium aggregate size distributions are reported.
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8

Chui, Jane Y. Y., Carine Douarche, Harold Auradou, and Ruben Juanes. "Rheology of bacterial superfluids in viscous environments." Soft Matter 17, no. 29 (2021): 7004–13. http://dx.doi.org/10.1039/d1sm00243k.

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Dense suspensions of pusher-type bacteria give rise to 'superfluids' in which the effective viscosity of the suspension is drastically reduced through collective motion, and in this study we investigate how a viscous environment affects this behavior.
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9

Tarchitzky, J., and Y. Chen. "Rheology of Sodium-montmorillonite suspensions." Soil Science Society of America Journal 66, no. 2 (2002): 406. http://dx.doi.org/10.2136/sssaj2002.0406.

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10

Tarchitzky, J., and Y. Chen. "Rheology of Sodium-montmorillonite suspensions." Soil Science Society of America Journal 66, no. 2 (March 2002): 406–12. http://dx.doi.org/10.2136/sssaj2002.4060.

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11

OTSUBO, Yasufumi. "Rheology Control of Colloidal Suspensions." Journal of the Society of Powder Technology, Japan 33, no. 12 (1996): 919–24. http://dx.doi.org/10.4164/sptj.33.919.

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12

Petrie, Christopher J. S. "The rheology of fibre suspensions." Journal of Non-Newtonian Fluid Mechanics 87, no. 2-3 (November 1999): 369–402. http://dx.doi.org/10.1016/s0377-0257(99)00069-5.

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13

Goodwin, James W., and Paul A. Reynolds. "The rheology of flocculated suspensions." Current Opinion in Colloid & Interface Science 3, no. 4 (August 1998): 401–7. http://dx.doi.org/10.1016/s1359-0294(98)80056-3.

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14

KLEIN, BERNHARD, SUSAN J. PARTRIDGE, and JANUSZ S. LASKOWSKI. "Rheology of Unstable Mineral Suspensions." Coal Preparation 8, no. 3-4 (January 1990): 123–34. http://dx.doi.org/10.1080/07349349008905180.

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15

Bossis, G., and J. F. Brady. "The rheology of Brownian suspensions." Journal of Chemical Physics 91, no. 3 (August 1989): 1866–74. http://dx.doi.org/10.1063/1.457091.

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16

Kiesgen de Richter, Sebastien, Caroline Hanotin, Naima Gaudel, Nicolas Louvet, Philippe Marchal, and Mathieu Jenny. "Rheology of vibrated granular suspensions." EPJ Web of Conferences 140 (2017): 09028. http://dx.doi.org/10.1051/epjconf/201714009028.

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17

SIDHU, B. K., C. WASHINGTON, S. S. DAVIS, and T. S. PUREWAL. "Rheology of Model Aerosol Suspensions." Journal of Pharmacy and Pharmacology 45, no. 7 (July 1993): 597–600. http://dx.doi.org/10.1111/j.2042-7158.1993.tb05659.x.

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18

Kang, Sang-Yoon, Ashok S. Sangani, Heng-Kwong Tsao, and Donald L. Koch. "Rheology of dense bubble suspensions." Physics of Fluids 9, no. 6 (June 1997): 1540–61. http://dx.doi.org/10.1063/1.869481.

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19

Denn, Morton M., and Jeffrey F. Morris. "Rheology of Non-Brownian Suspensions." Annual Review of Chemical and Biomolecular Engineering 5, no. 1 (June 7, 2014): 203–28. http://dx.doi.org/10.1146/annurev-chembioeng-060713-040221.

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20

Klein, B., and M. Pawlik. "Rheology modifiers for mineral suspensions." Mining, Metallurgy & Exploration 22, no. 2 (May 2005): 83–88. http://dx.doi.org/10.1007/bf03403119.

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21

Boudhani, Hassane, René Fulchiron, and Philippe Cassagnau. "Rheology of physically evolving suspensions." Rheologica Acta 48, no. 2 (September 11, 2008): 135–49. http://dx.doi.org/10.1007/s00397-008-0304-1.

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22

Truby, J. M., S. P. Mueller, E. W. Llewellin, and H. M. Mader. "The rheology of three-phase suspensions at low bubble capillary number." Proceedings of the Royal Society A: Mathematical, Physical and Engineering Sciences 471, no. 2173 (January 2015): 20140557. http://dx.doi.org/10.1098/rspa.2014.0557.

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We develop a model for the rheology of a three-phase suspension of bubbles and particles in a Newtonian liquid undergoing steady flow. We adopt an ‘effective-medium’ approach in which the bubbly liquid is treated as a continuous medium which suspends the particles. The resulting three-phase model combines separate two-phase models for bubble suspension rheology and particle suspension rheology, which are taken from the literature. The model is validated against new experimental data for three-phase suspensions of bubbles and spherical particles, collected in the low bubble capillary number regime. Good agreement is found across the experimental range of particle volume fraction ( 0 ≤ ϕ p ≲ 0.5 ) and bubble volume fraction ( 0 ≤ ϕ b ≲ 0.3 ). Consistent with model predictions, experimental results demonstrate that adding bubbles to a dilute particle suspension at low capillarity increases its viscosity, while adding bubbles to a concentrated particle suspension decreases its viscosity. The model accounts for particle anisometry and is easily extended to account for variable capillarity, but has not been experimentally validated for these cases.
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23

Papadopoulou, Anastasia, Jurriaan J. J. Gillissen, Manish K. Tiwari, and Stavroula Balabani. "Effect of Particle Specific Surface Area on the Rheology of Non-Brownian Silica Suspensions." Materials 13, no. 20 (October 16, 2020): 4628. http://dx.doi.org/10.3390/ma13204628.

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Industrial formulations very often involve particles with a broad range of surface characteristics and size distributions. Particle surface asperities (roughness) and porosity increase particle specific surface area and significantly alter suspension rheology, which can be detrimental to the quality of the end product. We examine the rheological properties of two types of non-Brownian, commercial precipitated silicas, with varying specific surface area, namely PS52 and PS226, suspended in a non-aqueous solvent, glycerol, and compare them against those of glass sphere suspensions (GS2) with a similar size distribution. A non-monotonic effect of the specific surface area (S) on suspension rheology is observed, whereby PS52 particles in glycerol are found to exhibit strong shear thinning response, whereas such response is suppressed for glass sphere and PS226 particle suspensions. This behaviour is attributed to the competing mechanisms of particle–particle and particle–solvent interactions. In particular, increasing the specific surface area beyond a certain value results in the repulsive interparticle hydration forces (solvation forces) induced by glycerol overcoming particle frictional contacts and suppressing shear thinning; this is evidenced by the response of the highest specific surface area particles PS226. The study demonstrates the potential of using particle specific surface area as a means to tune the rheology of non-Brownian silica particle suspensions.
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24

Turpeinen, Tuomas, Ari Jäsberg, Sanna Haavisto, Johanna Liukkonen, Juha Salmela, and Antti I. Koponen. "Pipe rheology of microfibrillated cellulose suspensions." Cellulose 27, no. 1 (October 19, 2019): 141–56. http://dx.doi.org/10.1007/s10570-019-02784-4.

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Abstract The shear rheology of two mechanically manufactured microfibrillated cellulose (MFC) suspensions was studied in a consistency range of 0.2–2.0% with a pipe rheometer combined with ultrasound velocity profiling. The MFC suspensions behaved at all consistencies as shear thinning power law fluids. Despite their significantly different particle size, the viscous behavior of the suspensions was quantitatively similar. For both suspensions, the dependence of yield stress and the consistency index on consistency was a power law with an exponent of 2.4, similar to some pulp suspensions. The dependence of flow index on consistency was also a power law, with an exponent of − 0.36. The slip flow was very strong for both MFCs and contributed up to 95% to the flow rate. When wall shear stress exceeded two times the yield stress, slip flow caused drag reduction with consistencies higher than 0.8%. When inspecting the slip velocities of both suspensions as a function of wall shear stress scaled with the yield stress, a good data collapse was obtained. The observed similarities in the shear rheology of both the MFC suspensions and the similar behavior of some pulp fiber suspensions suggests that the shear rheology of MFC suspensions might be more universal than has previously been realized.
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25

Bozdogan, Ihsan, Muserref Onal, Abdullah Devrim Pekdemir, and Yuksel Sarikaya. "Thermodynamic Interpretation on the Rheology of Aqueous Bentonite Suspensions." Revista de Chimie 71, no. 6 (July 1, 2020): 51–58. http://dx.doi.org/10.37358/rc.20.6.8169.

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Since their exceptional rheological behavior, bentonite suspensions are widely used in engineering, industrial, agricultural, and drilling applications. So, the aim of the present study is to investigate the rheological properties of three types aqueous suspensions prepared with calcium bentonite (CaB), sodium bentonite (NaB) obtained from that by Na2CO3 activation, and NaB with the excess soda. The CaB taken from Giresun/Turkey region contains calcium smectite (CaxS) as clay mineral and opal CT (SiO2.nH2O) as impurity which is paracrystalline silica. Soda content by the activation and bentonite content in the suspension were changed in the interval of 2.5-15.0% and 5-20% by mass, respectively. CaxS completely converted to sodium smectite (Na2xS) by the activation with the soda content of 2.5% and then Na2xS+Na2CO3 mixtures formed. Rheological properties of these aqueous suspensions were measured using a Fann Viscometer. These properties reached their maxima by the most thixotropic Na2xS suspensions and greatly increased with the increasing of smectite content. Rheological plots drawn of the shear rate vs. shear stress in the interval of 170-1020 s-1 showed that the suspensions flow as a Bingham Plastic. Change in rheological properties depending on the smectite type and content as well as excess soda content was explained thermodynamically based on the chemical potential gradient between interlayer and dispenser waters.
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26

Mueller, S., E. W. Llewellin, and H. M. Mader. "The rheology of suspensions of solid particles." Proceedings of the Royal Society A: Mathematical, Physical and Engineering Sciences 466, no. 2116 (December 16, 2009): 1201–28. http://dx.doi.org/10.1098/rspa.2009.0445.

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We present data for the rheology of suspensions of monodisperse particles of varying aspect ratio, from oblate to prolate, and covering particle volume fractions ϕ from dilute to highly concentrated. Rheology is characterized by fitting the experimental data to the model of Herschel & Bulkley (Herschel & Bulkley 1926 Kolloid Z. 39 , 291–300 ( doi:10.1007/BF01432034 )) yielding three rheometric parameters: consistency K (cognate with viscosity); flow index n (a measure of shear-thinning); yield stress τ 0 . The consistency K of suspensions of particles of arbitrary aspect ratio can be accurately predicted by the model of Maron & Pierce (Maron & Pierce 1956 J. Colloid Sci. 11 , 80–95 ( doi:10.1016/0095-8522(56)90023-X )) with the maximum packing fraction ϕ m as the only fitted parameter. We derive empirical relationships for ϕ m and n as a function of average particle aspect ratio r p and for τ 0 as a function of ϕ m and a fitting parameter τ *. These relationships can be used to predict the rheology of suspensions of prolate particles from measured ϕ and r p . By recasting our data in terms of the Einstein coefficient, we relate our rheological observations to the underlying particle motions via Jeffery’s (Jeffery 1922 Proc. R. Soc. Lond. A 102 , 161–179 ( doi:10.1098/rspa.1922.0078 )) theory. We extend Jeffery’s work to calculate, numerically, the Einstein coefficient for a suspension of many, initially randomly oriented particles. This provides a physical, microstructural explanation of our observations, including transient oscillations seen during run start-up and changes of rheological regime as ϕ increases.
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27

Hubbe, Martin A. "When defects dominate: Rheology of nanofibrillated cellulose suspensions." BioResources 16, no. 1 (November 1, 2020): 16–18. http://dx.doi.org/10.15376/biores.16.1.16-18.

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Conventional rheological tests can be difficult to carry out in the case of suspensions of nanofibrillated cellulose (NFC). Such suspensions tend to migrate away from the walls of a rheometer device, leaving a low-viscosity layer. The very high aspect ratio of typical nanofibrillated cellulose particles favors formation of tangled clusters. But application of hydrodynamic shear can cause fragmentation of those clusters. It is proposed in this essay that some focus be placed on the fragments of entangled clusters of NFC and interactions between them at their fractured surfaces. The condition of near-uniform, defect-free structures of nanocellulose spanning the volume within a sheared suspension might be regarded as an unlikely circumstance. Isaac Newton started with a very simple equation to start to understand rheology. It is proposed that a similarly bold and simplified approach may be needed to account for the effects of broken entangled clusters of NFC on flow phenomena, their assessment, and their consequences related to industrial processes.
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28

Tuntarawongsa, Sarun, and Thawatchai Phaechamud. "Homogenization and Melt-Emulsification Techniques for Ibuprofen Particle Size Reduction: Effect of Tween 80 & Sonication." Applied Mechanics and Materials 229-231 (November 2012): 179–82. http://dx.doi.org/10.4028/www.scientific.net/amm.229-231.179.

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Ibuprofen suspensions were prepared by simple homogenization with melt-emulsification process. Tween 80 was used as stabilizer. The homogenized suspensions were evaluated and compared with melt emulsificated suspension. The pH value and rheology behavior were not difference. The viscosity was very low. Zeta potential was -10 to -25 mV. In this study, the suitable process to minimize particle size of ibuprofen suspension was melt emulsification follow by sonication. This process could be developed to obtain nanosuspension by adjust sonication process and improved formulation to obtain suitable nanosuspension.
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29

Hirose, Yuji. "Electrorheological Behavior of Suspensions between Pattern Electrodes with Fine Projections." Nihon Reoroji Gakkaishi 43, no. 3_4 (2015): 113–17. http://dx.doi.org/10.1678/rheology.43.113.

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30

Yamamoto, Takehiro, Shinpei Hirota, and Takuya Fujiwara. "A Stochastic Rotation Dynamics Model for Dilute Spheroidal Colloid Suspensions." Nihon Reoroji Gakkaishi 44, no. 3 (2016): 185–88. http://dx.doi.org/10.1678/rheology.44.185.

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31

Hinch, E. J. "The measurement of suspension rheology." Journal of Fluid Mechanics 686 (October 24, 2011): 1–4. http://dx.doi.org/10.1017/jfm.2011.350.

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AbstractIn the following featured article, Boyer, Pouliquen & Guazzelli (J. Fluid Mech., this issue, vol. 686, 2011, pp 5–25) measure the normal stresses in a suspension of non-colloidal rigid spheres. They use the classical rod-climbing experiment, except that for interesting reasons the free surface near to the rotating rod does not rise but dips down. Careful techniques reveal that the normal stresses occur only above a volume concentration of 22 %. Over a period of hours the measurements drift, typical of many observations of suspensions. This is due to particles slowly migrating away from the rotating rod. A model of the migration gives good predictions of the observed changes.
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32

Shih, Wei-Heng, and Leh-Lii Pwu. "Rheology of aqueous boehmite-coated silicon nitride suspensions and gels." Journal of Materials Research 10, no. 11 (November 1995): 2808–16. http://dx.doi.org/10.1557/jmr.1995.2808.

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The rheological properties of boehmite-coated silicon nitride aqueous suspensions and gels are reported. In unidirectional rheological tests, it was found that the boehmite coating reduces the viscosity of the suspensions over a wide range of shear rates and volume fractions of particles. The suspension shear stress as a function of shear rate can be described by the Bingham model, and the Bingham yield stresses of boehmite-coated silicon nitride suspensions are lower than those of the uncoated suspensions. The reduction in the viscosity and the Bingham yield stress is attributed to a shallower secondary minimum in the Derjaguin-Landau-Verwey-Overbeek (DLVO) potential between coated particles than that for uncoated silicon nitride particles. Moreover, at low values of pH, the coated silicon nitride suspensions gelled over time, and the viscoelastic behavior of the gels was studied by dynamic oscillatory tests. It was found that the shear modulus (G′) and loss modulus (G″) remain constant up to a certain strain amplitude, γ°, beyond which G′ and G″ begin to vary. The value of G′ in the linear region increases exponentially, whereas γ° decreases exponentially with the volume fraction of coated silicon nitride particles. The exponential behavior of the shear modulus G′ of the gels is similar to the exponential pressure-density relationship found in the previous pressure filtration study, indicating that particulate rearrangement occurs as volume fraction of particles is increased.
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33

Keren, R. "Rheology of Mixed Kaolinite-Montmorillonite Suspensions." Soil Science Society of America Journal 53, no. 3 (May 1989): 725–30. http://dx.doi.org/10.2136/sssaj1989.03615995005300030014x.

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34

Burgos, Gilmer R., Andreas N. Alexandrou, and Vladimir Entov. "Thixotropic rheology of semisolid metal suspensions." Journal of Materials Processing Technology 110, no. 2 (March 2001): 164–76. http://dx.doi.org/10.1016/s0924-0136(00)00731-7.

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35

Talou, M. H., M. A. Villar, M. A. Camerucci, and R. Moreno. "Rheology of aqueous mullite–starch suspensions." Journal of the European Ceramic Society 31, no. 9 (August 2011): 1563–71. http://dx.doi.org/10.1016/j.jeurceramsoc.2011.03.031.

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36

Frith, W. J., J. Mewis, and T. A. Strivens. "Rheology of concentrated suspensions: experimental investigations." Powder Technology 51, no. 1 (June 1987): 27–34. http://dx.doi.org/10.1016/0032-5910(87)80037-2.

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37

Večeř, M., and J. Pospíšil. "Stability and Rheology of Aqueous Suspensions." Procedia Engineering 42 (2012): 1720–25. http://dx.doi.org/10.1016/j.proeng.2012.07.564.

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38

Grigelmo-Miguel, N., A. Ibarz-Ribas, and O. Martı́n-Belloso. "Rheology of peach dietary fibre suspensions." Journal of Food Engineering 39, no. 1 (January 1999): 91–99. http://dx.doi.org/10.1016/s0260-8774(98)00151-4.

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39

Rajaiah, Jayanth, Eli Ruckenstein, Graham F. Andrews, Eric O. Forster, and Rakesh K. Gupta. "Rheology of Sterically Stabilized Ceramic Suspensions." Industrial & Engineering Chemistry Research 33, no. 10 (October 1994): 2336–40. http://dx.doi.org/10.1021/ie00034a012.

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40

Metzner, A. B. "Rheology of Suspensions in Polymeric Liquids." Journal of Rheology 29, no. 6 (December 1985): 739–75. http://dx.doi.org/10.1122/1.549808.

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41

Nicodemi, M., M. P. Ciamarra, and A. Coniglio. "Rheology of sheared monodisperse granular suspensions." European Physical Journal Special Topics 179, no. 1 (December 2009): 157–63. http://dx.doi.org/10.1140/epjst/e2010-01200-9.

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42

Bossis, G., Y. Grasselli, E. Lemaire, A. Meunier, J. F. Brady, and T. Phung. "Rheology and microstructure in colloidal suspensions." Physica Scripta T49A (January 1, 1993): 89–93. http://dx.doi.org/10.1088/0031-8949/1993/t49a/015.

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43

Jenny, M., M. Ferrari, N. Gaudel, and S. Kiesgen de Richter. "Rheology of fiber suspensions using MRI." EPL (Europhysics Letters) 121, no. 3 (February 1, 2018): 34003. http://dx.doi.org/10.1209/0295-5075/121/34003.

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44

Shafiei-Sabet, Sadaf, Wadood Y. Hamad, and Savvas G. Hatzikiriakos. "Rheology of Nanocrystalline Cellulose Aqueous Suspensions." Langmuir 28, no. 49 (November 26, 2012): 17124–33. http://dx.doi.org/10.1021/la303380v.

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45

Teipel, Ulrich, and Ulrich Förter-Barth. "Rheology of Nano-Scale Aluminum Suspensions." Propellants, Explosives, Pyrotechnics 26, no. 6 (December 2001): 268. http://dx.doi.org/10.1002/1521-4087(200112)26:6<268::aid-prep268>3.0.co;2-l.

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46

Liang, Ruifeng, Long Han, Deepak Doraiswamy, and Rakesh K. Gupta. "The rheology of aramid platelet suspensions." Polymer Engineering & Science 51, no. 10 (October 2011): 1933–41. http://dx.doi.org/10.1002/pen.22013.

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47

Hobbie, E. K., and D. J. Fry. "Rheology of concentrated carbon nanotube suspensions." Journal of Chemical Physics 126, no. 12 (March 28, 2007): 124907. http://dx.doi.org/10.1063/1.2711176.

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48

Banchio, A. J., J. Bergenholtz, and G. Nägele. "Rheology and Dynamics of Colloidal Suspensions." Physical Review Letters 82, no. 8 (February 22, 1999): 1792–95. http://dx.doi.org/10.1103/physrevlett.82.1792.

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49

Mohtaschemi, Mikael, Antti Puisto, Xavier Illa, and Mikko J. Alava. "Rheology dynamics of aggregating colloidal suspensions." Soft Matter 10, no. 17 (2014): 2971. http://dx.doi.org/10.1039/c3sm53082e.

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50

Neaman, Alexander. "Rheology of Mixed Palygorskite-Montmorillonite Suspensions." Clays and Clay Minerals 48, no. 6 (2000): 713–15. http://dx.doi.org/10.1346/ccmn.2000.0480613.

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