End Matter

Nomenclature

latin
\(A\)	area
\(C_D\)	drag coefficient
\(d\)	diameter
\(e\)	restitution coefficient
\(g\)	gravity magnitude
\(L_i\)	length in the \(i^{th}\)-direction
\(\dot m\)	mass flow rate
\(M\)	bed mass
\(U\)	superficial (gas) velocity
\(P\)	pressure
\(Q\)	volumetric flow rate
\(R_{air}\)	specific gas constant for air
\(t\)	time
\(T\)	temperature
\(v\)	velocity
\(V\)	volume
greek
\(\mu\)	friction coefficient (particles) or material viscosity (gas)
\(\Psi\)	sphericity
subscripts and superscripts
\(atm\)	atmosphere
\(F\)	float (rotameter)
\(g\)	gas
\(lab\)	laboratory (conditions)
\(obs\)	observed (conditions)
\(p\)	particle
\(r\)	rise (through the bed)
\(std\)	standard (conditions)
\(x\), \(y\), \(z\)	coordinate direction

CFD	Computational Fluid Dynamics
DEM	Discrete Element Method
HDPE	High-Density Polyethylene
UQ	Uncertainty Quantification
VSSUQ	Very Small-Scale experiment for UQ

Hoomans, et al. (2001) Experimental validation of granular dynamics simulations of gas-fluidised beds with homogenous in-flow conditions using positron emission particle tracking, Powder Technology, 116, 166-177.
Khanam and AlMaadeed (2015) Processing and characterization of polyethylene-based composites, Advanced Manufacturing: Polymer & Composites Science, 1, 63-79.
LaMarche, et al. (2022) Very small-scale, segregating-fluidized-bed experiments: A dataset for CFD-DEM validation and uncertainty quantification, AIChE Journal, XXX, yy-yy.
Rosato, et al. (1987) Why the Brazil nuts are on top: Size segregation of particulate matter by shaking. Physical Review Letters, 58, 1038-1040.
Yuu, Umekage and Johno (2000) Numerical simulation of air and particle motions in bubbling fluidized bed of small particles, Powder Technology, 110, 158-168.

This work was supported by the U.S. Department of Energy under Grant No. DE-FE0026298.

This repository is released under the MIT License.