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Dive into the research topics where R.L.C. Flemmer is active.

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Featured researches published by R.L.C. Flemmer.


Powder Technology | 1986

On the drag coefficient of a sphere

R.L.C. Flemmer; C.L. Banks

Abstract A mathematical approximation to experimental data on the drag coefficient of a sphere is presented. The approximation is compared with other approximations and shown to be significantly better both in range and in accuracy. The Newton-Raphson technique is applied to the approximation, allowing the computation of the terminal velocity from a knowledge Of C d Re 2 and of particle diameter from a knowledge of Re/C d .


Powder Technology | 1993

An experimental study on the effect of particle shape on fluidization behavior

R.L.C. Flemmer; James Pickett; Nigel N. Clark

Abstract Few correlations exist to describe the effect of particle shape on the relationship between superficial velocity and void fraction in homogeneous fluid beds. Limestone, quartz, bottom ash and pea gravel particles were fluidized with water and a data bank of void fractions and fluidizing velocities was compiled. Each particle type was image analyzed to yield average shape descriptors, namely aspect ratio, fractal dimension, polygonal harmonic persistences and delta (Pipers) angles. Regression showed that the slope of a log (superficial velocity) versus log (void fraction) plot can be fitted using a function of a shape descriptor, with the persistence of the third harmonic being the descriptor yielding the best fit.


Powder Technology | 1978

Flow rates of dry powders in inclinded rotating cylinders under open-ended discharge conditions

L.G. Austin; K. Shoji; R. Hogg; J. Carlson; R.L.C. Flemmer

Abstract A physical model is presented which describes axial flow of dry powders through inclined rotating cylinders under conditions of open-ended discharge. The model has been solved numerically for a wide range of operating conditions. The results are presented as a series of curves expressing local and cumulative fractional filling levels as a function of dimensionless position along the cylinder, mass flow rate, and cylinder inclination. Experimental verification of the model was obtained on a laboratory scale for a limited number of mass flow rates and cylinder inclinations.


Particulate Science and Technology | 1989

The effect of particle shape on fluid-particle interactions

Nigel N. Clark; Richard Turton; R.L.C. Flemmer

ABSTRACT Few correlations exist to predict the drag on non-spherical particles, although drag on spheres has been well characterized. A problem in developing predictive equations is the lack of adequate shape descriptors, although sphericity is a good descriptor for smooth nonspherical particles, such as geometric objects. Following a review of the topic, an approach to predicting drag on smooth particles is developed by modifying the Turton-Levenspiel equation for drag on a sphere, using sphericity as the shape descriptor. An alternative approach using polygonal harmonics as shape descriptors, proved less accurate.


Particulate Science and Technology | 1984

HYDRAULIC TRANSPORT OF ABRASIVE SOLIDS: THE AIR-LIFT PUMP

Nigel N. Clark; R.L.C. Flemmer; T.P. Meloy

ABSTRACT Although the air-lift pump has been superseded by submersible pumps in raising water from wells and mines, it still provides an attractive means of lifting abrasive slurries because, unlike mechanical pumps, it has no moving parts to wear. However, current design of air-lift pumps must rely on empirical equations, or, at best, incremental computer solutions. Design is complicated by the fact that relative velocities of the phases change over the whole pump length. A new design equation is developed to predict the lift of an air-lift pump, given the flowrates of air, liquid and solid in the pump, and the dimensions of the air-lift tube. The new equation is baaed on well-established multiphase flow theory, and offers significant advantages over current design techniques. In combination with an equation for the overall pump efficiency, the new equation provides a method for optimizing the design parameters for the air-lift pump.


Aiche Journal | 1985

Predicting the holdup in two‐phase bubble upflow and downflow using the Zuber and Findlay drift‐flux model

Nigel N. Clark; R.L.C. Flemmer


Aiche Journal | 1987

Turbulent circulation in bubble columns

Nigel N. Clark; Christopher M. Atkinson; R.L.C. Flemmer


Chemical Engineering Science | 1984

On vertical downward two phase flow

Nigel N. Clark; R.L.C. Flemmer


International Journal of Multiphase Flow | 1986

The effect of varying gas voidage distributions on average holdup in vertical bubble flow

Nigel N. Clark; R.L.C. Flemmer


Industrial & Engineering Chemistry Fundamentals | 1985

Two-phase pressure loss in terms of mixing length theory. 1. Derivation for the general case of dispersed flow

Nigel N. Clark; R.L.C. Flemmer

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Nigel N. Clark

West Virginia University

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L.G. Austin

Pennsylvania State University

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J. Carlson

Pennsylvania State University

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James Pickett

West Virginia University

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K. Shoji

Pennsylvania State University

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R. Hogg

Pennsylvania State University

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Richard Turton

West Virginia University

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T.P. Meloy

West Virginia University

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