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Pan Xu

Researcher at Southeast University

Publications -  14
Citations -  118

Pan Xu is an academic researcher from Southeast University. The author has contributed to research in topics: Pulverized coal-fired boiler & Pressure drop. The author has an hindex of 6, co-authored 14 publications receiving 96 citations.

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Investigation on characterization of powder flowability using different testing methods

TL;DR: In this article, the powder flowability of pulverized coal and glass bead powders was characterized by using different testing methods, including fluidization test, packing properties test, AOR test and shear test, which correspond to different stress levels of the powders, from the highly dispersed state in fluidized beds to the highly consolidated state in shear testers.
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Investigation on Dynamic Calibration for an Optical-Fiber Solids Concentration Probe in Gas-Solid Two-Phase Flows

TL;DR: The results show that the output voltage has a tendency to increase with the decreasing particle size, and the effect of particle color on calibration result is more predominant than that of sphericity.
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Investigation of influence of coal properties on dense-phase pneumatic conveying at high pressure

TL;DR: In this paper, the effects of coal type, particle size and moisture content on flow characteristics were investigated using the Jenike shear test and scanning electron microscopy (SEM) to provide a better understanding of effects of the material properties on flow properties.
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Effect of moisture content on conveying characteristics of pulverized coal for pressurized entrained flow gasification

TL;DR: In this article, the influence of moisture content on conveying characteristics in an experimental test facility with the conveying pressure up to 4MPa was investigated, and the experiments included soft coal and lignite with similar density and particle size.
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Resistance Properties of a Bend in Dense-Phase Pneumatic Conveying of Pulverized Coal under High Pressure

TL;DR: In this article, the effects of three representative operating parameters (solids-to-gas mass flow ratio, conveying pressure, mean particle size) on the total pressure drop were examined.