Boundaries of the unstable zone in horizontal slug flow pneumatic conveying

被引:0
作者
Orozovic, Ognjen [1 ]
Lavrinec, Aleksej [1 ,2 ]
机构
[1] Univ Newcastle, Sch Engn, Callaghan, NSW 2308, Australia
[2] Univ Newcastle, Ctr Bulk Solids & Particulate Technol, Callaghan, NSW 2308, Australia
关键词
Pneumatic conveying; Dense phase; Slug flow; Unstable zone; Pressure; SALTATION VELOCITIES; SIMULATION; BEHAVIOR; POROSITY; MINIMUM;
D O I
10.1016/j.ces.2025.121543
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Among many modes of flow within pneumatic conveying, slug flow is usually preferred when pipe wear, particle attrition and gas use are constraining factors. However, the operating space of slug flow is bounded by blockage and the so called Unstable Zone. The latter is often less problematic, but it still leads to highly undesirable conditions where extreme pressure fluctuations may damage conveying equipment. These pressure fluctuations are a result of the system alternating between strand flow and unusually long slugs, however, the exact mechanism is poorly understood. This paper provides a theoretical basis for the physics underpinning the emergence and properties of the Unstable Zone in horizontal slug flow. It is shown that the Unstable Zone emerges from a combination of steady flow transitions not being possible due to formation of stationary layers, high stationary layers forming due to saltation, high particle velocities from high superficial gas velocities, and a single dominant slug forming based on gas conservation. The latter allows simplified single slug analysis to be applied and a theoretical upper bound on horizontal slug lengths in the Unstable Zone is derived based on assuming slugs form at the maximum saltation layer fraction. Comparisons with experimental pressure data validates the developed theory and future work is identified to further reduce the upper bound predicted within. Overall, via a novel model predicting both the emergence and properties of the Unstable Zone in horizontal slug flow, this work provides significant progress towards more reliable dense phase design.
引用
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页数:12
相关论文
共 45 条
[1]  
Agarwal A T., 2005, Powder HandlingProcessing, V17, P18
[2]   Application of nonlinear dynamics analysis to gas-solid flow system in horizontal pneumatic conveying of plastic pellets [J].
Alshahed, Osamh S. ;
Kaur, Baldeep ;
Bradley, Michael S. A. ;
Armour-Chelu, David .
POWDER TECHNOLOGY, 2023, 428
[3]  
Arastoopour H., 1979, Technical Report
[4]   Fluidized dense phase pneumatic conveying: a review [J].
Behera, Niranjana ;
Alkassar, Yassin ;
Agarwal, Vijay K. ;
Pandey, R. K. .
PARTICULATE SCIENCE AND TECHNOLOGY, 2023, 41 (02) :277-296
[5]   Determination of a particle size distribution criterion for predicting dense phase pneumatic conveying behaviour of granular and powder materials [J].
Deng, Tong ;
Bradley, Michael S. A. .
POWDER TECHNOLOGY, 2016, 304 :32-40
[6]   SALTATION VELOCITIES IN HIGH-PRESSURE CONVEYING OF FINE COAL [J].
GELDART, D ;
LING, SJ .
POWDER TECHNOLOGY, 1992, 69 (02) :157-162
[7]   ON THE PREDICTION OF PICKUP AND SALTATION VELOCITIES IN PNEUMATIC CONVEYING [J].
Gomes, L. M. ;
Amarante Mesquita, A. L. .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2014, 31 (01) :35-46
[8]  
Hinkle B.L., 1953, Acceleration of Particles and Pressure Drops Encountered in Horizontal Pneumatic Conveying
[9]   An investigation of the prevailing flow patterns and pressure fluctuation near the pressure minimum and unstable conveying zone of pneumatic transport systems [J].
Jama, GA ;
Klinzing, GE ;
Rizk, F .
POWDER TECHNOLOGY, 2000, 112 (1-2) :87-93
[10]   Analysis of unstable behavior of pneumatic conveying systems [J].
Jama, GA ;
Klinzing, GE ;
Rizk, F .
PARTICULATE SCIENCE AND TECHNOLOGY, 1999, 17 (1-2) :43-68