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   Cfd Study and Energy Optimization of Industrial Double-Cyclone in Hdpe Drying Process  
   
نویسنده Razavi Alavi Abolfazl ,Nemati Lay Ebrahim
منبع مهندسي و مديريت انرژي - 2021 - دوره : 10 - شماره : 4 - صفحه:14 -29
چکیده    A doublec-yclone is used as a gas-solid separator in the fluid bed-drying process to prepare dry hdpe powder from a wet feed rate of 56000 kg/hr. particles rsquo; behavior and flow pattern in the dryer affect the cyclones as effective equipment. in evaluation of this system, the numerical simulation of the fluid flow field and particle dynamics, presented by cfd technique, characterize cyclone pressure drop and turbulence parameters. navierstoke equations through the euelerianlagrangian framework by rng kɛ turbulence model are used as mathematical methods and the calculated results are in an acceptable agreement with industrial parameters. the obtained carrier gas flow rates of 14040, 14011 and 14000 m3hr1 as thermal energy for pe100, bl3, and ex5 respectively cause excellent flow regime, desired final volatile of 0.04%, 0.06% and 0.07% as well as high separation efficiency in different hdpe grades. the created flow pattern in the dryer makes the efficient use of the immersed coils as another source of energy for drying the particles. doublecyclones conduct the minimum escaped contents of 70.2, 75.8 and 76.2 for the distributor section and 69.3, 75.3, 75.9 gr in 1 hr for the scrubbing tower. these rates of dusts provide the optimized electrical energy consumptions with maximum saving value of 17%.
کلیدواژه Cfd ,Hdpe ,Fluidized Bed Drying ,Energy Optimization ,Double-Cyclone ,Pressure Drop
آدرس University Of Kashan, Faculty Of Engineering, Department Of Chemical Engineering, Iran, University Of Kashan, Faculty Of Engineering, Department Of Chemical Engineering, Iran
پست الکترونیکی enemati@kashanu.ac.ir
 
   CFD Study and Energy Optimization of Industrial Double-Cyclone in HDPE Drying Process  
   
Authors Nemati Lay Ebrahim ,Razavi Alavi S. Abolfazl
Abstract    A doublecyclone is used as a gassolid separator in the fluid beddrying process to prepare dry HDPE powder from a wet feed rate of 56000 kg/hr. Particles rsquo; behavior and flow pattern in the dryer affect the cyclones as effective equipment. In evaluation of this system, the numerical simulation of the fluid flow field and particle dynamics, presented by CFD technique, characterize cyclone pressure drop and turbulence parameters. NavierStoke equations through the EuelerianLagrangian framework by RNG kɛ turbulence model are used as mathematical methods and the calculated results are in an acceptable agreement with industrial parameters. The obtained carrier gas flow rates of 14040, 14011 and 14000 m3hr1 as thermal energy for PE100, BL3, and EX5 respectively cause excellent flow regime, desired final volatile of 0.04%, 0.06% and 0.07% as well as high separation efficiency in different HDPE grades. The created flow pattern in the dryer makes the efficient use of the immersed coils as another source of energy for drying the particles. Doublecyclones conduct the minimum escaped contents of 70.2, 75.8 and 76.2 for the distributor section and 69.3, 75.3, 75.9 gr in 1 hr for the scrubbing tower. These rates of dusts provide the optimized electrical energy consumptions with maximum saving value of 17%.
Keywords CFD ,HDPE ,Fluidized Bed Drying ,Energy Optimization ,Double-Cyclone ,Pressure Drop
 
 

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