Modeling of vibrated fluidized‐bed dryers

2020 ◽  
Vol 92 (9) ◽  
pp. 1161-1161
Author(s):  
S. E. Lehmann ◽  
A. Jongsma ◽  
F. Innings ◽  
S. Heinrich
Keyword(s):  
Fluidized Bed ◽  
Vibrated Fluidized Bed

scholarly journals ANALISA ENERGI DAN EKSERGI PADA PENGERINGAN TEPUNG TAPIOKA MENGGUNAKAN PENGERING KONTINYU UNGGUN FLUIDISASI GETAR

REAKTOR ◽  
2016 ◽  
Vol 16 (1) ◽  
pp. 24 ◽  
Author(s):  
Suherman Suherman ◽  
Rona Trisnaningtyas
Keyword(s):  
Energy Efficiency ◽  
Fluidized Bed ◽  
Exergy Analysis ◽  
Cassava Starch ◽  
Energy Utilization ◽  
Exergetic Efficiency ◽  
Energy And Exergy ◽  
Vibrated Fluidized Bed ◽  
Energy And Exergy Analysis ◽  
Utilization Ratio

Energy and exergy analysis of cassava starch drying in continuous vibrated fluidized bed dryer were carried out to assess the performance of the system in terms of energy utilization ratio, energy efficiency, exergy inflow and outflow, exergy loss, and exergetic efficiency. The results showed cassava starch has starch content 87%, degree of whiteness 95%, negative fiber content, sperichal granula with average diameter12.32 μm, orthorhombic crystal structure and crystal size 47.467 nm . Energy utilization and energy utilization ratio increased from 0.08 to 0.20 J/s and 0.35 to 0.4 as the drying temperature  increased from 50 to 70 oC. Energy efficiency increased from 13.80 % to 23.31 %, while exergy inflow, outflow, and losses increased from 4.701 to 14.678, 2.277 to 6.344, and 2.424 to 8.334 J/s respectively in the above temperature range. Exergetic efficiency decreased with increase in drying air temperature, while exergetic improvement potential increased with increased drying air temperature. Keywords: Cassava starch, continuous drying, energy and exergy analysis, vibrated fluidized bed Abstrak Analisis energi dan eksergi pengeringan pati tapioka menggunakan pengering kontinu unggun fluidisasi getar, telah dilakukan untuk menilai kinerja sistem dalam bentuk utilisasi energi, efisiensi energi, eksergi masuk dan keluar, eksergi hilang dan efisiensi eksergi. Hasil analisis pati memiliki kandungan starch 87%, tingkat keputihan 95%, kandungan serat negatif, bentuk partikel granular spherical dengan diameter 12,32 μm, struktur kristal orthorhombic dan ukuran kristal sebesar 47,467 nm. Peningkatan suhu pengering dari 50 menjadi 70 0C akan meningkatkan utilisasi energi dan rasio utilisasi energi dari 0,08 menjadi 0,20 J/s dan 0,35 menjadi 0,4. Efisiensi energi meningkat dari 13,80% hingga 23,31%, sedangkan eksergi masuk dan keluar, eksergi hilang meningkat dari 4,701 menjadi 14,678, 2,277 menjadi 6,344, dan 2,424 menjadi 8,334 J/s. Efisiensi eksergi menurun dengan naiknya suhu sedangkan potensi pengembangan eksergi meningkat dengan naiknya suhu. Kata kunci:. Analisis energi dan eksergi, pati tapioka, pengeringan kontinu, unggun fluidisasi getar

Results of tests on a dryer with a vibrated fluidized bed

1969 ◽  
Vol 5 (11) ◽  
pp. 866-869 ◽  
Author(s):  
V. P. Osinskii ◽  
B. S. Sazhin ◽  
E. A. Chuvpilo
Keyword(s):  
Fluidized Bed ◽  
Vibrated Fluidized Bed

The Pressure Drop at Critical Fluidization of Large Particles in Vibrated Fluidization Bed

2012 ◽  
Vol 550-553 ◽  
pp. 2763-2766
Author(s):  
Xue Jun Zhu ◽  
Jun Deng
Keyword(s):  
Pressure Drop ◽  
Fluidized Bed ◽  
Large Particle ◽  
Particle Diameter ◽  
Future Design ◽  
Vibration Strength ◽  
Bed Height ◽  
Large Particles ◽  
Vibrated Fluidized Bed ◽  
Critical Fluidization

The pressure drop at critical fluidization for two-dimensional vibrated fluidized bed(240 mm×80 mm) was studied, with large particle glass beads of average diameters dp of 1.8mm, 2.5mm and 3.2mm.The effect of the vibration strength, the static bed height and the particle diameter on the pressure drop was analyzed. The results of the study show that the pressure drop decreases with the increase of the vibration strength. It plays an even more prominent part with decreases of the static bed height and the particle diameter. The empirical correlation equations to predict the pressure drop was established, and the results of the prediction was compared with the experimental data, the error is in range of ±10%. The results can provide references for future design and research on the vibrated fluidized bed.

Dynamic response of a vibrated fluidized bed of fine and cohesive powders

2013 ◽  
Vol 237 ◽  
pp. 276-285 ◽  
Author(s):  
Diego Barletta ◽  
Paola Russo ◽  
Massimo Poletto
Keyword(s):  
Dynamic Response ◽  
Fluidized Bed ◽  
Vibrated Fluidized Bed ◽  
Cohesive Powders

Numerical simulation of particle motion in vibrated fluidized bed

2004 ◽  
Vol 59 (2) ◽  
pp. 437-447 ◽  
Author(s):  
Yuji Tatemoto ◽  
Yoshihide Mawatari ◽  
Tomoya Yasukawa ◽  
Katsuji Noda
Keyword(s):  
Numerical Simulation ◽  
Fluidized Bed ◽  
Particle Motion ◽  
Vibrated Fluidized Bed

Numerical simulation of cohesive particle motion in vibrated fluidized bed

2005 ◽  
Vol 60 (18) ◽  
pp. 5010-5021 ◽  
Author(s):  
Yuji Tatemoto ◽  
Yoshihide Mawatari ◽  
Katsuji Noda
Keyword(s):  
Numerical Simulation ◽  
Fluidized Bed ◽  
Particle Motion ◽  
Vibrated Fluidized Bed

Pyrite enrichment in vibrated fluidized bed based on density segregation

2016 ◽  
pp. 1-9 ◽  
Author(s):  
Chenyang Zhou ◽  
Chenlong Duan ◽  
Bo Zhang ◽  
Yuemin Zhao ◽  
Xuchen Fan ◽  
...  
Keyword(s):  
Fluidized Bed ◽  
Vibrated Fluidized Bed

DRYING OF STICKY GRANULAR MATERIALS DWING THE CONSTANT RATE PERIOD IN A VIBRATED FLUIDIZED BED

1991 ◽  
Vol 9 (4) ◽  
pp. 1067-1079 ◽  
Author(s):  
Y.K Pan ◽  
Y.M Gan ◽  
X.D Liu ◽  
Z Wei ◽  
Arun S Mujumdar
Keyword(s):  
Granular Materials ◽  
Fluidized Bed ◽  
Constant Rate ◽  
Rate Period ◽  
Vibrated Fluidized Bed

scholarly journals Experimental study on the motion of solids around an isolated bubble rising in a vertically vibrated fluidized bed

2017 ◽  
Vol 330 ◽  
pp. 120-133 ◽  
Author(s):  
E. Cano-Pleite ◽  
F. Hernández-Jiménez ◽  
L.M. Garcia-Gutierrez ◽  
A. Acosta-Iborra
Keyword(s):  
Experimental Study ◽  
Fluidized Bed ◽  
Vibrated Fluidized Bed ◽  
Bubble Rising
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