Difference between revisions of "Analisis aliran didalam Cyclone Separator dengan Simulasi CFD menggunakan CFDSOF"

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(1. Pengantar)
(Agus Nuryadi)
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[[File:rumusA.jpg|600px|thumb|centre|alt text]]
 
[[File:rumusA.jpg|600px|thumb|centre|alt text]]
  
Where, '''d50''' is the particle diameter for which the cyclone is 50 per cent efficient, '''Dc'''  is diameter of the cyclone chamber, ''u'' is liquid viscosity, '''L''' is feed flow rate, ''p''l    = density of the liquid, and ''p''s    = density of the solid, g/cm3.
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Where, '''d50''' is the particle diameter for which the cyclone is 50 per cent efficient, '''Dc'''  is diameter of the cyclone chamber, ''u'' is liquid viscosity, '''L''' is feed flow rate, ''p''l    = density of the liquid, and ''p''s    = density of the solid.
  
 
== 2. Objektif ==
 
== 2. Objektif ==

Revision as of 16:25, 30 November 2020

Analisis aliran didalam Cyclone Separator dengan Simulasi CFD menggunakan CFDSOF Abstrak


1. Pengantar

Abi Rizky

Agus Nuryadi

The nomographs by Zanker can be used to make a preliminary estimate of the size of cyclone needed. The specialist manufacturers of hydrocyclone equipment should be consulted to determine the best arrangements and design for a particular application. Zanker’s method is outlined below and illustrated in the Example below and based on an empirical equation by Bradley (1960):

alt text

Where, d50 is the particle diameter for which the cyclone is 50 per cent efficient, Dc is diameter of the cyclone chamber, u is liquid viscosity, L is feed flow rate, pl = density of the liquid, and ps = density of the solid.

2. Objektif

3. Metodologi

4. Model Komputasi dan Simulasi

5. Hasil dan Pembahasan

5.1 Verifikasi 5.2 Validasi 5.3 Pembahasan

   5.3.1 ....


.... ...

6. Kesimpulan

7. Referensi