Difference between revisions of "Analisis aliran didalam Cyclone Separator dengan Simulasi CFD menggunakan CFDSOF"
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== 1. Pengantar == | == 1. Pengantar == | ||
| + | === Abi Rizky === | ||
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| + | === Agus Nuryadi === | ||
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| + | '''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): | ||
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| + | [[File:rumusA.jpg|600px|thumb|centre|alt text]] | ||
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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, g/cm3. | ||
== 2. Objektif == | == 2. Objektif == | ||
Revision as of 16:24, 30 November 2020
Analisis aliran didalam Cyclone Separator dengan Simulasi CFD menggunakan CFDSOF Abstrak
Contents
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):
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, g/cm3.
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 ....
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