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Commit 547e34b1 authored by Delvigne Frank's avatar Delvigne Frank
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#!/usr/bin/env python3
# -*- coding: utf-8 -*-
"""
Created on Thu Feb 27 07:52:51 2020
@author: delvigne
"""
import math
from math import pi
## Basic data : pilot bioreactor
D1 = 1 #m
d1 = D1/3 #%m -> standard geometry
N1 = 180/60 #s-1
rho = 1000 #Kg/m3
mu = 0.001 #Pa.s dynamic viscosity
N_p = 5.4 #Power number
N_qc = 1.5 #Circulation number
## Computation at pilot scale
Periph_speed_pilot = pi*N1*d1 #m/s
Q_c_pilot = N_qc*N1*((D1/3)**3) #Circulation flow rate m3/s
V_pilot = pi*D1**3/4 #m3
t_c_pilot = V_pilot/Q_c_pilot #circulation time s
## Basic data : industrial bioreactor
V_indus = 50 #m3
## Scaling-up criteria : volumetric power
Re = rho*N1*((D1/3)**2)/mu # if > 10^4 -> turbulent regime
P = N_p*rho*(N1**3)*((D1/3)**5) # One impeller
P_V = P/V_pilot # Volumetric power (W/m3)
## Computation at industrial scale
P_indus = P_V*V_indus #W
D2 = ((4*V_indus)/pi)**(1/3) #m
d2 = D2/3 #m
N2 = (P_indus/(rho*N_p*d2**5))**(1/3) #s-1
Periph_speed_indus = pi*N2*d2 #m/s
Q_c_indus = N_qc*N2*((D2/3)**3) #Circulation flow rate m3/s
t_c_indus = V_indus/Q_c_indus #circulation time s
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