Hello every one,
Please help with reliable set of equations used to calculate the pressure drop across a catalyst bed. highly appreciated if any free simple software is available.
Kind reagrds
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Pressure Drop In Catalyst Bed
Started by Alawi, Jun 03 2007 12:49 AM
4 replies to this topic
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#1
Posted 03 June 2007 - 12:49 AM
#2 Guest_saeid_*
Posted 12 December 2007 - 08:10 AM
dear alawi
some catalyst manufacturer get press drop across the catalyst vs gas velocity.
you can contact with your catalyst manufacturer.
some catalyst manufacturer get press drop across the catalyst vs gas velocity.
you can contact with your catalyst manufacturer.
#3
Posted 17 December 2007 - 09:16 AM
Dear,
I hope the reactor which you have mentioned here is a fixed bed reactor and, if so, you can calculate the pressure drop by using <b>Ergun Equation</b><u></u>.
Pressure drop is calculated in terms of (ΔP/L), the pressure drop per unit length of packing.
I hope the reactor which you have mentioned here is a fixed bed reactor and, if so, you can calculate the pressure drop by using <b>Ergun Equation</b><u></u>.
Pressure drop is calculated in terms of (ΔP/L), the pressure drop per unit length of packing.
#4
Posted 25 June 2010 - 07:54 AM
Hello
Yeah, try using the Ergun equation for modeling the pressure drop through the reactor.
It looks like the following:
dP/dW=[-(150(1-Φ)^2)/Φ^3 (μ*u)/〖d_p〗^2 -(〖1,75(1-Φ) ρ〗_gas u^2)/(d_p Φ^3 )](1-Φ) A_c ρ_cat
where,
u = the spacial velocity of the gas,
rho = the gas density
fi = the bed's void factor
Ac = the reactor's section area
Yeah, try using the Ergun equation for modeling the pressure drop through the reactor.
It looks like the following:
dP/dW=[-(150(1-Φ)^2)/Φ^3 (μ*u)/〖d_p〗^2 -(〖1,75(1-Φ) ρ〗_gas u^2)/(d_p Φ^3 )](1-Φ) A_c ρ_cat
where,
u = the spacial velocity of the gas,
rho = the gas density
fi = the bed's void factor
Ac = the reactor's section area
#5
Posted 26 June 2010 - 06:34 AM
Using Ergun equation to predict pressure drop in fixed bed reactor requires data from catalyst vendor which can be proprietary or unavailable.
In such cases developing a simple Mathematical Model based on Ergun Equation can really help:
From operating plant actual ∆P in reactor for various flow rates can be recorded and plotted in as shown in attachment. This type of data can be represented as:
∆P
---- = [ A*(V)] + [B *(V2)]
L
Where A, B = Constants derived from graph.
This should solve the problem!
In such cases developing a simple Mathematical Model based on Ergun Equation can really help:
From operating plant actual ∆P in reactor for various flow rates can be recorded and plotted in as shown in attachment. This type of data can be represented as:
∆P
---- = [ A*(V)] + [B *(V2)]
L
Where A, B = Constants derived from graph.
This should solve the problem!
Attached Files
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