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When sizing up a vessel, what are the dimensionless parameters that I have to take into account such that the flow dynamics can be maintained?
I have a reactor of 1.2m diameter positioned vertically, and the gaseous reactants enters from the top. If I size up the reactor to 1.4m diameter, how should I correlated that to the position of the reactor fixed bed and the position of the burner?
Application: Formalin plant - silver process.
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Sizing Up - Fluid Dynamics
Started by Ming Hooi, Jul 27 2005 09:33 PM
1 reply to this topic
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Guest_aarti_*
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Posted 16 August 2005 - 02:54 AM
QUOTE (MH.C @ Jul 27 2005, 09:33 PM)
When sizing up a vessel, what are the dimensionless parameters that I have to take into account such that the flow dynamics can be maintained?
I have a reactor of 1.2m diameter positioned vertically, and the gaseous reactants enters from the top. If I size up the reactor to 1.4m diameter, how should I correlated that to the position of the reactor fixed bed and the position of the burner?
Application: Formalin plant - silver process.
I have a reactor of 1.2m diameter positioned vertically, and the gaseous reactants enters from the top. If I size up the reactor to 1.4m diameter, how should I correlated that to the position of the reactor fixed bed and the position of the burner?
Application: Formalin plant - silver process.
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