Dear All,
Anybody know what is the flow coefficient and pressure coefficient of centrifugal compressor?
Is that related with aerodynamic design for the impeller? If so, what is the relation and impact to design of impeller? Is this number so important like NSS (suction specific speed) of the pump? What is the maximum or minimum limit (number) for these coefficient to ensure that vendor design is OK.
Regards,
mach
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Pressure And Flow Coefficient Of Centrifuga Compressor
Started by Guest_machinery_*, Mar 02 2007 08:50 AM
3 replies to this topic
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#1
Guest_machinery_*
Posted 02 March 2007 - 08:50 AM
#2
Posted 04 March 2007 - 07:13 AM
The head coefficient coefficient or pressure coefficient Ψ is a dimensionless parameter defined by
Head per impeller (m) = Ψ * u2 / g
The head coefficient is dependend of impeller design, having a value of 0.5 to 0.65. The average value is 0.55 ( at the best efficiency point).
The flow coefficient Φ is a dimensionless parameter described relationship of the suction gas flow rate to impeller diameter and tip speed.
Φ = Q / (3.1416* D2/4* u)
The value of flow coefficient ranges from 0.01 to 0.14
The curve of Ψ venus Φ is equivlent to Capacity-Head curve, is characterised only for impeller design & shape and should be valid for different inler gas conditions and speed.
Where:
u : tip speed (m/s) = N (rpm) * 3.1416 * D (m) / 60
N : rotation speed (rpm)
g: gravity constant = 9,81 m/s2
D: impeller diameter (m)
Q: suction gas flow (m3/s)
Head per impeller (m) = Ψ * u2 / g
The head coefficient is dependend of impeller design, having a value of 0.5 to 0.65. The average value is 0.55 ( at the best efficiency point).
The flow coefficient Φ is a dimensionless parameter described relationship of the suction gas flow rate to impeller diameter and tip speed.
Φ = Q / (3.1416* D2/4* u)
The value of flow coefficient ranges from 0.01 to 0.14
The curve of Ψ venus Φ is equivlent to Capacity-Head curve, is characterised only for impeller design & shape and should be valid for different inler gas conditions and speed.
Where:
u : tip speed (m/s) = N (rpm) * 3.1416 * D (m) / 60
N : rotation speed (rpm)
g: gravity constant = 9,81 m/s2
D: impeller diameter (m)
Q: suction gas flow (m3/s)
#3
Guest_machinery_*
Posted 04 March 2007 - 09:32 AM
QUOTE (npp @ Mar 4 2007, 08:13 PM) <{POST_SNAPBACK}>
The head coefficient coefficient or pressure coefficient Ψ is a dimensionless parameter defined by
Head per impeller (m) = Ψ * u2 / g
The head coefficient is dependend of impeller design, having a value of 0.5 to 0.65. The average value is 0.55 ( at the best efficiency point).
The flow coefficient Φ is a dimensionless parameter described relationship of the suction gas flow rate to impeller diameter and tip speed.
Φ = Q / (3.1416* D2/4* u)
The value of flow coefficient ranges from 0.01 to 0.14
The curve of Ψ venus Φ is equivlent to Capacity-Head curve, is characterised only for impeller design & shape and should be valid for different inler gas conditions and speed.
Where:
u : tip speed (m/s) = N (rpm) * 3.1416 * D (m) / 60
N : rotation speed (rpm)
g: gravity constant = 9,81 m/s2
D: impeller diameter (m)
Q: suction gas flow (m3/s)
Head per impeller (m) = Ψ * u2 / g
The head coefficient is dependend of impeller design, having a value of 0.5 to 0.65. The average value is 0.55 ( at the best efficiency point).
The flow coefficient Φ is a dimensionless parameter described relationship of the suction gas flow rate to impeller diameter and tip speed.
Φ = Q / (3.1416* D2/4* u)
The value of flow coefficient ranges from 0.01 to 0.14
The curve of Ψ venus Φ is equivlent to Capacity-Head curve, is characterised only for impeller design & shape and should be valid for different inler gas conditions and speed.
Where:
u : tip speed (m/s) = N (rpm) * 3.1416 * D (m) / 60
N : rotation speed (rpm)
g: gravity constant = 9,81 m/s2
D: impeller diameter (m)
Q: suction gas flow (m3/s)
Dear Npp,
Thank for your response. I have the equation for both flow and pressure coefficient. However, I don't have the guidance value for it. Can you inform me what is the standard ranges for the value that you specified. And what happen if the flow and pressure coefficient higher or lower than ranges that you given. This is becuase, if I want to make technical bid analysis for 2 compressors, how to say that one vendor better in "aerodynamic" compare with other with regard to the value of flow and pressure coefficient.
Many thanks,
mach
#4
Posted 05 March 2007 - 10:55 AM
These parameters are only a mean to characterise a machine. I don’t think they have relation to reliability and effective of the machine. The vendor should give some guarantee about energy consumption and performance. They tell how effective the machine is. Check the references to evaluate the reliability.The most downtime is due to problem of the shaft, impeller, motor, seal and bearing. Estimate the cost for downtime and compare the total annual cost of the machine (annual cost of investment, utility cost, cost of maintenance, cost of downtime, etc.)
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