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Determination ofDetermination of
Vacuum PumpVacuum Pump
Operational EfficiencyOperational Efficiency
deveshksinghal@gmail.com, March 2014
1
By:
D K Singhal
deveshksinghal@gmail.com
Why to CheckWhy to Check
Is vacuum pump sufficient for our need?
Do we need to change the vacuum pump, or
relocation may be tried?
deveshksinghal@gmail.com, March 2014
2
Existing TrendsExisting Trends
No standard available information on efficiency
determination on operational conditions.
Standard methods use standard conditions, which
generally are entirely different than the mill environment.
deveshksinghal@gmail.com, March 2014
3
No FlowVacuumNo FlowVacuum
This is also called as “peak vacuum” of the pump.
Some mills check the level of vacuum developed with
inlet valves closed.
A drop in gauge vacuum is considered a drop in vacuum
pump efficiency.
deveshksinghal@gmail.com, March 2014
4
pump efficiency.
Yet, if you are operating at low vacuum levels, the result
obtained by this may be misleading.
Wet & Dry OperationWet & Dry Operation
Routine tests account only for dry air.
The air is sucked in at 100% RH with some
entrained water.When the pressure of the
same increases in the vacuum pump, some of
deveshksinghal@gmail.com, March 2014
5
same increases in the vacuum pump, some of
the water vapor (moisture) condenses. So, at
exhaust side, you get slightly lesser airflow.
Also, at inlet during normal operation due to
water evaporation, you get lower gauge
reading.
5
Points to RememberPoints to Remember
Exhaust airflow reduces with increase in vacuum.
An old vacuum may give (almost) same airflow as rated
at low vacuum levels, but at high vacuum levels, capacity
reduces rapidly.
deveshksinghal@gmail.com, March 2014
6
reduces rapidly.
Seal water consumption may be high at such conditions.
Typical Pump DataTypical Pump Data
Take a look at a typical data supplied by a manufacturer.
mmHg Inlet Flow Capacity Loss
0 3000 0.0
50 2990 10.0
deveshksinghal@gmail.com, March 2014
7
7
50 2990 10.0
100 2970 30.0
200 2940 60.0
300 2900 100.0
400 2800 200.0
500 2700 300.0
600 2400 600.0
660 2040 960.0
Data Supplied Calculated
DeDe--rating at IncreasedVacuumrating at IncreasedVacuum
For normal operating ranges between 200mmHG and
500mmHg, the capacity drop can be linearly correlated
with vacuum level.
300.0
350.0
deveshksinghal@gmail.com, March 2014
8
8
y = 0.82x - 122
R2
= 0.9689
0.0
50.0
100.0
150.0
200.0
250.0
300.0
0 100 200 300 400 500 600
CapacityDrop
Vacuum Level, mmHG
Why does the vacuum reduce?Why does the vacuum reduce?
• The drop of capacity is mainly due to two reasons-
▫ At higher vacuum level, some part of exhaust air gets short
circuited to inlet air, no matter how good is sealing.
Furthermore, some part of sealing water gets evaporated due
to vacuum.This process increases as the vacuum pump gets
deveshksinghal@gmail.com, March 2014
9
to vacuum.This process increases as the vacuum pump gets
older due to wear and tear.
▫ At higher vacuum levels, there is a lot of moisture in process air
to be handled.This moisture condenses in vacuum pump, and
exhaust volume is lower than expected. Due to this, dry
checking of vacuum pump is generally not satisfactory to
process persons.
9
What to Check?What to Check?
Obtain existing performance data on vacuum pump.
Preferably, it should be at exhaust side, and the inlet side
may be calculated as under-
y = 0.82x - 122
R2
= 0.9689
0.0
50.0
100.0
150.0
200.0
250.0
300.0
350.0
0 100 200 300 400 500 600
Vacuum Level, mmHG
CapacityDrop
deveshksinghal@gmail.com, March 2014
10
Inlet flow = (760-mmHg)*Outlet Flow / 760
Vacuum levels can be changed by throttling the inlet
valves, while the machine clothing is running in wet
condition.
Instruments for Flow MeasurementInstruments for Flow Measurement
As flow is to be checked at
exhaust side, a conventional
vane flow anemometer can
be used easily.
deveshksinghal@gmail.com, March 2014
11
be used easily.
A hot wire anemometer, if
used, has to be calibrated
properly at operating
temperature and humidity
conditions.
11
Instruments for Flow MeasurementInstruments for Flow Measurement
Alternatively, a PitoTube (Pilot Tube)
connected with a differential pressure gauge
can be used. But, the major problem is relative
deveshksinghal@gmail.com, March 2014
12
can be used. But, the major problem is relative
low accuracy in case of oversized piping or in
case of high vacuum, low exhaust airflow
condition.
12
Vacuum MeasurementVacuum Measurement
A calibrated bourdon tube vacuum gauge can
be used for better accuracy.
A glycerin filled gauge ensures reading stability
deveshksinghal@gmail.com, March 2014
13
A glycerin filled gauge ensures reading stability
with no pulsations.
Alternatively, a mercury filled manometer can
be used.
13
Sample CalculationsSample Calculations
In this typical case, volumetric efficiency is reducing more
at higher vacuum levels.
Vacuum Exh. Flow Inlet Flow Inlet Flow Volumetric
mmHg (Measured) (Calculated) (Design) Efficiency
0 2950 2950 3000 98%
deveshksinghal@gmail.com, March 2014
14
0 2950 2950 3000 98%
50 2700 2890 2990 97%
100 2370 2729 2970 92%
200 1900 2579 2940 88%
300 1500 2478 2900 85%
400 1050 2217 2800 79%
500 650 1900 2700 70%
550 250 1188 2400 49%
600 - - - -
Operational EfficiencyOperational Efficiency
As we can see that the operational efficiency is reducing
rapidly with increase in vacuum levels.
For practical purposes, the efficiency at the operational
levels can be considered. For example, if the pump has to
be operated at 400mmHg vacuum, the efficiency would
deveshksinghal@gmail.com, March 2014
15
be operated at 400mmHg vacuum, the efficiency would
be 79%.
Or, we may consider that vacuum pump is giving 79% of
the rated airflow.
ResultsResults
On the basis of this analysis, we may conclude something
like this-
“This vacuum can be used for low vacuum applications
such as Low-Vac boxes of wire part etc. as the efficiency
is better at lower vacuum levels.”
deveshksinghal@gmail.com, March 2014
16
is better at lower vacuum levels.”
“On an 400mmHg operating vacuum, the pump has been
de-rated by 21%. So, if it does not serve the process
requirement, it should be replaced.”
“If it is serving the process right now, we may replace the
same with a new pump of smaller capacity and save
power (same 21%).”
Changing theVacuum PumpChanging theVacuum Pump
Many mills do not want to replace vacuum pump with a
new one, as the present one is OK.
In case, there is a drop in efficiency, please do consider
the cost of electricity loss due to reduction in efficiency.
If payback period suits you, talk to the best vacuum pump
deveshksinghal@gmail.com, March 2014
17
If payback period suits you, talk to the best vacuum pump
suppliers, negotiate well, but, replace the vacuum pump at
the earliest.
ThankYou.ThankYou.
deveshksinghal@gmail.com, March 2014
18
ThankYou.ThankYou.

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Determination of vacuum pump operational efficiency

  • 1. Determination ofDetermination of Vacuum PumpVacuum Pump Operational EfficiencyOperational Efficiency deveshksinghal@gmail.com, March 2014 1 By: D K Singhal deveshksinghal@gmail.com
  • 2. Why to CheckWhy to Check Is vacuum pump sufficient for our need? Do we need to change the vacuum pump, or relocation may be tried? deveshksinghal@gmail.com, March 2014 2
  • 3. Existing TrendsExisting Trends No standard available information on efficiency determination on operational conditions. Standard methods use standard conditions, which generally are entirely different than the mill environment. deveshksinghal@gmail.com, March 2014 3
  • 4. No FlowVacuumNo FlowVacuum This is also called as “peak vacuum” of the pump. Some mills check the level of vacuum developed with inlet valves closed. A drop in gauge vacuum is considered a drop in vacuum pump efficiency. deveshksinghal@gmail.com, March 2014 4 pump efficiency. Yet, if you are operating at low vacuum levels, the result obtained by this may be misleading.
  • 5. Wet & Dry OperationWet & Dry Operation Routine tests account only for dry air. The air is sucked in at 100% RH with some entrained water.When the pressure of the same increases in the vacuum pump, some of deveshksinghal@gmail.com, March 2014 5 same increases in the vacuum pump, some of the water vapor (moisture) condenses. So, at exhaust side, you get slightly lesser airflow. Also, at inlet during normal operation due to water evaporation, you get lower gauge reading. 5
  • 6. Points to RememberPoints to Remember Exhaust airflow reduces with increase in vacuum. An old vacuum may give (almost) same airflow as rated at low vacuum levels, but at high vacuum levels, capacity reduces rapidly. deveshksinghal@gmail.com, March 2014 6 reduces rapidly. Seal water consumption may be high at such conditions.
  • 7. Typical Pump DataTypical Pump Data Take a look at a typical data supplied by a manufacturer. mmHg Inlet Flow Capacity Loss 0 3000 0.0 50 2990 10.0 deveshksinghal@gmail.com, March 2014 7 7 50 2990 10.0 100 2970 30.0 200 2940 60.0 300 2900 100.0 400 2800 200.0 500 2700 300.0 600 2400 600.0 660 2040 960.0 Data Supplied Calculated
  • 8. DeDe--rating at IncreasedVacuumrating at IncreasedVacuum For normal operating ranges between 200mmHG and 500mmHg, the capacity drop can be linearly correlated with vacuum level. 300.0 350.0 deveshksinghal@gmail.com, March 2014 8 8 y = 0.82x - 122 R2 = 0.9689 0.0 50.0 100.0 150.0 200.0 250.0 300.0 0 100 200 300 400 500 600 CapacityDrop Vacuum Level, mmHG
  • 9. Why does the vacuum reduce?Why does the vacuum reduce? • The drop of capacity is mainly due to two reasons- ▫ At higher vacuum level, some part of exhaust air gets short circuited to inlet air, no matter how good is sealing. Furthermore, some part of sealing water gets evaporated due to vacuum.This process increases as the vacuum pump gets deveshksinghal@gmail.com, March 2014 9 to vacuum.This process increases as the vacuum pump gets older due to wear and tear. ▫ At higher vacuum levels, there is a lot of moisture in process air to be handled.This moisture condenses in vacuum pump, and exhaust volume is lower than expected. Due to this, dry checking of vacuum pump is generally not satisfactory to process persons. 9
  • 10. What to Check?What to Check? Obtain existing performance data on vacuum pump. Preferably, it should be at exhaust side, and the inlet side may be calculated as under- y = 0.82x - 122 R2 = 0.9689 0.0 50.0 100.0 150.0 200.0 250.0 300.0 350.0 0 100 200 300 400 500 600 Vacuum Level, mmHG CapacityDrop deveshksinghal@gmail.com, March 2014 10 Inlet flow = (760-mmHg)*Outlet Flow / 760 Vacuum levels can be changed by throttling the inlet valves, while the machine clothing is running in wet condition.
  • 11. Instruments for Flow MeasurementInstruments for Flow Measurement As flow is to be checked at exhaust side, a conventional vane flow anemometer can be used easily. deveshksinghal@gmail.com, March 2014 11 be used easily. A hot wire anemometer, if used, has to be calibrated properly at operating temperature and humidity conditions. 11
  • 12. Instruments for Flow MeasurementInstruments for Flow Measurement Alternatively, a PitoTube (Pilot Tube) connected with a differential pressure gauge can be used. But, the major problem is relative deveshksinghal@gmail.com, March 2014 12 can be used. But, the major problem is relative low accuracy in case of oversized piping or in case of high vacuum, low exhaust airflow condition. 12
  • 13. Vacuum MeasurementVacuum Measurement A calibrated bourdon tube vacuum gauge can be used for better accuracy. A glycerin filled gauge ensures reading stability deveshksinghal@gmail.com, March 2014 13 A glycerin filled gauge ensures reading stability with no pulsations. Alternatively, a mercury filled manometer can be used. 13
  • 14. Sample CalculationsSample Calculations In this typical case, volumetric efficiency is reducing more at higher vacuum levels. Vacuum Exh. Flow Inlet Flow Inlet Flow Volumetric mmHg (Measured) (Calculated) (Design) Efficiency 0 2950 2950 3000 98% deveshksinghal@gmail.com, March 2014 14 0 2950 2950 3000 98% 50 2700 2890 2990 97% 100 2370 2729 2970 92% 200 1900 2579 2940 88% 300 1500 2478 2900 85% 400 1050 2217 2800 79% 500 650 1900 2700 70% 550 250 1188 2400 49% 600 - - - -
  • 15. Operational EfficiencyOperational Efficiency As we can see that the operational efficiency is reducing rapidly with increase in vacuum levels. For practical purposes, the efficiency at the operational levels can be considered. For example, if the pump has to be operated at 400mmHg vacuum, the efficiency would deveshksinghal@gmail.com, March 2014 15 be operated at 400mmHg vacuum, the efficiency would be 79%. Or, we may consider that vacuum pump is giving 79% of the rated airflow.
  • 16. ResultsResults On the basis of this analysis, we may conclude something like this- “This vacuum can be used for low vacuum applications such as Low-Vac boxes of wire part etc. as the efficiency is better at lower vacuum levels.” deveshksinghal@gmail.com, March 2014 16 is better at lower vacuum levels.” “On an 400mmHg operating vacuum, the pump has been de-rated by 21%. So, if it does not serve the process requirement, it should be replaced.” “If it is serving the process right now, we may replace the same with a new pump of smaller capacity and save power (same 21%).”
  • 17. Changing theVacuum PumpChanging theVacuum Pump Many mills do not want to replace vacuum pump with a new one, as the present one is OK. In case, there is a drop in efficiency, please do consider the cost of electricity loss due to reduction in efficiency. If payback period suits you, talk to the best vacuum pump deveshksinghal@gmail.com, March 2014 17 If payback period suits you, talk to the best vacuum pump suppliers, negotiate well, but, replace the vacuum pump at the earliest.