BFP PUMP SERGING AND IMPELLER CUTTING-OFF
BFP PUMP SERGING AND IMPELLER CUTTING-OFF
(OP)
Let me say about problems of BFP Pump, its rated specification is follows.
1) rated flow : around 500m^3/hr
2) Min. flow : 200m^3/hr
3) Discharge Head : 240 bar
4) Centrifugal Type and 8 Stage
5) NHSPr : 8m
6) NPSHa : 16m
7) Test water temperature : 20 oC
8) Operation water temperature : 170 oC
1. Current Situation
When we get this BFP pump operation, we found so serious noise and vibration in a discharge ppiping line and it also appears on suction piping.( Currently, we call this phenomenon as Pump serging)
Currently, we guess that this caused by lower NPSHa at suction piping where deaerator was located at 16m height above BFP pump, In there are 3 sets of BFP pump, one of them is little bit better than others, so we believe that this was caused by NHPSa because each BFP head loss in suction line is different, thereby, short piping where located BFP is better relatively.
When we get pump test performence curve as attached file.
2. My opinion is follows at current pump operation
1) This pump should be getting right side inclined curve basically, so flow have to be decreased as much as head loss, otherwise, excessive head could cause suction head loss and thereby, serging occurs in suction line due to excessive pressure accumulation at min. flow.
and then this energy accumulation cause water hammering not only suction line but discharge cline together.
3. Query over this situation
Is it possible to get impeller cutting off in order to have inclined curve right side against parallel line between Min. flow(200m^3/h and rated flow(500m^3/h)
And how much we can expect decreased discharge head and flow rate at 5% Impeller cutting off.
1) rated flow : around 500m^3/hr
2) Min. flow : 200m^3/hr
3) Discharge Head : 240 bar
4) Centrifugal Type and 8 Stage
5) NHSPr : 8m
6) NPSHa : 16m
7) Test water temperature : 20 oC
8) Operation water temperature : 170 oC
1. Current Situation
When we get this BFP pump operation, we found so serious noise and vibration in a discharge ppiping line and it also appears on suction piping.( Currently, we call this phenomenon as Pump serging)
Currently, we guess that this caused by lower NPSHa at suction piping where deaerator was located at 16m height above BFP pump, In there are 3 sets of BFP pump, one of them is little bit better than others, so we believe that this was caused by NHPSa because each BFP head loss in suction line is different, thereby, short piping where located BFP is better relatively.
When we get pump test performence curve as attached file.
2. My opinion is follows at current pump operation
1) This pump should be getting right side inclined curve basically, so flow have to be decreased as much as head loss, otherwise, excessive head could cause suction head loss and thereby, serging occurs in suction line due to excessive pressure accumulation at min. flow.
and then this energy accumulation cause water hammering not only suction line but discharge cline together.
3. Query over this situation
Is it possible to get impeller cutting off in order to have inclined curve right side against parallel line between Min. flow(200m^3/h and rated flow(500m^3/h)
And how much we can expect decreased discharge head and flow rate at 5% Impeller cutting off.





RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Multistage boiler feed pumps are unique and demand a bit more engineering knowledge and experience than simple single stage pumps.
As a minimum, BFP suction piping must satisfy two complex and related criteria:
1) The NPSHa must be greater than the NPSHr with a sufficient margin. ( I am not sure the margin is acceptable here)
2) Upon startup, the suction piping diameter and configuration must allow an adequate volume of liquid to flow into the pump very quickly. The liquid flow cannot undergo cavitation conditions within any stage of the pump during this startup event.
With multiple boiler feed pumps, it sounds like your suction piping is a mess.... Can you provide an isometric sketch of the suction piping with diameters ? What is the suction piping diameter compared with the suction nozzle of the pump ?
I have never seen a worse performance curve for pump operation......
Have you disassembled the pump and examined the first stage impeller ?
MJCronin
Sr. Process Engineer
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Thank for your review, additionally this BFP pump inlet and outlet, piping nozzle size is follows.
1) Pump Inlet nozzle (10"), Velocity : 2.5 m/sec
2) Pump outlet nozzle (8")
3) Inlet nozzle piping line (14")
Currently, this pump was disassemblied, and have plan to get impeller trimming
in order for lower discharge head as attached performance curve.
So, I need to confirm if this impeller diameter to be cutting off (Except first impeller)
from 2nd vane to 8th vane, is it to get expected curve as shown on attached curve.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
I think you're missing the point here. From the information you've given us, I'm finding it difficult to work out how this pump works at all, but without more information on the suction/inlet system, you can trim the impellors all you like, but if the inlet system is flashing into steam as you describe, then all you will achieve by trimming the impellor is getting an unbalanced machine which has a worse performance than you had before. Only the pump vendor can tell you with any certainty what the curve would look like with smaller impellors, but I don't think the basic shape of the curve wil change, only a curve in parallel but further to th bottom left corner.
This sounds a bit like someone trying to drive a car with the handbrake on then changing the gearbox ratios, but still leaving the handbrake on and expecting the car to some how suddenly work better and not have a burning smell....
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Do you have five to 10 diameters of straight piping upstream of the suction nozzle ?
In your IOM manual from the manufacturer, what was the recommendation for suction piping configurations ?
Was the pump used in another service ?
Some owners use a VFD for high energy, multi staged pumps. They are important for smooth startup.
Has this been considered ?
MJCronin
Sr. Process Engineer
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Let me tell you additional information alongwith Piping Sketch as attached.
1. Pump specification is follows.
1) Density : 0.888
2) Dgn Temp : 220oC
3) Operating Temp : 179oC
4) Suction flow rate : 528.3 m^3/h
5) DIscharge flow rate : 515m^3/h
6) Bleed off flow rate : 13.3m^3/h
7) Suction pressure : 11.29 kg/cm^2a
8) DIscharge pressure : 177.3 kg/cm^2g
9) Bleed off pressure : 61 kg/cm^2a
10) Total TDH, HP/IP : 1870m/ 560m
11) NPSHab : 16m
12) NPSHre : 8m
13) Surge margin : 5%
14) Shut-off pressure : around 1.2 time TDH
2. Current situation at commissioning operation in cold condition.
Surging(Noise and Vibration in suction line and discharge line) occurs at mininum flow rate around 200m^3/h and, when flow rate to be gradually increased to MCR, No surging occurs.
3. I believe that this pump have some problems in performance curve at mininum flow due to parallel line of H.Q curve (that should be inclined line)
Moreover, I find out that surge margin is little bit small of 5% considering suction pressure loss.
4. If we change suction line to 20" from current 14" as long as 5m just front of BFP pump,
is this better than trimming impeller diameter, In my opinion, trimming impeller can change performance curve, this is my key concern in this matter.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Let me show you BFP pump ISO line, as attached file.
1) Pump Inlet nozzle (10"), Velocity : 2.5 m/sec
2) Pump outlet nozzle (8")
3) Inlet nozzle piping line (14")
I got a realized that suction line is smaller considering NPSHav even if Pump vendor they followed requirement of API code, Current flow velocity is around 2.5m/s,
Can we getting down of velocity to 1.0 m/s with change of inlet size.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Can you post the pump curve please and any details for the impellors you have.
There is something strange happening here at your lower flow rates which isn't clear from the information supplied. It tends to indicate that your issue is a pump related one if the issue is at low flow rates.
The other option is to ask the vendor for his CAVITATION curve, which can be quite different from the NPSH curve. I suspect something is happening in the pump at your lower flows which is either causing the liquid to heat up further such that the water boils or that the pump at that flow requires higher pressure to avoid cavitation.
At that temperature (180C), what do you calculate your vapour pressure to be? My estimate is somewhere between 9 and 10 kg/cm2.
what is your suction pressure graph doing during these "surging" events?
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
http://www.chemicalprocessing.com/articles/2006/09...
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Let me show you performance and NPSHr as shown on Vendor data.
Actually, there is different performance during commissioning test. Currently I'm sure that NPSHa is less than NPSHr at mininum flow as shown on attached performance curve at my first post.
NPSHr : 8m
NPSHa : 16m
However, at mininum flow condition, there might be additional pressure loss or NPSHr is more greater than Vendor data.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
That curve is more or less what I would expect.
If you read the article carefully, it shows that in some instances - may be this one maybe not - the Cavitation curve can detach from the NPSH curve (normally 1 to 2 m above it) and increase dramatically at lower flow rates.
Therefore ask the vendor specifically for the Cavitation curve. You might need to get hold of the technical office and not the sales person to get what you need, but it looks clear to me that your system struggles below 200m3/hr and this is a possible cause.
To fix it you either need to modify the first impellor or just run it higher than 200 and put in a minimum flow bypass??
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
With all of the money and time you have invested, I suggest that you consider hiring an experienced pump consultant to get a quick opinion. Find one that has solved high energy fluid flow pumping problems in the past.
You have not stated if you have contacted the pump vendor..... What has the pump vendor advised you about the installation ?
At the end of this problem , please respect us..... and share your final solution.
MJCronin
Sr. Process Engineer
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Thanks for your recommendation until now, I will let you know what happen after impeller trimming in a week. Pump vendor have a plan to trim impeller 2nd to 8th to avoid surging at minimum flow.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
I wanna post the BFP performance curve after impeller trimming, this curve nothing improved with impeller trimming, on the contrary, Actually, this Curve get more worsed against before.
Once again, this BFP pump had problem with surging in a minimum flow range, however, after impeller trimming, surging range is increased and flowrate to be hunting in normal flow range.
We got this BFP pump impeller trimming from 2nd impeller through 8th impeller leaving 1st impeller
in order to improve surging probelems at minimum flow.
I believe that NPSHre was increased and, Q, H, L was also decresed as much as principle of similarity as below.
Q2=Q1(N2/N1) * (D2/Q1)^3
H2=H1(N2/N1) * (D2/D1)^2
L2=L1(N2/N1) * (D2/D1)^5
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
You were warned above that what you were doing was not a recommended course of action to solve the issues you face.
I think you have now proved the old proposition which is that it is rarely the pump which is at fault, more the manner in which it is used and controlled.
It was clear to most of us that below minimum flow and in your case approx. 200m3/hr, the pump was unstable, especially when operated in parallel with other pumps. You don't say how or where the flow is controlled and unless and until you can determine what your system curve looks like, I don't think you'll get very far.
You seem to have made things much worse and there is little I can suggest other than to have someone experienced in BFP system design (pumps, piping, controls) etc look at this and provide some planned modifications.
Sorry, but you sometimes have to admit you've made an error early on and then propose a way out rather than blame someone else.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Measure twice cut once come to mind....
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
I missed one thing to give you additional information, minimum flow is controlled by ARC valve, I also believe that the initial force of ARC valve would occurs chattering at Min. Flow.
Actually, previous P. Curve was modified as attached file. Surging range slightly moved to more flow rate against before trimming.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
http://turbolab.tamu.edu/proc/turboproc/T5/T5pg45-...
I still maintain that vibrations and surging (note the spelling)are due to improperly designed suction piping. (You will note that the pump has two elbows just upstream of the suction nozzle and does NOT have an adequate straight length of piping feeding into the suction.
There are safe operating ranges (both minimum and maximum flow) for all centrifugal pumps. Again, have you contacted the pump vendor ?
Are you sure that the pump was not repurposed from another installation ???
It's time to pay for an expert and accept the cost of a suction pipe
MJCronin
Sr. Process Engineer
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
As I said previous, for results of Impeller trimming. Let me say what is going on after trimming.
Actually, this 8 stage BFP pump impeller was trimmed about 2% diameter from 4th impeller to last 8th impeller except but 1st to 3rd. the results of this trimming was little bit good aganist before trimming, so Surging and hunting in Min. flow rage was disappear. and total discharge and flow as well was decreased as much as impeller trimming. however,
1) pump head at bleed line was increase where located at 3rd to 4th impeller.
2) Electric Current is hunting against before impeller trimming.
I guess that decreased circumference velocity(Dynamic Pressure) at 4th impeller turn into static pressure, finally this get increased bleed line head.
Are there any this kind of experience or how to explain this situation in pump theory, pls let me know.
I don't have any idea why current is hunting after trimming but flow and head is not hunting.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Dear ALL
Against my previous post, after trimming BFP Pump 4th to 8th as much as 2%, we are now facing another problems of Bleeding flowrate that decreased to 60m^3/h from 70m^3/h and discharge head to 50kg/cm^2 from 60kg/cm^2, Are there any idea for explanation why this bleeding flowrate was decreased. Actually, this BFP pump discharge head was decreased to 220 Kg/cm^2 from 240 Kg/cm^2.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Why not trying to change the pump speed rather than trimming impeller ?Most of our customers never trim impeller themselves.Not good for the service life.
Heavy-Duty Centrifugal Slurry Pump Manufacturer
www.gempump.com
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Can you get your story straight?
Post from 9th November "We got this BFP pump impeller trimming from 2nd impeller through 8th impeller leaving 1st impeller"
Post from 26 Nov "after trimming BFP Pump 4th to 8th as much as 2%.."
post of 19th Nov "pump head at bleed line was increase where located at 3rd to 4th impeller"
Post of 26th Nov "and discharge head to 50kg/cm^2 from 60kg/cm^2" i.e.decrease in pressure?
Now if the first one is correct, then your bleed after third impellor will reduce. but has it reduced?
This post is getting more confusing as time goes on rather than less....
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Dear ALL
During posting this issue, there was some changes, the correct one is follows.
1. Post from 26 Nov "after trimming BFP Pump 4th to 8th as much as 2%.."
2. Post of 26th Nov "and discharge head was decreased to 50kg/cm^2 from 60kg/cm^2".
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF
Suggest the OP reviews the complete story and edits all the data to come up with a coherent story on the actual problem and changes----alternately employ a competent engineer to undertake a thorough engineering study of the problem and make some fact based suggestions.
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BFP PUMP SERGING AND IMPELLER CUTTING-OFF