×
INTELLIGENT WORK FORUMS
FOR ENGINEERING PROFESSIONALS

Log In

Come Join Us!

Are you an
Engineering professional?
Join Eng-Tips Forums!
  • Talk With Other Members
  • Be Notified Of Responses
    To Your Posts
  • Keyword Search
  • One-Click Access To Your
    Favorite Forums
  • Automated Signatures
    On Your Posts
  • Best Of All, It's Free!

*Eng-Tips's functionality depends on members receiving e-mail. By joining you are opting in to receive e-mail.

Posting Guidelines

Promoting, selling, recruiting, coursework and thesis posting is forbidden.

Students Click Here

Sundyne Pump Impeller and Indecer damage

Sundyne Pump Impeller and Indecer damage

Sundyne Pump Impeller and Indecer damage

(OP)
Hi Everyone!
We have a sundyne pump at Crude Distillation Unit to inject stripped water to desalters.. The pump was opened due to seal leakage issues. Internal Inspection revealed damage to impeller and Inducer.
Following are the process conditions
Serive : Stripped Water
pH : 10.5 to 11.0 on average
Rated Flow: 37 m3/h
Suction Presssure : ~ 0.5 kg/cm2.G
Discharge Pressure : 31 kg/cm2
Flow variation: 15 ~ 38 m3/h
Normal Flow : 32 m3/h
Design Minimum Flow : 7.2 m3/h
Stripped Water Temp : 65 ~ 70 C ( Temperature remained 80 ~ 85 C for 4 to 5 months as well)
Material of Impeller : ss316L
Pictures are attached for reference.
Can anyone help me sort out the root cause of the problem and remedial actions:

http://files.engineering.com/getfile.aspx?folder=9...

Abdul Rauf
Replies continue below

Recommended for you

RE: Sundyne Pump Impeller and Indecer damage

problem of cavitation, NPSHa is too low

RE: Sundyne Pump Impeller and Indecer damage

Is all of the damage at the eye?

= = = = = = = = = = = = = = = = = = = =
P.E. Metallurgy, Plymouth Tube

RE: Sundyne Pump Impeller and Indecer damage

It could be also a too low flow with inlet recirculation

RE: Sundyne Pump Impeller and Indecer damage

(OP)
Dear EdStainless,
Yes, all the damage is at eye. The edges of the inducer have some material loss as well.
I have checked the flow history of the pump. The flow varied from 17 to 38 m3/h with normally @ 27 ~ 30 m3/h. Average pH of the fluid ~10.8. This pump has a history of seal leakage.

Abdul Rauf

RE: Sundyne Pump Impeller and Indecer damage

NPSH curve with an inducer increases at high AND at low flows. Check the curve NPSHR against NPSHA at 17 m3/hr, could be insufficient NPSHA there. Obviously could be a problem at 38 m3/hr also.

RE: Sundyne Pump Impeller and Indecer damage

What is "stripped water"?

Does it have a vapour pressure higher than normal water?

At the moment it looks like cavitation damage.

Remember - More details = better answers
Also: If you get a response it's polite to respond to it.

Red Flag This Post

Please let us know here why this post is inappropriate. Reasons such as off-topic, duplicates, flames, illegal, vulgar, or students posting their homework.

Red Flag Submitted

Thank you for helping keep Eng-Tips Forums free from inappropriate posts.
The Eng-Tips staff will check this out and take appropriate action.

Reply To This Thread

Posting in the Eng-Tips forums is a member-only feature.

Click Here to join Eng-Tips and talk with other members! Already a Member? Login



News


Close Box

Join Eng-Tips® Today!

Join your peers on the Internet's largest technical engineering professional community.
It's easy to join and it's free.

Here's Why Members Love Eng-Tips Forums:

Register now while it's still free!

Already a member? Close this window and log in.

Join Us             Close