×
INTELLIGENT WORK FORUMS
FOR ENGINEERING PROFESSIONALS

Are you an
Engineering professional?
Join Eng-Tips Forums!
• Talk With Other Members
• Be Notified Of Responses
• Keyword Search
Favorite Forums
• Automated Signatures
• 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.

# NPSH and TDH

## NPSH and TDH

(OP)
There is a discussion between myself and another engineer as to the actual definition of TDH (total dynamic head), being the head condition that is specified to the pump manufacturer for the duty point.

Assume that this is a suction lift pump (so that both suction and discharge lifts are +), so it was my assumption that friction and minor losses and the suction lift were used for the NPSH calculation.  Then once it was determined that the NPSHr was met, then a sepetate dynamic discharge head is calculated also for static, friction and minor losses.  Now when spec-ing the pump, are the Suction and Discharge static + losses added to get the Total Dynamic Head OR do you use the Total Dynamic Discharge Head when specifying the duty point?  I assumed that the Suction calcs were only used for NPSH and not TDH.

### RE: NPSH and TDH

TDH=static head + friction loss + discharge pressure

static head = discharge elevation - suction elevation

### RE: NPSH and TDH

My understanding has always been that TDH stands for Total Discharge Head and is the total of the static head, friction head, and pressure heads.

static head = max. height of liquid being pumped (pump centerline to liquid level taking into consideration siphoning effects.

friction head = losses due to pipe and fitting resistance.

pressure head = any pressurized vessels on the discharge side of pump.

So as per my understanding the suction conditions do not apply to the pump manufacturers TDH value.

### RE: NPSH and TDH

(OP)
ok, thats 1 for Total Dynamic and 1 for Total Discharge! :D

I have thought the same as CPMech up until i was challenged recently and I could not prove it otherwise.  Text books show Total Dynamic Head, but as we all know, text book -> real world isn't always applicable.  Don't get me wrong, I understand what each of them are and what the difference is, but when you are writing a spec to a pump manufacturer, what do they need to get you the right pump?

Thanks for the input so far... anyone else with an opinion?

### RE: NPSH and TDH

A example in the book Cameron Hydraulic Data can give you good answer. Page 3-9.

For a suction lift, you have to add it to the TDH; for a suction level higher than the pump center line, you have to take away the suction head; for a suction level higher than discharge level, fluid can gravity flow...I guess everyone knows this.

### RE: NPSH and TDH

Best to leave it at TDH=Total Dynamic Head. This must include the "Suction" as well as the "Discharge" conditions in order to specify to a pump manufacturer the required duty. To me, "Total Discharge Head" is just referring to conditions on the discharge side of the pump.

The amount of Suction Head or Suction Lift obviously plays a part in the available NPSH, but is also a factor in the differential head that the pump has to accommodate.

### RE: NPSH and TDH

From the Pump Handbook by Karassik et al:

#### Quote:

Total Suction Lift ... exists where the total suction head is below the atmospheric pressure. ... is the reading of a liquid manometer or pressure gage at the suction nozzle of the pump, converted to feet (meters) of liquid, and referred to datum minus the velocity head at the point of gage attachement.

Total Suction Head... exists when it is above atmospheric pressure. ... is the reading of a gage at the suction of the pump, converted to feet (meters) of liquid and referred to datum plus the velocity head at the point of gage attachement.

Total Discharge Head... is the reading of a pressure gage at the discharge of the pump, converted to feet (meters) of liquid and referred to datum plus the velocity head at the point of gage attachement.

### RE: NPSH and TDH

(OP)
ok, just wanted to be sure... thanks for replying to such an amature question, but it clears up the uncertainty.  Thanks!

### RE: NPSH and TDH

Here's the way I have ALWAYS looked at it:

TDH = Total Dynamic Head. If you call it total discharge head, in a centrifugal pump you are by definition incorrectly inferring what’s going on at the discharge. You will be ignoring what energy is available (or not available) on the suction side of the pump, energy that does not need to be imparted by the pump to the system.

Another way to look at it is total "differential" head. That is, what does the PUMP have to impart to the system?  When you specify TDH, the pump manufacturer looks at it as if you already accounting for what's going on on the suction side.

No one has mentioned this, but that the above discussions apply to centrifugal pumps. Things are different for positive displacement pumps.

### RE: NPSH and TDH

"CPMech (Mechanical) 16 Feb 06 13:56
------------,
So as per my understanding the suction conditions do not apply to the pump manufacturers TDH value."

This is incorect, when a centrifugal pump is tested in accordance with test code, whether it is the US, European or other, the inlet conditions are also included it the HQ curve, as either an addition or a subtraction to the measured discharge head.

Quoting from Cameron:
" Total system head (H) - formally total dynamic head - is the total discharge head (hd) minus the total suction head(hs) if positive or plus if a suction lift: H = hd -hs (head)or H = hd+hs (lift). -------"

Naresuan University
Phitsanulok
Thailand

### RE: NPSH and TDH

I have seen pump data sheets with a simple sketch that defines each of the terms. This will remove all uncertainty when procuring a pump.

#### 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.

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:

• Talk To Other Members
• Notification Of Responses To Questions
• Favorite Forums One Click Access
• Keyword Search Of All Posts, And More...

Register now while it's still free!