Very informative thank you bro for this one

Well explained ❤

This isn't teaching. It is reading a lesson. Anyone thinking this is good material doesn't get out enough. Take a look at the views and the number of comments.

Please Vapor head we add to the NPSH available or the Required !!? Because all people add to the availabe and you add to required sir ?!

This is GOLD

I think you wrongly explained about the Total Suction Head.

How can I get the note in PDF

Hi you! Do you know that NPSHa Booster pums ??? thanks!

How to handle a higher static head before final destination point

It is very helpful. thank you.

At 4:55 why you added the friction head loss, it should be minus

great knowledge

Thank you so much

Thank you so much

Sir, I cant understand still, why the total static discharge head is 5mtr. Why not 5+5.5 = 10.5mtr as the water is lifted upto top of the pipe turned. Please explain. ( duration 4.50 in the video )

Excelent video for teaching about pumps, very helpful to me, congratulations...!!!

Brilliant tutorial..

A slight mistake in final calculation because the static pressure was 150 kpa instead of 90 kpa. 90 was the temp in celcius.🤓🤓✌

Great video. Thank you Terry

İ wish my lecturers teach us like Terry.thx for lesson

NO confusion left, great knowledge

At 8: 50 the minimum operating suction pressure required is 377 kpa