Part 4: System curve and pump performance curve of centrifugal pump

[@anupghosh1627]

Sandeepji you are truly contributing to engineering fraternity.

[@sachinkabadi9975]

Sandeepji... you are doing a great thing.... God bless you

[@dhavalpatel6707]

Very good explaination with real practical example👌. Thank you for the valuable information👏👏

[@MultiTanmoy]

You have explained it very well..thank you

[@rajeshdsouza5809]

Sandeep! Thank you so much for the presentation.

[@shilpikainth9640]

awesome explanation . great work

[@ismileali2089]

Thank u sir , plzz esey hi practical videos banate rehna

[@hadeedahmed7693]

Is this for CENTRIFUGAL COMPREESOR ALSO?

[@najmulhassanofficial3104]

Great sir..kindly also start a series lectures on furnace and plant control syatema

[@kuldeep836]

Very good explanation.

[@kuldeep836]

I would like to request please make such videos in English, so that other countries engineer can also understand.

[@hadeedahmed7693]

is this for CENTRIFUGAL COMPREESOR ALSO??????

[@061shubham7]

No

[@gatechemicalengineering4920]

Very Informative Video Thank you Sir

[@santhoshkumar3863]

Hello sir , your content was great pls upload video on pump curve explanation in english for better understanding for non hindi speaking people.

[@anilpal5947]

Sir , control valve suction me lga hai ki discharge me

[@k.t.p2958]

Sir , you have posted centrifugal comp performance derivation related video

[@mareibelgasim1656]

Good job bro

[@aniketagrawal589]

Hello Sir, What to do if more viscous fluid is to be used in centrifugal pump? (like we should open control valve?)

[@ravikumar-ys6ig]

Sir, please make a video on cooling tower for Interview purpose 🙏🙏

[@adityabansod8493]

At 6.40, as you mentioned in this video, if we increase the operating pressure of the source tank (let's say by supplying more fuel gas), while keeping the level control valve opening the same (30%), we change the system curve and get more flow (since total differential head requirement is less). Does this mean the normal operating level in the source tank will decrease (assuming inlet flow the facility is the same?).

[@SandeepAcademy9]

Yes,

[@karunasharma262]

Sir we install a new ethanol Pump in our company n it was not working properly it was making air now we maintain its discharge pressure 4-4.2 while pump head is 50m but the flow rate is only 17cumeter while the given flow rate is 60 why it is so?

[@RAHULKUMAR-dd6vk]

Guru ji mai Gujarat refinery me job karata hu. ACPS exam.me instrument and control se bahut question puchta hai. Example First order second order. P,PI,PID controller .Plz iska bhi lecture series chala dijiye sir. U tube per or video hai per samajh nahi nahi ata hai. Apka teaching style bahut acha hai.

[@RAHULKUMAR-dd6vk]

Interview me kam se three question instrument and control se pucha jata hai.

[@SandeepAcademy9]

Bhai topic bahut hai....aur time kam milta hai..... guarantee to nahi de sakte....par try karenge...

[@AbhishekGupta-sc1ct]

Why we can't operate the pump before the point of intersection of system curve and characteristic curve ?

[@bipulkumarpaul4324]

sir wet bulb temperature and adiabatic saturation temperature me kya difference hota hai

[@upendrarauta3749]

Mera plant me ek same is type ka tripping issue horah hai, to me kya karu?? Please suggest me...

[@SandeepAcademy9]

To aap discuss kijiye apne senior se is option ke baare me

[@souravtomar9013]

Sir operating point ke baad agar pump operate krte h jiska discharge operating point se jyada. Plz explain

[@SandeepAcademy9]

Could not understand your question.

[@souravtomar9013]

@@SandeepAcademy9 Sir agar characteristics curve m discharge operating point se jyada hoga & Havailable below h Hrequired curve pe. Uss time pe pump work krega? Issi ka explanation chhaiye sir

[@SandeepAcademy9]

Jaha pe H available ....H required ke barabar hoga....wahi to operating point hoga....Mujhe abhi bhi question samjh me nahi aaya

[@vivekfaldu]

Sir, Plz make video on centrifugal compressor characteristica curve

[@AK-qo6vw]

Then why do we operate with partially opened valve?

[@shivanshutewari4415]

Make video on DCS

[@ashitosh.k.from_IITM]

Why system curve doesn't start from zero, even at zero Flow rate

[@Wd-zb5hq]

Sir Heat transfer ke BARC based questions par video banado please

[@sajjadanwar4590]

👍🏻

[@alokpatel325]

Nuclear fuel complex ke question batao sir chemical dipolma kis types ke aate h

[@ramakrishnan6913]

Last explanation on impeller trimming is not clear.

[@dataking3784]

Aapko dam hai kai, kitne saas nikalte ho!!!

[@apnikisani.up65]

Hmko to kuchh samjh nhi aaya

[@hadeedahmed7693]

Is this for CENTRIFUGAL COMPREESOR ALSO?

[@hadeedahmed7693]

Is this for CENTRIFUGAL COMPREESOR ALSO?

[@hadeedahmed7693]

Is this for CENTRIFUGAL COMPREESOR ALSO?