Video

Very nice explained sir . Sir , please cover 1 numerical example. Also requesting you to plz upload video on p&Id loops / Arrangement for heat exchanger, pumps , etc

Hello, can you please share the excel sheet..

Which size of tube to be considered in HE calculations?? In every HE designed

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Good

Sir do you offer online course on Process engineering?

Really good video

Sir can I send excel sheet...

Thanks for the wonderful lecture series. It would be helpful if you could make videos on absorption column, ideal L/G ratios etc.

How to know we have to use steam ejector or vaccum pump?

Hii...Thankyu for your initiative...can I get excel?

Cam please make a video in english it is very useful for so many peoples Please do the needful

Thanks a lot for the information But I think in line losses : K Value method formula should be f(L/D+Sigma*K)v2/2g...Bracket is missing

Appreciate 👍🙏

best video....❤ thank you sir.

In case of wetted pool fire in eg of column if reboiler is isolated and if it falls in range of 7.5 m then it is also to be considered for PSV, like in our case there is thermosyphon reboiler there is no isolation valve so it's area along with column wetted area both to be consider or two different PSV one on column and one on reboiler to be consider pls justify.... Point no 2 for column there is a feed pump and if there is a fire then from discharge valve which is now isolated then the length to the column immediate flange, line hold up how it is to be consider for PSV design.

Bro Is there any paid course for p and Id Also with autocad p and Id I will pay for that sir Please reply

Thanks sir.... Pls cover topics in upcoming lecture regarding HTU,NTU and HETP concept

Thank you 👍

what is your age

thanks sir for such knowledgeable videos. you teach us like Bhaiya not a sir. have a small request please make videos about bottling and filling machine design in mainly beverage and beer plants , working principle in detail as you teach other videos.

Sir please upload your presentation slides on your linkdin profile. I already told you and also you said that you will. I requesting you sir please upload.

Sir pressure drop sathi Moody friction factor cha formula kay ahe in case of two phase flow?

Very well explained, truly like explaining to small kid without skipping basic concepts...keep it up...

Please make a video on the heat exchanger design in an Excel sheet. Or if any video is already available then share the link with me.

Very nice sir ji

Please share the excel sheet

Make video on Double pipe heat exchanger

Please make a video on Cause and Effect Matrix

understanding is excellent, but at the end, please share an Excel sheet for ease of calculation

Thank you so much sir.. So informative

Sir steam condensate temp. Decrease ... Why condensate temp. Is 100 degrees write sir..

Hello, thank you for such a wonderful video. Regarding MAWP @14:12 you explained its defination by saying that from operating pressure we take design pressure and from the thickness obtained from designed pressure by taking the next upper standard thickness, the pressure at this standard thickness is MAWP. (part -1) If this is the case then @38:25, you are explaining about the Hydrotest which should be 1.5x of MAWP and equipment can withstand upto 4-5 x MAWP. (part-2) isn't it contradictory? The equiment should fail at (part-1 pressure already).

Nice explanation dear sir😊😊

Nice explanation dear sir😊😊

Sir HHLL and TTL seems to be matching .... Between HHLL and TTL there should be again 300 mm Gap? Then where should be Overflow nozzle ?

Also sir want you to make video on thermal calculations for plate heat exchanger

Hi Sir , Your videos are very helpful, Can you please share API 650 criteria also excel sheet for vessel sizing , Heat exchanger sizing and line sizing

Please share this sheet

Sir at 19:41 the formula for converting pressure to head should be (deltaP *10.2) / S.G. Correct me if I'm wrong

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Good❤

I watched a lot of distillation video but from the application POV you are great sir

P&ID part 7 link please

Yes

Excellent work Could you please make videos on PID tuning Thanks

Shut off head formula varies in excel and initial explanation of formulas .. In excel shut iff head = max suction pressure * 1.25 + diff pressure While at initial explantion Max shut off head = max suction pressure + (1.25 * diff head) Can u pls give the crct ans

Thank you 🙏

Sir please make video on mass and heat balance in process engineering

sir Please share the PPT