Part-1: Shell & Tube Heat Exchanger design with Example, Shell dia.& tube bundle dia., No of tubes

[@halynoor2882]

very very nice lecture😇😇

[@sudeeppathak108]

being honest, i have never came across such a beautiful video on shell and tube HE design. thanksss sir

[@chintanconcept]

Glad you liked it

[@akashraval2532]

Very informative and excellent 👌💐

[@anilpal5947]

Most important video and understanding very clearly thanks sir

[@chintanconcept]

Most welcome

[@hariharanradhakrishnan2366]

thank you brother, very useful, keep posting🤝

[@yondugaming4619]

Best video... explained very well ❤

[@chintanconcept]

Glad you liked it

[@diwakar_3321]

awesome video

[@abdultaiyebcyclewala6096]

I have never seen a video explaining STHE in such a simplified form❤

[@chintanconcept]

Glad it was helpful!

[@tapendukoley9942]

I am very impressed to getting such informative videos.kindly make some videos over Chemical batch reactor (SSR or glr) design , accessories, performance etc .And Thermopac heater / boiler . Thank you

[@chintanconcept]

Sure I will

[@hariharanradhakrishnan2366]

very helpful,, please explain about designing of distributors and significance of distributors in S&T HE

[@PramodShankar-b5m]

Very good explanation Sir! I am a chemical engineering student and it really helped me.

[@chintanconcept]

Glad to hear that

[@ShubhamPatil-nv4oe]

best lecture sir

[@gmrachit7964]

Very Well Explained

[@chintanconcept]

Keep watching

[@DHRUVPATEL-e6n]

exellent

[@31-aniketjanbandhu2]

Sir best video

[@sunnys5412]

Excellent...

[@RutujaByale]

Great sir. Thank you very much 🙏

[@GowthamKulal-v9m]

Bro how to do thermal analysis for this heat exchanger

[@ilyaskhan56]

Loved it. Amazing work. For improvement, can u add reference to where can we find the relevant graphs and tables used in the video. Referring to LMTD correction factor graph and Heat Transfer Coefficient Tables ( U )

[@preetrana2871]

Excellent video bhaiya. Can you make video for design of pressure vessel

[@chintanconcept]

Yes I will

[@aniketkambli9581]

Hii sir, How do you calculated inside tube dia(di)

[@aniketkambli9581]

Which is 0.013 how it is come??

[@HarshPatel-rl4uw]

​@@aniketkambli9581part3 dekho....😊

[@HarshPatel-rl4uw]

tube inside diameter kaha se aaya?

[@Sqb1998]

Ammzing video.. Pls make video on pumps

[@chintanconcept]

Regarding NPSH, performance already uploaded

[@krupalsinhrathod1359]

The way of explanation was good , but I still have a question that initally how can we decide the number of Tube side passages???

[@anilpal5947]

Sir please upload for phase change, how will select heat exchanger

[@ShivamIT]

Sir paper mai agar Kern's method likhane ko aaye to yehi likhe usme?

[@chintanconcept]

Yes, This is the kern’s method.

[@dpd_edits_]

Sir in case of phase change which type calculation are coming?

[@chintanconcept]

Equations will be different to calculate heat transfer coefficients ( Density of both phase will be included)

[@laaibakhurramqureshi3839]

Sir i want to bring down the temperature of my syngas from 800°C to 500°C. What approached should I use and tell me if it is practical to bring temperature this much down?

[@chintanconcept]

of course it is possible… many options there use of heat exchangers using cold stream on other side, integration approach with heat integration and many more

[@S.Rajput971]

Can you please provide the ‘U’ value range for therminol D12

[@chintanconcept]

The other fluid??

[@chintanconcept]

You may start with 200-300 (If liquid liquid fluid there)

[@owaiskhokar5228]

Hello, nice video. My question is, is there any relation, that we can relate weight of the heat exchanger with the surface area (may be after calculating shell dia?

[@ChintanModi-v6u]

Yes, that comes under mechanical designing.

[@rohitgawas3803]

Thank You bhaii❤

[@S.Rajput971]

Flow-7.5kg/s, specific heat-0.604, and delta 20 then how you calculated heat duty 279kw. As per my calculation it’s 90kw only

[@chintanconcept]

Thanks for watching the video cautiously. But yes may b you're making a small mistake somewhere. Flowrate conversion : 450 L/m --->27 m3/hr ---> 23463 kg/hr ---> 6.5175 kg/s Cp : 2.1413 Kj/kg C Del T : 20 Q = m Cp Del T= 297 KW Hope this will help, let me know if still any confusion there.

[@MuhammadAzeemKhan-vz8cq]

@@chintanconcept Sir why you have not multiply 1000 m3/hr to get kg/hr?

[@MuhammadAzeemKhan-vz8cq]

Sir any source to take out the value of Cp?

[@selvakumar-uq3sm]

Sir every day i am watching your youtube channel for you added english subtitle or not

[@chintanconcept]

sorry couldn’t

[@sunilshar82]

Plz share mi Heat exchanger design calculation Excel sheet

[@chintanconcept]

Will upload soon

[@HopeScreen]

if u assume U, it means all the calculations are just skipped including Reynol, Nusselt, prandtel and dettius bolteir equations

[@chintanconcept]

No, If I will not assume U, Then how we gonna calculate available area, no pf tubes. Base on no of tube we calculate shell diameter Shell diameter is used in baffle spacing calculation and many more calculations are dependent on that. Basically this kern’s method is trail & error method.. Its not the straight forward method Hope that clears ur doubt

[@yudhveersingh1615]

If you are here, means you forgot the above concept. So Better study😂

[@kunallichade9457]

What if TEMA dont have U value for my specific fluid

[@chintanconcept]

Its a generalised value, like organic , inorganic, viscous fluid etc