being honest, i have never came across such a beautiful video on shell and tube HE design. thanksss sir
@chintanconcept
4 ай бұрын
Glad you liked it
@PramodShankar-b5m
2 күн бұрын
Very good explanation Sir! I am a chemical engineering student and it really helped me.
@chintanconcept
2 күн бұрын
Glad to hear that
@anilpal5947
4 ай бұрын
Most important video and understanding very clearly thanks sir
@chintanconcept
4 ай бұрын
Most welcome
@akashraval2532
11 ай бұрын
Very informative and excellent 👌💐
@abdultaiyebcyclewala6096
5 ай бұрын
I have never seen a video explaining STHE in such a simplified form❤
@chintanconcept
5 ай бұрын
Glad it was helpful!
@yondugaming4619
2 ай бұрын
Best video... explained very well ❤
@chintanconcept
2 ай бұрын
Glad you liked it
@diwakar_3321
2 ай бұрын
awesome video
@tapendukoley9942
9 ай бұрын
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
9 ай бұрын
Sure I will
@ilyaskhan56
3 ай бұрын
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 )
@krupalsinhrathod1359
4 ай бұрын
The way of explanation was good , but I still have a question that initally how can we decide the number of Tube side passages???
@gmrachit7964
Ай бұрын
Very Well Explained
@chintanconcept
28 күн бұрын
Keep watching
@sunnys5412
5 ай бұрын
Excellent...
@laaibakhurramqureshi3839
6 ай бұрын
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
6 ай бұрын
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
@ShubhamPatil-nv4oe
7 ай бұрын
best lecture sir
@RutujaByale
5 ай бұрын
Great sir. Thank you very much 🙏
@ShivamIT
3 ай бұрын
Sir paper mai agar Kern's method likhane ko aaye to yehi likhe usme?
@chintanconcept
3 ай бұрын
Yes, This is the kern’s method.
@preetrana2871
2 ай бұрын
Excellent video bhaiya. Can you make video for design of pressure vessel
@chintanconcept
2 ай бұрын
Yes I will
@owaiskhokar5228
6 ай бұрын
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
6 ай бұрын
Yes, that comes under mechanical designing.
@31-aniketjanbandhu2
2 ай бұрын
Sir best video
@dpd_edits_
7 ай бұрын
Sir in case of phase change which type calculation are coming?
@chintanconcept
7 ай бұрын
Equations will be different to calculate heat transfer coefficients ( Density of both phase will be included)
@aniketkambli9581
8 ай бұрын
Hii sir, How do you calculated inside tube dia(di)
@aniketkambli9581
8 ай бұрын
Which is 0.013 how it is come??
@HarshPatel-rl4uw
7 ай бұрын
@@aniketkambli9581part3 dekho....😊
@HarshPatel-rl4uw
7 ай бұрын
tube inside diameter kaha se aaya?
@selvakumar-uq3sm
2 ай бұрын
Sir every day i am watching your youtube channel for you added english subtitle or not
@chintanconcept
2 ай бұрын
sorry couldn’t
@anilpal5947
4 ай бұрын
Sir please upload for phase change, how will select heat exchanger
@Sqb1998
10 ай бұрын
Ammzing video.. Pls make video on pumps
@chintanconcept
10 ай бұрын
Regarding NPSH, performance already uploaded
@DHRUVPATEL-e6n
11 ай бұрын
exellent
@S.Rajput971
5 ай бұрын
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
5 ай бұрын
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
4 ай бұрын
@@chintanconcept Sir why you have not multiply 1000 m3/hr to get kg/hr?
@MuhammadAzeemKhan-vz8cq
4 ай бұрын
Sir any source to take out the value of Cp?
@S.Rajput971
5 ай бұрын
Can you please provide the ‘U’ value range for therminol D12
@chintanconcept
5 ай бұрын
The other fluid??
@chintanconcept
5 ай бұрын
You may start with 200-300 (If liquid liquid fluid there)
@rohitgawas3803
6 ай бұрын
Thank You bhaii❤
@sunilshar82
4 ай бұрын
Plz share mi Heat exchanger design calculation Excel sheet
@chintanconcept
4 ай бұрын
Will upload soon
@kunallichade9457
6 ай бұрын
What if TEMA dont have U value for my specific fluid
@chintanconcept
5 ай бұрын
Its a generalised value, like organic , inorganic, viscous fluid etc
@HopeScreen
7 ай бұрын
if u assume U, it means all the calculations are just skipped including Reynol, Nusselt, prandtel and dettius bolteir equations
@chintanconcept
7 ай бұрын
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
Ай бұрын
If you are here, means you forgot the above concept. So Better study😂
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