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

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  • Опубликовано: 24 дек 2024

Комментарии • 60

  • @akashraval2532
    @akashraval2532 Год назад +1

    Very informative and excellent 👌💐

  • @sudeeppathak108
    @sudeeppathak108 6 месяцев назад +3

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

  • @anilpal5947
    @anilpal5947 6 месяцев назад +2

    Most important video and understanding very clearly thanks sir

  • @hariharanradhakrishnan2366
    @hariharanradhakrishnan2366 28 дней назад

    thank you brother, very useful, keep posting🤝

  • @yondugaming4619
    @yondugaming4619 4 месяца назад +2

    Best video... explained very well ❤

  • @diwakar_3321
    @diwakar_3321 4 месяца назад

    awesome video

  • @abdultaiyebcyclewala6096
    @abdultaiyebcyclewala6096 8 месяцев назад

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

  • @ShubhamPatil-nv4oe
    @ShubhamPatil-nv4oe 10 месяцев назад

    best lecture sir

  • @sunnys5412
    @sunnys5412 7 месяцев назад

    Excellent...

  • @gmrachit7964
    @gmrachit7964 3 месяца назад

    Very Well Explained

  • @RutujaByale
    @RutujaByale 7 месяцев назад

    Great sir. Thank you very much 🙏

  • @PramodShankar-b5m
    @PramodShankar-b5m 2 месяца назад

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

  • @31-aniketjanbandhu2
    @31-aniketjanbandhu2 5 месяцев назад

    Sir best video

  • @tapendukoley9942
    @tapendukoley9942 11 месяцев назад +1

    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

  • @DHRUVPATEL-e6n
    @DHRUVPATEL-e6n Год назад

    exellent

  • @hariharanradhakrishnan2366
    @hariharanradhakrishnan2366 28 дней назад

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

  • @Sqb1998
    @Sqb1998 Год назад

    Ammzing video..
    Pls make video on pumps

    • @chintanconcept
      @chintanconcept  Год назад

      Regarding NPSH, performance already uploaded

  • @ilyaskhan56
    @ilyaskhan56 5 месяцев назад

    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 )

  • @rohitgawas3803
    @rohitgawas3803 9 месяцев назад

    Thank You bhaii❤

  • @preetrana2871
    @preetrana2871 4 месяца назад +1

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

  • @krupalsinhrathod1359
    @krupalsinhrathod1359 6 месяцев назад

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

  • @aniketkambli9581
    @aniketkambli9581 10 месяцев назад +1

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

  • @GowthamKulal-v9m
    @GowthamKulal-v9m Месяц назад

    Bro how to do thermal analysis for this heat exchanger

  • @ShivamIT
    @ShivamIT 6 месяцев назад

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

  • @anilpal5947
    @anilpal5947 6 месяцев назад

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

  • @dpd_edits_
    @dpd_edits_ 9 месяцев назад

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

    • @chintanconcept
      @chintanconcept  9 месяцев назад

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

  • @owaiskhokar5228
    @owaiskhokar5228 8 месяцев назад

    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
      @ChintanModi-v6u 8 месяцев назад

      Yes, that comes under mechanical designing.

  • @laaibakhurramqureshi3839
    @laaibakhurramqureshi3839 8 месяцев назад

    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
      @chintanconcept  8 месяцев назад

      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

  • @selvakumar-uq3sm
    @selvakumar-uq3sm 5 месяцев назад

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

  • @S.Rajput971
    @S.Rajput971 7 месяцев назад

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

    • @chintanconcept
      @chintanconcept  7 месяцев назад

      The other fluid??

    • @chintanconcept
      @chintanconcept  7 месяцев назад

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

  • @S.Rajput971
    @S.Rajput971 7 месяцев назад

    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
      @chintanconcept  7 месяцев назад +1

      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
      @MuhammadAzeemKhan-vz8cq 7 месяцев назад

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

    • @MuhammadAzeemKhan-vz8cq
      @MuhammadAzeemKhan-vz8cq 7 месяцев назад

      Sir any source to take out the value of Cp?

  • @sunilshar82
    @sunilshar82 6 месяцев назад

    Plz share mi Heat exchanger design calculation Excel sheet

  • @HopeScreen
    @HopeScreen 9 месяцев назад

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

    • @chintanconcept
      @chintanconcept  9 месяцев назад +1

      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
      @yudhveersingh1615 3 месяца назад

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

  • @kunallichade9457
    @kunallichade9457 8 месяцев назад

    What if TEMA dont have U value for my specific fluid

    • @chintanconcept
      @chintanconcept  8 месяцев назад

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