Flow HT208 People associated with the expt. Instructor Prof. - - PowerPoint PPT Presentation

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Flow HT208 People associated with the expt. Instructor Prof. - - PowerPoint PPT Presentation

Heat Transfer in Laminar Flow HT208 People associated with the expt. Instructor Prof. Jayesh Bellare Teaching Assistants Satpute Kushal Dadasaheb Sudip Kumar Das Praveen Nayak Laboratory Staff Member Mr. S. V.


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SLIDE 1

Heat Transfer in Laminar Flow

HT208

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SLIDE 2

People associated with the expt.

  • Instructor
  • Prof. Jayesh Bellare
  • Teaching Assistants
  • Satpute Kushal Dadasaheb
  • Sudip Kumar Das
  • Praveen Nayak
  • Laboratory Staff Member
  • Mr. S. V. Deshpande
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SLIDE 3

Objective

For laminar flow heat transfer

  • Determination of the overall heat transfer

coefficient using logarithmic mean temperature difference

  • Calculation for the individual film heat transfer

coefficient

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SLIDE 4

Principle

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SLIDE 5

Background Theory

With respect to the inside area Sieder-Tate equation

Nu = 1.86 x (Re)1/3(Pr)1/3

h = const. x u1/3 1 𝑉𝑗 1 𝑣1/3

= Constant1 x + Constant2

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SLIDE 6

Set up

Flow regulator Calibrated cylinder Heater Pumps Heat exchanger Rotameter

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SLIDE 7

Experimental Procedure

  • 1. Start up circulating pumps for both hot and cold fluid
  • 2. Switch on the heater for heating up the hot fluid
  • 3. Steady state reached:
  • Note hot fluid and cold fluid inlet and outlet temperature
  • Measure volumetric flow rate of hot fluid (laminar flow regime)
  • 4. Change volumetric flow rate of hot fluid keeping other

parameter unchanged

  • 5. Repeate step no. 3
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SLIDE 8

Data collection

  • From experiment
  • Cold fluid volumetric flow rate (fixed)
  • Cold fluid inlet and outlet temperature
  • Hot fluid volumetric flow rate (manipulated variable)
  • Hot fluid inlet and outlet temperature
  • From literature
  • Density of cold fluid at 30OC
  • Density, viscosity, thermal conductivity and heat capacity of hot

fluid at 65OC

  • Supplied
  • Dimensions of heat exchanger, tubes
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SLIDE 9

Calculation

Q = V x ρ x Cp x (T1-T2) LMTD = 𝑈1 − 𝑢1 − (𝑈2 − 𝑢2) ln⁡ * 𝑈1 − 𝑢1 /(𝑈2 − 𝑢2)+ U =

𝑅 𝐵Δ𝑈𝑚𝑜

1/U 1/u1/3 Wilson Plot for Laminar flow heat transfer

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SLIDE 10

Safety issue

  • Careful during volumetric

flow rate measurement of hot fluid

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SLIDE 11

THANK YOU