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Basics of Heat Exchangers

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Onset of Heat Exchangers The Plain Cylinder Boiler: The Scientific Development of HXs The Cornish Boiler The Scotch Boiler The Scientific Engineering !!!!! – PowerPoint PPT presentation

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Title: Basics of Heat Exchangers


1
Basics of Heat Exchangers
  • P M V Subbarao
  • Professor
  • Mechanical Engineering Department
  • I I T Delhi

The story of a First Thermodynamic Device?!?!?!
2
HEAT EXCHANGER
Human Need of Power is Responsible for Its
Innovation! Heat Exchanger Made Power Generation
Viable!!! A first Step towards Scientific
living Style A True Mediator !!!
3
Invention of FIRE, FLAME and TORCH
  • Fire is a discovery rather than an invention.
  • Homo erectus probably discovered fire by
    accident.
  • Fire was most likely given to man as a 'gift from
    the heavens' when a bolt of lightning struck a
    tree or a bush, suddenly starting it on fire.
  • The flaming touch and the campfire probably
    constituted early man's first use of 'artificial'
    lighting.
  • As early as 400,000 BC, fire was kindled in the
    caves of Peking man.
  • Prehistoric man, used primitive lamps to
    illuminate his cave.
  • Various Oils were used as fuels.

4
Sharing of Skills
5
The First Civilized Food Processing !!!!!
Fire Can only Heat Solids !!!!!
6
A Search for Ubuntu Device .
  • A generous, hospitable, friendly, caring and
    compassionate.
  • They share what they have/get/earn..
  • A person with ubuntu is open and available to
    others.
  • Various religions identified them as Mediators.
  • Business Mediators.
  • Energy Mediators A first step in Civilization
    and Development

7
EARLIEST TYPES OF HX COOKING
  • Primitive humans may first have savoured roast
    meat by chance, when the flesh of a beast killed
    in a forest fire was found to be more palatable
    and easier to chew and digest than the customary
    raw meat.
  • They probably did not deliberately cook food,
    though, until long after they had learned to use
    fire for light and warmth.
  • It has been speculated that Peking man roasted
    meats, but no clear evidence supports the theory.
  • During Palaeolithic Period, Aurignacian people of
    southern France apparantly began to steam their
    food over hot embers by wrapping it in wet
    leaves.
  • Crude procedures
  • as toasting wild grains on flat rocks and using
    shells, skulls,
  • or hollowed stones to heat liquids.
  • Introduction of pottery during the Neolithic
    Period.
  • A paste, toasted to crustiness when dropped on a
    hot stone, made the first bread.

8
  • Heat Exchangers Enhance the Utility of Fire .
  • Can they do so beyond stomach ????

9
The Aelopile
  • In 130BC. Hero, a Greek mathematician and
    scientist is credited with inventing the first
    practical application of steam power, the
    aelopile.

10
Branca's Steam Turbine
  • In 1629, Giovanni Branca, of the Italian town of
    Loretto, described, in a work' published at Rome,
    a number of ingenious contrivances.

11
The Savery Engine
Thomas Savery, July 2, 1698, patented the design
of the first engine which had the most important
advance in actual construction. A working model
was submitted to the Royal Society of London.
12

Newcomen Engine
The original Thomas Newcomen engine was invented
in 1712.
13
James Watts Engine
James Watt radically improved Newcomen's engine
(1769) by condensing the steam outside the
cylinder .
14
No Recognition to The Heat Exchanger !!!?!?!?
15
Onset of Heat Exchangers
The Plain Cylinder Boiler
16
The Scientific Development of HXs
The Cornish Boiler
17
The Scotch Boiler
18
The Scientific Engineering !!!!!!
19
Progress in Rankine Cycle
Year 1907 1919 1938 1950 1958 1959 1966 1973 1975
MW 5 20 30 60 120 200 500 660 1300
p,MPa 1.3 1.4 4.1 6.2 10.3 16.2 15.9 15.9 24.1
Th oC 260 316 454 482 538 566 566 565 538
Tr oC -- -- -- -- 538 538 566 565 538
FHW -- 2 3 4 6 6 7 8 8
Pc,kPa 13.5 5.1 4.5 3.4 3.7 3.7 4.4 5.4 5.1
h, -- 17 27.6 30.5 35.6 37.5 39.8 39.5 40
20
A Train of External HXs in A Power Plant
21
Consequence of An Internally Efficient Power Plant
22
Impact of Cycle Improvement on Capability of Fire
23
Stockholm 1920The Ljungström Air Preheater
24
(No Transcript)
25
Economic Impact of the Landmark
  • The use of a Ljungström Air Preheater in a modern
    power plant saves a considerable quantity of
    fuel.
  • So much that the cost of the preheater is
    generally recovered after only a few months.
  • It has been estimated that the total world-wide
    fuel savings resulting from all Ljungström Air
    Preheaters which have been in service is
    equivalent to 4,500,000,000 tons of oil.
  • An estimate shows that the Ljungström Air
    Preheaters in operation annually saves about 30
    Billion US.
  • The distribution of thermal power capacity in
    which Ljungström Air Preheaters are installed
    over the world is shown in the table below.

26
Heat Exchanger An Effective Landlord
  • Creates a housing for both donor and Receiver.
  • How to accommodate both in a single housing?
  • Space Sharing Time sharing
  • Space sharing Donor and Receiver are present
    always.
  • Develop partition(s) in the house(HX).
  • Time Sharing Donor And Mediator for sometime
    and Mediator and Receiver for sometime Repeat!
  • Central Limit Theorem It is impossible to have
    time and space sharing in one system.
  • Time Sharing Regenerators
  • Space Sharing Recuperators
  • Shell Tube HXs

27
Design Considerations for Heat Exchangers
  • When preparing to design a heat exchanger, do you
    ever wonder where to start? 
  • You've done it before, but you hate that feeling
    of getting half way through the design and
    realizing that you forgot to consider one
    important element. 
  • The thought process involved is just as important
    as the calculations involved. 
  • Let's try to map out a heat exchanger design
    strategy. 
  • We'll do so with a series of questions followed
    by information to help you answer the questions

28
Is there a phase change involved in my system?
  • A quick look at the boiling points compared with
    the entrance and exit temperatures will help you
    answer this question.

29
How many "zones" are involved in my system?
30
Various Simple Zones
31
What are the physical properties of the streams
involved?
  • Get the physical properties for each zone
    separately to ensure accuracy, but in some cases
    it is acceptable to use an average value.   
  • Physical properties that you will want to
    collect for each phase of each stream will
    include  heat capacity, viscosity, thermal
    conductivity, density, and latent heat (for phase
    changes). 
  • These are in addition to the boiling points of
    the streams at their respective pressures.

32
What are the allowable pressure drops and
velocities in the exchanger?
  • Pressure drops are very important in exchanger
    design (especially for gases). 
  • The pressure drop and velocities must be
    limited. 
  • The velocity is directly proportional to the heat
    transfer coefficient which is motivation to keep
    it high, while erosion and material limits are
    motivation to keep the velocity low. 
  • Typical liquid velocities are 1-3 m/s. 
  • Typical gas velocities are 15-30 m/s. 

33
What is the estimated area of the exchanger?
  • Unfortunately, this is where the real fun begins
    in heat exchanger design! 
  • You'll need to find estimates for the heat
    transfer coefficients that you'll be dealing
    with. 
  • Once you've estimated the overall heat transfer
    coefficient, use the equation Q UoADTlm to get
    your preliminary area estimate. 
  • Remember to use the above equation to get an area
    for each zone, then add them together.

34
What geometric configuration is right for my
exchanger?
  • Now that you have an area estimate, it's time to
    find a geometry that meets your needs. 
  • Once you've selected a shell diameter, tubesheet
    layout, baffle and tube spacing, etc., it's time
    to check your velocity and pressure drop
    requirements to see if they're being met. 
  • Experienced designers will usually combine these
    steps and actually obtain a tube size that meets
    the velocity and pressure drop requirements and
    then proceed. 
  • If your pressure drop requirements are low, avoid
    using four or more tube passes as this will
    drastically increase your pressure drop. 
  • Now you have a geometry selected that meets all
    of your needs.
  • Now that I have a geometry in mind, what is the
    actual overall heat transfer coefficient?
  • What is the actual area of the exchanger using
    the 'actual' heat transfer coefficient?
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