Monday, September 30, 2019

Types of Heat Exchangers and their Applications

Heat Exchanger

  • A device that facilitate the exchange of heat between two fluids that are at different temperatures 

Applications of Heat Exchangers

  • Chemical reactors (Jackets)
  •  Preheating feeds
  • Reboilers (Distillation column)
  • Condensers (Distillation column)
  • Air heaters for driers
  • Crystallisers
  • Heat transfer fluids 

Types of Heat Exchangers

Types of heat exchangers
Direct /Indirect Contact Heat Exchanger

Direct contact heat exchanger:

  o   Two fluids are not separated

  • Gas bubbled through the liquid
  • Liquid sprayed in the forms of droplets into the gas

Indirect contact heat exchanger:

  o   Two fluids are separated

  o   Heat transfer through the metal surface from one fluid to another 


Parallel /Counter/Cross Flow Heat Exchanger

Parallel Flow:

Both the hot & cold fluids enter the heat exchanger at the same end and move in the same direction

Counter Flow:

Hot and cold fluids enter the heat exchanger at opposite ends and flow in opposite directions

Cross Flow:

Hot and cold fluids usually move perpendicular to each other 


Double Pipe Heat Exchanger

One fluid flows through the smaller pipe

Other flows through the annular apace

Advantages:

  o   Simplest and Cheapest

  o   Used for high pressure applications

Disadvantages:

  o   Expensive for large duties

  o   Can’t be used in handling dirty fluids

  o   (Choking problem)(Used for only clean fluids)

Applications:

  o   Effluent cooling

  o   Pre heating

  o   Heat recovery 


Compact Heat Exchanger

  • Thin plates or corrugated fins are attached closely spaced to walls separating two fluids
  •  Commonly used in gas-gas and gas-liquid

Advantages:

    o   Large heat transfer surface area per unit volume

    o   Increase the H.T.C. of gas with increase surface area

    o   Lower cost

Disadvantages:

    o   Limited choice for high pressure

    o   Small passages likely to foul

Applications:

  o   Oil / water coolers

  o   Water / water coolers

     o   Condensers and evaporators 


Shell & Tube Heat Exchanger

Advantages:

o   Extremely flexible & robust design

o   Easy to maintain & repair

o   Dismantled for cleaning

Disadvantages:

o   Relatively large size & weight

o   Not suitable for automotive & aircraft

Applications:

o   Petrochemical: Processing & Refining

o   Food & Beverage

o   Metals and Mining

o   Pharmaceuticals 


Plate & Frame Heat Exchanger

  • Hot & Cold fluids flow in alternate passages
  • Suited for liquid-to-liquid heat exchange
  • Hot & cold fluid streams at about same pressure

Advantages:

  o   Effective heat transfer (turbulence on both sides)

  o   Low cost because plates are thin

  o   Can easily be opened up for inspection and cleaning

  o   Less fouling

Disadvantages:

o   Gaskets may not be suitable for organic solvents

o   Usually not considered for refinery duties (Cannot withstand prolonged fire)

Applications:

o   Ethanol and Corn Processing

o   Industrial Energy

o   Power Plants

o   Food & Beverage 


Regenerative Heat Exchanger

Static type:

o    Hot & cold fluid flow through the mass alternatively

o    Heat transferred from hot fluid to the matrix

o    Heat transferred from matrix to the cold fluid

Dynamic type:

  •  Rotating drum & continuous flow of hot & cold fluid
  •  Periodic passing of drum through:
Regenerative heat exchanger
  • Drum serves as medium to transport of heat

Advantages:

  o   Simple design

  o   Porous mass having large heat storage capacity

Disadvantages:

  o   Mixing of the fluid streams (separation problem)

  o   Constant heating and cooling puts a lot of stress cause cracking or breakdown of materials

Applications:

  o   Heat recovery from exhaust gases

  o   Air conditioning applications

  o   In food industry

  o   Temperature control of sewage sludge 


Spiral Heat Exchanger

Composed of two concentric spiral channels

Advantages:

  o   Applied where fouling and plugging are problems

  o   Ease of maintenance

Disadvantages:

  o   Higher initial cost

  o   Maximum design temperature is 400oC (Special designs: operate up to 850oC)

  o   Maximum design pressure is usually 15 bar (Special designs with pressures up to 30 bar

Applications:

  o   Food industry

  o   TiCl4 cooling

  o   PVC slurry duties

  o   Oleum processing

  o   Temperature control of sewage sludge 


Fouling of Heat Exchanger

  • Deposition of undesirable substance on the heat transfer surfaces.
  • Increases the overall thermal resistance and lowers the overall heat transfer coefficient of heat exchangers.
  • Impedes fluid flow, accelerates corrosion and increases pressure drop across the heat exchanger
  • Strangely more heat exchangers are opened for cleaning due to excessive pressure drop than for an inability to meet the heat transfer requirement. 

References

1.         Cengel, Y. A. Heat Transfer: A  Practical Approach, 2nd Edition, McGraw-Hill.

2.         Bergman, T. L.; Lavine, A. S.; Incropera, F. P.; DeWitt, D. P. Fundamentals of Heat and Mass Transfer, Seventh Edition, Wiley.

3.         J. P. Holman, Heat Transfer. Sixth Edition, McGraw-Hill Book Company.

4.         McCabe W. L.; Smith, J. C.; Harriott, P. Unit Operations of Chemical Engineering. Fifth Edition, McGraw-Hill International Editions.


Related article:

Friday, September 27, 2019

Chemical Engineering Equations

Expression of Rate of Heat Flow Through a Composite Wall

This expression is used for calculating the rate of heat flow through the series of resistances. Here the rate is calculated as the ratio of overall temperature difference to the overall resistance of the wall. 

Composite Wall


Expression of Rate of Heat Flow Through a Composite Cylinder

This expression is used for calculating the heat flow through a composite cylinder. Here the heat transfer area depends on the radius or the radial position.

 

Composite Cylinder


Expression of Rate of Heat Flow Through a Composite Sphere

This expression is used for calculating the rate of heat flow through a composite sphere.

 

Composite Sphere


Expression for Logarithmic Mean Temperature Difference

Logarithmic Mean Temperature Difference (LMTD) is used to determine the driving force (temperature difference) for heat transfer in flow system; especially it is used for heat exchanger. However, it should not be used when overall heat transfer coefficient (U) changes appreciably or when temperature difference (ΔT) is not a linear function of q. The expression of LMTD can be written as 

Logarithmic Mean Temperature Difference/LMTD


Expression of Overall Heat Transfer Coefficient

For calculating the rate of heat transfer in case heat transfer from one fluid to another separated by a plane solid wall, overall heat transfer coefficient is important. The expression of overall heat transfer coefficient in such case can be written as 

Overall Heat Transfer Coefficient


Expression of Overall Heat Transfer Coefficient for the Heat Transfer in a Cylindrical Geometry

As a cylindrical geometry we can consider heat transfer from one fluid phase to another in the double-pipe heat exchanger. It consists of two concentric pipes properly fitted or welded with arrangements for pumping one of the fluids through the inner pipe and the other through the annular space. The fluids are thus brought in thermal contact in order to achieve the heat transfer.

 The overall heat transfer coefficient Ui based on the inside surface area

Overall Heat Transfer Coefficient

Overall heat transfer coefficient U0 based on the outside surface area

Overall Heat Transfer Coefficient


Where, ri and ro are the inner and outer radii of the inner pipe

      hi and ho are the heat transfer coefficients of the inner and outer side of the pipe

      kw is the thermal conductivity of the material of the pipe wall

 

Reference:

1.   Heat Transfer Principles and Applications, by Binay K. Dutta

2. Unit operations of Chemical Engineering, 6th edition, by Warren L. McCabe, Julian C.                Smith, and Peter Harriott.



Related article:

Tuesday, September 24, 2019

Chemical Engineering Equations

Kozeny - Carman equation

This equation is used for calculating pressure drop for flow through packed beds. The equation is valid for the particle Reynolds number up to about 1.0. 

Kozeny - Carman equation


Burke – Plummer equation

This equation is applied for calculating pressure drop in packed beds at high Reynolds number (Rep > 1000). 

Burke – Plummer equation


Ergun equation

The Ergun equation is applicable for entire range of flow rates in flow through packed bed. Here the viscous losses and the kinetic losses are assumed to be additive.

Ergun equation


Expression for NPSH

To avoid cavitation in pump, the pressure in the pump inlet must exceed the vapour pressure by a certain value, called the net positive suction head (NPSH). The equation of NPSH can be written as 

Expression for NPSH


Expression for volumetric flow rate in venturi meter

The volumetric flow rate through the venturi meter can be written by the expression

 

venturi meter


Expression for volumetric flow rate in orifice meter

The volumetric flow rate through a orifice meter can be written as

 

orifice meter


Expression for Friction loss because of sudden expansion and contraction in cross section

The expression for expansion loss coefficient is

Friction loss

Where, Sa and Sb are the cross sectional area a of upstream and downstream conduits, respectively.

 

Reference:

1.      Unit operations of Chemical Engineering, 6th edition, by Warren L. McCabe, Julian C. Smith, and Peter Harriott.


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