**Chemical and Process Engineering Resources**

**Chemical and Process Engineering Resources**

## Basics of Industrial Heat Transfer

Nov 08 2010 01:30 PM | Chris Haslego in Heat Transfer Share this topic:
Heat transfer is one of the most important industrial processes. Throughout any industrial facility, heat must be added, removed, or moved from one process stream to another. Understanding the basics of the heart of this operation is key to any engineers' mastery of the subject.

There are three basic types of heat transfer: conduction, convection, and radiation. The two most common forms encountered in the chemical processing industry are conduction and convection. This course will focus on these key types of heat transfer.

In theory, the heat given up by the hot fluid is never exactly equal to the heat gained by the cold fluid due to environmental heat losses. In practice, however, they are generally assumed to be equal to simplify the calculations involved. Any environmental losses are generally minimized with insulation of equipment and piping.

Any overall energy balance starts with the following equations:

Where:

Q = heat transferred in thermal unit per time (Btu/h or kW)

M = mass flow rate

T = temperature

Cp = heat capacity or specific heat of fluid

Subscript "H" = hot fluid

Subscript "C" = cold fluid

When examining industrial systems, it is common practice to use a graphical form of these equations know as "T-Q diagrams" to enhance understanding and to make sure that the Second Law of Thermodynamics is not disobeyed. In other words, heat can only move from a higher to a lower temperature fluid. Here is how the generic diagram is constructed:

It's easy to see how viewing a particular heat transfer problem in this way is extremely valuable.

Now that's we've seen how heat moves from a hot fluid to a cold fluid, let's examine the third basic equation that is used to govern the equipment used for transferring heat.

The "Heat Exchanger Equation" takes the form:

Where:

Q = heat transferred in thermal unit per time (Btu/h)

f = temperature correction factor

U = overall heat transfer coefficient (Btu/h ft

A = heat transfer area (ft

LMTD = log mean temperature difference

These three (3) equations are the basis for virtually all heat exchanger design.

There are three basic types of heat transfer: conduction, convection, and radiation. The two most common forms encountered in the chemical processing industry are conduction and convection. This course will focus on these key types of heat transfer.

In theory, the heat given up by the hot fluid is never exactly equal to the heat gained by the cold fluid due to environmental heat losses. In practice, however, they are generally assumed to be equal to simplify the calculations involved. Any environmental losses are generally minimized with insulation of equipment and piping.

Any overall energy balance starts with the following equations:

Eq. (1) | |

Eq. (2) |

Where:

Q = heat transferred in thermal unit per time (Btu/h or kW)

M = mass flow rate

T = temperature

Cp = heat capacity or specific heat of fluid

Subscript "H" = hot fluid

Subscript "C" = cold fluid

When examining industrial systems, it is common practice to use a graphical form of these equations know as "T-Q diagrams" to enhance understanding and to make sure that the Second Law of Thermodynamics is not disobeyed. In other words, heat can only move from a higher to a lower temperature fluid. Here is how the generic diagram is constructed:

Figure 1: Correct Example of a T-Q Diagram | Figure 2: Incorrect Example of a T-Q Diagram |

It's easy to see how viewing a particular heat transfer problem in this way is extremely valuable.

Now that's we've seen how heat moves from a hot fluid to a cold fluid, let's examine the third basic equation that is used to govern the equipment used for transferring heat.

The "Heat Exchanger Equation" takes the form:

Eq. (3) |

Where:

Q = heat transferred in thermal unit per time (Btu/h)

f = temperature correction factor

U = overall heat transfer coefficient (Btu/h ft

^{2}Â°F)A = heat transfer area (ft

^{2})LMTD = log mean temperature difference

These three (3) equations are the basis for virtually all heat exchanger design.

## 3 Comments

Heat Exchanger iOS application

https://itunes.apple...633422031?mt=8#!I think it may be helpful to introduce an application (Heat Exchanger) which can be used in solving heat transfer equation and designing double pipe heat exchanger with following features:

THANKS FOR THE ARTICLE. IF YOU SO KIND TO GIVE THE INFORMATION ABOUT DIRECT CONTACT JUICE HEATERS CALCULATION. THE HEATERS MAINLY USED IN SUGAR INDUSTRIES TO TEMPERATURE THE JUICE.

Thanks