Equipments - CounterCurrent Heatx

Use the CounterCurrent_Heatx to simulate a counter-current shell and tube heat exchanger.
The tube side is normally the liquor (and pulp) side. The shell side is usually the steam side. However, there are no restrictions on the type of material flowing on either side of the exchanger.

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Data Description

Data Unit Description
Set Item Type Native
Equipment Properties Tube Outlet Flow Given If True the current tube outlet flow is used as the tube side flow. If False the current tube inlet flow is used as the tube side flow.
Shell Outlet FlowGiven If True the current shell outlet flow is used as the shell side flow. If False the current shell inlet flow is used as the shell side flow.
Heat Loss Fraction or Percent Fraction The fraction of the total heat transferred that is lost.
Tube Side Pressure Drop Pressure Change psi The change in pressure on the tube side of the exchanger.
Shell Side Pressure Drop Pressure Change psi The change in pressure on the shell side of the exchanger.
Tube Outlet Temp
Temperature F The temperature of the tube outlet.
Shell Outlet Temp
Temperature F The temperature of the shell outlet.
Approach Temp
Temperature Change Delta F The approach temperature (Approach Temperature = Shell Inlet Temperature - Tube Outlet Temperature).
Heat Trans Area
Area ft2 Total area through which heat is transferred.
Heat Trans Coef
Heat Transfer Coefficient BTU/hr/F/ft2 The overall heat transfer coefficient.
Temperature Warning
If checked (True), displays a warning if the tube outlet temperature is greater than the shell outlet temperature.
Output Data Heat Transferred Energy Flow BTU/hr Energy flow between tube and shell.
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Equipment Properties

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Example of using equipment

 

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Method&Equations

If the Tube Outlet Temperature or the Shell Outlet Temperature specified, the model calculates the resulting enthalpy of the outlet stream and the outlet temperature. 

If it is specified the Approach Temperature the model can calculate the Shell Outlet Temperature, the total heat transferred and the Tube Outlet Temperature.

If it is specified the Heat Transfer Area and the Heat Transfer Coefficient, the CounterCurrent_Heatx model uses an error function to calculate the outputs. The error function is the difference between the calculated heat exchanger area and the specified area as a function of shell side outlet enthalpy.

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Warnings

Zero shell side flow!

Zero tube side flow!

Tube out hotter than shell in!

Tube out colder than cold in!

Shell out colder than cold in!

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Errors

Missing Stream(s)!

Tube outlet temperature exceeds inlet range!

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Related Topics
Heat Exchanger Example

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