Equipments - Heater

Use the Heater to indirectly heat or cool a stream.
Specify only one parameter, choosing between DeltaT, Outlet Temp or Heat Duty. If one of these is specified and there is steam in the Shell, the Shell_Out stream is considered as saturated condensate.

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Data Description

Data Unit Description
Set Item Type Native
Equipment Properties Tube Outlet Flow Given If checked (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.
Delta T Temperature Change Delta F The temperature change on the tube side.
Outlet Temperature Temperature F The temperature of the Tube_Out stream.
Heat Duty Energy Flow BTU/hr Heat transferred to or from the tube side. The change in energy of the Tube_In stream.
Outlet Pressure Pressure psia The pressure of the Tube_Out stream. Defaults to the Tube_In stream's pressure.
Copy Tube_In to Tube_Out on failure  Temperature F Only applies to tube side heating with steam (shell side flow is calculated).
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Equipment Properties

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Example of using equipment

 

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Method&Equations

If the temperature of the Tube_Out stream is set, with no steam involved, the Heater sets the outlet stream temperature and pressure and it determines the enthalpy of the stream.

If the Tube_Out stream temperature is specified and inlet steam stream is connected, the Heater back-calculates the steam flow by first determining the enthalpy of the Tube_Out stream at the new temperature and pressure.

It calculates the steam flow as:

       FI2 = ((HO1 - HI1) * FI1) / (HI2 - HO2)

where:

      FI2 is the flow rate of steam required and resulting condensate

      HO1 is the specific enthalpy of the Tube_Out stream

      HI1 is the specific enthalpy of the Tube_In stream

      FI1 is the total flow in the Tube_In stream

      HI2 is the specific enthalpy of the steam stream

      HO2 is the saturated condensate specific enthalpy

If the temperature of the Tube_Out stream is not specified and there is a steam stream connected, the Heater assumes saturated condensate and the enthalpy of the Tube_Out stream is determined as follows:

      HO1 = ((FI2 * HI2 - FO2 * HO2 ) + FI1 * HI1) / FO1

where:

     FO2 is the flow rate in the condensate stream

     FO1 is the flow rate in the Tube_Out stream

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Warnings

Zero flow entering!

Condensate temp > steam temp!

Delta T or Outlet Temp or Heat Duty needed!

Shell out colder than cold in!

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Errors

Missing Stream(s)!

Outlet temperature exceeds inlet range!

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