Equipments - Condenser Model

The condenser is used to condense vapors of water and ethanol of the inlet stream, assuming indirect cooling.
The inlet stream may contain liquid phase.
If not specified, the cooling medium is water.

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Data Description

Data Unit Description
Set Item Type Native
Equipment Properties Condensate Temperature Temperature F The temperature of the condensate stream. The default is the saturated temperature at the Condensate Pressure. Ignored if the specified temperature is higher than the condensing temperature.
Condensate Pressure Pressure psia The pressure of the condensate stream. The default is the inlet pressure.
Hot Water Temperature Temperature F The outlet temperature for the coolant.
Vapor Condensed Fraction or Percent Fraction Fraction of inlet vapor that is condensed.
Heat Transfer
Efficiency
Fraction or Percent Fraction The fraction of the heat which can be taken by the coolant.
Surface Area Area ft2 Surface area of condenser.
Output Data Heat Transfer Coefficient Heat Trans Coef BTU/hr/F/ft2 Heat transfer coefficient, calculated from the heat transferred, and the specified surface area.
Heat Duty Energy Flow BTU/hr Heat picked up by the cooling water.
Condensing Temperature Temperature F The temperature at which the input "Vapor fraction condensed" can be satisfied. Determined from the VLE data.
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Equipment Properties

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Example of using equipment

 

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Method&Equations

If the condensate pressure is not specified it is set to the inlet vapor pressure.

The condensate is set to the temperature specified (if it is lower than the condensing temperature). If the temperature is not specified, the condensate is set to the saturated temperature.

The energy available for transfer to the cold inlet stream is calculated as:

Q = FI1 * HI1 - FO1 * HO1 - FO2 * HO2

where

Q - energy available for transfer

FI1- the flow in the inlet vapor stream

HI1- the enthalpy of the inlet vapor stream

FO1 - the flow in the outlet vapor stream

HO1- the enthalpy of the outlet vapor stream

FO2 - the flow in the outlet condensate stream

HO2 - the enthalpy of the outlet condensate stream

The outlet hot water enthalpy is then:

HO3 = (FI2 * HI2 + Q) / FO3

where:

HO3 is the enthalpy of the outlet hot water stream

FI2 is the flow in the inlet cold water stream

HI2 is the enthalpy of the inlet cold water stream

FO3 is the flow in the outlet hot water stream

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Warnings

No steam entering!

No cold water entering; defaults used!

No condensed fraction specified!

Specified condensate temperature higher than the calculated condensing temperature. Specified temperature ignored!

The specified hot water temperature higher than the specified condensate outlet temperature! The condensate temperature will be used for hot water outlet! 

 Hot water temperature not specified! The condensate temperature will be used!

Hot water outlet temperature exceeds the condensate temperature! The condensate temperature will be used!

Hot water outlet temperature exceeds inlet range!

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Errors

Missing Stream(s)!

Specified condensate temperature lower than the coolant inlet temperature!

Input hot water temperature lower than cold water temperature!

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