PartialHeatExchanger
This components contains partial equation describing a generic
adiabatic heat exchanger using the effetiveness method. The
advantage of the effetiveness method regarding the mean logarithmic
method is to avoid a non linear equation where oulet temperature
are unknown(see explainations in the theoretical note). The system
of equations describing an heat exchanger derives:
Where:
- Qc is the thermal flow rate unit.m_flow and
cp being the mass flow rate and the specific heat
capacity
- Cr is the ration of the thermal flow rate units
- NTU is the number of transfer unit
- h_global is the global heat exchange coeffcient
- A is generally the maximal exchange surface (if exchange
surfaces for both fluid are different )
- Eff is the effectiveness of the exchanger
- Q_flow is the exchanged power. It is defined as positive
when the fluid A is cooled
- Q_flow_max is the maximal exchangeable power for an
infinite exchanger
- T_A is temperature of the fluid A (T_B for fluid
B).
An heat exchanger is a complex object that can have various
configurations such as:
- counter, cross or parallel flow
- single or multi passes
- etc
Therefore, it has been chosen to develop a partial heat
exchanger containing the common equations to all kind of exchanger
whatever its configuration. For a specific exchanger the user just
have to inherit this partial model and give the specific missing
equations for:
- The relation between the effectiveness and geometrical and flow
configuration: Eff = f(Cr, NTU, ...)
- The thermal flow rate: Qc_A and Qc_B
- The inlet temperature: T_A_in, T_B_in
- The global heat exchange coefficient: K_global
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