This is the model of a very simple heat exchanger. The modelling assumptions are as follows:
- The boiler contains Nr rows of tubes, connected in series; each one is made of Nt identical tubes in parallel.
- Each tube has a length L, internal and external diameters Dint and Dext, and is made of a metal having density rhom and a specific heat capacity of cm.
- The series connection of the tubes is discretised with Nr+1 nodes, so that each cell between two nodes corresponds to a single row.
- The gas flow is also discretised with Nr+1 nodes, so that each gas cell interacts with a single tube row.
- The gas flows through a volume having a (net) cross-section Sb and a (net) length Lb.
- Mass and energy dynamic balances are assumed for the water side.
- The mass and energy balances for the gas side are either static or dynamic, depending on the value of the StaticGasBalances parameter.
- The fluid in the water side remains liquid throughout the boiler.
- The heat transfer coefficient on the water side is computed by Dittus-Boelter's correlation.
- The external heat transfer coefficient is computed according to the simple law declared Flow1DGasHT. To change that correlation, it is only necessary to change equations in that model.
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