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To replace cross heat exchanger in conventional PCC (with packed column) process, printed circuit heat exchanger will be preferred.
Energy losses due to inefficient heat recovery design of the system are identified by cross heat pinch analysis.
Fixed cross heat exchanger approach temperature of 10 °C and stripper bottom temperature of 120 °C are used as design specifications.
The results show that process uncertainty have a direct effect on the sizes of the absorber and stripper columns and operation of the reboiler duty, whereas the cross heat exchanger and condenser's heat transfer areas are not significantly affected.
Then the rich amine solution is pressured into the regenerator before preheating in the cross heat exchanger.
The rich solvent leaving the absorber is heated to about 80 °C in a cross heat exchanger by hot lean solvent, before it enters the stripper.
The regenerated CO2 is cooled in condenser and compressed for storage, and remaining solution (lean solution) is recycled to the cross heat exchanger to exchange heat with rich amine.
Thermal degradation occurs due to the high temperature in the stripper, and may also occur in the cross heat exchanger and the reclaimer, depending on the configuration [7, 8].
The model employs a cross flow heat exchanger able to exchange heat, but unable to exchange humidity since the two air fluxes are kept separate by specific sealing in the plates.
Different heat exchanger configurations, including counter flow and cross flow heat exchangers are modeled and verified.
In this work, a wickless heat pipes flat plate solar collector with a cross flow heat exchanger was investigated theoretically and experimentally under the meteorological conditions of Cairo, Egypt.
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