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3 ENERGY-EFFICIENT PROCESSES INNOVA2 In order to achieve the project objectives, the InnovA2 collaborative project was split into four project areas each with up to five subprojects, see Fig. 90. The interfaces between the individual project areas, subprojects and work packages are also shown. 3.4.3 Results The experiments performed on the different types of heat exchanger equip- ment yielded an extensive and publicly accessible database that allows flu- id dynamic and thermodynamic performance assessments to be made. The objective was to provide guidance on designing and dimensioning such devices, so that users, especially those in the process industry, could make comparisons with the standard reference system that uses cylindrical smooth tubes. It is particularly noteworthy that the data from all of the ex- periments was determined using the same uniform, transparent and docu- mented method. This made it necessary, for example, to specify exactly how to calculate the surface area of a finned tube or pillow plate heat exchanger. Fig. 91: Sample results from the InnovA2 project. Above: Increased heat transfer on finned tubes compared with smooth tubes.; Below: Operating windows for pillow-plate and tube-bundle natural circulation evaporators for water at pabs = 200 mbar 214PDF Image | Chemical Processes and Use of CO2
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