21 European Symposium on Computer Aided Process Engineering by Pistikopoulos E. N. (EDT)/ Georgiadis Michael C. (EDT)/

By Pistikopoulos E. N. (EDT)/ Georgiadis Michael C. (EDT)/ Kokossis Antonis C. (EDT)

The eu Symposium on desktop Aided method Engineering (ESCAPE) sequence provides the newest strategies and achievements of best pros from the economic and educational groups. The get away sequence serves as a discussion board for engineers, scientists, researchers, managers and scholars to offer and speak about development being made within the region of laptop aided method engineering (CAPE). eu industries huge and small are bringing concepts into our lives, even if within the kind of new applied sciences to handle environmental difficulties, new items to make our houses more well-off and effort effective or new treatments to enhance the future health and health of eu voters. in addition, the ecu must adopt examine and technological tasks in accordance with humanity's "Grand Challenges," defined within the statement of Lund, particularly, worldwide Warming, Tightening offers of strength, Water and nutrition, getting older Societies, Public future health, Pandemics and defense. therefore, the Technical subject matter of break out 21 can be "Process platforms techniques for Addressing Grand demanding situations in strength, atmosphere, well-being, Bioprocessing & Nanotechnologies."

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4. 5 mm. The two EFCE test systems (toluene-acetone-water and butyl acetateacetone-water) are used. The direction of mass transfer is from the continuous to the dispersed phase. The inlet solute concentrations in the continuous and dispersed phases 3 4 M. JARADAT et al. 22 and 0 % respectively. The pulsation intensity (a. f) = 1 cm/sec and the total flow rate of the continuous phase: Qc = 40 lit/hr and dispersed phase: Qd = 48 lit/hr. 5 0 sim. exp. 5 1 sim. exp. 1: Simulated mean droplet diameter along the column height compared to the experimental data [25].

5 1 sim. exp. 1: Simulated mean droplet diameter along the column height compared to the experimental data [25]. Left panel the test system is (toluene–acetone-water) and the right panel is (butyl acetate-acetone-water). (1) shows the variation of the mean droplet diameter along the column height compared to the experimental data for both chemical systems. A fairly good agreement between the experimental and simulated profiles is achieved for both systems. (2). Again, a very good agreement is achieved for both test systems.

T is the temperature, Jq the heat flux, Fi the flow rate of component i and Cp the heat capacity. Figure 2: Illustration of a membrane reactor. 1: The hot exhaust gas. 2: The feed gas mixture. 3: The permeate. A flat-plate membrane reactor configuration (left) and a tubular membrane reactor configuration (right). 8 Ø. Wilhelmsen et al. Table 1: geometrical parameters Parameter: Tubular: Flat-plate Ȗ1 Ȗ2 Ȗ3 2ʌR3 2ʌR2 ʌR32-ʌR22 W W WH2 The momentum balance of the exhaust gas section was omitted due to an insignificant contribution to the simulations within the relative accuracy of 5E-6.

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