Liquid-phase mass-transfer coefficients of Mellapak structured packings under desorption of oxygen from primary alcohols

Volumetric mass-transfer coefficient in the liquid phase, kLa, for Mellapak 250.Y, 350.Y and 500.Y structured packings has been measured by standard method of desorption of oxygen into nitrogen from pure methanol, ethanol and n-propanol in the column of i.d. of 150 mm. Although utilization of organic solvents for absorption experiments provides valuable behavior interlink between properties of aqueous absorption systems and ordinary (organic) systems under distillation conditions, studies of such kind are not published in the open literature. The behavior of the kLa data on alcohol systems do not differ significantly from that found for aqueous system, the kLa values rise with the liquid load powered to â\u88¼0.5â\u80\u930.78. For one solvent the kLa are almost identical for all three packings under the same liquid load. According to the expectations the kLa values under the same superficial liquid flow rate are highest for the solvent with the lowest viscosity and the highest diffusivity of oxygen, methanol, and decrease in the order ethanol, n-propanol and water. The kLdata for all three packings, alcohols and also for water has been successfully correlated by dimensionless correlation Sh = 0.207 â\u88\u99 Re0.798Frâ\u88\u920.563We0.511Sc0.528with mean relative deviation of 12%

Performance and Modelling of the Pre-combustion Capture Pilot Plant at the Buggenum IGCC

This paper summarizes the final results of the pilot plant operation and R&D programme of the CO2 Catch-up project (2008- 2013). The objective of the CO2 Catch-up project is to demonstrate pre-combustion CO2 capture at the pilot plant in Buggenum, the Netherlands, in order to verify the technology performance and to generate knowledge in the form of validated models and operational experience.Process and EnergyMechanical, Maritime and Materials Engineerin