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{"ops":[{"insert":"The relation between local radial pressure gradient, with packaging material and liquid dr properties is represented in Eq (1) dp \u0424\u0440 \u0430\u0437 dr pvz 1-a 150u(1-a) 1.75y + \u03c1\u03bd\u03bf\u03a6\u03a1 Eq(1) Where : Pp: packing material properties diameter (m) a: fraction void (dimensionless) y: correction factor (dimensionless)=0.2 p: liquid solvent density (kgm?) u: amine liquid viscocity (Pa.s) Characteristics of the proprietary packing considered in this project and the simplified stream pilot plant data can be obtained in Table 1 and Table 2 respectively. Size Packing EnviPaerings VSprings Material Plastics Metal 80 mm. no 3 25 mm, no. 1 0.050 0.055 (m) 0.065 0.015 Table 1: Characteristics of the proprietary packing considered in this project (Wankat, 2011) Liquid phase 0.03 Process parameters Volume flow rate (m's!) Column inner radius (m) Column outer radius (m) Viscosity (Pa.s) Density (kg\/m) Column length (m) 0.08 8 0.101 250 0.1 Table 2: Simplified stream data obtained from the pilot plant Your specific task for this project are as follows: a) Analyze the radial pressure drop (in bar) across the proprietary packing considered in this project based on the data in Table 1 and Table 2 [30 marks] ** Process assumption: Incompressible and steady flow condition Column cross sectional area : 2nrl The solvent moves towards to inlet radius (from outer radius)\n"}]}

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