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Microfiltration of the Sugar Refinery Wastewater Using Ceramic Membrane with Kenics Static Mixer

Year: 2015 Volume: 9 Issue: 9 1069 - 1072 Pages

• Authors:
• Zita Šereš
• Ljubica Dokić
• Nikola Maravić
• Dragana Šoronja–Simović
• Cecilia Hodur
• Ivana Nikolić
• Biljana Pajin

Abstract: New environmental regulations and the increasing market preference for companies that respect the ecosystem had encouraged the industry to look after new treatments for its effluents. The sugar industry, one of the largest emitter of environmental pollutants, follows this tendency. Membrane technology is convenient for separation of suspended solids, colloids and high molecular weight materials that are present in a wastewater from sugar industry. The idea is to microfilter the wastewater, where the permeate passes through the membrane and becomes available for recycle and re-use in the sugar manufacturing process. For microfiltration of this effluent a tubular ceramic membrane was used with a pore size of 200 nm at transmembrane pressure in range of 1–3 bars and in range of flow rate of 50–150 l/h. Kenics static mixer was used for permeate flux enhancement. Turbidity and suspended solids were removed and the permeate flux was continuously monitored during the microfiltration process. The flux achieved after 90 minutes of microfiltration was in a range of 50–70 l/m2h. The obtained turbidity decrease was in the range of 50-99 % and total amount of suspended solids was removed.

• Keywords:
• Ceramic membrane
• microfiltration
• sugar industry
• wastewater.

Simulation of the Flow in a Packed-Bed with and without a Static Mixer by Using CFD Technique

Year: 2009 Volume: 3 Issue: 5 273 - 278 Pages

• Authors:
• Phavanee Narataruksa
• Karn Pana-Suppamassadu
• Sabaithip TungkamaniRungrote Kokoo
• Prayut Jiamrittiwong

Abstract: The major focus of this work was to characterize hydrodynamics in a packed-bed with and without static mixer by using Computational Fluid Dynamic (CFD). The commercial software: COMSOL MULTIPHYSICSTM Version 3.3 was used to simulate flow fields of mixed-gas reactants i.e. CO and H2. The packed-bed was a single tube with the inside diameter of 0.8 cm and the length of 1.2 cm. The static mixer was inserted inside the tube. The number of twisting elements was 1 with 0.8 cm in diameter and 1.2 cm in length. The packed-bed with and without static mixer were both packed with approximately 700 spherical structures representing catalyst pellets. Incompressible Navier-Stokes equations were used to model the gas flow inside the beds at steady state condition, in which the inlet Reynolds Number (Re) was 2.31. The results revealed that, with the insertion of static mixer, the gas was forced to flow radially inward and outward between the central portion of the tube and the tube wall. This could help improving the overall performance of the packed-bed, which could be utilized for heterogeneous catalytic reaction such as reforming and Fischer- Tropsch reactions.

• Keywords:
• Packed Bed
• Static Mixer
• Computational Fluid Dynamic (CFD).