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<span lang="IN">The oxidation process as the activated sludge (AS) system has been implemented widely in urban and industrial wastewater treatment. Oxidation ditch can be categorized as an advanced aeration activated sludge. </span><span>I</span><span lang="IN">ntegrated Fix-Film Activated Sludge</span><span> (</span><span lang="IN">IFAS</span><span>)</span><span lang="IN"> process has been already developed for decades that was a reasonable approach for technology to upgrade the activated sludge wastewater treatment plant (WWTP). IFAS processes are a combination of biofilm reactors and activated sludge processes, biofilm is introducing and retaining as the carrier media for microorganism growth. Both IFAS and AS processes can achieve similar percent removal of COD and ammonia. Current WWTPâs development was food chain reactor</span><span> (</span><span lang="IN">FCR</span><span>)</span><span lang="IN"> which mainly IFAS process of engineered media that combining with natural plants with the plant roots submerging into the reactors. The references review and secondary data of the application in Jababekaâs WWTP-2 for both AS and FCR system showed that FCR is needless parameters to be controlled. In both AS and FCR have KPIs of flow rate (m<sup>3</sup>/day), F/M ratio, energy consumption (kWh/m<sup>3</sup> wastewater), Oxygen supply (kgO<sub>2</sub> / m<sup>3</sup> wastewater in each reactor, % removal of COD, BOD, TSS, NH<sub>3</sub>, TKN, NO<sub>2</sub>, and heavy metals, and pH, Dissolved Oxygen, microorganism performance in</span><span lang="IN"> the reactor. Different from AS, the FCR system is not required to control the parameters of </span><span>sludge retention time (</span><span lang="IN">SRT</span><span>)</span><span lang="IN">, </span><span>recirculated activated sludge (</span><span lang="IN">RAS</span><span>)</span><span lang="IN">, </span><span>sludge volume index (</span><span lang="IN">SVI</span><span>),</span><span lang="IN"> and </span><span>mixed liquor suspended solids (</span><span lang="IN">MLSS</span><span>)</span><span>of </span><span lang="IN">activated sludge.</span><br /><!--[if gte mso 9]><xml> <o:OfficeDocumentSettings> <o:RelyOnVML/> <o:AllowPNG/> </o:OfficeDocumentSettings> </xml><![endif]--><!--[if gte mso 9]><xml> <w:WordDocument> <w:View>Normal</w:View> <w:Zoom>0</w:Zoom> <w:TrackMoves/> <w:TrackFormatting/> <w:PunctuationKerning/> <w:ValidateAgainstSchemas/> <w:SaveIfXMLInvalid>false</w:SaveIfXMLInvalid> <w:IgnoreMixedContent>false</w:IgnoreMixedContent> 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<span lang="IN">The oxidation process as the activated sludge (AS) system has been implemented widely in urban and industrial wastewater treatment. Oxidation ditch can be categorized as an advanced aeration activated sludge. </span><span>I</span><span lang="IN">ntegrated Fix-Film Activated Sludge</span><span> (</span><span lang="IN">IFAS</span><span>)</span><span lang="IN"> process has been already developed for decades that was a reasonable approach for technology to upgrade the activated sludge wastewater treatment plant (WWTP). IFAS processes are a combination of biofilm reactors and activated sludge processes, biofilm is introducing and retaining as the carrier media for microorganism growth. Both IFAS and AS processes can achieve similar percent removal of COD and ammonia. Current WWTPâs development was food chain reactor</span><span> (</span><span lang="IN">FCR</span><span>)</span><span lang="IN"> which mainly IFAS process of engineered media that combining with natural plants with the plant roots submerging into the reactors. The references review and secondary data of the application in Jababekaâs WWTP-2 for both AS and FCR system showed that FCR is needless parameters to be controlled. In both AS and FCR have KPIs of flow rate (m<sup>3</sup>/day), F/M ratio, energy consumption (kWh/m<sup>3</sup> wastewater), Oxygen supply (kgO<sub>2</sub> / m<sup>3</sup> wastewater in each reactor, % removal of COD, BOD, TSS, NH<sub>3</sub>, TKN, NO<sub>2</sub>, and heavy metals, and pH, Dissolved Oxygen, microorganism performance in</span><span lang="IN"> the reactor. Different from AS, the FCR system is not required to control the parameters of </span><span>sludge retention time (</span><span lang="IN">SRT</span><span>)</span><span lang="IN">, </span><span>recirculated activated sludge (</span><span lang="IN">RAS</span><span>)</span><span lang="IN">, </span><span>sludge volume index (</span><span lang="IN">SVI</span><span>),</span><span lang="IN"> and </span><span>mixed liquor suspended solids (</span><span lang="IN">MLSS</span><span>)</span><span>of </span><span lang="IN">activated sludge.</span><br /><!--[if gte mso 9]><xml> <o:OfficeDocumentSettings> <o:RelyOnVML/> <o:AllowPNG/> </o:OfficeDocumentSettings> </xml><![endif]--><!--[if gte mso 9]><xml> <w:WordDocument> <w:View>Normal</w:View> <w:Zoom>0</w:Zoom> <w:TrackMoves/> <w:TrackFormatting/> <w:PunctuationKerning/> <w:ValidateAgainstSchemas/> <w:SaveIfXMLInvalid>false</w:SaveIfXMLInvalid> <w:IgnoreMixedContent>false</w:IgnoreMixedContent> 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Coupling the hydrodynamic and biokinetic models, was done on a lab-scale oxidation ditch as the bioreactor of the activated sludge process and validated against the available experimental data. The simulation was carried out in three-phase, three-dimensional conditions with k-Ń and Eulerian-Eulerian methods. A simplified activated sludge model No.1 (ASM1) has been added to transport terms to account for the biokinetic model. Rotatory speed for surface aerator was initially increased and its corresponding effects on solid volume fraction, dissolved oxygen, and velocity profile and values were observed. A 150 rpm increase in the rotational velocity resulted in 36% higher average liquid phase velocity for the one-aerator arrangement, which was 3% more than that of the two-aerator oxidation ditch. The 150% increase in the solid volume fraction led to a 10% reduction in the maximum liquid phase velocity. The effect of aerators number has been considered explicitly on baffle performance and liquid phase velocity profile. Finally, a new design for the aerator has been offered that provides an ordered flow field and optimal conditions for the performance of the baffle and oxidation process.
Spirulina platensis is a type of blue -green algae that has a micro-sized spiral shape and lives in marine waters. There are so many benefits of this microalgae, one of which is it can degrade organic pollutants in wastewater. Excessive nitrate and phosphate in the water can cause eutrophication which is indicated by the death of many sea biotas because of phytoplankton bloom. In this research, tofu which high in organic pollutants are used as experimental test media. The microalgae which will be tested is cultivated first to obtain a sufficient amount for research, then the microalgae are acclimatized before being put into an Oxidation Ditch Reactor mixed with tofu waste with a capacity of 250 liters, ran with 60 rpm brush aerator for 7 x 24 hours and also uses natural lighting from sunlight. samples were taken once a day at 12 noon each day. This research has a variety of wastewater: algae that are 1:1. From the results, it can be observed that Spirulina platensis microalgae could reduce maximum phosphate by 33,15 %, from 18,1 mg/L to 12,1 mg/. Furthermore, microalgae also capable of decreasing nitrates by 46,07 from 0,89 mg/L to 0,48 mg/L.
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