Process parameter optimization of urban biowaste carbonization

dc.contributor.advisorNarayana M
dc.contributor.authorPerera SMHD
dc.date.accept2020
dc.date.accessioned2020
dc.date.available2020
dc.date.issued2020
dc.description.abstractAbout 75% of Municipal solid waste (MSW) collected around the country is organic biomass which mainly includes food waste, wood, paper, saw dust and paddy husk. Urban councils in Colombo city and nearby suburbs collect biowaste separately which has created a huge potential in converting urban biowaste into value-added component like biochar, thus resolving the problems associated with MSW management and mitigating socio-economic and environmental issues related to MSW. In this study, torrefaction is identified as the most viable technology available for the conversion of organic MSW into biochar and the study mainly focuses on developing a three dimensional computational fluid dynamics (CFD) model of a continuous packed-bed torrefaction reactor for organic MSW and then optimizing the process variables and the geometry. A mathematical model including all heat, mass and energy transfers, and heterogeneous & homogeneous reactions is firstly developed and then converted to a numerical model and simulated using OpenFOAM for an insulated cylindrical reactor in which hot gas at elevated temperatures (473 – 623K) is provided from the bottom while solid at ambient conditions is fed from the top. The torrefaction reactor is optimized for gas inlet temperature and residence time and then the geometry of the reactor is optimized for the optimum gas inlet temperature and residence time. Four reaction zones are identified in the reactor domain; i.e. drying, softening & depolymerization, limited devolatilization & carbonization and extensive devolatilization and carbonization. The optimum inlet gas temperature, residence time and D/L ratio are 573K, 13000s and 0.24 respectively. For the optimum conditions, biochar yield is 55.7% while ash content is 19.1%. Further In dry basis, 95.9% of biomass is decomposed and the total weight loss based on the initial wet biomass is 86.6%.en_US
dc.identifier.accnoTH4123en_US
dc.identifier.degreeMSc in Sustainable Process Developmenten_US
dc.identifier.departmentDepartment of Chemical and Process Engineeringen_US
dc.identifier.facultyEngineeringen_US
dc.identifier.urihttp://dl.lib.mrt.ac.lk/handle/123/16197
dc.language.isoenen_US
dc.subjectCHEMICAL AND PROCESS ENGINEERING-Dissertationsen_US
dc.subjectSUSTAINABLE PROCES DEVELOPMENT-Dissertationsen_US
dc.subjectWASTE DISPOSALen_US
dc.subjectSOLID WASTE MANAGEMENTen_US
dc.subjectMASS TRANSFER-Packed Bedsen_US
dc.subjectTORREFACTIONen_US
dc.subjectCOMPUTATIONAL FLUID DYNAMICSen_US
dc.subjectBIOCHARen_US
dc.subjectHEAT TRANSFER-Packed Bedsen_US
dc.titleProcess parameter optimization of urban biowaste carbonizationen_US
dc.typeThesis-Full-texten_US

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