Personal identification

Full name

Daniela Eusébio

Citation names

• Eusébio, Daniela

Author identifiers

Ciência ID

A51D-B757-15BC

	Degree	Classification
2015/06/05 Attended	Contabilidade e Administração (Licenciatura) Instituto Politécnico do Porto Instituto Superior de Contabilidade e Administração do Porto, Portugal

Science

	Category Host institution	Employer
2017/02/01 - Current	Researcher (Research)	Instituto Politécnico de Portalegre, Portugal

Grant

	Designation	Funders
2019/02/01 - 2019/08/30	PoliTechWaste CMU Research Technician Fellow Instituto Politécnico de Portalegre, Portugal	Concluded

Publications

Newspaper article

Eusébio, Daniela. "Modelling and experimental analysis of a small-scale olive pomace gasifier for cogeneration applications: A techno-economic assessment.", 2019 https://doi.org/10.2298/CICEQ190109010C Eusébio, Daniela. "Municipal Solid Waste as a valuable recycled asset for small-scale electricity production in rural communities.", 2019 Eusébio, Daniela. "Process optimization and robustness analysis of Municipal Solid Waste gasification using air-carbon dioxide mixtures as gasifying agent.", 2019 https://doi.org/10.1002/er.4611 Eusébio, Daniela. "Techno-economic Analysis of a Biomass Gasification Power Plant Dealing with Forestry Residues Blends for Electricity Production in Portugal.", 2019 https://doi.org/10.1016/j.jclepro.2018.12.054

Other

Other output

Improved numerical approaches to predict hydrodynamics in a pilot-scale bubbling fluidized bed biomass reactor: A numerical study with experimental validation. A computational 2-D Eulerian-Eulerian approach was developed to simulate the hydrodynamics and heat transfer of a biomass gasification process in a pilot-scale bubbling fluidized bed reactor. The mathematical model was validated under experimental results collected from fluidization curves gathered at different temperatures in a pilot-scale reactor (75 kWth). Own user defined functions (UDFs) were. 2018. Cardoso, João; Silva, Valter; Eusébio, Daniela; Brito, Paulo; Tarelho, Luís. http://hdl.handle.net/10400.26/27947. https://doi.org/10.1016/j.enconman.2017.11.005 Experimental and Numerical Analysis of Olive Pomace Gasification for Cogeneration Apllications in Small Facilities: a techno-economic evaluation. A 2-D numerical simulation approach was developed to describe the gasification process of olive pomace in a bubbling fluidized bed reactor. The numerical model was validated under experimental gasification runs performed in a 250 kWth quasi-industrial biomass gasifier. The producer gas composition, H2/CO ratio, CH4/H2 ratio, cold gas efficiency and tar content were evaluated. The most suitable app. 2018. Cardoso, João; Silva, Valter; Eusébio, Daniela; Trninic, Marta; Carvalho, Tiago; Brito, Paulo. http://hdl.handle.net/10400.26/27956. Comparative scaling analysis of two different sized pilot-scale fluidized bed reactors operating with biomass substrates. This paper presents a comparative scaling analysis of two different sized pilot-scale fluidized bed reactors operating with biomass substrates. A multiphase Eulerian-Eulerian 2-D mathematical model was implemented, coupled with in-house user-defined functions (UDF) built to enhance hydrodynamics and heat transfer phenomena. The model validation was attained by comparison to experimental data gathe. 2018. Cardoso, João; Silva, Valter; Eusébio, Daniela; Brito, Paulo; Hall, M.J.; Tarelho, Luís. http://hdl.handle.net/10400.26/27953. https://doi.org/10.1016/j.energy.2018.03.090 Introductory Chapter: How to Use Design of Experiments Methodology to Get Most from Chemical Processes. Economic pressure and the need to target more competitive levels drive organizations to invest in efficient methodologies to get solutions able to provide clear advantages in a very demanding market. In this scenario, statistical approaches emerge as valuable tools to be used in the chemical process industry. Indeed, the chemical industry uses a wide set of statistical methodologies, ranging from. 2018. Silva, Valter; Eusébio, Daniela; Cardoso, João. http://hdl.handle.net/10400.26/27945. http://dx.doi.org/10.5772/intechopen.74061 Hydrodynamic Modelling of Municipal Solid Waste Residues in a Pilot Scale Fluidized Bed Reactor. The present study investigates the hydrodynamics and heat transfer behavior of municipal solid waste (MSW) gasification in a pilot scale bubbling fluidized bed reactor. A multiphase 2-D numerical model following an Eulerian-Eulerian approach within the FLUENT framework was implemented. User defined functions (UDFs) were coupled to improve hydrodynamics and heat transfer phenomena, and to minimize. 2017. Cardoso, João; Silva, Valter; Eusébio, Daniela; Brito, Paulo. http://hdl.handle.net/10400.26/27952. 10.3390/en10111773