Department of Chemical Engineering, Universitas Islam Indonesia, Indonesia
BibTex Citation Data :
@article{IJRED31982, author = {Fadilla Rahma and Cholila Tamzysi and Arif Hidayat and Muflih Adnan}, title = {Investigation of Process Parameters Influence on Municipal Solid Waste Gasification with CO2 Capture via Process Simulation Approach}, journal = {International Journal of Renewable Energy Development}, volume = {10}, number = {1}, year = {2021}, keywords = {CaO sorption; CO2 capture; gasification; municipal solid waste; syngas}, abstract = { Integration of gasification with CO 2 capture using CaO sorbent is proposed as an alternative treatment to convert municipal solid waste (MSW) into energy. Aspen Plus process simulator was employed to study the process. Two models were built to represent the non-sorbent and the sorbent-enabled MSW gasification. The model validation against available experimental data shows high accuracy of the simulation result. The effect of CO 2 capture using CaO sorbent on the syngas composition and lower heating value (LHV) was observed by comparing the two models, and sensitivity analysis was performed on both models. Several process parameters affecting the syngas composition and LHV were investigated, including CaO/MSW ratio, temperature, equivalence ratio, and steam/MSW ratio. The addition of CaO sorbent for CO 2 capture was found to successfully reduce the CO 2 content in the syngas, increase the H 2 composition, and improve the syngas LHV at the temperature below 750 o C. The maximum H 2 composition of 56.67% was obtained from the sorbent-enabled gasification. It was found that increasing equivalence ratio leads to a higher H 2 concentration and syngas LHV. Raising steam/MSW ratio also increases the H 2 production, but also reduces the LHV of the syngas. Observation of the temperature effect found the highest H 2 production at 650 o C for both non-sorbent and sorbent-enabled gasification. }, pages = {1--10} doi = {10.14710/ijred.2021.31982}, url = {https://ejournal.undip.ac.id/index.php/ijred/article/view/31982} }
Refworks Citation Data :
Integration of gasification with CO2 capture using CaO sorbent is proposed as an alternative treatment to convert municipal solid waste (MSW) into energy. Aspen Plus process simulator was employed to study the process. Two models were built to represent the non-sorbent and the sorbent-enabled MSW gasification. The model validation against available experimental data shows high accuracy of the simulation result. The effect of CO2 capture using CaO sorbent on the syngas composition and lower heating value (LHV) was observed by comparing the two models, and sensitivity analysis was performed on both models. Several process parameters affecting the syngas composition and LHV were investigated, including CaO/MSW ratio, temperature, equivalence ratio, and steam/MSW ratio. The addition of CaO sorbent for CO2 capture was found to successfully reduce the CO2 content in the syngas, increase the H2 composition, and improve the syngas LHV at the temperature below 750 oC. The maximum H2 composition of 56.67% was obtained from the sorbent-enabled gasification. It was found that increasing equivalence ratio leads to a higher H2 concentration and syngas LHV. Raising steam/MSW ratio also increases the H2 production, but also reduces the LHV of the syngas. Observation of the temperature effect found the highest H2 production at 650 oC for both non-sorbent and sorbent-enabled gasification.
Article Metrics:
Last update:
Gasification of refuse-derived fuel from municipal solid waste for energy production: a review
Improving the prediction of biochar production from various biomass sources through the implementation of eXplainable machine learning approaches
Solid waste management by RDF production from landfilled waste to renewable fuel of Nonthaburi
Aspen plus simulation model of municipal solid waste gasification of metropolitan city for syngas production
A general model for air gasification of heterogenous municipal solid waste
Negative carbon dioxide gas power plant integrated with gasification of sewage sludge
Improving carbon-reduced catalytic gasification of microalgae for biohydrogen production
Potential of renewable agricultural wastes in the smart and sustainable steelmaking process
Plastic waste/chickpea straw-to-fuels and power through co-gasification in a novel zero-emission system by CO2 capturing and utilization
Simulation and experimental study of refuse-derived fuel gasification in an updraft gasifier
Co-gasification of refuse-derived fuels and bituminous coal with oxygen/steam blend to hydrogen rich gas
Waste to energy: An experimental study on hydrogen production from food waste gasification
Conversion of municipals waste into syngas and methanol via steam gasification using CaO as sorbent: An Aspen Plus modelling
Ce/Pumice and Ni/Pumice as heterogeneous catalysts for syngas production from biomass gasification
Last update: 2024-12-02 00:12:28
This journal provides immediate open access to its content on the principle that making research freely available to the public supports a greater global exchange of knowledge. Articles are freely available to both subscribers and the wider public with permitted reuse.
All articles published Open Access will be immediately and permanently free for everyone to read and download. We are continuously working with our author communities to select the best choice of license options: Creative Commons Attribution-ShareAlike (CC BY-SA). Authors and readers can copy and redistribute the material in any medium or format, as well as remix, transform, and build upon the material for any purpose, even commercially, but they must give appropriate credit (cite to the article or content), provide a link to the license, and indicate if changes were made. If you remix, transform, or build upon the material, you must distribute your contributions under the same license as the original.
International Journal of Renewable Energy Development (ISSN:2252-4940) published by CBIORE is licensed under a Creative Commons Attribution-ShareAlike 4.0 International License.