Parametric gasification process of sugarcane bagasse for syngas production |
| |
| Affiliation: | 1. School of Environment, Tsinghua University, Beijing 100084, China;2. Mechanical Engineering Department, Quaid-e-Awam University of Engineering Science and Technology, 67450, Pakistan;3. School of Environmental Science & Technology, Dalian University of Technology, Dalian 116024, Liaoning, China;4. Electrochemical Innovation Lab (EIL), Department of Chemical Engineering, University College London, Torrington Place, London, WC1E 7JE, UK;1. Department of Applied Chemistry, School of Chemistry, College of Science, University of Tehran, Tehran, Iran;2. Department of Energy Engineering, Science and Research Branch of Islamic Azad University, Tehran, Iran;1. Centro de Engenharia, Modelagem e Ciências Sociais Aplicadas (CECS), Universidade Federal do ABC (UFABC), Av dos Estados, 5001, Bairro Bangu, Santo André, S.P, 09210-580, Brazil;2. Environmental Engineering Department, Universidad Católica de Manizales, Manizales, Caldas, Colombia;1. School of Environment, Tsinghua University, Beijing 100084, China;2. Key Laboratory for Solid Waste Management and Environment Safety, Ministry of Education, Beijing, 100084, China;3. School of Environmental Science and Technology, Dalian University of Technology, Dalian, Liaoning 116024, China;1. Centre for Tropical Crops and Biocommodities, Queensland University of Technology, Australia;2. Biofuel Engine Research Facility, School of Chemistry, Physics and Mechanical Engineering, Science and Engineering Faculty, Queensland University of Technology, 2 George St, Brisbane, Queensland, 4000, Australia;1. (ICARE)-CNRS UPR3021, 1C avenue de la recherche scientifique, 45071, Orléans Cedex 2, France;2. Université d’Orléans, Institut Universitaire de Technologie, 16 rue d’Issoudun BP16724, 45067 Orléans Cedex 2, France |
| |
| Abstract: | This research focuses on parametric influence on product distribution and syngas production from conventional gasification. Three experimental parameters at three different levels of temperature (700, 800 and 900 °C), sugarcane bagasse loading (2, 3 and 4 g) and residence time (10, 20 and 30 min) were studied using horizontal axis tubular furnace. Response Surface Methodology supported by central composite design was adopted in order to investigate parameters impact on product distribution (i.e., gas, tar and char) and gaseous products (i.e., H2, CO, CO2 and CH4). The highest H2 fraction obtained was 42.88 mol% (36.91 g-H2 kg-biomass−1) at 3 g of sugarcane bagasse loading, 900 °C and 30 min reaction time. The temperature was identified as the most influential parameter followed by reaction time for H2 production and diminishing the bio-tar and char yields. An increase in sugarcane bagasse loading, on other hand, favored the production of bio-tar, CO2 and CH4 production. The statistical analysis verified temperature as most significant (p-value 0.0008) amongst the parameters investigated for sugarcane bagasse biomass gasification. |
| |
| Keywords: | Sugarcane bagasse Biomass gasification Parametric effect Hydrogen fuel Central composite design |
| 本文献已被 ScienceDirect 等数据库收录！ |
|
