scholarly journals Effect of Equivalence Ratio on an Efficiency of Single Throat Downdraft Gasifier Using RDF from Municipal solid waste

2017 ◽  
Vol 138 ◽  
pp. 784-788 ◽  
Author(s):  
Trirat Khosasaeng ◽  
Ratchaphon Suntivarakorn
Fuel ◽  
2020 ◽  
Vol 263 ◽  
pp. 116509 ◽  
Author(s):  
Arif Rahman Saleh ◽  
Bambang Sudarmanta ◽  
Hamzah Fansuri ◽  
Oki Muraza

2020 ◽  
Vol 15 (4) ◽  
pp. 180-188
Author(s):  
Saravanakumar Ayyadurai ◽  
Thomas B Reed ◽  
Muthukathan Rajendran Sudha

2021 ◽  
Vol 1192 (1) ◽  
pp. 012023
Author(s):  
A D D Diallo ◽  
M F R Alkhatib ◽  
M Z Alam ◽  
M Mel

Abstract The work deals with the simulation of biomass and municipal solid waste pellet gasification using Aspen Plus software. The effects of key parameters on the composition of the emitted gas are discussed, including gasification temperature, moisture content, and equivalence ratio. The sensitivity analysis was studied with the Aspen Plus Software, which includes FORTRAN modules. The simulation is validated using experimental results, which revealed that it was roughly correct. Using air as the gasification agent, the sensitivity analysis findings confirm higher temperatures promote syngas production with increased hydrogen and energy content. The simulation results demonstrated that CO2 concentration (3.95%) increases from 450°C to 600°C and then decreased drastically near 0.225kmol/hr. at 900°C. As the gasification temperature rises from 450°C to 900°C, the CO concentration rises and the H2: CO ratio falls. At 900°C, increasing the gasification temperature results in a product gas with more H2 (65%) and CO (12.43%), resulting in a higher calorific value, whereas the contents of CH4, CO2, and H2O followed an inverse correlation. CH4 decreased with temperature because of the formation of exothermic methane reactions. When the gasification process reaches 800°C, all components except CO2 become steady, and gasification reactions were achieved. The equivalence ratio (ER) ranged from 0.2 to 0.3. The gas produced by a gasifier is highly dependent on the ER value. The ER determines the gas quality, and it must be less than 1 to ensure that it gasifies the fuel rather than burnt. Moisture content was 10wt. %, this is an essential parameter for the optimum conditions during the gasification process. Moisture content determines the gas characteristics at the exit phase. The model predictions and calculated values are in good agreement.


2020 ◽  
Vol 10 (1) ◽  
pp. 1-10
Author(s):  
Fadilla Noor Rahma ◽  
Cholila Tamzysi ◽  
Arif Hidayat ◽  
Muflih Arisa Adnan

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. 


Data in Brief ◽  
2020 ◽  
Vol 30 ◽  
pp. 105521
Author(s):  
Apri Wiyono ◽  
Nugroho Agung Pambudi ◽  
Miftah Hijriawan ◽  
Indra Mamad Gandidi ◽  
Asep Setiadi Husen ◽  
...  

2019 ◽  
Vol 8 (2) ◽  
pp. 179 ◽  
Author(s):  
Nigran Homdoung ◽  
Nattawud Dussadee ◽  
Kittikorn Sasujit ◽  
Tanongkiat Kiatsiriroat ◽  
Nakorn Tippayawong

Municipal solid waste (MSW) and charcoal can be used as a substitute fuel in a gas engine. In this work, performance of a downdraft gasifier and gas engine system operated on MSW briquette fuel was investigated. Experimental test was carried out on a 62 kW, four-cylinder, naturally aspirated engine coupled to a 20 kW dynamometer. The downdraft gasifier was used to generate producer gas from MSW briquettes and charcoal. The engine load was varied between 1.5-9.0 kW. Biomass consumption, producer gas production, cold gas efficiency, thermal efficiency of the gas engine, carbon monoxide (CO), hydrocarbon (HC) emissions and exhaust temperature were evaluated. The MSW briquette fuelled operation was compared against that with charcoal. It was found that, the use of MSW briquette led to lowering performance of the downdraft gasifier and gas engine system, in comparison with the use of charcoal. Maximum cold gas and thermal efficiencies obtained were 64.6% and 16% at 4.5 kW and 9 kW loading, respectively. The CO and HC emissions of the gas engine operated on MSW briquettes were higher than that on charcoal, while the exhaust temperatures were similar. ©2019. CBIORE-IJRED. All rights reserved


Energy ◽  
2018 ◽  
Vol 163 ◽  
pp. 513-518 ◽  
Author(s):  
Prakashbhai R. Bhoi ◽  
Raymond L. Huhnke ◽  
Ajay Kumar ◽  
Natarianto Indrawan ◽  
Sunil Thapa

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