Biomass gasification of oil palm fronds (OPF) and Koompassia malaccensis (Kempas) in an entrained flow gasifier: A performance study

Ismail, Wan Muhammad Syafiq Wan; Thaim, Thuraiya; Rasid, Ruwaida Abdul

doi:10.1016/j.biombioe.2019.03.012

Cited by 14 publications

(4 citation statements)

References 25 publications

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“…The reactions involved during biomass conversion process are summarized in Table 1 [7]. In Malaysia, many work related to the thermochemical conversion of biomass has been concentrated on palm oil derived biomass due to its abundancy and wide availability [8,9]. In order to broaden the range of biomass utilized for renewable energy generation, which directly supports the fuel diversification policy of Malaysia, new potential renewable energy resources are being explored.…”

Section: Introductionmentioning

confidence: 99%

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

et al. 2019

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Fuel resource diversification is a global effort to deviate from non-renewable fossil fuels. Biomass has been identified as an alternative solid biofuel source due to its desirable properties and carbon neutrality. As reported in the literature, biomass can positively contribute towards combating climate change while providing alleviation for energy security issue. As part of efforts to diversify biomass resources, this work intends to explore the potential of Napier grass, one type of energy crop, for the production of renewable syngas via gasification. This energy crop is originally from Africa, which is highly productive with low cost (40 tonnes per year per hectare). Limited studies were conducted to analyze the potential of such an energy crop as a fuel source, which is the subject of this work. In order to analyze the full potential of such energy crop, the physical and chemical characteristics of this biomass was first analyzed. To determine the productivity of syngas from this biomass, fluidized bed gasifier was used in this work. The effects of gasification process parameters (i.e., equivalence ratio and temperature) on product yield and producer gas compositions were examined. Besides, the effects of equivalence ratio towards higher heating value of syngas and carbon conversion efficiency were analyzed. Based on the ultimate analysis results, the molecular formula of Napier gas was CH1.56O0.81N0.0043. Meanwhile, the higher heating value of such biomass was determined as 16.73 MJ/kg, which was comparable to other biomasses. It is noted that in this work, the volatile matter was determined as 85.52% and this promoted gasification process remarkably. The dynamics of the reactions involved were observed as a significant variation in product yield and biogas components were recorded at varying equivalence ratio and gasifier operating temperature.

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Section: Introductionmentioning

confidence: 99%

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

et al. 2019

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“…The temperature is selected as the popular gasification temperature of biomass in the actual gasifier at 800 °C. 29 The total gas volume at room temperature was controlled at 1.8 L/min, and both carrier gas and fluidized gas were Ar gas. The specific experimental parameters are shown in Table 2.…”

Section: Methodsmentioning

confidence: 99%

Characteristics of Gas–Liquid–Solid Products in Corn Straw Gasification: Effect of the Char–Tar–H₂O Interaction

et al. 2019

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The characteristics of gas–liquid–solid products during corn straw–H2O gasification were studied by the one-stage fluidized-bed/fixed-bed quartz reactor. The results indicate that the transformation between gas and solid products is mainly presented with the increase of feeding time (0–40 min). The aromaticity of biochar decreases slightly in the feeding period of 10–20 min but gradually increases in 20–40 min. The oxygen-containing functional groups in biochar increase gradually with the increase of the feeding time. The K content in biochar increases by 27% in 10–30 min, while that of Ca increases by 36% in 10–20 min. When the carbon conversion rate is less than 8%, the reactivity of biochar produced by 30 min of feeding is highest. The contents of phenol and 2,3-dihydrobenzofuran of tar increase by 25 and 34%, respectively in 20–40 min. The char–tar–H2O interaction in biomass gasification is a two-stage reaction. The first stage is dominated by the volatile–char interactions, while the second stage is mainly due to the char–H2O reaction.

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“…Outcomes endorsed that with two carbon-based reactants, it is feasible to check gas formation concerning the significant outputs. On 1500 o C, that steadiness results correctly divined the synthesis gas composition plus it may be applied for design optimization from the syngas to downstream fluid fuel synthesis manufactory(Ismail et al, 2019).…”

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confidence: 92%

Energy production from steam gasification processes and parameters that contemplate in biomass gasifier – A review

Siwal

Zhang

Sun

et al. 2020

Bioresource Technology

110

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The transformation of biomass using steam gasification is a chemical route to facilitate changes in organic or residue supported carbonaceous substances addicted to carbon mono-oxide, hydrogen including carbon-dioxide , etc. However, to commercialize the method of steam gasification, the hurdles persist during the gasification as well as downstream processing. This article delivers a summary of the different approaches that are described in the previous studies to achieve H2 refinement and adaptation within the gasifier system. These include advanced aspects in the research and development of biomass gasification (alike advancements under the gasification operation). The upshot of diverse operating conditions like steam flow rate, operating temperature, moisture content, gasifier agents, residence time, biomass to air, steam to biomass, equivalence ratio, etc. towards the execution of biomass gasifier. This review accomplishes that the interdependence of several issues must be considered in point to optimise the producer gas.

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Biomass gasification of oil palm fronds (OPF) and Koompassia malaccensis (Kempas) in an entrained flow gasifier: A performance study

Cited by 14 publications

References 25 publications

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

Characteristics of Gas–Liquid–Solid Products in Corn Straw Gasification: Effect of the Char–Tar–H₂O Interaction

Energy production from steam gasification processes and parameters that contemplate in biomass gasifier – A review

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Biomass gasification of oil palm fronds (OPF) and Koompassia malaccensis (Kempas) in an entrained flow gasifier: A performance study

Cited by 14 publications

References 25 publications

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

Thermochemical Conversion of Napier Grass for Production of Renewable Syngas

Characteristics of Gas–Liquid–Solid Products in Corn Straw Gasification: Effect of the Char–Tar–H2O Interaction

Energy production from steam gasification processes and parameters that contemplate in biomass gasifier – A review

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Characteristics of Gas–Liquid–Solid Products in Corn Straw Gasification: Effect of the Char–Tar–H₂O Interaction