2020
DOI: 10.1021/acs.energyfuels.0c01323
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Coke Formation during Thermal Treatment of Bio-oil

Abstract: Bio-oil is a mixture of organics produced from pyrolysis of biomass. The organics in bio-oil serve as the feedstock for the production of hydrogen, chemicals, biofuels, and carbon materials. In many processes for conversion of bio-oil, heating is required. The thermal treatment of bio-oil induces the polymerization/cracking of the organics in bio-oil, producing coke. Coke could lower the carbon conversion efficiency of bio-oil, clog the reactor chamber, and deactivate the catalyst, imposing the main challenge … Show more

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Cited by 137 publications
(61 citation statements)
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References 351 publications
(1,214 reference statements)
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“…Bio-oil is a mixture of organic compounds obtained from the pyrolysis of biomass. Among these compounds are sugar monomers and oligomers, as well as sugar derivatives, such as carboxylic acids, aldehydes, ketones, esters, and alcohols [78]. e abundant presence of carboxylic acids makes the bio-oil corrosive.…”
Section: Bio-oilmentioning
confidence: 99%
“…Bio-oil is a mixture of organic compounds obtained from the pyrolysis of biomass. Among these compounds are sugar monomers and oligomers, as well as sugar derivatives, such as carboxylic acids, aldehydes, ketones, esters, and alcohols [78]. e abundant presence of carboxylic acids makes the bio-oil corrosive.…”
Section: Bio-oilmentioning
confidence: 99%
“…Currently, most industrial chemicals as well as those used in daily life are obtained from fossil fuel feedstocks. Nevertheless, research on the production and separation of chemicals from bio-oil has been stimulated in the last few years [58]. Different methods have been applied to separate chemicals from bio-oil.…”
Section: Bio-oil To High-value Chemicalsmentioning
confidence: 99%
“…Fixed bed reactors are more commonly used and, as shown in Figure 4, they are typically made up of a cylindrical vessel packed with catalyst pellets. However, fixed bed reactors are susceptible to coke deposition over the catalyst surface, limiting the operating time and hydrogen yield due to the large amount of residue formed, especially when reforming larger model compounds or crude bio-oil [105]. Thus, this type of reactor is preferred for the reforming of lighter model compounds, such as acetic acid and ethanol.…”
Section: Effect Of the Reactor Typementioning
confidence: 99%
“…This effect is more pronounced when reforming raw bio-oil. An excellent review, presenting issues related to coking in the processes of bio-oil upgrading, the properties of coke formed, the mechanism for coking and the methods developed for tackling it has been provided by Hu et al [105].…”
Section: Coke Formationmentioning
confidence: 99%
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