Title:
Separation processes to improve utilization of bio-oil from switchgrass pyrolysis

dc.contributor.advisor Yiacoumi, Sotira
dc.contributor.author Park, Lydia Kyoung-Eun
dc.contributor.committeeMember Tsouris, Costas
dc.contributor.committeeMember Pavlostathis, Spyros G.
dc.contributor.committeeMember Fernandez, Facundo M.
dc.contributor.committeeMember Borole, Abhijeet P.
dc.contributor.department Civil and Environmental Engineering
dc.date.accessioned 2018-05-31T18:08:48Z
dc.date.available 2018-05-31T18:08:48Z
dc.date.created 2017-05
dc.date.issued 2017-04-06
dc.date.submitted May 2017
dc.date.updated 2018-05-31T18:08:48Z
dc.description.abstract Bio-oil produced from biomass pyrolysis, a thermochemical decomposition process, has potential as a biorenewable energy source. Its challenging properties, including high acidity and high moisture content, however, hinder its applications. The main objective of this study is to separate components of switchgrass pyrolysis bio-oil through various processes in order to improve its utilization. The research targets the acidity of bio-oil and explores separation processes such as solvent extraction, water addition, pH neutralization, and capacitive deionization (CDI). A standard total acid number (TAN) analysis was employed to better understand the acidity of aqueous bio-oil. Aqueous and organic components of switchgrass bio-oil were separated via solvent extraction, water addition, and pH neutralization in order to produce an aqueous bio-oil phase that has high concentrations of organic acids and low concentrations of heavy organic compounds. Optimal phase separation occurred after the pH of bio-oil was raised to 6. The aqueous bio-oil phase is suitable for microbial electrolysis to produce hydrogen as an energy source; hydrogen is also needed to further upgrade bio-oil via hydrodeoxygenation. TAN analysis of aqueous bio-oil revealed that some organic acids (e.g., vanillic acid) that act as polyprotic acids have a stronger influence on the acidity of bio-oil than acids (e.g., acetic acid) that act as monoprotic acids. Process-intensification devices, including a static mixer and a centrifugal contactor, were employed as continuous-flow pH-neutralization reactors. These continuous-flow systems were found to be effective, and the results were comparable to those from batch systems with long reaction times demonstrating a potential to scale up pH neutralization of bio-oil. In addition, the study involves removal of acidic components via water extraction to reduce the acidity of the organic bio-oil phase, which can be used to produce fuel or other products such as resin. Acids removed by water were recovered through CDI for use in microbial electrolysis. This research is an intermediate step between biomass pyrolysis for bio-oil production and microbial electrolysis for hydrogen generation and further upgrading of bio-oil. It is a necessary step toward closing the carbon cycle of the overall bio-oil production and upgrading processes, so that bio-oil can become a carbon-neutral energy source.
dc.description.degree Ph.D.
dc.format.mimetype application/pdf
dc.identifier.uri http://hdl.handle.net/1853/59780
dc.language.iso en_US
dc.publisher Georgia Institute of Technology
dc.subject Bio-oil
dc.subject Pyrolysis oil
dc.subject Capacitive deionization
dc.subject Centrifugal contactor
dc.subject Total acid number
dc.subject Acidity
dc.title Separation processes to improve utilization of bio-oil from switchgrass pyrolysis
dc.type Text
dc.type.genre Dissertation
dspace.entity.type Publication
local.contributor.advisor Yiacoumi, Sotira
local.contributor.corporatename School of Civil and Environmental Engineering
local.contributor.corporatename College of Engineering
relation.isAdvisorOfPublication fc1c6a3a-5a00-40ba-9671-5944666a4688
relation.isOrgUnitOfPublication 88639fad-d3ae-4867-9e7a-7c9e6d2ecc7c
relation.isOrgUnitOfPublication 7c022d60-21d5-497c-b552-95e489a06569
thesis.degree.level Doctoral
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