Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process

Fluidized catalytic cracking (FCC) converts hydrocarbons in the presence of a catalyst based on faujasite zeolite (USY and REY). While hydrocarbon is poorly reactive, biomass and its derived compounds are highly functionalized and not suitable to a typical FCC process. To overcome this limitation bi...

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Main Authors: Joana Pinto, Igor Pedrosa, Camila Linhares, Rosane A. S. San Gil, Yiu Lau Lam, Marcelo Maciel Pereira
Format: Article
Language:English
Published: Frontiers Media S.A. 2019-11-01
Series:Frontiers in Chemistry
Subjects:
USY
Online Access:https://www.frontiersin.org/article/10.3389/fchem.2019.00720/full
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spelling doaj-af61501055d44549a74f247b1b38fa432020-11-24T21:44:15ZengFrontiers Media S.A.Frontiers in Chemistry2296-26462019-11-01710.3389/fchem.2019.00720480146Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking ProcessJoana PintoIgor PedrosaCamila LinharesRosane A. S. San GilYiu Lau LamMarcelo Maciel PereiraFluidized catalytic cracking (FCC) converts hydrocarbons in the presence of a catalyst based on faujasite zeolite (USY and REY). While hydrocarbon is poorly reactive, biomass and its derived compounds are highly functionalized and not suitable to a typical FCC process. To overcome this limitation biomass was first converted into a dense and stable bio-crude composed mainly of ketal-sugar derivatives by using acetone in diluted acid. Here, a representative compound of this bio-crude, 1,2:3,5-di-O-isopropylidene-α-D-xylofuranose (DX) in n-hexane, was converted by USY and a commercial FCC catalyst containing USY, at 500°C, in a fixed bed and fluidized bed reactors, respectively. Faujasite Y is very efficient in converting DX. More than 95% conversion was observed in all tests. Over 60 wt.% was liquid products, followed by gas products and only around 10% or less in coke. The higher the catalyst activity the greater the aromatics in the liquid products and yet higher coke yields were observed. In particular, simulating more practical application conditions: using deactivated catalyst in a fluidized bed reactor, improved green hydrocarbons production (mono-aromatic up to 10 carbons and light hydrocarbon up to eight carbons) and unprecedented lower coke yield (≈5 wt.%) for bio-feeds. The present results further suggest that catalyst will play a primary role to convert the bio-crude into target hydrocarbons and overcome the transition of a non-renewable to a renewable refinery feed.https://www.frontiersin.org/article/10.3389/fchem.2019.00720/fullsugar ketalsbiocrudeUSYhydrocarbonsaromatics
collection DOAJ
language English
format Article
sources DOAJ
author Joana Pinto
Igor Pedrosa
Camila Linhares
Rosane A. S. San Gil
Yiu Lau Lam
Marcelo Maciel Pereira
spellingShingle Joana Pinto
Igor Pedrosa
Camila Linhares
Rosane A. S. San Gil
Yiu Lau Lam
Marcelo Maciel Pereira
Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
Frontiers in Chemistry
sugar ketals
biocrude
USY
hydrocarbons
aromatics
author_facet Joana Pinto
Igor Pedrosa
Camila Linhares
Rosane A. S. San Gil
Yiu Lau Lam
Marcelo Maciel Pereira
author_sort Joana Pinto
title Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
title_short Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
title_full Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
title_fullStr Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
title_full_unstemmed Ketal Sugar Conversion Into Green Hydrocarbons by Faujasite Zeolite in a Typical Catalytic Cracking Process
title_sort ketal sugar conversion into green hydrocarbons by faujasite zeolite in a typical catalytic cracking process
publisher Frontiers Media S.A.
series Frontiers in Chemistry
issn 2296-2646
publishDate 2019-11-01
description Fluidized catalytic cracking (FCC) converts hydrocarbons in the presence of a catalyst based on faujasite zeolite (USY and REY). While hydrocarbon is poorly reactive, biomass and its derived compounds are highly functionalized and not suitable to a typical FCC process. To overcome this limitation biomass was first converted into a dense and stable bio-crude composed mainly of ketal-sugar derivatives by using acetone in diluted acid. Here, a representative compound of this bio-crude, 1,2:3,5-di-O-isopropylidene-α-D-xylofuranose (DX) in n-hexane, was converted by USY and a commercial FCC catalyst containing USY, at 500°C, in a fixed bed and fluidized bed reactors, respectively. Faujasite Y is very efficient in converting DX. More than 95% conversion was observed in all tests. Over 60 wt.% was liquid products, followed by gas products and only around 10% or less in coke. The higher the catalyst activity the greater the aromatics in the liquid products and yet higher coke yields were observed. In particular, simulating more practical application conditions: using deactivated catalyst in a fluidized bed reactor, improved green hydrocarbons production (mono-aromatic up to 10 carbons and light hydrocarbon up to eight carbons) and unprecedented lower coke yield (≈5 wt.%) for bio-feeds. The present results further suggest that catalyst will play a primary role to convert the bio-crude into target hydrocarbons and overcome the transition of a non-renewable to a renewable refinery feed.
topic sugar ketals
biocrude
USY
hydrocarbons
aromatics
url https://www.frontiersin.org/article/10.3389/fchem.2019.00720/full
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