200 °C). Finally, a key feature of this technology is it permits recycling and reuse of the catalysts, solvents and reaction media.' />
Source: UNIVERSITY OF TOLEDO, THE submitted to NRP
A NEW TECHNOLOGY FOR HIGH YIELD CONVERSION OF BIOMASS CARBOHYDRATES TO FURANS FOR BIOPRODUCTS
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
ACTIVE
Funding Source
Reporting Frequency
Annual
Accession No.
1015100
Grant No.
2018-67021-27953
Cumulative Award Amt.
$489,987.00
Proposal No.
2017-06808
Multistate No.
(N/A)
Project Start Date
Mar 15, 2018
Project End Date
Dec 14, 2025
Grant Year
2018
Program Code
[A1531]- Biorefining and Biomanufacturing
Recipient Organization
UNIVERSITY OF TOLEDO, THE
2801 W BANCROFT ST
TOLEDO,OH 43606-3390
Performing Department
Chemical Engineering
Non Technical Summary
Furans are versatile "platform molecules" that can be converted to "drop-in" fuels as well as a wide array of chemical products. The biomass derived furans - hydroxymethyl furfural (HMF) and furfural - made from dehydration of glucose and xylose are ranked second among the top-ten most promising building block chemicals in DOE's recently revised list. HMF and furfural can serve as precursors for a number of industrially-important syntheticic materials, solvents, resins and pharmaceutical molecules. Noteworthy among these are the monomer molecules diformyl-furan and furandicarboxylic acid (FDCA) obtained from catalytic oxidation of HMF. FDCA was shown by Avantium Chemicals to be a superior replacement for terephthalic acid - the petrochemical precursor for poly-ethylene terephthalate (PET) plastic, with multi-billion dollar market capitalization worldwide. Furans can also be converted to hydrocarbon molecules compatible with jet fuel, diesel and gasoline. In spite of this huge potential, the promise of furan-derived products remains unfulfilled to date due to the inability to produce furans economically from biomass feedstocksThis project will develop bio-based furfural and HMF that can be further upgraded to biopolymers, biosolvents, fuel additives and fuels. Although sugars derived from biomass carbohydrates are aldoses (i.e., glucose and xylose), the best furan yields can be obtained via dehydration of the corresponding keto-isomers (i.e., fructose and xylulose) in non-aqueous media. The challenge then is to devise a pathway to efficiently transfer sugars from biomass hydrolysate into the non-aqueous media; produce the furan in high yield; and isolate it for downstream processing, all with low energy input and recycling of process streams. This research project addresses these challenges: we propose a process in which (1) the conversion of hydrolyzate sugars to ketoses and their near-complete recovery is accomplished through a novel simultaneous-isomerization-and-reactive-extraction (SIRE) process, and (2) the recovered ketoses are dehydrated to furans in an acidic ionic liquid (IL) reaction medium and simultaneously extracted into a low-boiling immiscible solvent to prevent side reactions, increase process yields and facilitate easy product recovery. Reactions of ketoses to furans in IL-media result in superior yields and also occur at mild operating conditions (IL rxn T ~ 50 °C; aqueous rxn T >200 °C). Finally, a key feature of this technology is it permits recycling and reuse of the catalysts, solvents and reaction media.
Animal Health Component
40%
Research Effort Categories
Basic
10%
Applied
40%
Developmental
50%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
51106502020100%
Goals / Objectives
The overall goal is to develop a cohesive pathway for high-yield production of HMF and furfural from C6 and C5 sugars in biomass hydrolysates. For high yield production of furans directly from biomass hydrolysates, our technology uses a three step hybrid enzyme- and chemo-catalytic approach that in Step 1 converts the aldose sugars in biomass hydrolysate to their keto-forms in high yields via simultaneous-isomerization-and-reactive-extraction (SIRE); in Step 2 efficiently and selectively transfers the isomerized keto-sugars into an ionic liquid (IL) reaction medium by back-extraction (BE) with no concomitant transfer of hydrolysate impurities (e.g. phenolics); and in Step 3 facilitates high yield ketose dehydration to furans with in situ extraction. In addition, the high selectivity of each of the process steps allows for efficient recycle and reuse of the IL medium and extraction solvents to minimize costs and environmental impacts associated with fresh chemical inputs. Finally, all processing steps occur at mild operating conditions (T = 50-60 °C, P = 1 bar) that allows for a safe process with low capital and energy costs. To our knowledge, this is the first technology that is able to convert both the hemicellulose and cellulose sugars simultaneously to their corresponding furans in high yield in an integrated process.The specific goal of this research project is to demonstrate an economically viable and environmentally sustainable process for the production of furans from biomass hydrolysates via an integrated SIRE-BE-dehydration-in-IL process. To obtain process metrics, we will perform studies using hydrolysates from several established pretreatment techniques, namely dilute acid- , IL- , and ammonia fiber explosion (AFEX)- pretreatment methods. The specific objectives of the project are to:Achieve high ketose selectivity (>95%) during SIRE from concentrated hydrolysates (up to 160 g/L sugars) through comprehensive assessment of the reaction/extraction chemistries (Step 1).Design a two-stage back-extraction (BE) protocol for selective recovery of unreacted aldoses for re-isomerization and exclusive transfer of ketose sugars to the IL (Step 2).Maximize furan yields in a tailored IL reaction medium designed through (i) judicious evaluation of a broad range of acidic ILs, and (ii) incorporation of specific Lewis and/or Brønsted acid catalysts and other metal halides for promoting the desired reaction pathway (Step 3).Develop strategies for in situ recovery of the thermally-labile furans from reaction media including (i) extraction into low boiling point (bp) immiscible solvents; (ii) entrainer-enhanced vacuum distillation; and (iii) simultaneous dehydration and conversion to stable and easily recoverable HMF derivatives (e.g. acetoxy methyl furfural).Assess performance of solvent and reaction media during prolonged reuse.Conduct techno-economic evaluation to inform and assess process alternatives.
Project Methods
First the three principal process steps our our technology are described briefly and then the tasks proposed to optimize these steps are outlined.In Step 1 the conversion of hydrolysate sugars to ketoses and their near-complete recovery is accomplished through SIRE process. SIRE uses commercially-available immobilized glucose-xylose isomerase (GXI) enzyme pellets, single-pass ketose yields are low (50%) due to unfavorable equilibrium for the isomerization. In SIRE, the ketose sugars are rapidly extracted into an immiscible organic phase (octanol) as they are formed. This reactive-extraction is facilitated through selective and pH-dependent ester formation (pH = 8-8.5) of the ketose sugars with an arylboronic acid (ABA) solubilized in octanol and coincides with the pH optimum of GXI. A lipophilic ammonium salt (Aliquat® 336 or Q+Cl-) in the organic phase serves to stabilize the sugar-ABA ester. As a result, near-complete isomerization of the sugars is achieved at mild process conditions.In Step 2, the ketose-rich octanol phase is contacted with the immiscible IL 1-ethyl-3-methylimidazolium hydrogen sulfate ([EMIM]HSO4). This acidic IL promotes the hydrolysis of the ketose-ABA ester to back-extract (BE) ketose sugar into the IL medium. The ABA and hydrophobic phenolics stay in the octanol phase during the transfer of ketoses to IL, and as a result of the back-extraction, only keto-sugar-isomers are transferred into the IL medium. The sugar-lean organic phase (containing ABA and octanol) is recycled back to Step 1 for re-use.In Step 3, ketoses in the IL medium are dehydrated to furans (fructose to HMF and xylulose to furfural, Trxn = 50°C) with in situ extraction into the immiscible and low-boiling solvent tetrahydrofuran (THF; b.p. 66°C) that has a high affinity for furans. The removal of furans by extraction permits re-use of the reaction medium without exposing IL to the high boiling temperature of furfural (T>160°C) and avoids its thermal degradation. After distillation and recovery of furans, THF can also be recycled.Task 1: Comprehensive assessment of the reaction/extraction chemistries for high ketose selectivity during SIRE from concentrated hydrolysates.Task Summary: Each boronic acid in the organic phase is capable of reversibly complexing one sugar molecule in the aqueous phase. Thus, the molar solubility of the ABA in the organic phase represents an upper limit on the concentration of sugar that can be transferred into the organic phase. In Task 1.1, we will implement SIRE using Napthalene2- Boronic acid (N2B) on IL-pretreated biomass hydrolysates (prepared using our patented technologies) at concentrations of 120 to 160 g/l sugar at up 1 L scale. Since the sugar binding capacity of the organic phase is dependent on both the ABA and the organic phase diluent, in Task 1.2 we will screen ABAs and organic phase components to determine other ABA/organic phase compositions that can perform better than N2B with regards to sugar-extraction and ketose-selectivity. In Task 1.3 we evaluate SIRE performance at up to 1 L scale on biomass hydrolysate from dilute-acid and AFEX pretreatments. A 1 L hollow-fiber liquid/liquid contacting system designed and built for these reactive extractions will be used for larger scale experiments.Milestone 1.2.1 Identify alternate ABA and organic diluent combinations for 1 stage SIRE with ≥55% sugar recovery and ≥85% ketose selectivity on IL-pretreated biomass hydrolysate at 120-160 g/l sugar. (M24)Milestone 1.2.2 Identify alternate ABA and organic diluent combinations for 3-stage SIRE with ≥85% sugar recovery and ≥85% ketose selectivity on IL-pretreated biomass hydrolysate at 120-160 g/l sugar. (M33)Milestone 1.3.1 Validate 3-stage SIRE on 1 L scale with ≥85% sugar recovery and ≥85% ketose selectivity on dilute acid- and AFEX-pretreated biomass hydrolysate at 120-160 g/l sugar. (M42)Task 2: Two-stage back extraction for transfer of high-purity ketose sugars to IL.Task Summary: Following SIRE, a ketose-rich mixture of sugars complexed to ABA resides in the organic phase. Aldose can be stripped from the ABA more-easily. If the fructose extraction selectivity during SIRE is <95%, the organic phase can be enriched in ketose by selectively back-extracting aldose sugar from the organic phase. By back-extracting sugars in two-stages, aldose sugar can be concentrated and recovered in the first stage aqueous strip solution and recycled back to SIRE. The highly-pure ketose sugars (≥ 95%) remaining in the organic phase can be back-extracted into IL in a second stage for dehydration. To assess whether a two-stage back-extraction process is suitable for a specific ABA/organic phase combination, sugar stripping curves (i.e. aldose/ketose binding equilibrium curves as a function of pH) will be generated and used to evaluate suitability of the organic phases for ketose-sugar enrichment by staged back-extraction.Milestone 2.1.1 Demonstrate stage 1 back-extraction criteria for enriching the organic phase to >95% ketose while releasing <40% of the ketose sugars into the stripping solution. (M33)Milestone 2.2.1 Validate 3-stage SIRE-BE on 1 L scale with >90% sugar isomerization and ≥95% ketose back-extracted into IL for dilute acid- and AFEX-pretreated biomass hydrolysate at 120-160 g/l sugar. (M45)Task 3: Dehydration of ketoses in IL, furan recovery and IL recycle (M0-M39) - Co-leads: Varanasi & RelueTask Summary: ILs provide an ideal non-volatile catalytic medium for high-yield furan formation as they mitigate many undesirable side reactions . Yield can be further improved if in-situ furan recovery is implemented. Several strategies can be envisioned: (1) in-situ extraction into a solvent immiscible with the IL; (2) entraining the furan in vapor form with a carrier gas via vacuum-distillation of the IL-reaction medium; and (3) in-situ transformation of the furan (in IL) to a more stable and readily extractable high-value compound. These strategies for furan isolation from IL, coupled with near-complete conversion of ketoses, facilitate the recycle of the IL. We have demonstrated in-situ extraction of both HMF and furfural from [EMIM]HSO4 into the immiscible low-boiling solvent THF; furans can be recovered from THF via distillation with no risk of HMF degradation. During this task, we will first optimize the base case of IL/HMF/IL-immiscible extraction-solvent system for different reaction conditions.Milestone 3.1.1: Validate 80% furan reaction yield for 10 wt % sugar (g sugar/g IL) starting from IL-pretreated biomass hydrolysate at 120-160 g/l sugar (M18)Milestone 3.1.2: Validate IL recyclability for 8-10 cycles of dehydration/furan removal with < 10% loss in dehydration yield. (M36)Milestone 3.2.1-To be considered viable, the alternate scheme should lead to 70% total furan yield in the IL for 10 wt % sugar (g sugar/g IL) starting from IL-pretreated biomass hydrolysate at 120-160 g/l. (M39)Task 4: Evaluation of alternate ILs and process TEA (M15-M48)Task summary: Through the screening process, the best task-specific ILs will be identified based on performance and cost. Techno-economic analysis (TEA) will be used to assess the impact of process parameters such as conversion yields, separation efficiencies, reaction conditions, and material loading rates on the overall economics of our process and guide us toward the most important process parameters for R&D.Milestone 4.1.1 To be considered a viable alternate to [EMIM]HSO4, the IL, in addition to meeting the criteria listed above, should lead to 80% furan reaction yield for 10 wt % sugar (g sugar/g IL) starting from IL-pretreated biomass hydrolysate at 80 g/l. (M42)Milestone 4.2.1 The TEA of the process with the final case metrics will be used to calculate the minimum HMF production cost (M48)

Progress 03/15/24 to 12/14/24

Outputs
Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?The project provided training opportunities for an undergraduate student. How have the results been disseminated to communities of interest?A conference presentation; broader community engagement was through activities in the UToledo College of Engineering such as the UT Experience Day. What do you plan to do during the next reporting period to accomplish the goals?We would like to complete and submit the following two manuscripts, if provided an additional NCE. Gogar R, Viamajala S, Relue P, Varanasi S. 2025. "High yield synthesis of HMF from glucose in the water-organic solvent system." Manuscript under preparation Bharadwaz A, Raheja G, Relue P, Viamajala S. 2025. "Recovery of high-purity glycerol from biodiesel waste? via reactive extraction?." Manuscript under preparation

Impacts
What was accomplished under these goals? This year we investigated downstream conversion of glycerol to acrolein and acrylic acid. Acrylic acid is one of the most desirable and high demand products obtainable from glycerol and its annual production is ~10 million tons and is expected to continue growth. The traditional process for the synthesis of acrylic acid, developed by BASF, involves oxidation of propylene to acrolein and a subsequent oxidation of acrolein to acrylic acid. As an alternative to this petroleum-based approach to acrylic acid, we investigated a biobased pathway for acrolein (and subsequently acrylic acid) production from glycerol by catalytic dehydration. We investigated both liquid phase and gas phase conversion. Aqueous phase dehydration was explored with a number of acid catalysts at varying concentrations, as well as with the addition of organic additives or co-solvents. The most promising result was obtained in a biphasic system comprised of aqueous glycerol and isododecane with KHSO4 as the acid catalyst. After a 6 h reaction time, the acrolein yield was ~10% and compared favorably with previous results reported in the literature. We also investigated glycerol dehydration by cracking on a hot catalyst bed comprising of 40 wt% acid (H2SO4 or H3PO4)/silica gel catalysts. The acrolein yields using H2SO4, KHSO4 and H3PO4 were 7.7%, 6.4%, and 4.7%, respectively. Finally, we also investigated gas phase dehydration and oxidations reactions of glycerol. Advantages to this approach as compared to homogenous liquid phase catalysis include higher attainable reaction temperatures at lower pressure, simpler separation of reaction products and the ability to couple glycerol dehydration with the known gas phase oxidation of acrolein to afford acrylic acid, which is already employed in the industrial production of acrylic acid from propene. Conversion of glycerol was generally high; however, analysis by GC was difficult due to broad bands and other analyses will need to be pursued.

Publications

  • Type: Conference Papers and Presentations Status: Published Year Published: 2024 Citation: Bharadwaz A, Raheja G, Relue P, Viamajala S. Recovery of High-purity glycerol from biodiesel waste via reactive extraction. Poster presentation at the 46th Symposium on Biomaterials, Fuels and Chemicals. Alexandria, VA. (April 28 - May 1, 2024).


Progress 03/15/23 to 03/14/24

Outputs
Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?This project provided training for graduate students and undergraduate students. How have the results been disseminated to communities of interest?Broadcommunity engagement was through activities in the UToledo College of Engineering such as the UT Experience Day. What do you plan to do during the next reporting period to accomplish the goals?Evaluate the production of polyacrylic acid from purified glycerol obtained after the RE-BE process. Glycerol purified through the RE-BE process will be reacted in a two-phase system to generate acrolein, following a process similar to what we have used previously in generating furans from biomass sugars. The acrolein produced in the reactor would be extracted into toluene and then oxidized to acrylic acid.

Impacts
What was accomplished under these goals? This year we had the following accomplishments for recovery of diols and triols. Below is a summary of our key results: Diols - We screened the reactive extraction of 1,3 propanediol and 2,3 butanediol due to their importance in several industrial applications. Our results show that we have been able to achieve approximately 36% extraction in the case of 1,3 propanediol at room temperature with a 1-octanol-based organic phase containing 1 M each of the quaternary ammonium salt and boronic acid. Similarly, during our 2,3 butanediol reactive extraction studies with the same organic phase composition at room temperature, the two isomers of the diol - meso and racemic - were reactively extracted to the organic phase at 57% and 43%, respectively, relative to the initial concentration in the feed during a single-stage RE-BE process. We also evaluated extraction using a mixture of the isomers and found that the process has potential use for separating the two isomers due to their differential extraction affinity. Triols - In addition to diols, we assessed the efficacy of using the single-stage RE-BE mechanism on the triol glycerol due to the extensive demand for a cost-effective purification method for glycerol, primarily for biorefinery crude stocks/waste. The prevalent purification methods for obtaining glycerol from a crude glycerol stock are energy intense and therefore expensive. In contrast, using facile extraction conditions, we were able to demonstrate >90% recovery of high purity glycerol in a 3-stage RE-BE process.

Publications


    Progress 03/15/22 to 03/14/23

    Outputs
    Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?This project provided training opportunities for a graduate studentand an undergraduate student. Students also presented their work at national conferences. How have the results been disseminated to communities of interest?Conference presentations; broader community engagement was through activities in the UToledo College of Engineering such as the UT Experience Day and Introduce a Girl to Engineering Day. What do you plan to do during the next reporting period to accomplish the goals?Next year, we plan to complete studies on recovery of diols and glycerol using SIRE.

    Impacts
    What was accomplished under these goals? This year we had the following accomplishments. A novel alternate pathway to separate unreacted sugar and product HMF from the mixed-solvent system was developed by addition of toluene as a ternary solvent. Addition of toluene to the water-DME solution results in the formation of two immiscible phases - (i) a water-acetone phase (heavy) and (ii) a DME-toluene phase (light). HMF preferably partitions into the light organic phase while the unreacted sugars remain in the heavy aqueous phase After single-stage phase splitting, about 85% of initial HMF was recovered in the top-organic phase, which is lean in sugar, spent acid, and water. This enables recovery of HMF without the possibility of its degradation into humins or levulinic acid usually caused by sugar, acid, water, or high temperature. After separation of DME by distillation, HMF could be recovered in toluene and can be used for the synthesis of 2,5-diformylfuran, which can be converted into 2,5-furan dicarboxylic acid - a high value polymer precursor. We have performed initial screening experiments for high-purity recovery of propanediol, butanediol, and glycerol. These polyols are versatile platform chemicals, and when recovered in high purity, can serve as precursors for biobased polymers. Our interest in generating these precursors aligns with the recently-released Federal goal of "demonstrate and deploy cost-effective and sustainable routes to convert bio-based feedstocks into recyclable-by-design polymers that can displace >90% of today's plastics and other commercial polymers at scale". Propanediol and butanediol also have broad applications in cosmetics, antifreeze, solvents, and stabilizers. Similarly, glycerol is a triol that is an equally sought-after commodity in areas such as cosmetics, medicine, industrial applications like hydraulic fluids, and the food industry. The cost-effective recovery of these polyols from fermentation broths or from biodiesel production processes have been a long-standing challenge and our approach provides a novel, economically promising solution.

    Publications

    • Type: Conference Papers and Presentations Status: Published Year Published: 2022 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. Integrated Pathway for the Efficient Conversion of Lignocellulosic Sugars to HMF. Platform presentation at the 2022 AIChE Annual Meeting, Phoenix, AZ (November 13-18, 2022).


    Progress 03/15/21 to 03/14/22

    Outputs
    Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?Training opportunities were provided for a graduate student. How have the results been disseminated to communities of interest?Conference presentations to the scientific community; broader community engagement was through activities in the UToledo College of Engineering such as the UT Experience Day. What do you plan to do during the next reporting period to accomplish the goals?Next year, we plan to continue work on the following aspects: Develop methods for separation and recovery of furans from the reaction media. Investigate the use of sire for recovery and purification of industrially relevant polyols such as propane diol, butane diol, and glycerol.

    Impacts
    What was accomplished under these goals? This year we had the following accomplishments. We performed experiments in a 2 L meso-scale flow set-up and completed a mass transfer analysis of the SIRE processes to provide process metrics for further scale-up. To study the SIRE process in the meso-scale flow set-up, isomerization and reactive-extraction were first studied as stand-alone processes in a packed bed reactor and hollow fiber membrane contactor, respectively. The transient behavior of the sugar concentration was compared with those from the bench-scale shake-flask experiments. A good agreement of the experimental concentration profile of sugar in the reactive extraction with that predicted from a theoretical model (mass balance/mass transfer) was observed. Finally, the packed bed reactor and HFMC module were integrated and operated together to experimentally implement the simultaneous-isomerization-and-reactive-extraction process. Isomerization studies demonstrated that the packed bed column provides a large interfacial area and local enzyme concentration for isomerization. At a superficial velocity of 20 mm/s, isomerization was not external-diffusion limited. The theoretical model developed for reactive- extraction in recirculation mode agreed with the experimental data. The reactive-extraction experiments in the hollow fiber module revealed that the mass transfer is limited by diffusion across the hydrophobic membrane. We concluded that as the diffusivity of fructose in the aqueous phase was less than that of fructose-complex in the octanol phase, the use of hydrophilic membrane can reduce the resistance to the mass transfer across the membrane. Performed preliminary investigations on extraction of hydroxymethyl furfural in a ternary phase system.

    Publications

    • Type: Conference Papers and Presentations Status: Published Year Published: 2021 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. High Yield Synthesis of HMF from Glucose in the Water-Organic Solvent System. Platform presentation at the 2021 AIChE Annual Meeting, Boston, MA (November 07-19, 2021).
    • Type: Conference Papers and Presentations Status: Published Year Published: 2020 Citation: Gogar R, Schreur J, Viamajala S, Relue P, Varanasi S. Meso-Scale Studies of Simultaneous-Isomerization-Reactive-Extraction of Glucose to Fructose in a Flow Reactor. Platform presentation at the 2021 AIChE Annual Meeting, Boston, MA (November 07-19, 2021).
    • Type: Peer Reviewed Journal Articles Status: Published Year Published: 2021 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. 2021. Techno-Economic Assessment of Mixed-Furan Production from Diverse Biomass Hydrolysates. ACS Sustainable Chemistry and Engineering 9: 34283438.


    Progress 03/15/20 to 03/14/21

    Outputs
    Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems:During the year, our lab was shut down for nearly 4 months due to COVID lockdown. What opportunities for training and professional development has the project provided?The project provided training opportunities for a graduate student. How have the results been disseminated to communities of interest?Public dissemination of results was limited due to Covid restrictions. A thesis was published. What do you plan to do during the next reporting period to accomplish the goals?Next year, we plan to continue work on the following aspects: Perform experiments for a membrane process for SIRE that would represent a scaled model of a continuous process. Explore methods for separation and recovery of furans from the reaction media.

    Impacts
    What was accomplished under these goals? This year we had the following accomplishments. During the year, our lab was shut down for nearly 4 months due to COVID lockdown. Technoeconomic assessments of the SIRE-BE-dehydration process were performed under two scenarios - (i) using ionic liquid (EMIM-HSO4) as the dehydration medium in a biphasic system with tetrahydrofuran, and (ii) using an acidic water-DME reaction medium. Due to the high yields of ketose sugars during SIRE-BE and high HMF yields during dehydration, both process alternatives showed promising price points. At a feed sugar price of $0.30 per kg, the IL process was estimated to produce HMF at a minimum selling price of $1.42/kg after improvements in solvent recovery costs were included. At the same feed sugar price, the water-DME method simulations assessed the minimum furan selling price (MFSP) to be $1.35/kg. Performed initial assessment of a continuous flow, meso-scale SIRE system using a hollow fiber membrane module.

    Publications

    • Type: Theses/Dissertations Status: Published Year Published: 2020 Citation: Gogar R. Economic Production of Furans from Lignocellulosic Sugars. Ph.D. Thesis. The University of Toledo, 2020.


    Progress 03/15/19 to 03/14/20

    Outputs
    Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?This project provided training opportunities for graduate students and an undergraduate student. Students also presented their work at national conferences. How have the results been disseminated to communities of interest?Conference presentations; broader community engagement was through activities in the UToledo College of Engineering such as the UT Experience Day and Introduce a Girl to Engineering Day. What do you plan to do during the next reporting period to accomplish the goals?Next year, we plan to continue work on the following aspects: Complete technoeconomic analyses for the sugar to furan pathway. Perform experiments for a membrane process for SIRE that would represent a scaled model of a continuous process.

    Impacts
    What was accomplished under these goals? This year we had the following accomplishments: Developed reaction media that result in high dehydration yields. Developed monophasic systems of water-organic solvents-acid catalyst that result in high HMF yields when combined with SIRE-BE Multiple co-solvents (tetrahydrofuran, γ-valerolactone, acetonitrile, acetone, and 1,2-dimethoxy ethane (DME)) and multiple acid catalysts (H2SO4, HCl, and methane sulfonic acid) were tested, with and without the addition of NaCl as a furan rate promoter/stabilizer. Results showed that the novel solvent system of water-DME with added HCl (55mM) gave the highest reaction yields. Hydroxymethyl furfural (HMF) yields were nearly 85% at optimal reaction conditions starting with 150 g/L glucose feed that was processed through SIRE-BE and dehydration. Initiated TEA of the integrated SIRE process with a downstream water-DME dehydration step. Completed experimental setup for membrane based SIRE process.

    Publications

    • Type: Conference Papers and Presentations Status: Published Year Published: 2019 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. Techno-Economic Analysis of Production of Mixed-Furans from Biomass Hydrolysate. Platform presentation at the 2019 AIChE Annual Meeting, Orlando, FL (November 10-14, 2019).
    • Type: Conference Papers and Presentations Status: Published Year Published: 2019 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. A Novel Method of Producing 2,5-Diformylfuran at High Yields from Glucose. Platform presentation at the 2019 AIChE Annual Meeting, Orlando, FL (November 10-14, 2019).
    • Type: Conference Papers and Presentations Status: Published Year Published: 2019 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. Furan production from biomass hydrolysates: Scale-up and techno-economic study of a novel, high-yield 'SIRE-BE-Dehydration' process. Platform presentation at the 2019 Gordon Research Conference on Biomass to Biobased Chemicals and Materials, Newry, ME (July 14-19, 2019).


    Progress 03/15/18 to 03/14/19

    Outputs
    Target Audience:The target audience is the scientific community and bioproduct industry. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?This project provided post-doctoral training for Peng Zhang. How have the results been disseminated to communities of interest?Conference presentations and thesis. What do you plan to do during the next reporting period to accomplish the goals?Next year, we plan to continue work on the following aspects: Develop reaction media that results in high sugar dehydration yields for formation of hydroxymethyl furfural (HMF) and furfural Perform experiments for a membrane process for SIRE that would represent a scaled model of a continuous process. Initiate technoeconomic analyses for the sugar to furan pathway.

    Impacts
    What was accomplished under these goals? This year we had the following accomplishments: 1. Demonstrated high ketose selectivity with concentrated sugar streams in SIRE Demonstrated >90% selectivity of fructose and xylulose after a 4-stage SIRE process on a 40 g/L feed stream containing glucose and xylose in a 3:1 mass ratio. Demonstrated ~80% fructose selectivity after single stage SIRE on a 160 g/L glucose feed stream. 2. Designed multiple BE strategies that improved purity of the ketose products Developed a two-stage BE method that resulted in high overall purity (~90%) of ketose sugars when concentrated mixed sugar feed stream (220 g/L) was used. The second BE stage resulted in nearly pure ketose sugars (96%). We demonstrated that the conditions of SIRE can be customized to maximize xylulose purity or xylulose yield under equilibrium conditions by changing the N2B:C5 sugar mole ratio. Transient SIRE can be used to exploit the differential isomerization kinetics of glucose and xylose to further increase xylulose purity of the separation. Xylulose yield can be increased by conducting SIRE on the hydrolysate for multiple cycles. Using 5 cycles of transient SIRE, on a sugar stream containing a 1:2 xylose:glucose mass ratio resulted in a 40% xylulose yield with ~90% xylulose purity. This is particularly significant considering that C5 is a minor sugar, initially present in a mole ratio of xyluse:glucose of 0.6, a ratio expected for biomass hydrolysate.

    Publications

    • Type: Conference Papers and Presentations Status: Published Year Published: 2018 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. Furan Production from Biomass Hydrolysates: Scale-up of a Novel, High-Yield SIRE Process. Platform presentation at the 2018 AIChE Annual Meeting, Pittsburgh, PA (October 28 - November 2, 2018).
    • Type: Conference Papers and Presentations Status: Published Year Published: 2018 Citation: Gogar R, Viamajala S, Relue P, Varanasi S. Production of 2,5-Furan Dicarboxylic Acid (FDCA) in Ionic Liquid Media. Platform presentation at the 2018 AIChE Annual Meeting, Pittsburgh, PA (October 28 - November 2, 2018).
    • Type: Theses/Dissertations Status: Published Year Published: 2018 Citation: Zhang, P. (2018). Optimizing Simultaneous-Isomerization-and-Reactive-Extraction (SIRE) Followed by Back-Extraction (BE) Process for Efficient Fermentation of Ketose Sugars to Products [Doctoral dissertation, University of Toledo]. OhioLINK Electronic Theses and Dissertations Center. http://rave.ohiolink.edu/etdc/view?acc_num=toledo1524617555286546