Source: MISSISSIPPI STATE UNIV submitted to NRP
DEVELOPMENT OF NEW CATALYTIC SYSTEMS FOR THE PRODUCTION OF RENEWABLE FUELS AND CHEMICALS FROM BIOMASS.
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
1012125
Grant No.
(N/A)
Cumulative Award Amt.
(N/A)
Proposal No.
(N/A)
Multistate No.
(N/A)
Project Start Date
Jul 1, 2017
Project End Date
Jun 30, 2022
Grant Year
(N/A)
Program Code
[(N/A)]- (N/A)
Recipient Organization
MISSISSIPPI STATE UNIV
(N/A)
MISSISSIPPI STATE,MS 39762
Performing Department
Forest Products
Non Technical Summary
Non-renewable petroleum feedstocks are currently used to provide liquid hydrocarbons that serve as liquid fuels and to supply unsaturated hydrocarbons that serve as feedstocks for the production of chemicals and consumer products. Lignocellulosic biomass, consisting of cellulose, hemicellulose and lignin, is the most promising alternative source for fuels and chemicals. It has been estimated that 20% replacement of transportation fuel demands by 2030 can be obtained from lignocellulosic biomass. Several processes currently exist to convert biomass to liquid fuels, including the hydrocracking of bio-oils, Fischer-Tropsch synthesis of biomass-derived CO/H2 gas mixtures, and fermentation of biomass carbohydrates into ethanol. The high cost of the produced biofuels from biomass compared to the price of fossil fuels is the major challenge limiting wide applications of the above technologies. Therefore, production of fuels and chemicals from biomass in a manner that is cost-competitive with the refining of petroleum is the major goal of this proposal. This goal will be achieved through development of new catalysts for both carbohydrate conversion and bio-oil upgrading to fuels and chemicals.
Animal Health Component
40%
Research Effort Categories
Basic
20%
Applied
40%
Developmental
40%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
51106502000100%
Goals / Objectives
The goal of this project is to reduce the reliance of the United States on non-renewable petroleum feedstock, and to provide forest-rich regions and farmers with an additional source of revenue. This goal will be achieved through the development novel and cost efective magnetic nanocatalysts for dehydration/hydrogenation of biomass carbohydrates to produce high value fuel additives and chemical intermediates such as HMF, furfural, DMF, MTHF and DMTHF. Also, through the development cost efective biochar based catalysts for bio-oil upgrading to biofuels.
Project Methods
Biomass characterizationPine wood and agricultural residues will be used as raw materials in this project. Prior to biomass compositional analysis, all feedstocks will milled to a particle size range of 40-60 mesh according to ASTM standard E1757-01. Samples will be dried in a 105 °C oven for 6 h for moisture content analysis. Ash content will be performed according to the ASTM standard D 1102-84 by heating samples in a muffle furnace at 575 °C for 6 h and weighing the residue after cooling in a desiccator. Carbon, hydrogen, nitrogen content and oxygen (by subtraction) will be determined with a CE-440 Elemental Analyzer (Exeter Analytical, North Chelmsford, MA).Biomass hydrolysis and sugar content determination Biomass will be hydrolyzed by treatment with 72% sulfuric acid for one hour at room temperature by agitating and crushing constantly with glass rod. Then, calculated amount of deionized water (DI) will be added to obtain 4% sulfuric acid solution and the mixture will be autoclaved at 121oC for one hour in a pressure tube to completely hydrolyze all oligomeric sugars into monomers. Then, the sugar solution will be neutralized with calcium carbonate to pH 5.5 and filtered with 0.2µm syringe nylon membrane (Millex-GN) for removal of fine particles. The solution will then be analyzed with high performance liquid chromatography (HPLC) using an Agilent 1200 instrument equipped with a refractive index detector and Biorad column HPX 87P (7.8 mm x 300 mm) at 80oC. Deionized water will be used as an eluent at flow rate of 0.6 mL/min. Quantification of sugars will be done by comparing the peak integration values with those of chromatograms made with known sugar standards and presented in percentages based on dry biomass weight.Bio-oil preparation and characterizationPyrolysis experiments will be conducted at a ~7 kg/h feed rate in a stainless steel auger reactor [15]. This auger reactor will be operated without a carrier gas or an added heat carrier and nitrogen will be utilized to exclude oxygen from the system. The pyrolysis vapors will be condensed to bio-oil and the non-condensable gases and char yields will be calculated. The physical and chemical properties for the produced bio-oils will be analyzed for water content, higher heating value (HHV), viscosity, density, total acid number (TAN) and pH value [16]. Water content will be determined by the Karl Fisher titration method using a Cole-Parmer Model C-25800-10 titration apparatus (Thermo Fisher Scientific Inc., Waltham, MA) according to ASTM D5291. HHV will be determined by a Parr 6200 oxygen bomb calorimeter (Parr Instrument Co., Moline, IL) according to ASTM D240 method. Viscosities and densities will be determined by the Stabinger Viscometer TM SVM 3000 (Anton Paar, Austria) at 40 °C according to ASTM D7042. TAN will be obtained by dissolving 1 g sample in 50 mL of 35:65 volume ratios of isopropanol to distilled water mixture and titrating to a final pH of 8.5 with 0.1M KOH solution according to ASTM D664. The pH values will be determined by addition of 1 g sample to 50 mL of 35:65 volume ratios of isopropanol to distilled water mixture according to the ASTM E70 method. Carbon, hydrogen, nitrogen, and oxygen (by difference) content will be measured with a CE-440 Elemental Analyzer (Exeter Analytical, MA, USA) according to ASTM D3291 method. The volatile and semi-volatile components of each specimen will analyzed by GC/MS spectrometerCatalyst preparation and characterizationThe catalysts used for carbohydrate conversions and bio-oil upgrading will be prepared based on several published methods [17-19]. The prepared catalysts will be characterized by the following techniques:Fourier Transform Infrared (FTIR) spectroscopy will be studied by using a Thermo Scientific Nicolet iS50 FTIR spectrometer.Thermal gravimetric analysis (TGA) will be studied by using a Thermo Scientific SDT Q600 series Thermogravimetric Analyzer.X-ray diffraction (XRD) patterns will be recorded with RINT Ultima III XRD(Rigaku Corp., Japan).Transmission Electron Microscopy (TEM) images will be obtained by usingJEOL 2100TEM with LaB6 emitteroperated at 200kV.Scanning Electron Microscope (SEM) will be examined by using a FE-SEM (JEOL JSM-6500F Field Emission Scanning Electron Microscope).Surface area determination (BET) and pore size distribution for the catalyst will be determined by using Autosorb-ASiQC0500-5.Carbohydrate conversion to furan derivativesDehydration and conversion of sugars to the hydrogenated furan derivatives will be performed through one-pot catalytic transformation process in 100 mL stainless steel Parr reactor connected to a H2 cylinder, temperature controller and heater. The reactor will be charged with biphasic solution consisting of aqueous sugar solution with MIBK as organic solvent and different loadings of magnetic nanoparticle catalyst and Ru/C. The percentage of the catalysts in each run will be calculated based on the concentration of sugars in the biphasic system. Conversion experiments will performed at different temperatures, times, and hydrogen pressures to get the optimum conditions that give the highest yield of the hydrogenated furan derivative (DMTHF and MTHF). Each experiment will repeated at least twice for reproducibility. The magnetic catalyst will also be characterized after being used to evaluate its robustness and effectiveness after multiple reaction cycles. The concentration of DMTHF and MTHF will be analyzed by gas chromatograph (GC, HP 6890) equipped with a flame ionization detector (FID), and methyl ocatanoate will be used as the internal standard. Identification of the products and reactants will be performed by using a GC-MS (HP 5890 gas chromatograph equipped with an HP 5971 mass spectrometer detector (Hewlett-Packard, Palo Alto, CA). The retention time for the products will be compared with the retention times of the standards. The concentrations of unreacted sugars will be analyzed by high performance liquid chromatography (HPLC) using Agilent 1200 instrument equipped with a refractive index detector and Bio-Rad Aminex HPX-87H ion Exclusion Column (7.8 mm × 300 mm) at 60 °C. The sample will be analyzed with 0.005 mol/L sulfuric acid as eluent at flow rate of 0.6 mL/min for 20 min.Bio-oil catalytic upgrading to biofuelsBio-oil upgrading experiments will be carried out in a 100 mL Parr reactor equipped with glass temperature controller, stirrer and heating mantle. In each experiment, approximately 15g of the bio-oil will be loaded in the reactor with catalyst and the process variables for the upgrading process such as time, temperature, and catalyst load will be examined in details. After each experiment, the reactor will be cooled by water to the ambient temperature, and a gas sample will be collected in a 1L Tedlar gas bag. Liquid products will be weighed and then transferred to the centrifuge tube for centrifuging at 4000 rpm for 4 h. The centrifuged products will poured to a separating funnel for 24 h, then, the aqueous phase at the bottom will be collected in one sealed bottle and organic liquid products at the top will be collected in another sealed bottle and the products yield will be calculated. Physical and chemical properties of the upgraded bio-oil such as water content, higher heating value (HHV), viscosity, density, total acid number (TAN), and pH value will be determined according to the same methods used for characterization of raw bio-oil.

Progress 10/01/19 to 09/30/20

Outputs
Target Audience:The target audience(s) during the current reporting period was mainly the biofuel industrial companies and the interested governmental agencies such USDA and DOE through publishing our data international journals. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?The project has provided training and professional development to one graduate student. How have the results been disseminated to communities of interest?Results has been disseminated for publication in the high impact factor journal. What do you plan to do during the next reporting period to accomplish the goals?All final goals will be completed. Final results will be analyzed, and additional manuscripts will be written.

Impacts
What was accomplished under these goals? In this study, 5-hydroxymethylfurfural (HMF) was converted into several biodiesel compounds such as 5-(alkoxymethyl)furans (AMFs) and 2,5-bis(alkoxymethyl)furans (BAMFs) through two-step sequential hydrogenation and etherification reactions. In the first step, zinc-iron magnetic nanocatalyst supported on activated carbon (ZnO-Fe3O4/AC) was prepared for the selective hydrogenation of HMF into furfuryl alcohols via Meerwein-Ponndorf-Verley (MPV) reaction in three different hydrogen donor alcohols (ethanol, 1-propanol, and 1-butanol). The important physical properties of the catalyst such as crystallinity, chemical composition, morphology, reduction behavior, and surface area were studied by using several analytical techniques. The effect of hydrogenation parameters such as catalyst concentration, temperature, and time on the selectivity of furfuryl alcohols and HMF conversion were studied. The best hydrogenation results were obtained with 0.2 mmole HMF and 100 mg of catalyst at 200 °C for 12h. In the second step, three commercial Brønsted acid catalysts including Amberlyst 16, Amberlyte IR120, and Dowex 50WX2 were used to convert the hydrogenated products into 5-(alkoxymethyl)furans (AMFs) and 2,5-bis(alkoxymethyl)furans (BAMFs). At the optimum etherification conditions (65°C and 10h), a spectrum of mono-, di-, and tri- ether compounds were obtained. At the end of the second step, 90% of ethoxymethyl, 86.6% of propoxymethyl, and 84% of butoxymethyl ether compounds were obtained with Amberlyst 16, Amberlyte IR120, and Dowex 50WX2 catalysts, respectively. Kinetic study was performed at three different temperatures (453.15, 463.15, and 473.15 K) to determine rate constants and activation energies of the hydrogenation reactions. The hydrogenation catalyst (ZnO-Fe3O4/AC) was recycled and used for five times without a remarkable reduction in its catalytic activity.

Publications

  • Type: Journal Articles Status: Published Year Published: 2020 Citation: Madduri, S., Elsayed, I., Hassan, E.B., 2020, Novel oxone treated hydrochar for the removal of Pb(II) and methylene blue (MB) dye from aqueous solutions.
  • Type: Theses/Dissertations Status: Published Year Published: 2020 Citation: Sunith Babu Madurri, 2020,Development of low-cost adsorbents from biomass residues for the removal of organic contaminants and heavy metals from aqueous solutions, Dissertation, Mississippi State University.
  • Type: Journal Articles Status: Published Year Published: 2020 Citation: Elsayed, I., Jackson, M.A., Hassan, E.B., Catalytic Hydrogenation and Etherification of 5-Hydroxymethylfufual into 2 (alkoxymathyl) 5 mothyfuran and 2,5 bis(alkoxymethyl)furan as potential biofuel additives, Fuel Processing Technology (in press) 2020 106672, https://doi.org/10.1016/j.fuproc.2020.106672


Progress 10/01/18 to 09/30/19

Outputs
Target Audience:Our target audience(s) during the current reporting period was mainly the biofuel industrial companies and the interested governmental agencies such USDA and DOE through publishing our data international journals. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?One Ph.D. graduate student was trained in this project. How have the results been disseminated to communities of interest?Results has been disseminated for publication in the high impact factor journal, and presented in two international conferences. What do you plan to do during the next reporting period to accomplish the goals?We plan to develop another novel catalyst and to prepare high value oxygenated biodiesel additives of furan ethers (Furanics).

Impacts
What was accomplished under these goals? 2,5-bis(hydroxymethyl)furan (BHMF) is the major diol formed from 5-hydroxymethylfurfural (5-HMF) hydrogenation process. It has a significant importance in many applications including the production of resins, fibers, foams, drugs, polymers, ketones and ethers. Through this period, a magnetically recoverable cost-effective bimetallic nanocatalyst supported on activated carbon (CuO-Fe3O4/CC) was successfully synthesized for the selective transformation of 5-HMF into BHMF via Meerwein-Ponndorf-Verley (MPV) reaction using ethanol as a hydrogen donor with the absence of external molecular hydrogen. The prepared catalyst was characterized by XRD, H2-TPR, XPS, ICP-OES, HRTEM-EDX, and N2 adsorption-desorption isothermal analyses (BET and BJH). The effect of various reaction parameters affecting on the selectivity of BHMF and the conversion of HMF such as catalyst concentration, temperature, and time has been studied. The prepared catalyst exhibited a unique catalytic reactivity for the selective hydrogenation of 5-HMF to BHMF. About 33.3% of the active copper iron metals in the prepared catalysts exhibited high catalytic activity. At the optimum reaction conditions, 92.5% of BHMF selectivity and 97.5% conversion of 5-HMF using ethanol as the hydrogen donor with low percentages of byproduct compounds (DMF, 5-MFA and 5-MF) was achieved in ethanol over 1:1 (5-HMF/Catalyst ratio), at 150°C for 5 h. At the end of the hydrogenation reaction, a strong magnet was used to separate the catalyst from the reaction mixture and the catalyst was recycled and used five times without a remarkable decrease in its catalytic activity.

Publications

  • Type: Conference Papers and Presentations Status: Other Year Published: 2019 Citation: 1- Hassan, E., El Sayed, I., Jackson, M. Hydrogen Free Catalytic Hydrogenation of biomass-derived 5-Hydroxymethylfurfural into 2,5-bis(hydroxymethyl)furan using Copper-iron/CC bimetallic catalyst. 73rd International Convention, Forest Products Society. Atlanta, GO. June 25-28, 2019.
  • Type: Conference Papers and Presentations Status: Other Year Published: 2018 Citation: 2- Hassan, E., El Sayed, I., Jackson, M. Application of Fe3O4@SiO2-SO3H magnetic nanocatalyst for glucose dehydration to 5-Hydroxymethylfurfural. Thermal & Catalytic Sciences Symposium (TCS) Auburn University, AL. Oct. 8-10, 2018.


Progress 10/01/17 to 09/30/18

Outputs
Target Audience:The target audience(s) during the current reporting period was mainly the biofuel industrial companies and the interested governmental agencies such USDA and DOE through publishing our data international journals. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?One Ph.D. graduate student has been trained in this project. How have the results been disseminated to communities of interest?Results has been disseminated through a journal article. Collaborative discussions with academic and government researchers have been ongoing. What do you plan to do during the next reporting period to accomplish the goals?We plan to develop a novel catalyst for the selective transformation of hydroxymethylfurfural 5-hydroxymethylfurfural (HMF) to 2,5-dihydroxymethylfuran (DHMF) and the high value oxygenated biodiesel additives of furan ethers (Furanics).

Impacts
What was accomplished under these goals? A core-shell Fe3O4@SiO2-SO3H nanoparticle acid catalyst was successfully synthesized for dehydration of glucose to form HMF. The magnetically recoverable (Fe3O4@SiO2-SO3H) nanoparticle catalyst was successfully prepared by supporting sulfonic acid groups (SO3H) on the surface of silica-coated Fe3O4 nanoparticles. The prepared catalyst was characterized by FTIR, TGA, XRD, HRTEM-EDX, and N2 adsorption-desorption isothermal analyses. Dehydration of glucose was performed in a biphasic system made up of water and methylisobutylketone (water/MIBK), and the effect of various reaction parameters affecting on the yield of HMF such as biphasic system ratio, catalyst concentration, temperature, time, and dimethylsulfoxide (DMSO) ratio were studied. High HMF yield and glucose conversion were achieved by the application of (water/MIBK) biphasic system with Fe3O4@SiO2-SO3H as a catalyst. In this process, the addition of the catalyst and extracting phase (MIBK) increased the dehydration reaction efficiency of glucose and the HMF yield by limiting the HMF hydration side reaction and removing HMF from the reactive aqueous medium. The process variables, including catalyst concentration, reaction temperature and reaction time, had significant effects on glucose conversion and HMF yield. The optimum reaction conditions were found to be 40% catalyst concentration, 140°C, 24 h, and the use of a biphasic system (water: MIBK) ratio of 1:4. Under such conditions, a glucose conversion of 98% with a HMF yield of 70.5% was achieved. The usage of 40% catalyst is considered to be very low compared with the concentration of catalyst previously used to achieve comparable HMF yield. The effect of DMSO in suppressing hydration reactions and increasing the yield of HMF was not remarkable in this study due to the presence of a very strong Fe3O4@SiO2-SO3H catalyst.

Publications

  • Type: Journal Articles Status: Published Year Published: 2018 Citation: Elsayed, I., Mashaly, M., Eltaweel, F., Jackson, M.A., Hassan, E. Dehydration of glucose to 5-hydroxymethylfurfural by a core-shell Fe3O4@SiO2-SO3H magnetic nanoparticle catalyst. Fuel 221: 407-416: 2018.


Progress 07/01/17 to 09/30/17

Outputs
Target Audience:Our target audience(s) during the current reporting period was mainly the biofuel industrial companies and the interested governmental agencies such USDA and DOE through publishing our data international journals. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?One Ph.D. graduate student has been trained in this project. How have the results been disseminated to communities of interest? Nothing Reported What do you plan to do during the next reporting period to accomplish the goals?We plan to use this catalyst for the conversion of glucose to hydroxymethylfurfural (HMF) and optimize the various reaction conditions affecting on the yield of HMF such as biphasic system ratio, catalyst concentration, temperature and time.

Impacts
What was accomplished under these goals? All the required chemicals were ordered, catalyst has been prepared and characterized by FTIR, TGA, XRD, TEM and SEM analysis.

Publications

  • Type: Other Status: Other Year Published: 2017 Citation: {Nothing to report}