Source: MICHIGAN STATE UNIV submitted to NRP
THERMOCHEMICAL CONVERSION OF WOODY BIOMASS TO FUELS AND CHEMICALS
Sponsoring Institution
State Agricultural Experiment Station
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
0212350
Grant No.
(N/A)
Cumulative Award Amt.
(N/A)
Proposal No.
(N/A)
Multistate No.
(N/A)
Project Start Date
Sep 1, 2007
Project End Date
Aug 31, 2012
Grant Year
(N/A)
Program Code
[(N/A)]- (N/A)
Recipient Organization
MICHIGAN STATE UNIV
(N/A)
EAST LANSING,MI 48824
Performing Department
BIOSYSTEMS & AGRIC ENGINEERING
Non Technical Summary
The value-addition contributed by thermochemical conversion is at least partially dependent upon the rates and extents of product formation, the energy quality of the fuel, and the composition of the product stream. This project aims to elucidate and alleviate the limiting mechanisms inherent in thermochemical conversion of woody biomass.
Animal Health Component
40%
Research Effort Categories
Basic
40%
Applied
40%
Developmental
20%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
4020650202080%
4020680202020%
Goals / Objectives
The project scope is to investigate the thermochemical conversion of woody biomass to fuels and chemicals. Economic models, for both a stand-alone thermochemical conversion facility and an integrated cellulosic ethanol biorefinery with thermochemical conversion, are to be formulated. The results of the economic model will be used to identify the processes or process steps that are sensitive to alterations. Beneficial alterations will be investigated to discern the nature of limiting mechanisms. A physicochemical model will be derived to describe the resultant data and assist in interpreting experimental results. A revised economic model, including information from the experimental results, will provide decision-making capability to industry regarding the deployment of thermochemical conversion.
Project Methods
The use of thermochemical conversion of woody biomass will be explored in a stand-alone and an integrated biorefinery format. Economic models will be formulated to provide insight into process limitations and to focus research effort. Process alterations that result in beneficial observations deviating from established theory will be investigated. Hypothesis formulation and experimental design will be tailored to elucidate the nature of limiting mechanisms. Physicochemical models will be formulated to describe the data and assist in interpreting experimental results. Both the stand-alone and integrated biorefinery models will be updated to reflect the scientific findings. A series of economic models will be constructed to identify the processing steps in the thermochemical conversion of woody biomass that are most sensitive to process improvements. Profitability metrics will be used to rank different processes (e.g. gasification followed by Fischer-Tropsch synthesis, gasification followed by synthesis gas fermentation to ethanol, pyrolysis oil formation, etc.) and process configurations (i.e. different methods of fractionating thermochemical products). Model results will guide experimentation in the laboratory by focusing resources on processes and process steps that are most economically sensitive to improvement. Hypothesis formulation will follow observation of limiting phenomena in the laboratory. The nature of the limiting mechanisms will be elucidated by bench-scale exploratory research--i.e. whether mass transfer rates, heat transfer rates, reaction rates, etc., are responsible for limiting the efficacy of the thermochemical routes under consideration. Spectroscopic methods, such as GC/MS, will measure the composition and quantity of the pyrolysis products. Physicochemical models will be formulated to describe the data and assist in interpreting the results. This detailed investigation is expected to result in an improved scientific understanding of the thermochemical conversion of woody biomass and of the fractionation of pyrolysis products. Further process and equipment design will be investigated in an attempt to alleviate the aforementioned limitations. In addition to the energy value of the upgraded fuel, the fractionation of value-added co-products will be considered. Revision of the economic model will commence upon interpretation of the experimental results. Integration of thermochemical conversion into cellulosic ethanol facilities (woody biomass or otherwise) will be explored to increase the product suite and energy quality of the biorefinery. Areas of focus include, but are not limited to: 1) thermochemical conversion of a fraction of the cellulosic feedstock, 2) the use of thermochemical methods as pretreatments, and 3) the thermochemical conversion of fermentation residue solids (i.e. cake solids). Profitability of the biorefinery will be estimated upon economic model formulation and is dependent upon the process material and energy balances. This biorefinery model is expected to be used as a decision-making tool for subsequent design and experimentation at the bench scale.

Progress 09/01/07 to 08/31/12

Outputs
OUTPUTS: The 2008 reporting period is the first full year of this project titled, "Thermochemical Conversion of Woody Biomass to Fuels and Chemicals." Outputs generated from January 1st, 2008 to December 31st, 2008 include graduate student recruitment, the design and setup of experiments, and the presentation of thermochemical technologies to public audiences. Two doctoral students were recruited to investigate the production of liquid fuels from biomass using thermochemical conversion technologies. A Thermochemical Conversion Laboratory is being equipped to accommodate experiments in this area. A pyroprobe was recently purchased to provide the analytical capability needed to efficiently assess the products produced upon biomass pyrolysis at a small scale. This device was linked to a gas chromatograph using a mass spectrometer for detection. The laboratory now has the capability to generate chromatograms by pyrolyzing milligram quantities of sample. Mass spectrometry is used to identify the components that are separated upon chromatography. A 60 meter Restek 1701 capillary column was installed to analyze oxygenates such as anhydrosugars and organic acids, as the previous DB-5 column resulted in misshapen peaks. A screening study is now being performed to analyze for organic acids upon fast pyrolysis in the pyroprobe. In addition to the pyroprobe, a bench-scale screw-conveyor reactor is being constructed to study the mass and heat transfer characteristics related to the pyrolysis reaction. A reactor housing has been acquired and a feed hopper, an extruder screw, and a drive motor have been ordered. It is anticipated that the reactor and recovery units will be assembled to make an operational process by the end of the first quarter of 2009. Information about pyrolysis was disseminated to the general public during two occasions in the past year. The first was a guest lecture at Andrew's University in the spring, titled: "Thermochemical conversion of woody biomass to bio-oil and value-added co-products." The second was a presentation to the Benzie County Planning Commission, titled: "Bioenergy: Challenges, technology and the path forward." PARTICIPANTS: Christopher M. Saffron, PI Shantanu Kelkar, Doctoral Student Zhenglong Li, Doctoral Student TARGET AUDIENCES: Nothing significant to report during this reporting period. PROJECT MODIFICATIONS: Nothing significant to report during this reporting period.

Impacts
Data collected from a pyroprobe connected to a gas chromatograph-mass spectrometer suggest that the concentrations of selected organic acids that are produced upon pyrolysis can be quantified. Quantification of organic acids using this technique provides ability for screening biomass varieties that result in bio-oil with a reduced total acid number. Decreased acidity is a desirable as the liquid product, i.e. bio-oil, is to be stored and transported in steel tanks and pipes. Also, reduced acidity requires reduced hydrogen during bio-oil upgrading, resulting in lower upgrading costs. In addition to organic acids, selected anhydrosugars, furans, and phenolics can also be identified and quantified. Anhydrosugars have interesting chiral characteristics; furans can be used as solvents, while phenolics can be used as food flavorings, dyes, nutraceuticals, and pharmaceuticals. Samples of forest biomass, agricultural residues, and energy crops will be analytically pyrolyzed during the first quarter of 2009. Those plant varieties that exhibit favorable acidities are candidates for bench-scale pyrolysis in the screw-conveyor reactor currently being constructed.

Publications

  • No publications reported this period


Progress 01/01/07 to 12/31/07

Outputs
This project, involving the thermochemical conversion of woody biomass to fuels and chemicals, is in the early stages of achieving objectives. Quantifiable outputs, e.g. journal articles and conference presentations, have yet to manifest. From the start date of August 16th to the present, tasks have included: graduate student recruitment, the statement of testable hypotheses, pyrolysis reactor design, analytical method development, and the development of a techno-economic model. Bio-oil fractionation is being considered as a focus area, though bio-oil upgrading to stationary and transportation fuel remains an objective. One graduate student has been recruited and will begin in February of 2008. This student will focus on wood conversion to fuels and chemicals using fast pyrolysis of biomass. A list of candidate wood species has been assembled, and the graduate student will convert selected wood species to fuels and chemicals during graduate study. In addition to Michigan native tree species, genetically modified trees are being considered for conversion. The academic and professional literatures are being reviewed, resulting in several hypothesis statements. Limitations inherent in pyrolysis are being considered as topics for further investigation. These limitations include heat transfer, mass transfer, multiphase fluid flow, and reaction kinetics. Identifying fundamental limitations for bio-oil production is a matter of continued investigation. In addition to bio-oil production, bio-oil fractionation is being considered as a means of generating value-added molecules. Means of separating bio-oil components, such as distillation and solvent extraction, are being reviewed for further investigation. These value-added chemicals can serve as products or intermediates that will enhance the profitability of bio-oil production. Several reactor configurations have been examined, though pyrolysis reactor design is ongoing. The goal reactor design is the construction of a sufficiently flexible research tool that has qualities amenable for scale-up. Ablative, fixed bed, fluidized bed, rotating cone and cyclonic reactor configurations are being considered. Both pyroprobes and inductive heaters are being considered as possible heat sources. Analytical method development is underway, esp. regarding the use of HPLC/MS and GC/MS. Mass spectrometry will be used to identify and quantify the products of the pyrolysis reaction. Graduate student assistance will be used for method development and spectra interpretation. The heating value of the bio-oil and upgraded bio-oil-derived fuels will be measured in a bomb calorimeter using ASTM method D4809. The Parr Instrument Company is being contacted to obtain quotes for an appropriate bomb calorimeter. A techno-economic model is being developed to better understand the costs and benefits associated with bio-oil production. Model development is important for guiding the fundamental research conducted at the bench scale. An interpretation of experiment results is expected to refine the model structure and alter the model predictions.

Impacts
The processes considered in this project are in the early stages of investigation. A quantifiable outcome has yet to be manifested. Expected outcomes include: 1) a better understanding of the mechanisms that limit the pyrolysis of woody biomass, 2) the identification and quantification of molecules that would add value to the bio-oil production process, 3) the economic viability of stand-alone bio-oil production, integrated thermochemical-biochemical conversion to fuels and chemicals, integrated biochemical-thermochemical conversion to fuels and chemicals, and 4) the potential environmental impact of integrated thermochemical and biochemical refineries.

Publications

  • No publications reported this period