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"Engineering bacteria to turn carbon dioxide into liquid fuel
Monday, December 14, 2009
Global climate change has prompted efforts to drastically reduce emissions of carbon dioxide, a greenhouse gas produced by burning fossil fuels.
In a new approach, researchers from the UCLA Henry Samueli School of Engineering and Applied Science have genetically modified a cyanobacterium to consume carbon dioxide and produce the liquid fuel isobutanol, which holds great potential as a gasoline alternative. The reaction is powered directly by energy from sunlight, through photosynthesis.
The research appears in the Dec. 9 print edition of the journal Nature Biotechnology and is available online.
This new method has two advantages for the long-term, global-scale goal of achieving a cleaner and greener energy economy, the researchers say. First, it recycles carbon dioxide, reducing greenhouse gas emissions resulting from the burning of fossil fuels. Second, it uses solar energy to convert the carbon dioxide into a liquid fuel that can be used in the existing energy infrastructure, including in most automobiles.
While other alternatives to gasoline include deriving biofuels from plants or from algae, both of these processes require several intermediate steps before refinement into usable fuels.
"This new approach avoids the need for biomass deconstruction, either in the case of cellulosic biomass or algal biomass, which is a major economic barrier for biofuel production," said team leader James C. Liao, Chancellor's Professor of Chemical and Biomolecular Engineering at UCLA and associate director of the UCLA–Department of Energy Institute for Genomics and Proteomics. "Therefore, this is potentially much more efficient and less expensive than the current approach."
Using the cyanobacterium Synechoccus elongatus, researchers first genetically increased the quantity of the carbon dioxide–fixing enzyme RuBisCO. Then they spliced genes from other microorganisms to engineer a strain that intakes carbon dioxide and sunlight and produces isobutyraldehyde gas. The low boiling point and high vapor pressure of the gas allows it to easily be stripped from the system.
The engineered bacteria can produce isobutanol directly, but researchers say it is currently easier to use an existing and relatively inexpensive chemical catalysis process to convert isobutyraldehyde gas to isobutanol, as well as other useful petroleum-based products.
In addition to Liao, the research team included lead author Shota Atsumi, a former UCLA postdoctoral scholar now on the UC Davis faculty, and UCLA postdoctoral scholar Wendy Higashide.
An ideal place for this system would be next to existing power plants that emit carbon dioxide, the researchers say, potentially allowing the greenhouse gas to be captured and directly recycled into liquid fuel.
"We are continuing to improve the rate and yield of the production," Liao said. "Other obstacles include the efficiency of light distribution and reduction of bioreactor cost. We are working on solutions to these problems."
The research was supported in part by a grant from the U.S. Department of Energy."
To repeat: "An ideal place for this system would be next to existing power plants that emit carbon dioxide, the researchers say, potentially allowing the greenhouse gas to be captured and directly recycled into liquid fuel."
As with the Department of Energy's extensive development of coal-to-liquid conversion technologies we have documented for you in earlier dispatches, they are also demonstrating that Carbon Dioxide can, through a multiplicity of promising approaches, be recycled, on a practical basis, into even more liquid fuels. Yet, none of us, none of us whose tax dollars paid for the research, none of us in US Coal Country, especially, has been afforded the privilege of being told about these coal-critical developments and innovations.
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M. Mahmoudkhan, K.R. Heide, J.C. Ferreira, D.W. Keith and R.S. Cherry
Energy and Environment System Group, Institute for Sustainable Energy Environment and Economy University of Calgary, Alberta, Canada
Idaho National Laboratory, Idaho Falls, ID, USA
We used a 6.5 m tall packed tower prototype to study the capturing rate of CO2 from air. The tower was operated at a pressure drop of less than 27 pa in the packing at 0.7 m/sec air speed with a counter current flow mode and with NaOH or KOH solution as the absorbent. The tower consumed an average of 30 kJe per mole CO2. We found that via an intermittent operation with a 5% duty cycle, the fluid pumping work reduced by 90%. A novel process for removing carbonates ions from alkaline solutions based on titanate compounds is compared to the traditional lime cycle for the caustic recovery. The titanate process reduces the high-grade heat requirement by
50%. The results from experimental data of leaching and precipitation test support process design of the titanate cycle. In this paper, we also present the chemical process design.
References
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(Letter reproduced with permission.)December 14, 2009WV Department of Environmental Protection
ATT: Secretary Randy Huffman
601-57th Street
Charleston, WV 25304Dear Secretary Huffman,This Thursday, your department will hold a public hearing in Mingo County to review a permit for the Coal-to-Liquid facility proposed by TransGas. In my mind, this is the most important decision facing your government agency, as the result will determine the success of this facility—I strongly urge you to grant this permit in a speedy manner.Coal-to-Liquid technology represents the future of industry in our state and I have dedicated the past year of my life to bring a facility like the TransGas project to my own district in Weirton, WV. I have flown to multiple destinations around this country in order to recruit investors and entrepreneurs in this field, and I have also spoken with TransGas officials. I am confident their investment will perform well in our state.Furthermore, the construction of such a plant truly brings a new era to the Mountain State and will help West Virginia turn the corner on the global recession we all face. With the implementation of this technology, we bring innovation to West Virginia—innovation which will produce thousands of jobs for our residents and open the road to economic prosperity.For decades, the American steel industry has been in decline and the city of Weirton has suffered the consequences—ranging from mass unemployment to increased poverty. With little employment opportunity, our children have been forced to leave behind their families and the Mountain State altogether. As our economic conditions worsen, our population continues to dwindle and side-effects are increasingly seen, such as poorer education and increased crime rates. Naturally, the generation of investment is one crucial way we can indirectly combat these negative results.Finally, not only will Coal-to-Liquid technology usher in economic prosperity for the foreseeable future, but it will also place West Virginia cities on the “national map”. We have a comparative advantage in coal energy and these new methods of utilizing this advantage will help decrease the value our nation places on foreign oil—one of the prime threats to our national security and sovereignty.The implementation of this investment in Mingo County will not only help this region of West Virginia, but the success of this project would most certainly pave the way for others, including my own project for Weirton. I urge you to pass this permit with due haste, as the future of our state’s economy may rest with your decision.Sincerely,
Delegate Pat McGeehan
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918 S. W. Mudd, 500 West 120th Street, New York, NY 10027, USA
Economics, University of Calgary, 2500 University Drive NW, Calgary, Alberta,
Canada T2N 1N4
Reducing greenhouse gas emissions from the transportation sector may be the most difficult aspect of climate change mitigation. We suggest that carbon neutral hydrocarbons (CNHCs) offer an alternative pathway for deep emission cuts that complement the use of decarbonized energy carriers. Such fuels are synthesized from atmospheric carbon dioxide (CO2) and carbon neutral hydrogen. The result is a liquid fuel compatible with the existing transportation infrastructure and therefore capable of a gradual deployment with minimum supply disruption. Capturing the atmospheric CO2 can be accomplished using biomass or industrial methods referred to as air capture. The viability of biomass fuels is strongly dependent on the environmental impacts of biomass production. Strong constraints on land use may favour the use of air capture. We conclude that CNHCs may be a viable alternative to hydrogen or conventional biofuels and warrant a comparable level of research effort and support."
Hydrocarbons can be carbon neutral if they are made from carbon recovered from biomass or captured from ambient air using industrial processes. The individual capture technologies required to achieve CNHCs have been considered elsewhere; our goal is to systematically consider CNHCs as an alternative and independent route to achieving carbon neutral transportation fuels.
"We define CNHCs as those whose oxidation does not result in a net increase in atmospheric CO2 concentrations. Hydrocarbon fuels can be made carbon neutral either directly by manufacturing them using carbon captured from the atmosphere, or indirectly by tying the production of fossil fuels to a physical transfer of atmospheric carbon to permanent storage. The indirect route allows for a gradual transition from the current infrastructure, based on petroleum, to a sustainable system based on atmospheric sources of carbon.
Report no. EPA420-F-05-001, Environmental Protection Agency, Washington, DC.
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Ethanol can contribute to energy and environmental goals. Science 311, 506–508.
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United States Department of Energy | |
Office of Fossil Energy | |
Project Fact Sheet | |
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Project Information | |
Project ID: | DE-FC26-00NT40933 |
Project Title: | Chemical Fixation of CO2 in Coal Combustion Products and Recycling Through Algal Biosystems |
FE Program: | Adv. Power - Supporting Research and Environmental Technology |
Research Type: | Basic Research |
Funding Memorandum: | Cooperative Agree't (nonCCT) - Tech R&D |
Project Performer | |
Performer Type: | U.S. Government Agency |
Performer: | Tennessee Valley Authority 3J Lookout Place 1101 Market Street |
Project Team Members: | |
Project Location | |
City: | Chattanooga |
State: | Tennessee |
Zip Code: | 37402-2801 |
Congressional District: | 03 |
Responsible FE Site: | NETL |
Project Point of Contact | |
Name: | Copeland, Robert |
Telephone: | (303) 940-2323 |
Fax Number: | |
Email Address: | |
Fossil Energy Point of Contact | |
Name: | Figueroa, Jose D. |
Telephone: | (412) 386-4966 ext. 4966 |
Location: | NETL |
Email Address: | |
Project Dates | |
Start Date: | 10/01/2000 |
End Date: | 09/30/2003 |
Contract Specialist | |
Name: | Pearse, Mary Beth J. |
Telephone: | (412) 386-4949 |
Cost & Funding Information | |
Total Est. Cost: | $755,291 |
DOE Share: | $604,233 |
Non DOE Share: | $151,058 |
Project Description | |
The overall objective is to develop basic methods for use of coal combustion products (CCP) produced at fossil fuel power plants as a sequestering medium for CO2 in stack gas from gas turbine plants, with subsequent production of methane and other recyclable carbon-containing products from the system. | |
Project Background | |
A research area under consideration by DOE to address carbon sequestration is pumping of CO2 to underground geologic formations, such as coal beds, to displace and recover methane. A more effective and economical alternative may be the use of coal combustion products (CCP) produced at fossil fuel power plants as a sequestering medium for CO2, with subsequent production of methane and other recyclable carbon-containing products from this system. Each year in the U.S., about 22 million metric tons of fly ash and flue gas desulfurization products (FGD) are stored on power plant sites in vast ponds or other disposal areas. Such CCP may serve as a sink for CO2 and eliminate the expense of locating suitable underground storage areas and costs of pumping stack gas over long distances. Conceptually, these impoundments may function as large reaction vessels wherein the fly ash and FGD, due to their large surface area and the presence of a surface electrical charge, might serve as highly reactive media for sequestration of the CO2 produced by gas turbine generators. After suitable adjustments to system pH, adsorption and exchange reactions of CO2 in the sterile CCP medium, followed by precipitation as carbonates, would maintain carbon in an inorganic, stable form and prevent reintroduction into the carbon cycle for an indefinite period. When economically feasible, the CCP might be used as flowable fill material for construction or could be back-hauled and used to fill underground mine voids. The carbon-enriched CCP media may also be used to create an algae biosystem, which is expected to extract and utilize carbon compounds sequestered in the CCP. Stack gas diverted into the biosystem will expose the algae to additional CO2. The CCP will provide a nutrient growth matrix for the algae, and more importantly, should provide the critical mechanism needed to increase the available CO2 in solution above the limits that are achievable with the dissolved gas alone. This would most likely increase algal growth beyond what is normally attainable. Carbon in the algal biomass can then be extracted and converted to hydrogen gas with a gasifier or converted to liquid CO2. An anaerobic digestor in the system may be used to convert the biomass into methane for on-site use in a gas turbine generator. The solid biomass residue from the digestor may be re-cycled as additional fuel stock for the gasifier. The liquid residue from the digestor may be re-cycled to provide nutrients to perpetuate the algal biosystem. The system provides for continued cycling of sequestered carbon within the system. Being solar driven, the CCP biosystem requires minimal inputs of energy and materials, and solves the energy storage problems associated with the photovoltaic cells of a solar collection system. The turnaround time for biomass production in the system is short, since it is not limited by transpiration or sunlight exposure, as would be terrestrial plants. A reasonable estimate for the area of algal biomass required to generate methane to support a 1000 MW gas turbine plant would be in the range of 2.5 - 25km2. The primary limiting factor for biosystem output would be the time required for the system to reach steady-state production of algae, methane, hydrogen, and liquid CO2. | |
Project Milestones | |
This information is currently unavailable. | |
Project Accomplishments | |
Title: | Technical Assessment |
Date: | 10/17/2002 |
Description | Conversion of CO2 to bicarbonate using fly ash as a catalyst. The rate of uptake of CO2 in a fly ash column id 5 to 9 times the rate of uptake in the control column containing glass beads. At 1.5 hours the fly ash column ph was 6.5 while the glass bead column was 5.6. This indicates the fly ash has a capacity to buffer the solution. At a ph of 6.5 the bicarbonate using the fly ash column was double that of the glass beads. The ph and higher bicarbonate level from the fly ash column are more suitable for biological systems than the glass bead column. Signifcantly increases in biomass production can be obtained by supplementing the algae growth medium with additional bicarbonate. The annual production of biomass from an algae facility could be in excess of 150 metric tons per hectare (74 metric tons per year)" |
