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At least 631 records · Page 35

Perspective on the U.S. Coal Industry 2013

This presentation provides an overview of the coal industry, focusing on the United States, but within a global context. Areas covered include coal prices, consumption, production, imports, exports, reserves, productivity measures, and more. Juxtapositions between the U.S. and other countries' coal industries are provided. In addition to providing a current snapshot of the U.S. coal industry, this work portrays both historical and projected aspects of the coal industry.

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Perspective on the U.S. Coal Industry 2014

This presentation provides an overview of the coal industry, focusing on the United States, but within a global context. Areas covered include coal prices, consumption, production, imports, exports, reserves, productivity measures, and more.

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Improving Energy Efficiency of Air Separation via Hollow Fiber Sorbents

This report summarizes the work performed under the Department of Energy’s National Energy Technology Laboratory (DOE-NETL) Advanced Energy Systems Program award number DE-FE0026163 Improving Energy Efficiency of Air Separation via Hollow Fiber Sorbents. The overall objective of the project was to develop technology to produce oxygen for use in coal gasification processes at a significantly lower cost than that of the commercial state-of-the-art technology. The focus of the project was development and optimization of hollow fiber sorbents for use in a pressure swing adsorption (PSA) process for producing oxygen from air. The key technical advancement under this program was the development of a hollow fiber sorbent capable of producing oxygen in a PSA process. PSAs produce oxygen by using a beaded zeolite material (typically lithium exchanged zeolites or LiX) that selectively adsorb nitrogen over oxygen. For a fiber to adsorb nitrogen, LiX needed to be integrated into a polymer fiber and then activated at over 350C to remove residual moisture. After screening multiple materials and process techniques, Matrimid/LiX hollow fibers were produced that were able to withstand the activation and had crystalline nitrogen capacity close to pure LiX crystals. The fibers were dual layer fibers with a barrier layer isolating the hollow bore from the LiX embedded layer. The barrier layer was formed from an Ultem® based solution. The hollow bore was intended for encapsulating phase change materials to ensure isothermal PSA operation. Modeling work from the project suggested that the benefits of this additional complexity were marginal, thus the team fabricated non-hollow fibers comprised of Matrimid and LiX. The Matrimid/LiX fibers were loaded into a module and tested on a bench scale PSA unit. The fibers were able to separate oxygen from air, but the purity and recovery were lower than expected and lower than traditional beaded LiX zeolites, although modeling results suggested that the bed sizes for fiber sorbents could be half the size of a beaded LiX bed. Additional work will be needed to understand the shortfall and to produce fiber sorbent modules with performance equal to the targets set for this program. In addition to producing fibers, modeling work was carried out at both the fiber level and process level to guide both fiber sorbent development and to determine the optimal process conditions for a PSA using fiber sorbents. A 2D hollow fiber model was developed in gPROMS Model Builder. This model was based on literature data for mass transfer and other parameters. This model used a basic single bed PSA process to determine important fiber properties and process conditions for achieving high oxygen recovery. The preliminary 2D fiber model was a valuable tool, however, for step-out technologies, such as a PSA process with fiber sorbents, intelligent optimization and plant control was needed to effectively determine minimum power designs. Therefore, a gPROMS Process Builder-based optimization tool was developed with an “Automated Cycle Optimizer” model that was able to determine optimal cycle conditions for a fiber sorbent PSA. The results from the optimizer were used in the final power analysis. Flow sheet analysis and techno-economic analysis (TEA) was carried out to determine a lower power solution versus the baseline case. The original project scope suggested that the fiber sorbent PSA could be used to debottleneck a cryogenic air separation plant (cryo-ASU) with the combined plant having lower power than a standalone cryo-ASU. However, early flowsheet analysis showed that the PSA/cryo-ASU concept would not lead to a lower power solution. However, further flowsheet analysis suggested that an oxygen PSA combined with a nitrogen PSA could have lower power versus state-of-the-art air separation technology. Work concluded with the TEA showing a fiber sorbent oxygen PSA combined with an advanced nitrogen PSA could be up to 8% lower power versus the base case cryo-ASU. Overall, there is significant potential remaining for the zeolite hollow fiber sorbent concept, and this project successfully identified -- and ultimately remedied -- many technical challenges associated with scale-up.

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Reduced Mode Sapphire Optical Fiber and Sensing System

This is the final technical report for the Virginia Tech Center for Photonics Technology (VT-CPT) research project entitled “Reduced Mode Sapphire Optical Fiber and Sensing System”. The objective of the five-year effort was to develop a low modal volume (LMV) single crystal sapphire fiber and demonstrate its advantages in current state-of-the-art sapphire-based temperature sensors and in novel distributed ultra-high temperature sensing systems. The project, sponsored by the Crosscutting Research Program, began in 2014 and had the original goal of developing the next generation of harsh environment sensing systems. After successfully completing the original scope of the award, the project was expanded and extended to allow for the development of harsh environment packaging and testing of a prototype sensor system. These novel fiber optic sensing technologies provide real-time, accurate, and reliable temperature measurements at distributed locations in existing coal-fueled electricity generating units to improve the overall performance, reliability, and flexibility of the nation’s coal-fired power plant fleet. In the final year (2018) of the project, prototype sensing systems were successfully deployed and operated in small commercial coal and natural gas fired boilers at the Virginia Tech Power Plant. The harsh environment quasi-distributed temperature sensing technology was advanced from a (Technology Readiness Level) TRL=1 to a TRL=7 by demonstrating the full validation of the sensing system prototype in a relevant industrial environment. The real-time, accurate and reliable monitoring of temperatures at distributed locations is expected to lower operating costs by allowing more accurate measurement of the harsh conditions inside a boiler system to better control its operation. The technologies developed by Virginia Tech’s Center for Photonics Technology will support the mission of the National Energy Technology Laboratory (NETL) to advance energy options to fuel our economy, strengthen our security, and improve the environment.

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Greenhouse Gas Reductions in the Power Industry Using Domestic Coal and Biomass - Volume 1: IGCC

The objective of this study was to simulate biomass co-firing in a dry-fed, entrained-flow gasifier in an integrated gasification combined cycle (IGCC) power plant and examine the resulting performance, environmental response, and economic response. To develop a more complete understanding of the impact of co-feeding biomass, each case was examined using a limited life cycle greenhouse gas (GHG) analysis, which examines GHG emissions beyond the plant stack. Included in the limited life cycle GHG analysis were anthropogenic greenhouse gas emissions from the production, processing, transportation, and fertilization of biomass and from mining, transporting and handling coal.

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CO 2 Capture with Ionic Liquids Involving Phase Change (Final Report)

Coal-fired power plants provide nearly 50% of all electricity in the U.S. While coal is a cheap and abundant natural resource, its continued use contributes to rising carbon dioxide (CO 2 ) levels in the atmosphere. Capturing and storing this CO 2 would reduce atmospheric greenhouse gas levels while allowing power plants to continue using inexpensive coal. Carbon capture and storage represents a significant cost to power plants that must retrofit their existing facilities to accommodate new technologies. Reducing these costs is the primary objective of ARPA-E's carbon capture program. Researchers at the University of Notre Dame and their partners at Matric developed a new CO 2 capture process that uses materials that we call Phase Change Ionic Liquids (PCILs). PCILs are solid at the temperature of the CO 2 absorption but change to liquid when they bind with CO 2 . The PCILs have a high capacity for CO 2 at post-combustion flue gas pressures and temperatures because of a chemical reaction between the CO 2 and the PCIL. Upon heating, the CO 2 is released, and the PCILs re-solidify. The heat released in the solidification process reduces the amount of external heat that must be added. As with conventional CO 2 capture processes, the PCIL process has an absorber and a regenerator. Computer simulation of the process enabled calculation of viable process conditions and power needs. The main concepts of the process were demonstrated using lab-scale apparatus. Capture of CO 2 was carried out using a sieve tray column in continuous mode. Desorption of the CO 2 in the regenerator occurred while the liquid droplets solidified. The key to making this process viable was the use of a mixture of the complexed liquid with the unreacted solid particles in the absorber. This mixture formed a well-behaved slurry that flowed readily. Therefore, handling of solid particles is avoided in the process. Parasitic power was decreased by 55% from the amount required by the monoethanolamine (MEA) process. For the PCIL process, parasitic power is only 23% of the net power generated by the plant, which is remarkably close to the 19% DOE target. The capital cost for the CO 2 capture unit is higher for the PCIL process than the MEA process. Nonetheless, the overall increase in the cost of electricity (COE) is dramatically lower - only 4.1¢/kWh for the PCIL process compared with 5.7¢/kWh for the MEA process. The cost of CO 2 avoided is $48/ton of CO 2 . As a result, we conclude that CO 2 capture with phase change ionic liquids is an exceedingly promising technology.

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Coal Fly Ash Disposal

Coal fly ash disposed of in a landfill. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=51451F09-EB9B-48E9-A600-0663B7967050

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Coal Handling Energy, Underground

The amount of electricity and diesel required to power a coal conveyor, service truck, and load haul dumper for an underground mine. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=C5786A5F-9828-41A1-BDE9-EDCCA3001BBE

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Coal Mine Methane Emissions

Coal mine methane emissions associated with coal mine operations. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=51F0506D-EB4D-477C-B53A-E671A2633C4A

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Illinois No. 6 Underground Coal Mine Assembly, Construction

Calculates the number of each piece of equipment included in an underground, Illinois No. 6 bituminous coal mine. Includes life expectancy and replacement rates for the longwall mining system, continuous miner, conveyor system, and shuttle car. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=E1F4C19D-E7C9-4385-914A-7432869882D5

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Powder River Basin Surface Subbituminous Coal Mine, Operations

Based on a compilation of mines, a surface mine for Powder River Basin subbituminous coal in Wyoming, producing ~6 billion kg of coal per year. Assumes 32,000 scf/kg coalbed methane (CBM) emissions, adjustable CBM capture rates. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=3B16F21E-6501-4B3B-BA28-0733F3513B3A

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Rosebud Surface Subbituminous Coal Mine, Operations

Based on a compilation of mines, a surface mine for Rosebud subbituminous coal in Montana, producing ~11 billion kg of coal per year. Assumes ~40 scf/kg coalbed methane (CBM) emissions, adjustable CBM capture rates. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=D6F57D21-6996-4FD3-9692-083AB93DE24B

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Storage/Disposal Coal Mine Tailings

Storage/Disposal Coal Mine Tailings in Pond, Piles, or Backfill. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=84A03556-8A92-4B6C-BB6F-CC789B1F2260

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Underground Mine, Illinois No. 6 Bituminous Coal, Operation

Based on Galatia Mine, an Illinois No. 6 underground, bituminous coal mine in Saline County, IL; producing ~6.6 million short tons of coal per year. Assumes 360 cubic feet/short ton coalbed methane (CBM) emissions, adjustable CBM capture rates. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=6AC5D31E-8F2D-4BE6-B01E-18ECF8A2C558

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Water use and quality from surface mining of coal

Water use and quality from surface mining of coal, based on data for PRB mines. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=DE21EDA6-C0F4-445F-BE06-1F7E899776B6

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Water use and quality from underground mining of coal

Water use and quality from surface mining of coal, based on data for Illinois No. 6 mines. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=6BDEB1C4-A6D3-4CD9-AFF2-3D15AFBD065C

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CBTL Zero Sulfur Diesel

Coal-and-Biomass-to-liquids (CBTL) via Fischer-Tropsch synthesis using Illinois No. 6 or PRB as the coal and switchgrass as the biomass feedstock where applicable. To access the model referenced in the report, please visit https://www.netl.doe.gov/energy-analysis/details?id=E61F2670-356F-4EA2-9146-81BF32D8353D

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