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Search indexed NASA NTRS and DOE OSTI research on propulsion, heat transfer, battery materials and energy systems. Follow report and document links to the original sources.

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At least 613 records · Page 34
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DOE OSTI2018

Coal Upgrading Technologies and the Extraction of Useful Materials from Coal Mine Products: History and Opportunities

This report will develop topics that may, resultant from successful research and development (R&D), improve the competitive position of United States coal in domestic and international markets. These topics will be exclusively focused on improvements in coal properties that can be achieved through processing of the material. As such, the discussion here will be primarily concerned with upgrading coal quality and optimizing coal properties for end use applications, as opposed to the end use technologies themselves. The objective of this report is the highlighting of the potential for R&D to produce more competitive coal products for existing markets, as well as opportunities for the production of feedstocks for other markets, including those that are emergent.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Small-scale pilot plant for gasification of coal and coal/biomass blends and conversion of derived syngas to liquid fuels via Fischer-Tropsch synthesis

This report describes the second phase of a project to design, construct and commission an integrated coal/biomass-to-liquids facility at a capacity of 1 bbl. /day at the University of Kentucky Center for Applied Energy Research (UK-CAER) – specifically for construction, commissioning and operating of the downstream process units for water-gas-shift, Fischer-Tropsch synthesis and balance of plant [BOP]. The deliverables from the operation of this pilot plant is firstly the liquid F-T products and finished fuels which are of interest to UK-CAER’s academic, government and industrial research partners. Going forward the facility will produce research quantities of F-T liquids and finished fuels for subsequent Fuel Quality Testing, Performance and Acceptability. Moreover, the facility is expected to be employed for a range of research and investigations related to: Feed Preparation, Characteristics and Quality; Coal and Biomass Gasification; Gas Clean-up/ Conditioning; Gas Conversion by -F-T Synthesis; Product Work-up and Refining; Systems Analysis and Integration; and Scale-up and Demonstration. Environmental Considerations - particularly how to manage and reduce carbon dioxide emissions from CBTL facilities and from use of the fuels will be a primary research objective. The results of this second phase study include the FEED study and detailed engineering design of the downstream processing units and BOP, the selection of a range of technologies and technology vendors, the as-built plant - its equipment and capabilities, and the results of two trial production runs, one with coal only and one with a coal/biomass blend. These are described in detail in this report.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

A Scaling Study of Microbially-Enhanced Methane Production From Coal (Mecbm): Optimizing Nutrient Delivery For Maximized Methane Production

Microbially-enhanced coalbed methane (MECBM) recovery is a novel method to stimulate gas production in CBM reservoirs. We first develop suitable nutrient recipes for native coals from sites each in the Illinois Basin and in the San Juan Basin. The optimal concentrations for statistically significant parameters are identified and the methane yields at laboratory scale are obtained (Part I & II). We then demonstrate the importance of replicating truly in-situ conditions for bio- gasification studies by investigating methane productivity in a core holder simulating in-situ conditions. Based on the experimental results, the resulting gas production correlates positively with the permeability of the samples. We examine the deliverability of engineered microbial solutions to promote coal bioconversion in coals and demonstrate that greater than milli-darcy permeability is required under in-situ stress conditions (Part III). This constraint is supplemented by imaging and a fractal-based characterization approach to evaluate changes in the physical properties of coal due to bio-gasification. High resolution SEM imaging is used to observe swelling of the coal matrix with sub-micron wide continuous pores observed to persist even after microbial treatment (IV). We explore the potential of generating, propping-open and sustaining the functionality of hydraulic fractures in coal using different fracturing fluids (Part V). The alteration of the nano-pore structure due to MECBM treatment is examined by using small angle X-ray scattering (SAXS) to define the in-situ porosity evolution as a proxy to infer permeability evolution (Part VI). Coupled hydro-mechanical and bio-gasification modeling is applied to determine the effectiveness of nutrient delivery by hydraulic fracturing and its field implementation. Compared with both the unstimulated and hydro-shear-dilated cases of the natural fracture network, hydraulic fracturing demonstrates a significant improvement to enhance nutrient delivery. A preliminary analysis of field-scale methane yield is completed with consideration of the combined influence of permeability evolution, solute transport and microbial growth (Part VII). Developing nutrient solutions for Illinois Basin and San Juan Basin (Task 2): To enhance methane release from coal through bio-gasification, suitable nutrient solutions are needed to stimulate microbial activities toward coal depolymerization and conversion to biogas. Specific for bituminous coal in the Illinois basin, a nutrient recipe that can be used to enhance coal bio- gasification in situ is developed. Based on our previous experience working with Illinois coal and the characteristics of the formation water and the indigenous microbial community, four parameters, Fe powder, methanol, ethanol, and trace minerals are optimized through using a Box-Behnken design. The optimal condition predicted by the models is: Fe-powder at 74 mM, methanol at 97.91 mM, ethanol at 100 mM, and trace minerals at 100%. Under these conditions, the predicted methane yield and content is 1,417.35 ft 3 /ton and 80.7%, respectively. These results are then validated by experimental studies. In addition, each added component is evaluated in terms of its contribution to methane generated. Specifically, the role of coal in the bio-gasification process is studied against two other solid materials. Experimental data from different solid matrices prove that coal is indeed degraded by the studied microbial community.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2015

Cost and Performance Baseline for Fossil Energy Plants Volume 1a: Bituminous Coal (PC) and Natural Gas to Electricity (Rev. 3)

This report presents the cost and performance results of pulverized coal (PC) and natural gas combined cycle (NGCC) plants, using a consistent technical and economic approach that reflects current market conditions. The primary value of this report lies not in the absolute accuracy of the capital cost estimates for the individual cases (estimated to be -15%/+30%), but in application of a consistent approach to allow meaningful comparisons of relative costs among the cases evaluated.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2015

Cost and Performance Baseline for Fossil Energy Plants Supplement: Sensitivity to CO 2 Capture Rate in Coal-Fired Power Plants

The cost and performance of various plants designed to meet a range of carbon dioxide (CO 2 ) emissions are evaluated in this report by varying the CO 2 capture rate. The base cases for these designs are the supercritical (SC) pulverized coal (PC) plant from the National Energy Technology Laboratory’s (NETL) report “Cost and Performance Baseline for Fossil Energy Plants, Volume 1a: Bituminous Coal (PC) and Natural Gas to Electricity, Revision 3” and the General Electric Energy (GEE) integrated gasification combined cycle (IGCC) plant in NETL’s report, “Cost and Performance Baseline for Fossil Energy Plants, Volume 1b: Bituminous Coal (IGCC) to Electricity, Revision 2 – Year Dollar Update.” The chosen SC PC plants were based on the Case B12B, differing only in the addition of a bypass flow path that allows for an appropriate portion of the flue gas stream exiting the desulfurization step to be directed towards the stack, which reduces the amount CO 2 captured in the Cansolv process. The chosen IGCC plants were based on the Case B5B, differing by bypassing (either partially or entirely) the water gas shift reactors and thereby reducing the amount of CO 2 captured in the Selexol process. The major components of the underlying CO 2 capture technology in the plants were preserved with minimal modifications to the overall processes. The SC PC cases include up-to-date cost and performance information from recent vendor quotes whereas the IGCC performance and cost are based upon the older quotes used for the Revision 2 report, with standard adjustments made to update the costs to 2011 dollars.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2015

Cost and Performance Baseline for Fossil Energy Plants Volume 1b: Bituminous Coal (IGCC) to Electricity Revision 2b – Year Dollar Update

This report presents the cost and performance results of an assessment of seven integrated gasification combined cycle (IGCC) plants. The primary value of this report lies not in the absolute accuracy of the capital cost estimates for the individual cases (estimated to be -15 percent/+30), but in the application of a consistent approach to allow meaningful comparisons of relative costs among the cases evaluated.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

ION Advanced Solvent CO 2 Capture Pilot Project

This final report to DOE/NETL presents all the work and tests performed during ION Engineering’s (ION) carbon dioxide (CO 2 ) capture pilot test campaign: “ION Advanced Solvent CO 2 Capture Project”. This project is comprised of three budget periods (BP): BP1 – Design of a 0.6 MWe system, BP2 – 0.5 MWe National Carbon Capture Center (NCCC) Testing Campaign, and BP3 – 12 MWe Technology Center at Mongstad (TCM) Testing Campaign. The program began in October 2013 and continued until December 2017. The campaign at NCCC, which took place from June to August of 2015, resulted in 1,116 operational hours where ~350 tonnes of CO 2 were captured from the 0.5 MWe coal-fired flue gas slipstream. The follow-up campaign at TCM took place from Oct 2016 to April 2017, where 2,775 hours of operation resulted in the capture of 14,820 tonnes of CO 2 , which is a cumulative of capturing CO 2 from the natural gas-fired Combined Heat and Power (CHP) plant, and a residue fluid catalytic cracker gas (RFCC) from Statoil at Mongstad. ION has conducted a thoughtful, comprehensive, and successful program in close collaboration with all its partners. CO 2 was successfully removed and captured for extended periods of time using three gas sources (NCCC Coal-fired Power plant, TCM CHP flue gas with and without CO 2 recycle, and TCM RFCC flue gas with air dilution) at various slipstream flows ranging from 0.5 MWe to 12 MWe. The data gathered on its solvent continues to strengthen the development of ION’s advanced solvent and positive track record in executing on-site test campaigns in highly industrialized settings. These existing pilot plants do not include the necessary process modifications that ION requires to obtain the lowest possible regeneration energy; processes such as a cold-rich bypass and intercooling, would allow for lowering the demonstrated specific reboiler duty. The resulting data was also used to validate the process model, and, in the absence of testing on a custom test rig specifically designed for ION’s advanced solvent, the results of the process model have shown specific reboiler duties under 2.5 MJ/kg CO 2 (1075 BTU/lb CO 2 ). When these regeneration energies are factored into the Techno-Economic Analysis (TEA), where ION’s technology is compared to the DOE/NETL BBS Case 12, which integrates a highly optimized and commercially available CO 2 capture technology, ION’s technology shows: 38% incremental reduction in capital cost of CO 2 capture; 28% incremental reduction in annual operating and maintenance costs of CO 2 capture; and $35-44 per tonne of CO 2 capture, which is a 20% to 40% reduction in cost of CO 2 capture. Throughout pilot testing, ION has confirmed its understanding of process improvements and analytics that will enable successful operation of its advanced solvent at significantly lower L/G circulation rates, packing heights and regeneration energies than MEA. ION has identified routes to further develop its technology and is looking forward to testing a fully optimized solvent and capture system in the near future.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Flue Gas Water Vapor Latent Heat Recovery for Pressurized Oxy-Combustion

This final report presents the results of a three-year technology development project carried out by a team of participants sponsored by the Department of Energy (DOE). This is addressing the FOA Area of Interest 2: Enabling Combustion Technology. Specifically, the technology targets for flue gas water vapor latent heat recovery from pressurized oxy-coal combustion power plants. A pilot scale Transport Membrane Condenser (TMC) system has been developed, fabricated, integrated, and performance-tested in a pressurized oxy-coal pilot-scale combustion system to prove its effectiveness. We have evaluated its performance and analyzed the results for application to commercial-scale power plants. We expect the same technology to be also applicable to pressurized chemical looping combustion (CLC) flue gas, which has similar conditions.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Pilot Scale Operation and Testing of Syngas Chemical Looping For Hydrogen Production

The Syngas Chemical looping (SCL) process provides efficient and economic means to utilize the abundant fossil reserve of coal. The main problem associated with coal utilization is the CO 2 emissions resulting from its combustion. Even though CO 2 regulation or carbon tax is currently not in place, its enforcement is expected in the near future. Such a greenhouse gas emission control, if adopted in current power plant systems, will drive the efficiency down and increase the cost of electricity, due to the energy and capital-intensive nature of current CO 2 separation techniques. This highlights the need to develop technologies that present a solution to the rising cost of electricity in the future. The integrated gasification combined cycle (IGCC) presents an improvement to the above predicament, but it is capital intensive due to the extensive unit operations involved. The efficiency for a CO 2 capture incorporated IGCC system is around ~32%, resulting in approximately 45% increase in cost of electricity. This is definitely a better path to traverse than the conventional pulverized coal (PC) power plants as it has improved economics and efficiencies accompanied by product flexibility. The SCL process advances the benefits even further when integrated with the IGCC process. The SCL process removes the expensive WGS system and CO 2 separation columns, thereby saving on capital and operational expenses. This integration results in a 12 – 21% increase in efficiency accompanied by a reduction in cost of electricity by 15 – 28%, over conventional IGCC systems. Therefore, SCL process provides the best route to harness the energy from coal. The overall project objective was to construct and operate a syngas chemical looping pilot scale test unit at the NCCC. The project scope of work was divided into 3 phases. In Phase I, cold flow model studies using a 1:1 scale acrylic test unit constructed at Particulate Solids Research, Inc. (PSRI) was successfully completed confirming robust solid flow control is achievable in the non-mechanical system design. In Phase II, the high pressure, high temperature, chemical looping reactor was successfully designed with all necessary equipment and safety instrumentation/controls specified to allow for fabrication, site construction, and assembly to commence in Phase III. In Phase III, the SCL pilot plant was successfully assembled and all necessary functional checks and pre-startup safety reviews completed. During unit commission over the course of 200 hours of testing, operational issues were observed with premix burner used for system startup. With the grants awarded by the National Energy Laboratory (NETL) and the Ohio Development Services Agency (ODSA) under awards DE-FE0023915 and D-14-18, the SCL pilot unit underwent three auxiliary equipment modifications to resolve all of the startup operational issues encountered. The unit was successfully demonstrated with 300+hr continuous operation. Key results obtained include high syngas conversion of 97.95% with 16.03% oxygen carrier conversion in the moving bed reducer and >99% purity H 2 produced from the moving bed oxidizer.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

FINAL SCIENTIFIC/TECHNICAL REPORT: Dry Solids Pump - Coal Feed Technologies

Gas Technology Institute (GTI) has concluded the Dry Solids Pump Coal - Feed Technologies (DSP-CFT) program that was initiated on October 1, 2013. The project’s primary objectives have been to gather data to increase the fidelity of the economic benefits of the Dry Solids Pump (DSP) technology for Integrated Gasification Combined Cycle (IGCC) plants, mature the technology to a Technology Readiness Level (TRL) of TRL 6 by continued testing and upgrades to the existing DSP, advance pump configuration knowledge to the point that a commercial pump can be confidently designed for low rank coal feed stocks and develop the next generation design configuration of a 1000 ton per day (tpd) DSP. After initial efforts with the existing DSP, a subscale pump was built to reduce the cost and time required to develop upgrades. The subscale development program evaluated three exit configurations and a host of geometric variations in each configuration concluding a side exit upward discharge configuration offered the greatest improvements. Both configuration and operation focused improvements were implemented on the full scale existing DSP and demonstrated 500 psi operation. An initial Techno-economic Analysis (TEA) and later update that was undertaken by Mr. Chris Higman and associates. The TEA quantifies the dramatic savings in capital and operational expenses achieved by reducing plant height and nitrogen consumption/compression, respectively in a commercial gasifier application. Drawings of the suggested design configuration for a commercial DSP feeder reflect the side exit design and incorporate lighter weight and lower cost fabrication methods. Features used for development testing are removed. A follow-on optimization program to allow the DSP technology to achieve TRL 7 is outlined.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Abstract - Cooperative Research and Development Agreement between Sotacarbo and National Energy Technology Laboratory

The objective of this CRADA between NETL and Sotacarbo is to develop mutual collaboration in the areas of: CFD Modeling for optimization of coal/biomass gasification processes, CO 2 Separation by Membranes, CO 2 -to-Liquids, & CO 2 Sequestration. The CFD modeling and optimization of coal/biomass gasification processes project will bring together NETL’s expertise in the area of computational multiphase flows with Sotacarbo’s expertise in the area of design and operation of coal and biomass gasifiers. The outcome of this collaboration should be validated coal/biomass CFD models, which can assist in design and scale-up studies of gasifiers. There are several gasification units at Sotacarbo’s Research Center which can be used for gasification model development and validation using NETL’s MFiX Suite of multiphase flow CFD software. The other remaining technical topic outcomes will be determined at a later time as a result of further discussions.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Abstract - Cooperative Research and Development Agreement between Ramaco Carbon and National Energy Technology Laboratory

NETL and Ramaco Carbon have developed an umbrella Cooperative Research and Development Agreement (CRADA). This umbrella CRADA will be used to initiate detailed technical discussions for assessing projects in 3 general areas: 1) The conversion of coal to value-added solid carbon products such as carbon fiber and carbon nanomaterials, 2) The use of computational modeling for developing coal beneficiation processes, and 3) The development of technologies for extracting rare earth elements from coal, beneficiated coal, coal-byproducts and mining byproducts.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Strategies for Lime Treatment Of D-Area Coal Storage Area (484-17D) Vadose Zone Soil

Sixty years of coal storage operations in the DCSA (484-17D, Figure 1) have resulted in vadose zone soils with a total acidity level typical of acid mine drainage soils. Field measurements from June 2018 show soil pH values ranging from 3 to 4.5 to water-table depth (10 to 12 feet). Best estimates for treatment of the acidic soils with dolomitic (agricultural) limestone suggest a required application rate ranging from 8 to 10 tons per acre per foot of soil depth to raise the soil pH from 3.5 to 5.5. The model predicts a lower bound of 3 tons per acre per foot for high-quality limestone with a particle size less than 60-mesh and an upper bound of 19 tons per acre per foot for lower-quality limestone. This compares to typical residential and agricultural lime application rates of one to four tons per acre per foot of depth.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2019

Integrated Flue Gas Purification and Latent Heat Recovery for Pressurized Oxy-Combustion (Final Scientific/Technical Report)

Pressurized oxy-combustion has been identified by DOE as a transformational technology for coal power with carbon capture due to the advantages that are realized when the combustion process is pressurized. The staged pressurized oxy-combustion (SPOC) process is particularly attractive as the efficiency of the process is almost 6 percentage points greater than that of first generation oxy-combustion. A critical component of the SPOC process, and potentially other pressurized combustion processes, is the Direct Contact Cooler (DCC) where the latent heat of the flue gas moisture is recovery to improve plant efficiency while simultaneously removing SO x and NO x from the flue gas, so that the FGD and de-NO x processes can be eliminated, and the cost of electricity minimized. The objective of this R&D effort was to advance the TRL of the DCC technology, which included performance testing at a 100 kW scale to validate the process and obtain key engineering data for scale-up. A collateral objective was to study the gas- and liquid-phase kinetics, and the development of a systematic chemical mechanism validated by experimental data. Experiments in a bench-scale stirred reactor provided an updated understanding of the liquid chemistry and the effects of temperature and pH. This information was used to develop a reduced reaction mechanism, which was subsequently incorporated in an ASPENbased process model, to allow for evaluation of the DCC at full scale. A small-pilot DCC column was designed, constructed and tested using simulated flue gas at the pressurized oxy-combustion test facility at Washington University in St. Louis. In the majority of tests, the SO 2 capture approached 100%, making the NO x capture the primary metric of capture efficiency. An NO x capture efficiency of 90% was achieved when the gas residence time was 95 seconds, demonstrating that high capture rates can be attained with reasonable reactor size. At higher temperatures (up to 200°C inlet gas temperature) the total NO x scrubbing efficiency was reduced by approximately 10% (compared to room temp.) and this was attributed to a reduced NO oxidation rate. A significant amount of SO 2 was present in the gas outlet (10%) only when the temperature was high and the N:S ratio was low (N/S < 1), which highlights the necessity of controlling the NOx concentration in the flue gas for complete sulfur scrubbing. After incorporated our optimized chemical mechanism into an ASPEN process model, various full-scale configurations of the DCC were evaluate, and the results indicate that the proposed DCC can accomplish its intended goals at full scale and at a modest size. Thus, the results of this project indicate that the DCC is a promising technology for recovery of the latent heat of the moisture in the flue gas while simultaneously scrubbing the nitrogen and sulfur oxides, thus enabling pressurized oxy-combustion, in general, and the SPOC process, in particular.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2019

Abstract - Cooperative Research and Development Agreement between Ramaco Carbon and National Energy Technology Laboratory

Domestic coal can be used to manufacture a wide range of solid carbon products including carbon fiber, carbon additives for cements and structural composites, battery and electrode materials, carbon nanomaterials and composites, and 3D printing materials. The market value of high performance carbons in these applications exceeds the fuel and heat value of coal by several orders of magnitude, which illustrates there are sustainable market forces to manufacture high performance carbon materials from domestic coal feedstocks.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2018

Advanced Integrated Technologies for Treatment and Reutilized of Impaired Water in Fossil Fuel-based Power Plant Systems (Final Report)

The water-energy nexus is an important issue in regards to U.S. energy security and its significance will increase in the future due to increasing populations, energy demand, and competition for available water. The subsurface storage of carbon dioxide (along with fossil energy resource extraction), could generate significant quantities of brine, which if effectively treated could be beneficially reutilized. This document reports results from U.S. Department of Energy Project DE-FE0026315 which evaluated the use of electrocoagulation (EC) and supercritical water (SCW) treatment as a means to generate a water product for beneficial reuse from brine. The use of a novel SCW treatment system was studied with simulated and field-derived brine fluids. In addition, selective removal of high-value brine components via EC was studied. Techno-economics for treatment of high dissolved solids content brine (180,000 ppm) is also reported.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2015

Coal Fleet Transition: Retirement Impacts in the Eastern Interconnection

This report examines the impact of announced retirements on the mix of available generating capacity, prices, resource availability, and air emissions in the Eastern Interconnection. The report uses a security constrained economic dispatch (SCED) model - Ventyx's PROMOD IV 11.1 - of the bulk electric system (BES) to model the interconnection.

01 COAL, LIGNITE, AND PEAT↗
DOE OSTI2012

Environmental Retrofit Tracking

This presentation tracks environmental retrofits to the existing coal-fired power fleet, through various stages of project development. Many of the environmental compliance strategies that are expected to be implemented are analyzed with respect to recent regulatory initiatives, that may impact the existing coal-fired asset base.

01 COAL, LIGNITE, AND PEAT↗