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124 records · Page 7

Tire-to-Surface Friction-Coefficient Measurements with a C-123B Airplane on Various Runway Surfaces

An investigation was conducted to obtain information on the tire-to-surface friction coefficients available in aircraft braking during the landing run. The tests were made with a C-123B airplane on both wet and dry concrete and bituminous pavements and on snow-covered and ice surfaces at speeds from 12 to 115 knots. Measurements were made of the maximum (incipient skidding) friction coefficient, the full-skidding (locked wheel) friction coefficient, and the wheel slip ratio during braking.

Sawyer, Richard H.↗

Assessment of Advanced Coal Gasification Processes

This report represents a technical assessment of the following advanced coal gasification processes: AVCO High Throughput Gasification (HTG) Process; Bell Single-Stage High Mass Flux (HMF) Process; Cities Service/Rockwell (CS/R) Hydrogasification Process; Exxon Catalytic Coal Gasification (CCG) Process. Each process is evaluated for its potential to produce SNG from a bituminous coal. In addition to identifying the new technology these processes represent, key similarities/differences, strengths/weaknesses, and potential improvements to each process are identified. The AVCO HTG and the Bell HMF gasifiers share similarities with respect to: short residence time (SRT), high throughput rate, slagging and syngas as the initial raw product gas. The CS/R Hydrogasifier is also SRT but is non-slagging and produces a raw gas high in methane content. The Exxon CCG gasifier is a long residence time, catalytic, fluidbed reactor producing all of the raw product methane in the gasifier. The report makes the following assessments: 1) while each process has significant potential as coal gasifiers, the CS/R and Exxon processes are better suited for SNG production; 2) the Exxon process is the closest to a commercial level for near-term SNG production; and 3) the SRT processes require significant development including scale-up and turndown demonstration, char processing and/or utilization demonstration, and reactor control and safety features development.

coal gasification↗

Making Activated Carbon by Wet Pressurized Pyrolysis

A wet pressurized pyrolysis (wet carbonization) process has been invented as a means of producing activated carbon from a wide variety of inedible biomass consisting principally of plant wastes. The principal intended use of this activated carbon is room-temperature adsorption of pollutant gases from cooled incinerator exhaust streams. Activated carbon is highly porous and has a large surface area. The surface area depends strongly on the raw material and the production process. Coconut shells and bituminous coal are the primary raw materials that, until now, were converted into activated carbon of commercially acceptable quality by use of traditional production processes that involve activation by use of steam or carbon dioxide. In the wet pressurized pyrolysis process, the plant material is subjected to high pressure and temperature in an aqueous medium in the absence of oxygen for a specified amount of time to break carbon-oxygen bonds in the organic material and modify the structure of the material to obtain large surface area. Plant materials that have been used in demonstrations of the process include inedible parts of wheat, rice, potato, soybean, and tomato plants. The raw plant material is ground and mixed with a specified proportion of water. The mixture is placed in a stirred autoclave, wherein it is pyrolized at a temperature between 450 and 590 F (approximately between 230 and 310 C) and a pressure between 1 and 1.4 kpsi (approximately between 7 and 10 MPa) for a time between 5 minutes and 1 hour. The solid fraction remaining after wet carbonization is dried, then activated at a temperature of 500 F (260 C) in nitrogen gas. The activated carbon thus produced is comparable to commercial activated carbon. It can be used to adsorb oxides of sulfur, oxides of nitrogen, and trace amounts of hydrocarbons, any or all of which can be present in flue gas. Alternatively, the dried solid fraction can be used, even without the activation treatment, to absorb oxides of nitrogen.

Fisher, John W.↗

Topical Report: Reference Plant Cost Estimates for TRIG™ Systems

Southern Company Services, Inc. has conducted a Reference Plant conceptual design for the Transport Integrated Gasification (TRIG™) IGCC technology. While the technical knowledge and cost data gathered from the Kemper County IGCC project provide a basis for this effort, this conceptual design incorporates cost improvements and commercially available technology advancements that are representative of a mature “nth” TRIG™ IGCC project. The design is based on an abundant, sub-bituminous coal feedstock, and includes two options for CO 2 capture. The resulting Reference Plant provides a basis for comparison with other technologies as a first step for evaluating the TRIG™ IGCC technology.

01 COAL, LIGNITE, AND PEAT↗

Developing Analytical Techniques for Modeling Construction/Infrastructure of Energy Systems - ISSST2019

This work was presented at the International Symposium on Sustainable Systems and Transportation (ISSST) 2019 Conference in Portland, OR on June 25, 2019. Using detailed component-level cost estimates for new fossil power plants as documented in Cost and Performance Baseline for Fossil Energy Plants Volume 1a: Bituminous Coal (PC) and Natural Gas to Electricity Revision 3, economic demands for the construction of a power plant and the manufacturing of its components are estimated. The model produces national average construction impact results for the life cycle of a power plant. This output highlights areas of further research that help to define valuable data collection efforts.

Carlson, Derrick R.↗

High CO2 Capture Rate Cost and Performance for F- and H-Class Natural Gas Combined Cycles (NGCC)

The National Energy Technology Laboratory (NETL) is updating its study titled “Cost and Performance Baselines for Fossil Energy Plants, Volume 1: Bituminous Coal and Natural Gas to Electricity.” Revision 4 was published in 2019. Pulverized coal (PC) and natural gas combined cycle (NGCC) cases with carbon capture in that study capture carbon dioxide (CO2) at 90% efficiency. Field-testing of post-combustion CO2 capture technology as well as vendor and industry feedback on projects currently in the planning stages (including FEED projects sponsored by DOE) indicate that capture rates as high as 95% are feasible for both coal- and natural gas-fueled electricity generating units. Technology suppliers (as reflected in vendor-supplied information provided to DOE for this study that included cost and performance estimates for both NGCC (97%) and PC (99%) study cases) as well as subject matter experts acknowledge and support that solvent-based post-combustion CO2 capture technologies are capable of achieving CO2 removal rates beyond 95% on low-purity streams representative of fossil-fueled combustion; however, the relatively limited experience with design and operation of capture systems that can routinely, reliably, and economically achieve very high removal rates (e.g., 97% for NGCC flue gas) requires further study. This presentation will address performance and cost estimates for 90%, 95%, and 97% capture for F- and H-class NGCC plants. This presentation was given at the 2022 Pittsburgh Coal Conference.

Fout, Timothy↗

M2CT-22IN1202096 Design for Carbon Conversion Product Pathways with Nuclear Power Plant Integration

Coal is a globally abundant resource that historically has been used for power generation via combustion. As the power industry replaces coal with cleaner methods of generation, energy-rich coal could be used in other chemical and fuel applications. This study presents a coal utilization option in which coal combustion is replaced with a carbon-free nuclear power plant and the coal is upgraded to valuable products for a variety of markets. Coal is prepared for conversion first by the pyrolysis process, which will optimize solid, liquid, and gaseous products based on the market size and potential product value, maximizing the monetary value of coal. This process is designed using bituminous coal from the Appalachian region as a basis to provide a pathway to preserve or transition coal-related jobs and create new jobs associated with the clean energy transition. Process modeling in the AspenOne Suite will be used to determine each component’s sensitivities, costs, inputs, and outputs. Dispatch modeling in the FORCE toolset will optimize the entire system and calculate the NPV for the refinery lifetime. Advanced and light-water reactors are considerations to supply the heat, steam, and electricity to the process. This paper focuses on the technical and market analysis used to determine the optimal processes and product pathways for the carbon refinery. Product pathways are on activated carbon, formic acid synthesis, and methanol synthesis for further upgrading to marketable chemical and polymer products.

01 COAL, LIGNITE, AND PEAT↗

M2CT-22IN1202096 Design for Carbon Conversion Product Pathways with Nuclear Power Plant Integration

Coal is a globally abundant resource that historically has been used for power generation via combustion. As the power industry replaces coal with cleaner methods of generation, energy-rich coal could be used in other chemical and fuel applications. This study presents a coal utilization option in which coal combustion is replaced with a carbon-free nuclear power plant and the coal is upgraded to valuable products for a variety of markets. Coal is prepared for conversion first by the pyrolysis process, which will optimize solid, liquid, and gaseous products based on the market size and potential product value, maximizing the monetary value of coal. This process is designed using bituminous coal from the Appalachian region as a basis to provide a pathway to preserve or transition coal-related jobs and create new jobs associated with the clean energy transition. Process modeling in the AspenOne Suite will be used to determine each component’s sensitivities, costs, inputs, and outputs. Dispatch modeling in the FORCE toolset will optimize the entire system and calculate the NPV for the refinery lifetime. Advanced and light-water reactors are considerations to supply the heat, steam, and electricity to the process. This paper focuses on the technical and market analysis used to determine the optimal processes and product pathways for the carbon refinery. Product pathways are on activated carbon, formic acid synthesis, and methanol synthesis for further upgrading to marketable chemical and polymer products.

01 COAL, LIGNITE, AND PEAT↗

Design for Carbon Conversion Product Pathways with Nuclear Power Plant Integration (PCC)

Coal is a globally abundant resource that historically has been used for power generation via combustion. As the power industry replaces coal with cleaner methods of generation, energy rich coal could be used in other chemical and fuel applications. This study presents a coal utilization option in which coal combustion is replaced with a carbon-free nuclear power plant and the coal is upgraded to valuable products for a variety of markets. Coal is prepared for conversion first by the pyrolysis process, which will optimize solid, liquid, and gaseous products based on the market size and potential product value, maximizing the monetary value of coal. This process is designed using bituminous coal from the Appalachian region as a basis to provide a pathway to preserve or transition coal-related jobs and create new jobs associated with the clean energy transition. Process modeling will be used to determine each component’s sensitivities, costs, inputs, and outputs Advanced and light-water reactors are considerations to supply the heat, steam, and electricity to the process. This paper focuses on the technical and market analysis used to determine the optimal processes and product pathways for the carbon refinery. Product pathways are on activated carbon, formic acid synthesis, and methanol synthesis for further upgrading to marketable chemical and polymer products.

01 COAL, LIGNITE, AND PEAT↗

Decommissioning of obsolete Nuclear Facilities in the UJV Rez, a. s. - 19027

UJV Rez, a. s. (further also UJV) is a leading institution in all areas of nuclear R and D in the Czech Republic and has had a dominant position in the nuclear program since it was established in 1955 as the Nuclear Research Institute Rez. The activities of UJV encompass nuclear physics, chemistry, nuclear power and many other topics. The main issues addressed at UJV in past decades have included research, development and services for NPPs, the fuel cycle and irradiation services for research and development in the industrial sector and medicine. UJV also manages most institutional radioactive wastes (RAW) produced in the Czech Republic (approx. 90 %). After more than 60 years of activities of the UJV in the nuclear field, there were obsolete nuclear facilities to be decommissioned. Decommissioning of nuclear facilities UJV is the only ongoing decommissioning project in the Czech Republic. Preparations for decommissioning began in 1996. Safety analysis report (SAR) was performed comprising the identification and characterization of potential sources of risk, potentially exposed receptors and exposure pathways, potential chemical compounds, radionuclides and media of concern. The results of the SAR enabled to determine the priorities of the decommissioning, the decommissioning the expenses and as well as project implementation. The decommissioning project was revised on the base of information obtained during decommissioning. The decommissioning was divided into two phases according to the level of risk and the financing limitations. The Ministry of Finance significantly financially contributed the decommissioning, although the UJV also contributed a considerable amount. Overall cost is close to the amount of Eur 27 million. Decommissioning started in 2003 and will be finished in 2018. Almost all facilities have already been successfully decommissioned. In the following table, the status of decommissioning of facilities is described. 1) Reloading site for RAW storage (Building 211/6): last item in progress 2003 - 2018; 2) Special Sewage System: decommissioned 2004 - 2005, reused; 3) Liquid RAW storage tanks (Building 211/3): decontaminated 2004 - 2013, reused; 4) Technology for RAW treatment (Building 241): decommissioned 2003 - 2011; 5) Contaminated equipment (Building 250): decommissioned 2003 - 2016; 6) Systems for storage of sealed sources (Building 261); decommissioned 2003 - 2005; 7) Decay tanks (Building 211/5); decommissioned 2003 - 2014, reused; 8) Old bituminating unit (Building 211/3); decommissioned 2004 - 2008; 9) Surface RAW storage site; decommissioned 2009 - 2014. Later, other unused decommissioning facilities, which were not included in the decommissioning project financed by the state, were included. These facilities are continuously decommissioned and financed from own resources of UJV. These facilities are like facilities already decommissioned: radiochemical laboratories, (including glove boxes), liquid RW storage tanks (including sewage systems), liquid RW treatment technology, hot cells, accumulated RW, etc. Realization started 2016 and expected duration is till 2026. Estimated budget is approximately Eur 17 million. The decommissioning of nuclear facilities in UJV is being carried out on the high level of radiation protection and up to now there was no extraordinary event or accident, although some challenges we were forced to address. (authors)

12 MANAGEMENT OF RADIOACTIVE AND NON-RADIOACTIVE W↗

Characterization and recovery of rare earth elements and other critical metals (Co, Cr, Li, Mn, Sr, and V) from the calcination products of a coal refuse sample

Here, the impacts of calcination on the leaching recovery of rare earth elements (REEs) and other critical metals from a Baker seam coal refuse material were investigated. Acid leaching test results showed that leaching recovery of the REEs, especially the light REEs, was increased significantly from around 24% to 80–90% after calcination under 600–750 °C for two hours. By considering the major element leaching kinetics and the mineralogical changes of the dominant minerals caused by calcination, two mechanisms were proposed for the improved leaching performance: (1) decomposition of difficult-to-dissolve REE-bearing minerals into soluble forms; and (2) liberation of REE-bearing minerals encapsulated in clays after calcination due to the dehydration and disintegration of the layered clay structure. Sequential chemical extraction tests showed that a significant fraction (around 75%) of the REEs in the raw material were present in an insoluble form. After calcination under proper temperatures (600–800 °C), the majority of the insoluble light REEs (LREEs) were converted into soluble forms. Changes in the modes of occurrence of the LREEs and phosphorous based on leaching rate and sequential leaching correlated well as a function of the calcination temperature. This finding in addition to SEM-EDX results tends to indicate the potential that the LREEs occur primarily as rare earth phosphates such as monazite in the untreated coal refuse material. The acid leaching and sequential chemical extraction results show that co-extraction of REEs and other critical metals such as Co, Mn, and Li is possible using a calcination-acid leaching procedure.

01 COAL, LIGNITE, AND PEAT↗

Dover Light & Power 10 MWe Coal Direct Chemical Looping (CDCL) (Large Pilot Plant Test - Phase I Feasibility)

A feasibility study was conducted to install a 10 MWe coal direct chemical looping large pilot plant at a host site. The coal direct chemical looping technology was based on The Ohio State University and Babcock & Wilcox iron-based metal oxide technology coupling a moving bed reduction reactor with a circulating fluidized-bed oxidation reactor. The host site was the Dover Light & power Plant in Dover, Ohio. The Electric Power Research Institute performed the host site evaluation. Trinity Consultants prepared the Environmental Information Volume. WorleyParsons Group performed the civil engineering. Clear Skies Consulting served as lead on the Industrial Advisory Committee.

20 FOSSIL-FUELED POWER PLANTS↗

The Coal Industry Perspective [Slides]

This report provides an overview of the global coal industry, with additional focus on the United States. Some of the areas it covers include coal prices, consumption, production, stockpiles, imports, exports, reserves, and productivity measures. It provides juxtapositions between the United States and other countries' coal industries. 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.

01 COAL, LIGNITE, AND PEAT↗

250 kWt Pilot Testing in Support of a 10 MWe Coal-Direct Chemical Looping Demonstration Feasibility Study

The Babcock & Wilcox Company and The Ohio State University have constructed a 250 kWt coal direct chemical looping pilot facility at the Babcock & Wilcox Research Center in Barberton, Ohio. Testing was conducted on the facility to support installation of a 10 MWe coal direct chemical looping large pilot facility at the Dover Light & Power Plant in Dover, Ohio. Results of the testing and their impact on the design of the large pilot facility are discussed.

20 FOSSIL-FUELED POWER PLANTS↗

NETL Coal Energy Atlas: A Collection of Coal/Energy Related Maps

The NETL Coal Energy Atlas contains a comprehensive collection of coal and energy-related maps and graphics curated by the National Energy Technology Laboratory (NETL) Systems Analysis group. It serves as a living document providing an overview of the U.S. coal and energy sectors. The volume is structurally organized into six key thematic areas. Ultimately, the atlas functions as a modular baseline for data integration, allowing researchers to drill down into specific regional locations or customize geographic base layers for advanced systems analysis.

bituminous coal↗