SLIDES: Costs and Benefits of Oil Shale Development

Presenter: James T. Bartis, Senior Policy Researcher, Rand Corporation 21 slide

SLIDES: Costs and Benefits of Oil Shale Development

Presenter: James T. Bartis, Senior Policy Researcher, Rand Corporation 21 slide

Anthracite R&D needs - CRADA 89-001. Final report

The purpose of this research is to foster the development of one or more high performance, anthracite-fired boiler systems suitable for meeting space heating and hot water requirements of large buildings. The boiler system research would include fuel handling, combustion and heat transfer, ash handling, and control systems

Integrated coal preparation and CWF processing plant: Conceptual design and costing

At the request of the US Department of Energy (DOE), Pittsburgh Energy Technology Center, a study was conducted to provide DOE with a reliable, documented estimate of the cost of producing coal-water fuel (CWF). The approach to the project was to specify a plant capacity and location, identify and analyze a suitable coal, and develop a conceptual design for an integrated coal preparation and CWF processing plant. Using this information, a definitive costing study was then conducted, on the basis of which an economic and sensitivity analysis was performed utilizing a financial evaluation model to determine a price for CWF in 1992. The design output of the integrated plant is 200 tons of coal (dry basis) per hour. Operating at a capacity factor of 83 percent, the baseline design yields approximately 1.5 million tons per year of coal on a dry basis. This is approximately equivalent to the fuel required to continuously generate 500 MW of electric power. The CWF produced by the plant is intended as a replacement for heavy oil or gas in electric utility and large industrial boilers. The particle size distribution, particularly the top size, and the ash content of the coal in the CWF are specified at significantly lower levels than is commonly found in typical pulverized coal grinds. The particle top size is 125 microns (vs typically 300m[mu] for pulverized coal) and the coal ash content is 3.8 percent. The lower top size is intended to promote complete carbon burnout at less derating in boilers that are not designed for coal firing. The reduced mineral matter content will produce ash of very fine particle size during combustion, which leads to less impaction and reduced fouling of tubes in convective passages