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Ikelic - Alliance Digital Repository

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STATUS OF COAL PROJECTS (Underline denotes changes since June 1994)<br />

COMMERCIAL AND R&D PROJECTS (Continued)<br />

- TAMPELLA IGCC PROCESS DEMONSTRATION Tampella<br />

Power (C-565)<br />

After having obtained the rights to the Institute of Gas Technology's fluidized bed gasification technology in 1989, Tampella Keeler<br />

began to design and initiate construction of a 10 MW thermal pilot plant at their research facilities in Tampere, Finland. The pilot<br />

plant is considered essential for determining operating parameters for specific coals and for continuing process development in the<br />

areas of in-gasifier sulfur capture and hot gas cleanup. The pilot plant will be operational in early 1991.<br />

The pilot plant is designed so that alternative hot gas filters and zinc ferrite absorber/regenerator design concepts can be<br />

evaluated. The gasifier is 66 foot tall, with an inside diameter ranging from 2 to 4 feet. The gasifier will be capable of operating at<br />

pressures up to 425 psig.<br />

After the pilot plant construction was underway, Tampella turned its attention towards locating a demonstration project in Finland<br />

and one in the U.S. A cogeneration project to be located at an existing papermill has been selected as the basis for the demonstra<br />

tion in Finland. The gasifier will have a capacity of 150 MW thermal which is equal to about 500 tons per day of coal consumption.<br />

The plant will produce about 60 MW of electricity and about 60 MW equivalent of district heating.<br />

In September, 1991 Tampella received support from the U.S. Department of Energy (DOE) to build an integrated gasification<br />

combined-cycle demonstration facility, known as the Toms Creek IGCC Demonstration Project, in Coeburn, Wise County, Virginia<br />

(see project C-580, below). The Toms Creek Project will utilize Tampella Power's advanced coal gasification technology to<br />

demonstrate improved efficiency for conversion of coal to electric power while significantly reducing SO and NO emissions.<br />

- TECO IGCC PLANT Teco<br />

Power Services, U.S. Department of Energy (C-567)<br />

Tampa Electric Company's new (TEC) Polk Power Station Unit #1 will be the first unit at a new site and will use Integrated<br />

Gasification Combined Cycle (IGCC) Technology. The project is partially funded by the U.S. Department of Energy (DOE) under<br />

Round III of its Clean Coal Technology Program. In addition to the TEC and DOE, TECO Power Services (TPS), a subsidiary a<br />

TECO Energy, Inc., and an affiliate of TEC, is also participating in the project. TPS is responsible for the overall project manage<br />

ment for the DOE portion of this IGCC project.<br />

The Polk Power Station IGCC Project will be constructed in two phases. TEC's operation needs called for 150 MW of peaking<br />

capacity in mid-1995, becoming part of the 260 MW of total IGCC capacity in mid-1996. The first phase will be the installation of<br />

an advanced combustion turbine (CT) scheduled for commercial operation in July 1995. This CT will fire No. 2 oil during its first<br />

year while in peaking service. During that year, TEC will complete installation of the gasification and combined cycle facilities<br />

which will be in commercial operation in July 1996.<br />

In addition, part of this DOE CCT project will be to test and demonstrate a new hot gas clean-up (HGCU) technology.<br />

The Texaco Gasification Process has been selected for integration with a combined cycle power block.<br />

Part of the Cooperative Agreement for this project is the two-year demonstration phase. During this period it is planned that<br />

about four to six different types of coal will be tested in the operating IGCC power plant. The results of these tests will compare<br />

this unit's efficiency, operability, and costs, and report on each of these test coals specified against the design basis coal. These<br />

results should identify operating parameters and costs which can be used by utilities in the future as they make their selection on<br />

methods for meeting both their generation needs and environmental regulations.<br />

Project Cost: $600 million<br />

TEXACO COOL WATER PROJECT - Texaco<br />

Syngas Inc. (C-569)<br />

Original Cool Water participants built a 1,000-1,200 tons per day commercial-scale coal gasification plant using the oxygen-blown<br />

Texaco Coal Gasification Process. The gasification system which includes two Syngas Cooler vessels, was integrated with a General<br />

Electric combined cycle unit to produce approximately 122 megawatts of gross power. Plant construction, which began in Decem<br />

ber 1981, was completed on April 30, 1984, within the projected $300 million budget. A 5-year demonstration period was com<br />

Project"<br />

pleted in January 1989. See "Cool Water in the December 1991 issue of the Synthetic Fuels Report, Status of Projects sec<br />

tion for details of the original completed project.<br />

Texaco plans to modify and reactivate the existing facilities to demonstrate new activities which include the addition of sewage<br />

sludge into the coal feedstock, production of methanol, and carbon dioxide recovery.<br />

Texaco intends to use a new application of Texaco's technology which will allow the Cool Water plant to convert municipal sewage<br />

sludge to useful energy by mixing it with the coal feedstock. Texaco has demonstrated in pilot runs that sludge can be mixed with<br />

coal and, under high temperatures and pressures, gasified to produce a clean synthesis gas. The plant will produce no harmful<br />

byproducts.<br />

4-75<br />

SYNTHETIC FUELS REPORT, JANUARY 1995

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