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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 />

would be the highest 10 percent price cap. During these negotiations, Columbia Gas withdrew from the project. On May 13, 1982,<br />

it was announced that a subsidiary of Pacific Lighting Corporation had acquired a 10 percent interest in the partnership; 15 percent<br />

from ANR's interest and 25 percent from Transco.<br />

Full-scale construction did not commence until August 6, 1981 when the United States Department of Energy (DOE) announced<br />

the approval of a S2.02 billion conditional commitment to guarantee loans for the project. This commitment was sufficient to cover<br />

the debt portion of the gasification plant, Great Plains'<br />

share of the coal mine associated with the plant, an SNG pipeline to con<br />

nect the plant to the interstate natural gas system, and a contingency for overruns. Final approval of the loan guarantee was<br />

received on January 29, 1982. The project sponsors were generally committed to providing one dollar of funding for each three dol<br />

lars received under the loan guarantee up to a maximum of $740 million of equity funds. The project's final cost was approximately<br />

$2 billion with a %\5 billion provided pursuant to the DOE guarantee and $500 million by the five partners.<br />

The project was designed to produce an average of 125 million cubic feet per day (based on a 91 percent onstream factor, i.e., a<br />

1373 million cubic foot per day design capacity) of high BTU pipeline quality SNG, 93 tons per day of ammonia, 88 tons per day of<br />

sulfur, 200 million cubic feet per day of carbon dioxide, potentially for enhanced oil recovery, and other miscellaneous by-products<br />

including tar oil, phenols, and naphtha to be used as fuels. Approximately 16,000 tons per day of North Dakota lignite were ex<br />

pected to be required as feedstock.<br />

In August, 1985 the sponsors withdrew from the project and defaulted on the loan, and DOE began operating the plant under a<br />

contract with the ANG Coal Gasification Company. The plant successfully operated throughout this period and earned revenues in<br />

excess of operating costs. The SNG is marketed through a 34 mile long pipeline connecting the plant with the Northern Border<br />

pipeline which in turn transports the SNG to Ventura, Iowa.<br />

In parallel with the above events, DOE and the Department of Justice (DOJ) filed suit in the District Court of North Dakota<br />

(Southwestern Division) seeking validation of the gas purchase agreements and approval to proceed with foreclosure. On<br />

January 14, 1986 the North Dakota Court found the gas purchase agreements valid, that state law was not applicable and that plain<br />

tiffs (DOE/DOJ) were entitled to a summary judgment for foreclosure. A foreclosure sale was held and DOE obtained legal title<br />

to the plant and its assets on July 16, 1986. This decision was upheld by the United States Court of Appeals for the Eighth Circuit<br />

on January 14, 1987. On November 3, 1987, the Supreme Court denied a petition for a writ of certiorari.<br />

The North Dakota District Court also held that the defendant pipeline companies were liable to the plaintiffs (DOE/DOJ) for the<br />

difference between the contract price and the market value price. This decision was upheld by the United States Court of Appeals<br />

for the Eighth Circuit on May 19, 1987. No further opportunity for appeal exists and the decisions of the lower court stands.<br />

In early 1987, the Department of Energy hired Shearson Lehman Bros, to help sell the Great Plains plant. In August, 1988 it was<br />

announced the Basin Electric Power Cooperative had submitted the winning bid for approximately $85 million up-front plus future<br />

with profit-sharing the government and a waiver of production tax credits. Two new Basin subsidiaries, Dakota Gasification Com<br />

pany (DGC) and Dakota Coal Company, operate the plant and manage the mine respectively. Ownership of the plant was trans<br />

ferred on October 31, 1988.<br />

Under Dakota Gasification ownership, the plant has been producing SNG at over 125 percent of design capacity on an annual<br />

basis.<br />

In 1989, DGC began concentrating on developing revenue from byproducts. On February 15, 1991, a phenol recovery facility was<br />

completed. This project produces over 2 million gallons of phenol annually, providing manufacturers an ingredient for plywood<br />

and chipboard resins. The first railcar of phenol was shipped in January 1991. DGC has signed contracts with three firms to sell<br />

all of its output of crude cresylic acids, which it produces from its phenol recovery project.<br />

Construction of a facility to extract krypton/xenon from the synfuel plant's oxygen plant was completed in March 1991. DGC<br />

signed a 15-year agreement in 1989 with Praxair (formerly Linde Division of Union Carbide Industrial Gases Inc.) to sell all of the<br />

plant's production of the krypton/xenon mixture. The first shipment of the product occurred on March 15, 1991. In March 1993,<br />

DGC installed a hydrotreater which enabled it to commence the sale of the plant's naphtha production. Other byproducts being<br />

sold from the plant include anhydrous ammonia, sulfur and liquid nitrogen. Argon, carbon dioxide, ammonium sulfate and cresote<br />

are also potential byproducts.<br />

In late 1990 DGC filed with the North Dakota State Health Department a revision to the applications to amend the Air Pollution<br />

Control Permit to Construct. The revised application defines the best available control technology to lower SO and other emis<br />

sions at the plant. In 1993, the North Dakota Department of Health approved the permit for the flue gas desulfurization system at<br />

the Great Plains Synfuels Plant. In March 1994, DGC announced it would install a flue gas scrubber which will use anhydrous am<br />

monia as the reagent, a process that will produce ammonium sulfate, a commercial fertilizer, which DGC intends to market.<br />

DGC has 4 years to complete construction of the main stack scrubber. The estimated cost of this environmental improvement is<br />

$100 million.<br />

4-59<br />

SYNTHETIC FUELS REPORT, JANUARY 1995

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