Breckinridge Project, initial effort. Report VIII. Capital cost estimate
Abstract
The major objective of the Initial Effort for the Breckinridge Project is to develop engineering to the point where realistic economics for the construction and operation of the plant can be made. The plant is designed to process 23,000 tons per day of run-of-mine coal to produce a nominal 50,000 barrels per day of liquid products using the H-COAL and standard industry technology. The plant will be located in Breckinridge County, Kentucky. Considerable preliminary engineering has been performed for this estimate. This work uses a single-point design based on the Process Demonstration Unit (PDU) data from run 5, period 29 of the pilot plant. The design basis is discussed in Volume II of this report. Many aspects of plant construction and cost have been considered that were not taken into account in the past studies. Ashland and Bechtel believe the accuracy of the capital estimate to be +19%, -17%. This accuracy is postulated on January 1981 dollars, the as-spent dollar amount naturally depending upon the inflation rate through the construction period. Considerable attention has been devoted to reliability of operation, and redundant equipment has been used where it was deemed necessary to assure reasonable onstream time. This equipment is includedmore »
- Publication Date:
- Research Org.:
- Ashland Synthetic Fuels, Inc., KY (USA); Airco Energy Co., Inc., Ashland, KY (USA)
- Sponsoring Org.:
- USDOE
- OSTI Identifier:
- 6837736
- Report Number(s):
- DOE/OR/20717-8
ON: DE83000173
- DOE Contract Number:
- FC05-80OR20717
- Resource Type:
- Technical Report
- Resource Relation:
- Other Information: Portions of document are illegible
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 01 COAL, LIGNITE, AND PEAT; COAL LIQUEFACTION; CAPITAL; DESIGN; H-COAL PROCESS; DEMONSTRATION PLANTS; ENGINEERING; NUMERICAL DATA; DATA; INFORMATION; LIQUEFACTION; THERMOCHEMICAL PROCESSES; 010405* - Coal, Lignite, & Peat- Hydrogenation & Liquefaction
Citation Formats
. Breckinridge Project, initial effort. Report VIII. Capital cost estimate. United States: N. p., 1982.
Web. doi:10.2172/6837736.
. Breckinridge Project, initial effort. Report VIII. Capital cost estimate. United States. https://doi.org/10.2172/6837736
. 1982.
"Breckinridge Project, initial effort. Report VIII. Capital cost estimate". United States. https://doi.org/10.2172/6837736. https://www.osti.gov/servlets/purl/6837736.
@article{osti_6837736,
title = {Breckinridge Project, initial effort. Report VIII. Capital cost estimate},
author = {},
abstractNote = {The major objective of the Initial Effort for the Breckinridge Project is to develop engineering to the point where realistic economics for the construction and operation of the plant can be made. The plant is designed to process 23,000 tons per day of run-of-mine coal to produce a nominal 50,000 barrels per day of liquid products using the H-COAL and standard industry technology. The plant will be located in Breckinridge County, Kentucky. Considerable preliminary engineering has been performed for this estimate. This work uses a single-point design based on the Process Demonstration Unit (PDU) data from run 5, period 29 of the pilot plant. The design basis is discussed in Volume II of this report. Many aspects of plant construction and cost have been considered that were not taken into account in the past studies. Ashland and Bechtel believe the accuracy of the capital estimate to be +19%, -17%. This accuracy is postulated on January 1981 dollars, the as-spent dollar amount naturally depending upon the inflation rate through the construction period. Considerable attention has been devoted to reliability of operation, and redundant equipment has been used where it was deemed necessary to assure reasonable onstream time. This equipment is included in the capital estimate. The capital is summarized by total plant cost on Table 1. The subtotal plant cost, excluding contingency, fee, and adjustment is $2,710,940,000. Adding the contingency, fee and adjustment, the total depreciable cost of the plant is $3,167,430,000. Adding the working capital to the total plant cost results in total capital requirements of $3,258,430,000 as shown on the individual plant cost summary Table 2.},
doi = {10.2172/6837736},
url = {https://www.osti.gov/biblio/6837736},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Fri Jan 01 00:00:00 EST 1982},
month = {Fri Jan 01 00:00:00 EST 1982}
}