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ISER was requested to conduct an economic analysis of a possible 'Cook Inlet Syngas Pipeline'. The economic analysis was incorporated as section 7.4 of the larger report titled: 'Beluga Coal Gasification Feasibility Study, DOE/NETL-2006/1248, Phase 2 Final Report, October 2006, for Subtask 41817.333.01.01'. The pipeline would carry CO{sub 2} and N{sub 2}-H{sub 2} from a synthetic gas plant on the western side of Cook Inlet to Agrium's facility. The economic analysis determined that the net present value of the total capital and operating lifecycle costs for the pipeline ranges from $318 to $588 million. The greatest contributor to this spread is the cost of electricity, which ranges from $0.05 to $0.10/kWh in this analysis. The financial analysis shows that the delivery cost of gas may range from $0.33 to $0.55/Mcf in the first year depending primarily on the price for electricity. | ISER was requested to conduct an economic analysis of a possible 'Cook Inlet Syngas Pipeline'. The economic analysis was incorporated as section 7.4 of the larger report titled: 'Beluga Coal Gasification Feasibility Study, DOE/NETL-2006/1248, Phase 2 Final Report, October 2006, for Subtask 41817.333.01.01'. The pipeline would carry CO{sub 2} and N{sub 2}-H{sub 2} from a synthetic gas plant on the western side of Cook Inlet to Agrium's facility. The economic analysis determined that the net present value of the total capital and operating lifecycle costs for the pipeline ranges from $318 to $588 million. The greatest contributor to this spread is the cost of electricity, which ranges from $0.05 to $0.10/kWh in this analysis. The financial analysis shows that the delivery cost of gas may range from $0.33 to $0.55/Mcf in the first year depending primarily on the price for electricity. | ||
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* [https://digital.library.unt.edu/ark:/67531/metadc934929/m2/1/high_res_d/963355.pdf https://digital.library.unt.edu/ark:/67531/metadc934929/m2/1/high_res_d/963355.pdf] | * [https://digital.library.unt.edu/ark:/67531/metadc934929/m2/1/high_res_d/963355.pdf https://digital.library.unt.edu/ark:/67531/metadc934929/m2/1/high_res_d/963355.pdf] | ||
| − | * [https://core.ac.uk/display/71335736 https://core.ac.uk/display/71335736],[ | + | * [https://core.ac.uk/display/71335736 https://core.ac.uk/display/71335736], |
| + | : [https://www.osti.gov/servlets/purl/963355 https://www.osti.gov/servlets/purl/963355], | ||
| + | : [https://academic.microsoft.com/#/detail/54057989 https://academic.microsoft.com/#/detail/54057989] | ||
Latest revision as of 12:55, 22 January 2021
Abstract
ISER was requested to conduct an economic analysis of a possible 'Cook Inlet Syngas Pipeline'. The economic analysis was incorporated as section 7.4 of the larger report titled: 'Beluga Coal Gasification Feasibility Study, DOE/NETL-2006/1248, Phase 2 Final Report, October 2006, for Subtask 41817.333.01.01'. The pipeline would carry CO{sub 2} and N{sub 2}-H{sub 2} from a synthetic gas plant on the western side of Cook Inlet to Agrium's facility. The economic analysis determined that the net present value of the total capital and operating lifecycle costs for the pipeline ranges from $318 to $588 million. The greatest contributor to this spread is the cost of electricity, which ranges from $0.05 to $0.10/kWh in this analysis. The financial analysis shows that the delivery cost of gas may range from $0.33 to $0.55/Mcf in the first year depending primarily on the price for electricity.
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Published on 01/01/2008
Volume 2008, 2008
DOI: 10.2172/963355
Licence: CC BY-NC-SA license
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