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Defining CCS Ready: An Approach to An International Definition

Defining CCS Ready: An Approach to An International Definition

Defining CCS Ready: An Approach to An International Definition

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Appendix C: Policy Considerations and Assessments of <strong>CCS</strong> <strong>Ready</strong> Economicsreduced for capture <strong>Ready</strong> plants because site selection expenditures have been made at thetime the plant was designed (and reflected in higher initial power plant capital costs) andbecause the time needed <strong>to</strong> find and develop the a suitable s<strong>to</strong>rage sites is reduced. In otherwords, the <strong>to</strong>tal dollar amount of the finding and developing the s<strong>to</strong>rage site is the same –only the timing of those costs is different. In contrast, there are significant savings expectedfor the transport costs.Exhibit C-4: Retrofit <strong>to</strong> Current <strong>CCS</strong> Technology Capitaland Operating Cost Assumptions (all cases)After Regular (Current Technology) <strong>CCS</strong> is Added<strong>CCS</strong> <strong>Ready</strong> OptionIncrementalCapital Costs($/Original MW)Fixed O&MCosts($/MW/yr)Variable O&MCosts ($/MWhr)Heat Rate(Btu/kWhr) aCO2 Transport& S<strong>to</strong>rage Cost($/metric <strong>to</strong>n)CO2Emissions(kg/MWhr)CapacityLostNot <strong>CCS</strong> <strong>Ready</strong> $ 1,088,200 $ 62,161 $ 4.18 12,637 $ 12.67 117 31%1: Throttle Valve Case $ 1,057,313 $ 60,840 $ 4.02 12,146 $ 10.96 112 28%2: Clutch Case $ 1,067,751 $ 59,922 $ 3.91 11,828 $ 9.24 109 26%3: Oversized Boiler Case $ 831,431 $ 53,582 $ 3.79 11,556 $ 9.24 107 13%aCoal burned for baseload.Exhibit C-5: S<strong>to</strong>rage and Pipeline Cost Assumptions(Incurred After Retrofit Decision)Best (Capture <strong>Ready</strong>) Middle (Capture <strong>Ready</strong>) Worse (BAU Plant)Miles of Pipelines NecessaryMiles of 12 inch Pipeline 25 50 75Miles of 16 inch Pipeline 25 50 75Miles of 36 inch Pipeline 100 50 0Total Miles 150 150 150Transport (Pipeline) and S<strong>to</strong>rage CostsPipeline Cost $/metric <strong>to</strong>n $ 4.74 $ 6.21 $ 7.67S<strong>to</strong>rage Cost $/metric <strong>to</strong>n $ 4.50 $ 4.75 $ 5.00Total Pipeline and S<strong>to</strong>rageCost $/metric <strong>to</strong>n $ 9.24 $ 10.96 $ 12.67The Monte Carlo analysis may include a representation of an advanced <strong>CCS</strong> Technology interms of when it might be available and its cost and performance characteristics. Theimportance of an advanced <strong>CCS</strong> technology is that it can make retrofitting <strong>to</strong> <strong>CCS</strong> moreeconomic (thus making <strong>CCS</strong> <strong>Ready</strong> investment more valuable) and it might change thespace, equipment and energy requirements for <strong>CCS</strong>, (possibly making some of the <strong>CCS</strong><strong>Ready</strong> investments unnecessary).Exhibit C-6 shows the incremental capital costs (per unit of original plant capacity) ofretrofitting the power plants <strong>to</strong> the assumed advanced capture technology. The advancecapture technology is assumed <strong>to</strong> be more energy efficient than current amine technologiesand <strong>to</strong> have somewhat lower capital costs. Capture efficiency is 90 percent in both cases.Because the advanced technology capture process requires less energy for solventregeneration, the net electricity generating capacity lost is substantially lower for the firstthree options in which steam needs <strong>to</strong> be diverted for solvent regeneration. The <strong>CCS</strong> <strong>Ready</strong>3 option (which assumes that the plant is built with an over-sized boiler <strong>to</strong> supply steam <strong>to</strong> afuture amine capture process) has nearly the same capacity loss with the current and the23 February 2010 112

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