Japan Geoscience Union Meeting 2021

Presentation information

[J] Oral

H (Human Geosciences ) » H-SC Social Earth Sciences & Civil/Urban System Sciences

[H-SC05] CCUS (Carbon Dioxide Capture, Utilization, and Storage) for Climate Mitigation

Fri. Jun 4, 2021 1:45 PM - 3:15 PM Ch.15 (Zoom Room 15)

convener:Masao Sorai(Institute for Geo-Resources and Environment, National Institute of Advanced Industrial Science and Technology), Ziqiu Xue(Research Institute of Innovative Tech for the Earth), Masaatsu Aichi(Graduate School of Frontier Sciences, University of Tokyo), Yoshihiro Konno(The University of Tokyo), Chairperson:Yoshihiro Konno(The University of Tokyo)

2:45 PM - 3:00 PM

[HSC05-17] Cost analysis of CO2 transportation in CCS deployed in Japan

*Hirotaka Isogai1, Corey Adam Myers2, Takao Nakagaki2, Takeshi Myoi3, Junichi Shimizu3 (1.Department of Modern Mechanical Engineering, Waseda University , 2.Faculty of Waseda University, 3.Geological Carbon Dioxide Storage Technology Research Association / Research Institute of Innovative Technology for the Earth)


Keywords:pipeline, ship transportation, CO2 avoided cost, hub and cluster

Carbon dioxide capture and storage (CCS) is regarded as an integral technology to meet net CO2 neutrality in Japan and abroad. The technology can be divided into three major activities: capture of CO2 from emission sources, transportation of CO2 to a storage site, and injection of CO2 into an appropriate underground geological formation. In Japan, the transportation of CO2 captured at a power plant in Kyoto to the existing storage site in Hokkaido is planned to be demonstrated within a few years. One of the barriers to a rapid deployment of CCS is recognized as the high costs. Discussion of cost has historically focused on CO2 capture, primarily because CO2 transport by onshore pipeline is a mature and relatively cheap activity. In Japan and coastal Europe area where onshore pipelines are far less deployed than US, a mixture of geology, geography, regulations, and public opinion make CO2 transport by ship a promising method as shown in hub and cluster system. The available data on cost of transport by ship is difficult to merge with existing data on CO2 capture and injection because of imprecise definitions of the boundaries of each activity. In this study, the cost of CO2 transport is calculated as part of a complete CCS chain to eliminate issues of boundary selection. Transport by ship and pipeline are evaluated in the context of Japan to provide a clear comparison. The cost of transport is reported per unit of avoided CO2.

For both the pipeline and ship-based transport methods, it is assumed that the emission source is either a GW-class supercritical pulverized coal-fired power plant (SCPC) or a natural gas combined cycle power plant (NGCC). In both cases, an amine-based CO2 capture system is retrofitted to existing power plant. For pipeline transport, captured CO2 is compressed to the supercritical state and is transported via onshore pipeline with intermediate boosters. The injection site is assumed to be operated from onshore though actual injection occurs at sea, similar to JCCS’ Tomakomai CCS demonstration facility. The pipeline cost estimate is broadly based on the “FE/NETL CO2 Transport Cost Model” by NETL with various location factors modified to account for differences between the US and Japan. The results of the cost estimation are corroborated by comparison with multiple existing CO2 pipeline projects. In all cases, pipeline transport costs are OPEX-dominated so long as the operation period is long to some extent (typically >20 years). Countries and localities with experience with pipelines show markedly lower costs due to the shorter permitting period, calling into question the applicability of pipeline transport in Japan. For transport by ship, the liquefaction of CO2 at around triple point, intermediate storage at port, loading to the ship, transport by ship, unloading, and conditioning prior to injection are considered. It is assumed that CO2 injection occurs at sea. The cost of ships and at-sea injection facilities are based on previously reported engineering analyses. The several conditioning steps applied to CO2, especially conditioning chilled and liquefied CO2, incurs a large electricity burden which means that the cost and CO2 intensity of electricity are important factors in determining the cost per unit of avoided CO2. At short transport distances, the cost for maintenance and repair of facilities also account for a large portion of the total cost. At longer transport distances, fuel costs become an increasingly large portion of total cost and the balance between ship speed and the number of ships gain importance. The results in this study are corroborated by comparison with cost estimates from literatures. Regardless of transport type, it was found that the SCPC case has a higher sensitivity of CO2 transportation cost on the CO2 avoided cost compared with NGCC case due to the difference in the amount of CO2 captured and emission.