Techno-Economic Assessment of a Combined Heat and Power Plant Integrated with Carbon Dioxide Removal Technology: A Case Study for Central Poland

The objective of this study is to assess the techno-economic potential of the proposed novel energy system, which allows for negative emissions of carbon dioxide (CO<sub>2</sub>). The analyzed system comprises four main subsystems: a biomass-fired combined heat and power plant integrated...

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Bibliographic Details
Main Authors: Paweł Gładysz, Anna Sowiżdżał, Maciej Miecznik, Maciej Hacaga, Leszek Pająk
Format: Article
Language:English
Published: MDPI AG 2020-06-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/13/11/2841
Description
Summary:The objective of this study is to assess the techno-economic potential of the proposed novel energy system, which allows for negative emissions of carbon dioxide (CO<sub>2</sub>). The analyzed system comprises four main subsystems: a biomass-fired combined heat and power plant integrated with a CO<sub>2</sub> capture and compression unit, a CO<sub>2</sub> transport pipeline, a CO<sub>2</sub>-enhanced geothermal system, and a supercritical CO<sub>2</sub> Brayton power cycle. For the purpose of the comprehensive techno-economic assessment, the results for the reference biomass-fired combined heat and power plant without CO<sub>2</sub> capture are also presented. Based on the proposed framework for energy and economic assessment, the energy efficiencies, the specific primary energy consumption of CO<sub>2</sub> avoidance, the cost of CO<sub>2</sub> avoidance, and negative CO<sub>2</sub> emissions are evaluated based on the results of process simulations. In addition, an overview of the relevant elements of the whole system is provided, taking into account technological progress and technology readiness levels. The specific primary energy consumption per unit of CO<sub>2</sub> avoided in the analyzed system is equal to 2.17 MJ<sub>LHV</sub>/kg CO<sub>2</sub> for biomass only (and 6.22 MJ<sub>LHV</sub>/kg CO<sub>2</sub> when geothermal energy is included) and 3.41 MJ<sub>LHV</sub>/kg CO<sub>2</sub> excluding the CO<sub>2</sub> utilization in the enhanced geothermal system. Regarding the economic performance of the analyzed system, the levelized cost of electricity and heat are almost two times higher than those of the reference system (239.0 to 127.5 EUR/MWh and 9.4 to 5.0 EUR/GJ), which leads to negative values of the Net Present Value in all analyzed scenarios. The CO<sub>2</sub> avoided cost and CO<sub>2</sub> negative cost in the business as usual economic scenario are equal to 63.0 and 48.2 EUR/t CO<sub>2</sub>, respectively, and drop to 27.3 and 20 EUR/t CO<sub>2</sub> in the technological development scenario. The analysis proves the economic feasibility of the proposed CO<sub>2</sub> utilization and storage option in the enhanced geothermal system integrated with the sCO<sub>2</sub> cycle when the cost of CO<sub>2</sub> transport and storage is above 10 EUR/t CO<sub>2</sub> (at a transport distance of 50 km). The technology readiness level of the proposed technology was assessed as TRL4 (technological development), mainly due to the early stage of the CO<sub>2</sub>-enhanced geothermal systems development.
ISSN:1996-1073