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Gas conditioning—The interface between CO2 capture and transport
Institution:1. Norwegian University of Science and Technology, NTNU, NO-7465 Trondheim, Norway;2. SINTEF Energy Research, NO-7465 Trondheim, Norway;1. The University of Tokyo, 5-1-5 Kashiwanoha, Kashiwa-shi, Chiba 277-8561, Japan;2. Central Research Institute of Electric Power Industry, 1646 Abiko, Abiko-shi, Chiba 270-1194, Japan;3. Chiyoda Corporation, 4-6-2 Minatomirai, Nishi-ku, Yokohama 220-8765, Japan;1. Progressive Energy Ltd, Stonehouse, United Kingdom;2. TNO, Utrecht, The Netherlands;3. SINTEF Energy Research, Trondheim, Norway;4. Centro Sviluppo di Materiali, Roma, Italy;5. GFZ German Research Centre for Geosciences, Potsdam, Germany;6. DNV GL, Oslo, Norway;7. CIUDEN, Ponferrada, Spain;1. Offshore CCS Research Unit, MOERI, Korea Institute of Ocean Science and Technology, Daejeon 305-343, Republic of Korea;2. Division of Ocean Systems Engineering, Korea Advanced Institute of Science and Technology, Daejeon 305-701, Republic of Korea;1. Chiyoda Corporation, 4-6-2, Minatomirai, nishi-ku, Yokohama 220-8765, Japan;2. Sasebo Heavy Industries Co., Ltd., 31-1, Nihonbashihamacho 2-chome, Chuo-ku, Tokyo 103-0007, Japan;3. The University of Tokyo, 5-1-5 Kashiwanoha, Kashiwa-shi, Chiba 277-8561, Japan;1. University of North Dakota, Grand Forks, ND, USA;2. Universidad Nacional de Colombia—Sede Medellín, Medellín, Colombia
Abstract:Gas conditioning is commonly referred to as the required processing for a produced natural gas to achieve transport and sales specifications. In this paper, gas conditioning as the processing required in the interface between CO2 capture and transport is studied for nine different natural gas fired power plant concepts and three different CO2 transport processes. Conditioning processes for both pipeline and ship transport are described and an enhanced process for volatile removal is developed. The energy requirement for the conditioning processes is normally between 90 and 120 kWh/tonne CO2; however, this depends on the pressure and composition of the captured CO2-rich stream. The loss of CO2 in the water purge is small for most capture processes. The waste streams from the gas conditioning processes can contain large amounts of CO2 and should therefore be further processed or reintroduced at an appropriate point upstream in the capture or gas conditioning process if possible. The integration benefit may vary depending on the composition of the CO2-rich stream. It could be particularly interesting for processes with “innovative reactors” (membranes, sorbents, chemical looping) to integrate CO2 capture and gas conditioning.
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