scholarly journals Energy-Efficient CO2 Capture from Flue Gas by Absorption with Amino Acids and Crystallization with a Bis-Iminoguanidine

2019 ◽  
Author(s):  
Radu Custelcean ◽  
Kathleen A. Garrabrant ◽  
Neil Williams ◽  
Erick Holguin ◽  
Flavien M. Brethomé ◽  
...  

A hybrid solvent/solid-state approach to carbon capture is demonstrated based on absorption with glycine or sarcosine, followed by crystallization of a guanidinium bicarbonate salt.

2019 ◽  
Author(s):  
Radu Custelcean ◽  
Kathleen A. Garrabrant ◽  
Neil Williams ◽  
Erick Holguin ◽  
Flavien M. Brethomé ◽  
...  

A hybrid solvent/solid-state approach to carbon capture is demonstrated based on absorption with glycine or sarcosine, followed by crystallization of a guanidinium bicarbonate salt.


2019 ◽  
Vol 58 (24) ◽  
pp. 10510-10515 ◽  
Author(s):  
Kathleen A. Garrabrant ◽  
Neil J. Williams ◽  
Erick Holguin ◽  
Flavien M. Brethomé ◽  
Costas Tsouris ◽  
...  

2020 ◽  
Vol 10 (21) ◽  
pp. 7669
Author(s):  
Yunje Lee ◽  
Junghwan Kim ◽  
Huiyong Kim ◽  
Taesung Park ◽  
Hailian Jin ◽  
...  

A new blending recipe of a polyamine-based solvent for capturing post-combustion CO2 was proposed, and its performance and characteristics were investigated using a pilot-scale carbon capture process (PCCP). The proposed solvent is a blend of three types of amines and was designed to separate the solvent roles into those of a main amine, auxiliary amine, and reaction-rate-enhancing amine. Polyamine 3,3′-iminobis (N, N-dimethylpropylamine) was selected as the main amine given its ability to capture large amounts of CO2. 2-Amino-2-methyl-1-propanol was used as the auxiliary amine, with piperazine added as the reaction-rate-enhancing amine. This solvent was tested in a PCCP that can handle 150 Nm3/h of flue gas. The proposed solvent was found to operate stably while consuming substantially lower reboiler duty than the monoethanolamine (MEA) 30 mass% solvent.


2018 ◽  
Vol 140 (6) ◽  
Author(s):  
Chiranjib Saha ◽  
Justin H. Anthony

The aerosols from CO2-depleted flue gas at the National Carbon Capture Center (NCCC) Pilot Solvent Test Unit (PSTU) and Slipstream Solvent Test Unit (SSTU) were measured in real-time using a Dekati Electric Low Pressure Impactor (ELPI+™). The coal-fired flue gas is provided by Alabama Power's Gaston Power Plant Unit 5. The utilization of ELPI+™ for aerosol research in postcombustion CO2 capture is very important due to its quick response time with size classification as low as 6 nm under transient conditions observed at the NCCC. Different process changes have been quantified at the PSTU and SSTU by multiple tests using the ELPI+™. The performance of smooth and sintered collection plates during dynamic process changes has been investigated. Between separate tests, upstream at unit 5, a new baghouse was installed. The aerosols measured at SSTU, before and after the baghouse installation, are compared. PSTU measurements demonstrated sample sensitivity to transient intercooler start-up conditions and dilution gas temperatures. During the tests, the typical concentration ranged from 106 to 107 cm−3. The aerosol's counter median diameter (CMD) for the sintered plates are lower (47–60 nm) compared to the normal plates (89–130 nm). The optical images indicate that sintered plates soak up all of the collected aerosols. The aerosol number concentration showed a significant drop after the baghouse installation. These results are promising and will enable the development of process control strategies to mitigate solvent losses and reduce operation and maintenance expenses.


2020 ◽  
Vol 8 ◽  
Author(s):  
Xiaoxing Wang ◽  
Chunshan Song

Climate change has become a worldwide concern with the rapid rise of the atmospheric Co2 concentration. To mitigate Co2 emissions, the research and development efforts in Co2 capture and separation both from the stationary sources with high Co2 concentrations (e.g., coal-fired power plant flue gas) and directly from the atmosphere have grown significantly. Much progress has been achieved, especially within the last twenty years. In this perspective, we first briefly review the current status of carbon capture technologies including absorption, adsorption, membrane, biological capture, and cryogenic separation, and compare their advantages and disadvantages. Then, we focus mainly on the recent advances in the absorption, adsorption, and membrane technologies. Even though numerous optimizations in materials and processes have been pursued, implementing a single separation process is still quite energy-intensive or costly. To address the challenges, we provide our perspectives on future directions of Co2 capture research and development, that is, the combination of flue gas recycling and hybrid capture system, and one-step integrated Co2 capture and conversion system, as they have the potential to overcome the technical bottlenecks of single capture technologies, offering significant improvement in energy efficiency and cost-effectiveness.


Author(s):  
Ram G. Narula ◽  
Harvey Wen

Coal is an abundant, widespread, cheap energy source and contributes to 39% of the world’s electric power generation. Coal releases large amounts of carbon dioxide (CO2), which is believed to play a major role in global warming and climate change. To de-carbonize power generation, three distinct carbon capture technologies are in varying stages of development. These include pre-combustion carbon capture through the use of integrated coal gasification combined cycle (IGCC), post-combustion carbon capture from a pulverized-coal (PC)-fired power plant flue gas using monoethanolamine (MEA) or ammonia (NH3), and oxy-combustion technology. In the latter technology, oxygen is first separated from nitrogen in an air separator unit and used for combustion of coal in a conventional PC boiler. With oxy-combustion technology, the resulting flue gas is predominantly CO2, which makes CO2 capture easier than in the PC-MEA case. This paper discusses the development status as well as the advantages, limitations, performance and economics of each technology in regard to the capture and non-capture cases.


2013 ◽  
Vol 37 ◽  
pp. 1785-1792 ◽  
Author(s):  
Koji Kadono ◽  
Asao Suzuki ◽  
Masaki Iijima ◽  
Tsuyoshi Ohishi ◽  
Hiroshi Tanaka ◽  
...  

2021 ◽  
Author(s):  
Amélie Cécile Martin ◽  
François Lacouture ◽  
Philip Llewellyn ◽  
Laurent Mariac

Abstract To curtail the global warming increase to less than 2°C by 2050, the IPCC highlights Carbon Capture Utilization and Storage (CCUS) as a vital approach. TotalEnergies, following its ambition to become a responsible energy major, invests 10% of its R&D budget in CCUS to reduce the global process cost and help decarbonize our activities. TotalEnergies is both working to decarbonize its own assets and developing a transport and storage infrastructure in Europe, with notably Northern Lights an example of note. It is equally of interest how this transport/storage infrastructure can be of use for other sectors and as such how various full CCUS chains may emerge. This explains the interest to develop techno-economic tools to evaluate CO2 capture processes applied to a wide range of industries. CO2 that is an integral part of the manufacturing process, is particularly difficult to abate in any future scenario, and one particular industry, which is facing such a challenge is the cement sector. CCUS has been identified as a potential solution to help with this issue. The present paper outlines the outcomes of a techno-economic study evaluating CO2 capture technologies based on cement factory retrofitting. A literature review aimed at identifying the main characteristics of a typical European cement plant (capacity, process mode, pollutant composition in the flue gas…) was carried out. In this paper, a base case scenario of 90% absorption-based CO2 capture with monoethanolamine (MEA) is compared with four alternative CO2 capture approaches: –An absorption technology based on non-amine solvent.–An adsorption technology based on a Concentration Swing Adsorption process.–An oxyfuel technology derived from the R&D works performed during the CEMCAP project (European CO2 capture project).–A Calcium Looping technology with tail-end process configuration. For each of these approaches, the whole carbon capture chain has been considered: this includes flue gas pretreatment, CO2 conditioning (including compression), steam generation, and utilities. Using process simulations, engineering studies have been carried out and have provided Key Performance Indicators (KPIs) such as Capital Costs, Operation Costs and Global Warming Potential (primary energy consumption per ton of CO2 avoided). It enabled mapping the technologies with regards to the cost and volume of CO2 avoided, as well as providing for each of the technologies the break-even point for an eventual CO2 tax. Based on these KPIs, several facts have been highlighted: –The need to consider the whole process (including utilities, compression…) and not only the capture unit.–The development of new materials for adsorption and contactor design is already driving down costs.–The availability of waste heat can be a game-changer to implement a CO2 capture technology.–Technology comparisons are location and site-specific and cannot be taken as a basis for concept selection. TotalEnergies approach to CCUS is collaborative. With these full-scale techno-economical assessments, generated via quotations from industrial equipment providers and using Engineering, Procurement and Construction standards, this not only gives a basis for comparison, but also assists our discussions with partners to identify key technological development pathways.


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