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Yagmur Goren A, Erdemir D, Dincer I. Comprehensive review and assessment of carbon capturing methods and technologies: An environmental research. ENVIRONMENTAL RESEARCH 2024; 240:117503. [PMID: 37907166 DOI: 10.1016/j.envres.2023.117503] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/21/2023] [Revised: 10/05/2023] [Accepted: 10/23/2023] [Indexed: 11/02/2023]
Abstract
A majority of the primary contributors of carbon dioxide (CO2) emissions into the environment have really been out of human-made activities. The levels of CO2 in the atmosphere have increased substantially since the time of the industrial revolution. This has been linked to the use of fossil fuels for energy production, as well as the widespread production of some industrial components like cement and the encroaching destruction of forests. An extreme approach is now necessary to develop the right policies and address the local and global environmental issues in the right way. In this regard, CO2 capturing, utilization, and storage are reliable options that industrial facilities can initiate to overcome this problem. Therefore, we have evaluated the two leading technologies that are used for carbon capture: direct (pre-combustion, post-combustion, and oxy-combustion) and indirect carbon (reforestation, enhanced weathering, bioenergy with carbon capture, and agricultural practices) capturing to provide their current status and progresses. Among the considered processes, the post-combustion techniques are widely utilized on a commercial scale, especially in industrial applications. Technology readiness level (TRL) results have showed that amine solvents, pressure-vacuum swing adsorption, and gas separation membranes have the highest TRL value of 9. In addition, the environmental impact assessment methods have been ranked to evaluate their sustainability levels. The highest global warming potential of 219.53 kgCO2 eq./MWh has been obtained for the post-combustion process. Overall, through this comprehensive review, we have identified some critical research gaps in the open literature in the field of CO2-capturing methods where there are strong needs for future research and technology development studies, for instance, developing stable and cost-effective liquid solvents and improving the adsorption capacity of commercialized sorbents. Furthermore, some research areas, like novel process design, environmental and economic impact assessment of capturing methods with different chemicals and modeling and simulation studies, will require further effort to demonstrate the developed technologies for pilot and commercial-scale applications.
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Affiliation(s)
- Aysegul Yagmur Goren
- Ontario Tech University, Clean Energy Research Laboratory, Oshawa, Ontario, Canada; Izmir Institute of Technology, Department of Environmental Engineering, Urla, Izmir, Turkey.
| | - Dogan Erdemir
- Ontario Tech University, Clean Energy Research Laboratory, Oshawa, Ontario, Canada; Yildiz Technical University, Department of Mechanical Engineering, Istanbul, Turkey
| | - Ibrahim Dincer
- Ontario Tech University, Clean Energy Research Laboratory, Oshawa, Ontario, Canada; Yildiz Technical University, Department of Mechanical Engineering, Istanbul, Turkey
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2
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Grimm A, Gazzani M. A Machine Learning-Aided Equilibrium Model of VTSA Processes for Sorbents Screening Applied to CO 2 Capture from Diluted Sources. Ind Eng Chem Res 2022; 61:14004-14019. [PMID: 36164596 PMCID: PMC9501812 DOI: 10.1021/acs.iecr.2c01695] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 05/13/2022] [Revised: 08/01/2022] [Accepted: 08/19/2022] [Indexed: 12/03/2022]
Abstract
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The large design space of the sorbents’ structure
and the
associated capability of tailoring properties to match process requirements
make adsorption-based technologies suitable candidates for improved
CO2 capture processes. This is particularly of interest
in novel, diluted, and ultradiluted separations as direct CO2 removal from the atmosphere. Here, we present an equilibrium model
of vacuum temperature swing adsorption cycles that is suitable for
large throughput sorbent screening, e.g., for direct air capture applications.
The accuracy and prediction capabilities of the equilibrium model
are improved by incorporating feed-forward neural networks, which
are trained with data from rate-based models. This allows one, for
example, to include the process productivity, a key performance indicator
typically obtained in rate-based models. We show that the equilibrium
model reproduces well the results of a sophisticated rate-based model
in terms of both temperature and composition profiles for a fixed
cycle as well as in terms of process optimization and sorbent comparison.
Moreover, we apply the proposed equilibrium model to screen and identify
promising sorbents from the large NIST/ARPA-E database; we do this
for three different (ultra)diluted separation processes: direct air
capture, yCO2 = 0.1%, and yCO2 = 1.0%. In all cases, the tool
allows for a quick identification of the most promising sorbents and
the computation of the associated performance indicators. Also, in
this case, outcomes are very well in line with the 1D model results.
The equilibrium model is available in the GitHub repository https://github.com/UU-ER/SorbentsScreening0D.
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Affiliation(s)
- Alexa Grimm
- Utrecht University, Copernicus Institute of Sustainable Development, Princetonlaan 8a, 3584 CBUtrecht, The Netherlands
| | - Matteo Gazzani
- Utrecht University, Copernicus Institute of Sustainable Development, Princetonlaan 8a, 3584 CBUtrecht, The Netherlands
- Sustainable Process Engineering, Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612 APEindhoven, The Netherlands
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3
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DeWitt SJA, Lively RP. MIL-101(Cr) Polymeric Fiber Adsorbents for Sub-Ambient Post-Combustion CO 2 Capture. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c01837] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
| | - Ryan P. Lively
- Georgia Institute of Technology, Atlanta, Georgia 30308, United States
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4
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Streb A, Mazzotti M. Performance limits of neural networks for optimizing an adsorption process for hydrogen purification and CO2 capture. Comput Chem Eng 2022. [DOI: 10.1016/j.compchemeng.2022.107974] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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Wiegner JF, Grimm A, Weimann L, Gazzani M. Optimal Design and Operation of Solid Sorbent Direct Air Capture Processes at Varying Ambient Conditions. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c00681] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Jan F. Wiegner
- Utrecht University, Princetonlaan 8a, 3584 CB Utrecht, The Netherlands
| | - Alexa Grimm
- Utrecht University, Princetonlaan 8a, 3584 CB Utrecht, The Netherlands
| | - Lukas Weimann
- Utrecht University, Princetonlaan 8a, 3584 CB Utrecht, The Netherlands
| | - Matteo Gazzani
- Utrecht University, Princetonlaan 8a, 3584 CB Utrecht, The Netherlands
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Zhang Z, Zheng Y, Qian L, Luo D, Dou H, Wen G, Yu A, Chen Z. Emerging Trends in Sustainable CO 2 -Management Materials. ADVANCED MATERIALS (DEERFIELD BEACH, FLA.) 2022; 34:e2201547. [PMID: 35307897 DOI: 10.1002/adma.202201547] [Citation(s) in RCA: 17] [Impact Index Per Article: 8.5] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/16/2022] [Revised: 03/07/2022] [Indexed: 06/14/2023]
Abstract
With the rising level of atmospheric CO2 worsening climate change, a promising global movement toward carbon neutrality is forming. Sustainable CO2 management based on carbon capture and utilization (CCU) has garnered considerable interest due to its critical role in resolving emission-control and energy-supply challenges. Here, a comprehensive review is presented that summarizes the state-of-the-art progress in developing promising materials for sustainable CO2 management in terms of not only capture, catalytic conversion (thermochemistry, electrochemistry, photochemistry, and possible combinations), and direct utilization, but also emerging integrated capture and in situ conversion as well as artificial-intelligence-driven smart material study. In particular, insights that span multiple scopes of material research are offered, ranging from mechanistic comprehension of reactions, rational design and precise manipulation of key materials (e.g., carbon nanomaterials, metal-organic frameworks, covalent organic frameworks, zeolites, ionic liquids), to industrial implementation. This review concludes with a summary and new perspectives, especially from multiple aspects of society, which summarizes major difficulties and future potential for implementing advanced materials and technologies in sustainable CO2 management. This work may serve as a guideline and road map for developing CCU material systems, benefiting both scientists and engineers working in this growing and potentially game-changing area.
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Affiliation(s)
- Zhen Zhang
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Yun Zheng
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Lanting Qian
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Dan Luo
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Haozhen Dou
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Guobin Wen
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Aiping Yu
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
| | - Zhongwei Chen
- Department of Chemical Engineering, Waterloo Institute for Nanotechnology, University of Waterloo, Waterloo, Ontario, N2L 3G1, Canada
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Peh SB, Farooq S, Zhao D. A metal-organic framework (MOF)-based temperature swing adsorption cycle for postcombustion CO2 capture from wet flue gas. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2021.117399] [Citation(s) in RCA: 8] [Impact Index Per Article: 4.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/22/2023]
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Abstract
The transport sector powered by internal combustion engines (ICE) requires novel approaches to achieve near-zero CO2 emissions. In this direction, using CO2 capture and storage (CCS) systems onboard could be a good option. However, CO2 capture in mobile sources is currently challenging due to the operational and space requirements to install a CCS system onboard. This paper presents a systematic review of the CO2 capture in ICE driven transport to know the methods, techniques, and results of the different studies published so far. Subsequently, a case study of a CCS system working in an ICE is presented, where the energy and space needs are evaluated. The review reveals that the most suitable technique for CO2 capture is temperature swing adsorption (TSA). Moreover, the sorbents with better properties for this task are PPN-6-CH2-DETA and MOF-74-Mg. Finally, it shows that it is necessary to supply the energy demand of the CCS system and the option is to take advantage of the waste heat in the flue gas. The case study shows that it is possible to have a carbon capture rate above 68% without affecting engine performance. It was also found that the total volume required by the CCS system and fuel tank is 3.75 times smaller than buses operating with hydrogen fuel cells. According to the review and the case study, it is possible to run a CCS system in the maritime sector and road freight transport.
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Adsorption for efficient low carbon hydrogen production: part 2—Cyclic experiments and model predictions. ADSORPTION 2021. [DOI: 10.1007/s10450-021-00308-w] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
Abstract
Abstract
Hydrogen as clean energy carrier is expected to play a key role in future low-carbon energy systems. In this paper, we demonstrate a new technology for coupling fossil-fuel based hydrogen production with carbon capture and storage (CCS): the integration of CO2 capture and H2 purification in a single vacuum pressure swing adsorption (VPSA) cycle. An eight step VPSA cycle is tested in a two-column lab-pilot for a ternary CO2–H2–CH4 stream representative of shifted steam methane reformer (SMR) syngas, while using commercial zeolite 13X as adsorbent. The cycle can co-purify CO2 and H2, thus reaching H2 purities up to 99.96%, CO2 purities up to 98.9%, CO2 recoveries up to 94.3% and H2 recoveries up to 81%. The key decision variables for adjusting the separation performance to reach the required targets are the heavy purge (HP) duration, the feed duration, the evacuation pressure and the flow rate of the light purge (LP). In contrast to that, the separation performance is rather insensitive towards small changes in feed composition and in HP inlet composition. Comparing the experimental results with simulation results shows that the model for describing multi-component adsorption is critical in determining the predictive capabilities of the column model. Here, the real adsorbed solution theory (RAST) is necessary to describe all experiments well, whereas neither extended isotherms nor the ideal adsorbed solution theory (IAST) can reproduce all effects observed experimentally.
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Streb A, Mazzotti M. Adsorption for efficient low carbon hydrogen production: part 1—adsorption equilibrium and breakthrough studies for H2/CO2/CH4 on zeolite 13X. ADSORPTION 2021. [DOI: 10.1007/s10450-021-00306-y] [Citation(s) in RCA: 9] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Abstract
Abstract
Reforming of fossil fuels coupled with carbon capture and storage has the potential to produce low-carbon H2 at large scale and low cost. Adsorption is a potentially promising technology for two key separation tasks in this process: H2 purification and CO2 capture. In this work, we present equilibrium adsorption data of H2 and CH4 on zeolite 13X, in addition to the already established CO2 isotherms. Further, we carry out binary (CO2–CH4) and ternary (H2–CO2–CH4) breakthrough experiments at various pressures and temperatures to estimate transport parameters, assess the predictive capacity of our 1D column model, and compare different multi-component adsorption models. CO2 adsorbs strongly on zeolite 13X, CH4 adsorbs less, and H2 adsorbs very little. Thus, H2 breaks through first, CH4 second (first in the binary breakthrough experiments) and CO2 last. Linear driving force (LDF) mass transfer coefficients are estimated based on a single breakthrough experiment and mass transfer is found to be fast for H2, slower for CH4, and slowest for CO2. The LDF parameters can be used in a predictive manner for breakthrough experiments at varying pressures, temperatures, flows, and, though with lower accuracy, even compositions. Heat transfer inside the column is described well with a literature correlation, thus yielding an excellent agreement between simulated and measured column temperatures. Ideal and real adsorbed solution theories (IAST and RAST, respectively) both model the observed breakthrough composition profiles well, whereas extended isotherms are inferior for predicting the competitive behavior between CH4 and CO2 adsorption. This study provides the groundwork necessary for full cyclic experiments and their simulation.
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11
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Sakanaka Y, Hiraide S, Tanaka H, Hiratsuka T, Kojima N, Yamane Y, Miyahara MT. Efficiency of Thermal Management Using Phase-Change Material for Nonisothermal Adsorption Process. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.0c02344] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Yuta Sakanaka
- Department of Chemical Engineering, Kyoto University, Nishikyo, Kyoto 615-8510, Japan
| | - Shotaro Hiraide
- Department of Chemical Engineering, Kyoto University, Nishikyo, Kyoto 615-8510, Japan
| | - Hideki Tanaka
- Research Initiative for Supra-Materials (RISM), Shinshu University, 4-17-1 Wakasato, Nagano 380-8553, Japan
| | - Tatsumasa Hiratsuka
- Department of Chemical Engineering, Kyoto University, Nishikyo, Kyoto 615-8510, Japan
| | - Natsuko Kojima
- Innovation & Development Department, Activated Carbon Business Division, Osaka Gas Chemicals Co., Ltd., 5-11-61, Torishima, Konohana-ku, Osaka 554-0051, Japan
| | - Yasuyuki Yamane
- Innovation & Development Department, Activated Carbon Business Division, Osaka Gas Chemicals Co., Ltd., 5-11-61, Torishima, Konohana-ku, Osaka 554-0051, Japan
| | - Minoru T. Miyahara
- Department of Chemical Engineering, Kyoto University, Nishikyo, Kyoto 615-8510, Japan
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Ajenifuja A, Joss L, Jobson M. A New Equilibrium Shortcut Temperature Swing Adsorption Model for Fast Adsorbent Screening. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.9b05579] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Abdulmalik Ajenifuja
- Centre for Process Integration, Department of Chemical Engineering and Analytical Science, The University of Manchester, M13 9PL Manchester, U.K
| | - Lisa Joss
- Centre for Process Integration, Department of Chemical Engineering and Analytical Science, The University of Manchester, M13 9PL Manchester, U.K
| | - Megan Jobson
- Centre for Process Integration, Department of Chemical Engineering and Analytical Science, The University of Manchester, M13 9PL Manchester, U.K
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Jiang N, Shen Y, Liu B, Zhang D, Tang Z, Li G, Fu B. CO2 capture from dry flue gas by means of VPSA, TSA and TVSA. J CO2 UTIL 2020. [DOI: 10.1016/j.jcou.2019.09.012] [Citation(s) in RCA: 29] [Impact Index Per Article: 7.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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14
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Optimized heat exchanger integration within a TSA-process based on experimentally evaluated heat transfer correlations for finned-tubes in fluidized-beds. POWDER TECHNOL 2019. [DOI: 10.1016/j.powtec.2019.09.030] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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15
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Streb A, Hefti M, Gazzani M, Mazzotti M. Novel Adsorption Process for Co-Production of Hydrogen and CO2 from a Multicomponent Stream. Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.9b02817] [Citation(s) in RCA: 22] [Impact Index Per Article: 4.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Anne Streb
- ETH Zurich, Institute of Process Engineering, Zurich 8092, Switzerland
| | - Max Hefti
- ETH Zurich, Institute of Process Engineering, Zurich 8092, Switzerland
| | - Matteo Gazzani
- Utrecht University, Copernicus Institute of Sustainable Development, 3512 JE Utrecht, The Netherlands
| | - Marco Mazzotti
- ETH Zurich, Institute of Process Engineering, Zurich 8092, Switzerland
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Experimental and Numerical Investigations on Heat Transfer of Bare Tubes in a Bubbling Fluidized Bed with Respect to Better Heat Integration in Temperature Swing Adsorption Systems. ENERGIES 2019. [DOI: 10.3390/en12142646] [Citation(s) in RCA: 8] [Impact Index Per Article: 1.6] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
Abstract
In this paper experimental and numerical investigations on heat transfer within a bubbling fluidized bed will be presented with respect to better heat integration in continuous temperature swing adsorption (TSA) processes for biogas upgrading. In the literature, mainly heat transfer measurements with glass or sand particles are carried out, thus special reference measurements with adsorbent material in a fluidized bed are missing. Therefore firstly, a series of experiments were carried out in the fluidized bed test facility to obtain heat transfer coefficients between tube surface and bed which were then compared to calculated heat transfer coefficients to determine whether suitable models were available. Horizontal bare tubes with different arrangements (i.e., single tubes and especially tube bundles) are immersed in fluidized amine layered particles with a mean diameter of 650 μ m which are used in the adsorption industry as adsorbent. The test facility enables a cross-current flow of the solids and gas phase as it prevails in a multi-stage fluidized bed reactor for TSA-applications. The heat transfer measurements with different arrangements and adsorbent material show very similar values in the range of 200 W/m 2 K. The mathematical model for single tubes multiplied by a tube diameter factor shows approximate agreement with the experimental results. However, the mathematical models for tube bundles were not able to predict the measured heat transfer coefficients with the required accuracy. Secondly, a computer fluid dynamics (CFD) program was used to perform a numerical investigation of the test facility using the Euler–Euler method in order to describe the required two-phase characteristic of a fluidized bed. The results of the numerical simulation were compared and validated with the experimental results. Bubbling fluidized bed flow regimes could be reproduced well but the heat transfer coefficients between tube and bed were clearly underestimated. However, a numerical study for a bubbling fluidized bed with external circulation, as used in novel continuous TSA systems, could be carried out and thus a tool for better heat integration measures was developed.
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Hefti M, Mazzotti M. Postcombustion CO2 Capture from Wet Flue Gas by Temperature Swing Adsorption. Ind Eng Chem Res 2018. [DOI: 10.1021/acs.iecr.8b03580] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Max Hefti
- Institute of Process Engineering, ETH Zurich, Sonneggstrasse 3, CH-8092 Zurich, Switzerland
| | - Marco Mazzotti
- Institute of Process Engineering, ETH Zurich, Sonneggstrasse 3, CH-8092 Zurich, Switzerland
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Hefti M, Joss L, Bjelobrk Z, Mazzotti M. On the potential of phase-change adsorbents for CO 2 capture by temperature swing adsorption. Faraday Discuss 2018; 192:153-179. [PMID: 27509258 DOI: 10.1039/c6fd00040a] [Citation(s) in RCA: 40] [Impact Index Per Article: 6.7] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
We investigate the potential of a class of recently discovered metal-organic-framework materials for their use in temperature swing adsorption (TSA) processes for CO2 capture; the particularity of the considered materials is their reversible and temperature dependent step-shaped CO2 adsorption isotherm. Specifically, we present a comprehensive modeling study, where the performance of five different materials with step-shaped isotherms [McDonald et al., Nature, 2015, 519, 303] in a four step TSA cycle is assessed. The specific energy requirement of the TSA process operated with these materials is lower than for a commercial 13X zeolite, and a smaller temperature swing is required to reach similar levels of CO2 purity and recovery. The effect of a step in the adsorption isotherm is illustrated and discussed, and design criteria that lead to an optimal and robust operation of the considered TSA cycle are identified. The presented criteria could guide material scientists in designing novel materials whose step position is tailored to specific CO2 separation tasks.
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Affiliation(s)
- Max Hefti
- ETH Zurich, Institute of Process Engineering, Sonneggstrasse 3, CH-8092 Zurich, Switzerland.
| | - Lisa Joss
- ETH Zurich, Institute of Process Engineering, Sonneggstrasse 3, CH-8092 Zurich, Switzerland.
| | - Zoran Bjelobrk
- ETH Zurich, Institute of Process Engineering, Sonneggstrasse 3, CH-8092 Zurich, Switzerland.
| | - Marco Mazzotti
- ETH Zurich, Institute of Process Engineering, Sonneggstrasse 3, CH-8092 Zurich, Switzerland.
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Capra F, Gazzani M, Joss L, Mazzotti M, Martelli E. MO-MCS, a Derivative-Free Algorithm for the Multiobjective Optimization of Adsorption Processes. Ind Eng Chem Res 2018. [DOI: 10.1021/acs.iecr.8b00207] [Citation(s) in RCA: 17] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Federico Capra
- Politecnico di Milano, Department of Energy, Via Lambruschini 4, 20156 Milano, Italy
| | - Matteo Gazzani
- Utrecht University, Copernicus Institute of Sustainable Development, Heidelberglaan 3584CS Utrecht, The Netherlands
| | - Lisa Joss
- Department of Chemical Engineering, Imperial College London, SW7 2AZ, London, United Kingdom
| | - Marco Mazzotti
- ETH Zurich, Institute of Process Engineering, Sonneggstrasse 3, 8092, Zurich, Switzerland
| | - Emanuele Martelli
- Politecnico di Milano, Department of Energy, Via Lambruschini 4, 20156 Milano, Italy
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20
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New hybrid composite honeycomb monolith with 13X zeolite and activated carbon for CO2 capture. ADSORPTION 2018. [DOI: 10.1007/s10450-018-9938-1] [Citation(s) in RCA: 29] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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21
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Grande CA, Blom R, Andreassen KA, Stensrød RE. Experimental Results of Pressure Swing Adsorption (PSA) for Pre-combustion CO2 Capture with Metal Organic Frameworks. ACTA ACUST UNITED AC 2017. [DOI: 10.1016/j.egypro.2017.03.1364] [Citation(s) in RCA: 11] [Impact Index Per Article: 1.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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22
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Joss L, Hefti M, Bjelobrk Z, Mazzotti M. On the Potential of Phase-change Adsorbents for CO2 Capture by Temperature Swing Adsorption. ACTA ACUST UNITED AC 2017. [DOI: 10.1016/j.egypro.2017.03.1375] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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23
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Salazar Duarte G, Schürer B, Voss C, Bathen D. Adsorptive Separation of CO2
from Flue Gas by Temperature Swing Adsorption Processes. CHEMBIOENG REVIEWS 2017. [DOI: 10.1002/cben.201600029] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Gabriel Salazar Duarte
- Linde AG/Engineering Division; Dr.-Carl-von-Linde-Strasse 6-14 82049 Pullach Germany
- Universität Duisburg-Essen; Chair for Thermal Process Engineering; Lotharstrasse 1 47057 Duisburg Germany
| | - Benedikt Schürer
- Linde AG/Engineering Division; Dr.-Carl-von-Linde-Strasse 6-14 82049 Pullach Germany
| | - Christian Voss
- Linde AG/Engineering Division; Dr.-Carl-von-Linde-Strasse 6-14 82049 Pullach Germany
| | - Dieter Bathen
- Universität Duisburg-Essen; Chair for Thermal Process Engineering; Lotharstrasse 1 47057 Duisburg Germany
- Institut für Energie-und Umwelttechnik IUTA e.V.; Bliersheimer Strasse 60 47229 Duisburg Germany
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Billemont P, Heymans N, Normand P, De Weireld G. IAST predictions vs co-adsorption measurements for CO2 capture and separation on MIL-100 (Fe). ADSORPTION 2016. [DOI: 10.1007/s10450-016-9825-6] [Citation(s) in RCA: 22] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/20/2022]
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