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Stampi-Bombelli V, Storione A, Grossmann Q, Mazzotti M. On Comparing Packed Beds and Monoliths for CO 2 Capture from Air Through Experiments, Theory, and Modeling. Ind Eng Chem Res 2024; 63:11637-11653. [PMID: 38983186 PMCID: PMC11228921 DOI: 10.1021/acs.iecr.4c01392] [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: 04/11/2024] [Revised: 05/30/2024] [Accepted: 05/30/2024] [Indexed: 07/11/2024]
Abstract
This study compares the performance of amine-functionalized γ-alumina sorbents in the form of 3 mm γ-alumina pellets and of a γ-alumina wash-coated monolith for CO2 capture for direct air capture (DAC). Breakthrough experiments were conducted on the two contactors to analyze the adsorption kinetics and performance for different gas feeds. A constant pattern analysis revealed dominant mass transfer resistances in the gas film and in the pores, with axial dispersion also observed, particularly at higher concentrations. A 1D, physical model was used to fit the experiments and thus to estimate mass transfer and axial dispersion coefficients, which appear to be consistent with the hypotheses derived from constant pattern analysis. A dual kinetic model to describe mass transfer was found to better describe the tail behavior in the monolith, whereas a pseudo-first-order model was sufficient to describe breakthroughs on packed beds. A substantial two-order magnitude decrease in mass transfer coefficients was noted when reducing the feed concentration from 5.6% to 400 ppm CO2, thus underscoring the significant mass transfer limitations observed in DAC. Comparison between the contactors revealed notably higher mass transfer coefficients in the monolith compared to the packed beds, which are attributed to shorter diffusion lengths and lower equilibrium capacity. While the faster mass transfer coefficients observed in the monolith experiments led to reduced specific energy consumption and increased adsorption productivity compared to the packed bed at 400 ppm, no significant improvement was observed for the same process at the higher concentration of 5.6% CO2 in the feed. This finding highlights the need to tailor the contactor design to the specific gas separation requirements. This research contributes to the understanding and quantification of mass transfer kinetics at DAC concentrations in both packed bed and monolith contactors. It demonstrates the crucial role of the contactor in DAC systems and the importance of optimizing the adsorption step to enhance productivity and DAC performance.
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Affiliation(s)
| | - Alba Storione
- Department of Civil, Chemical, Environmental and Materials Engineering (DICAM), Alma Mater Studiorum-University of Bologna, via Terracini 28, Bologna 40131, Italy
| | - Quirin Grossmann
- Institute of Energy and Process Engineering, ETH Zurich, Zurich 8092, Switzerland
| | - Marco Mazzotti
- Institute of Energy and Process Engineering, ETH Zurich, Zurich 8092, Switzerland
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2
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Robinson DB, Salloum M. Comparison of Designs of Hydrogen Isotope Separation Columns by Numerical Modeling. Ind Eng Chem Res 2023. [DOI: 10.1021/acs.iecr.2c03209] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/22/2023]
Affiliation(s)
- David B. Robinson
- Sandia National Laboratories, P.O. Box 969 MS 9161, Livermore, California 94551, United States
| | - Maher Salloum
- Sandia National Laboratories, P.O. Box 969 MS 9161, Livermore, California 94551, United States
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3
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Queiroz V, de Almeida DS, de Oliveira Miglioranza GH, Steffani E, Barbosa-Coutinho E, Schwaab M. Analysis of commonly used batch adsorption kinetic models derived from mass transfer-based modelling. ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH INTERNATIONAL 2022; 29:79875-79889. [PMID: 35015231 DOI: 10.1007/s11356-021-18479-y] [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: 08/14/2021] [Accepted: 12/29/2021] [Indexed: 06/14/2023]
Abstract
Modelling of liquid-solid batch adsorption based on mass transfer and conservation equations results in differential equations that may have or not an analytical solution. Even when analytical solutions are available, several simplified models can be considered for evaluating kinetic data of batch adsorption experiments. However, these simplified models are commonly used regardless of the premises considered in its development, and the analysis of the kinetic experiments based on these simplified models may be severely compromised. For this reason, this work presents a detailed development of the phenomenological models, and the hypotheses considered in its development are clearly stated. Typical simplified models derived from the phenomenological ones are obtained, and the conditions considered in the simplification are critically assessed. It was observed that the simplified models fail mainly for considering the concentration of the bulk phase constant over time or considering a linear adsorption isotherm. It must be emphasised that even when phenomenological models must be solved through numerical procedures, its use must be preferred, since the agreement with model premises and experimental conditions are closer, ensuring the quality of the kinetic data analysis.
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Affiliation(s)
- Vânia Queiroz
- Departamento de Engenharia Química, Escola de Engenharia, Universidade Federal Do Rio Grande Do Sul, Rua Ramiro Barcelos, 2777 - Prédio 22202, Porto Alegre, RS, 90035-007, Brazil
| | - Daniel Souza de Almeida
- Departamento de Engenharia Química, Escola de Engenharia, Universidade Federal Do Rio Grande Do Sul, Rua Ramiro Barcelos, 2777 - Prédio 22202, Porto Alegre, RS, 90035-007, Brazil
| | - Gabriel Henrique de Oliveira Miglioranza
- Departamento de Engenharia Química, Escola de Engenharia, Universidade Federal Do Rio Grande Do Sul, Rua Ramiro Barcelos, 2777 - Prédio 22202, Porto Alegre, RS, 90035-007, Brazil
| | - Evandro Steffani
- Departamento de Engenharia Química, Escola de Engenharia, Universidade Federal Do Rio Grande Do Sul, Rua Ramiro Barcelos, 2777 - Prédio 22202, Porto Alegre, RS, 90035-007, Brazil
| | - Elisa Barbosa-Coutinho
- Departamento de Físico-Química, Instituto de Química, Universidade Federal Do Rio Grande Do Sul, Av. Bento Gonçalves, Porto Alegre, RS, 950091501-970, Brazil
| | - Marcio Schwaab
- Departamento de Engenharia Química, Escola de Engenharia, Universidade Federal Do Rio Grande Do Sul, Rua Ramiro Barcelos, 2777 - Prédio 22202, Porto Alegre, RS, 90035-007, Brazil.
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4
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Recent advances on the modeling and optimization of CO2 capture processes. Comput Chem Eng 2022. [DOI: 10.1016/j.compchemeng.2022.107938] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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5
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Krishnamurthy S. Vacuum swing adsorption process for post-combustion carbon capture with 3D printed sorbents: Quantifying the improvement in productivity and specific energy over a packed bed system through process simulation and optimization. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.117585] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/03/2022]
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6
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Mennitto R, Sharma I, Brandani S. Extruded Monoliths for Gas Separation Processes: Height Equivalent to a Theoretical Plate and Pressure Drop Correlations. AIChE J 2022. [DOI: 10.1002/aic.17650] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
| | - Ishan Sharma
- School of Engineering University of Edinburgh Edinburgh UK
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7
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Hedlund J, Garcia G, Balsamo M, Zhou M, Mouzon J. Microchannel zeolite 13X adsorbent with high CO2 separation performance. Sep Purif Technol 2021. [DOI: 10.1016/j.seppur.2021.119483] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/13/2022]
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8
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9
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Peeters R, Verbruggen V, Rongé J, Martens JA. Non-Isothermal Kinetic Model of Water Vapor Adsorption on a Desiccant Bed for Harvesting Water from Atmospheric Air. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.1c01733] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Robin Peeters
- Centre for Surface Chemistry and Catalysis, KU Leuven, Celestijnenlaan 200f—bus 2461, 3001 Leuven, Belgium
| | - Vincent Verbruggen
- Centre for Surface Chemistry and Catalysis, KU Leuven, Celestijnenlaan 200f—bus 2461, 3001 Leuven, Belgium
| | - Jan Rongé
- Centre for Surface Chemistry and Catalysis, KU Leuven, Celestijnenlaan 200f—bus 2461, 3001 Leuven, Belgium
| | - Johan A. Martens
- Centre for Surface Chemistry and Catalysis, KU Leuven, Celestijnenlaan 200f—bus 2461, 3001 Leuven, Belgium
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10
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Georgiadis A, Charisiou ND, Gaber S, Polychronopoulou K, Yentekakis IV, Goula MA. Adsorption of Hydrogen Sulfide at Low Temperatures Using an Industrial Molecular Sieve: An Experimental and Theoretical Study. ACS OMEGA 2021; 6:14774-14787. [PMID: 34151059 PMCID: PMC8209825 DOI: 10.1021/acsomega.0c06157] [Citation(s) in RCA: 9] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 12/17/2020] [Accepted: 03/03/2021] [Indexed: 06/13/2023]
Abstract
In the work presented herein, a joint experimental and theoretical approach has been carried out to obtain an insight into the desulfurization performance of an industrial molecular sieve (IMS), resembling a zeolitic structure with a morphology of cubic crystallites and a high surface area of 590 m2 g-1, with a view to removing H2S from biogas. The impact of temperature, H2S inlet concentration, gas matrix, and regeneration cycles on the desulfurization performance of the IMS was thoroughly probed. The adsorption equilibrium, sorption kinetics, and thermodynamics were also examined. Experimental results showed that the relationship between H2S uptake and temperature increase was inversely proportional. Higher H2S initial concentrations led to lower breakpoints. The presence of CO2 negatively affected the desulfurization performance. The IMS was fully regenerated after 15 adsorption/desorption cycles. Theoretical studies revealed that the Langmuir isotherm better described the sorption behavior, pore diffusion was the controlling step of the process (Bangham model), and that the activation energy was 42.7 kJ mol-1 (physisorption). Finally, the thermodynamic studies confirmed that physisorption predominated.
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Affiliation(s)
- Amvrosios
G. Georgiadis
- Laboratory
of Alternative Fuels and Environmental Catalysis (LAFEC), Department
of Chemical Engineering, University of Western
Macedonia, GR-50100 Koila, Greece
| | - Nikolaos D. Charisiou
- Laboratory
of Alternative Fuels and Environmental Catalysis (LAFEC), Department
of Chemical Engineering, University of Western
Macedonia, GR-50100 Koila, Greece
| | - Safa Gaber
- Department
of Mechanical Engineering, Khalifa University
of Science and Technology, Abu Dhabi, P.O. Box 127788, UAE
| | - Kyriaki Polychronopoulou
- Department
of Mechanical Engineering, Khalifa University
of Science and Technology, Abu Dhabi, P.O. Box 127788, UAE
- Center
for Catalysis and Separations, Khalifa University
of Science and Technology, Abu Dhabi, P.O. Box 127788, UAE
| | - Ioannis V. Yentekakis
- Laboratory
of Physical Chemistry & Chemical Processes, School of Environmental Engineering, Technical University of Crete, GR-73100 Chania, Greece
| | - Maria A. Goula
- Laboratory
of Alternative Fuels and Environmental Catalysis (LAFEC), Department
of Chemical Engineering, University of Western
Macedonia, GR-50100 Koila, Greece
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11
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Abstract
The emission of untreated environmental harmful gases such as sulfur and nitrogen oxide (SOx and NOx) emissions is considered old fashioned, since industries are compelled by governments and legislations to meet the minimum threshold before emitting such substances into the atmosphere. Numerous research has been done and is ongoing to come up with both cost-effective equipment and regenerable catalysts that are adsorbent—or with enhanced sorption capacity—and with safer disposal methods. This work presents the general idea of a monolith/catalyst for environmental application and the technicality for improving the surface area for fast and efficient adsorption–desorption reactions. The chemical reactions, adsorption kinetics, and other properties, including deactivation, regeneration, and the disposal of a catalyst in view of environmental application, are extensively discussed.
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12
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DeWitt SJA, Sinha A, Kalyanaraman J, Zhang F, Realff MJ, Lively RP. Critical Comparison of Structured Contactors for Adsorption-Based Gas Separations. Annu Rev Chem Biomol Eng 2018; 9:129-152. [PMID: 29579401 DOI: 10.1146/annurev-chembioeng-060817-084120] [Citation(s) in RCA: 35] [Impact Index Per Article: 5.8] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Abstract
Recent advances in adsorptive gas separations have focused on the development of porous materials with high operating capacity and selectivity, useful parameters that provide early guidance during the development of new materials. Although this material-focused work is necessary to advance the state of the art in adsorption science and engineering, a substantial problem remains: how to integrate these materials into a fixed bed to efficiently utilize the separation. Structured sorbent contactors can help manage kinetic and engineering factors associated with the separation, including pressure drop, sorption enthalpy effects, and external heat integration (for temperature swing adsorption, or TSA). In this review, we discuss monoliths and fiber sorbents as the two main classes of structured sorbent contactors; recent developments in their manufacture; advantages and disadvantages of each structure relative to each other and to pellet packed beds; recent developments in system modeling; and finally, critical needs in this area of research.
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Affiliation(s)
- Stephen J A DeWitt
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
| | - Anshuman Sinha
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
| | - Jayashree Kalyanaraman
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
| | - Fengyi Zhang
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
| | - Matthew J Realff
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
| | - Ryan P Lively
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, USA; , , , , ,
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13
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Ma Q, Chen Z, Liu H. Multiple-relaxation-time lattice Boltzmann simulation for flow, mass transfer, and adsorption in porous media. Phys Rev E 2018; 96:013313. [PMID: 29347115 DOI: 10.1103/physreve.96.013313] [Citation(s) in RCA: 14] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/11/2016] [Indexed: 11/07/2022]
Abstract
In this paper, to predict the dynamics behaviors of flow and mass transfer with adsorption phenomena in porous media at the representative elementary volume (REV) scale, a multiple-relaxation-time (MRT) lattice Boltzmann (LB) model for the convection-diffusion equation is developed to solve the transfer problem with an unsteady source term in porous media. Utilizing the Chapman-Enskog analysis, the modified MRT-LB model can recover the macroscopic governing equations at the REV scale. The coupled MRT-LB model for momentum and mass transfer is validated by comparing with the finite-difference method and the analytical solution. Moreover, using the MRT-LB method coupled with the linear driving force model, the fluid transfer and adsorption behaviors of the carbon dioxide in a porous fixed bed are explored. The breakthrough curve of adsorption from MRT-LB simulation is compared with the experimental data and the finite-element solution, and the transient concentration distributions of the carbon dioxide along the porous fixed bed are elaborated upon in detail. In addition, the MRT-LB simulation results show that the appearance time of the breakthrough point in the breakthrough curve is advanced as the mass transfer resistance in the linear driving force model increases; however, the saturation point is prolonged inversely.
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Affiliation(s)
- Qiang Ma
- Institute for Energy Research, Jiangsu University, 301 Xuefu Road, Zhenjiang 212013, People's Republic of China.,Faculty of Engineering, University of Nottingham, University Park, Nottingham NG72RD, United Kingdom.,Jiangsu Provincial Key Laboratory of Solar Energy Science and Technology, School of Energy and Environment, Nanjing 210096, People's Republic of China
| | - Zhenqian Chen
- Jiangsu Provincial Key Laboratory of Solar Energy Science and Technology, School of Energy and Environment, Nanjing 210096, People's Republic of China
| | - Hao Liu
- Faculty of Engineering, University of Nottingham, University Park, Nottingham NG72RD, United Kingdom
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14
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15
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Sinha A, Darunte LA, Jones CW, Realff MJ, Kawajiri Y. Systems Design and Economic Analysis of Direct Air Capture of CO2 through Temperature Vacuum Swing Adsorption Using MIL-101(Cr)-PEI-800 and mmen-Mg2(dobpdc) MOF Adsorbents. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.6b03887] [Citation(s) in RCA: 87] [Impact Index Per Article: 12.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/22/2022]
Affiliation(s)
- Anshuman Sinha
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Drive, Atlanta, Georgia 30332, United States
| | - Lalit A. Darunte
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Drive, Atlanta, Georgia 30332, United States
| | - Christopher W. Jones
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Drive, Atlanta, Georgia 30332, United States
| | - Matthew J. Realff
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Drive, Atlanta, Georgia 30332, United States
| | - Yoshiaki Kawajiri
- School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Drive, Atlanta, Georgia 30332, United States
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16
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Adsorption of phenol in flow systems by a monolithic carbon cryogel with a microhoneycomb structure. ADSORPTION 2016. [DOI: 10.1007/s10450-016-9799-4] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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17
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Slavik I, Uhl W, Börnick H, Worch E. Assessment of SOC adsorption prediction in activated carbon filtration based on Freundlich coefficients calculated from compound properties. RSC Adv 2016. [DOI: 10.1039/c5ra21005d] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022] Open
Abstract
Three models using compound properties to calculate Freundlich constants for adsorption of SOCs on activated carbon were evaluated using data obtained from the literature and in our own experiments.
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Affiliation(s)
- I. Slavik
- Wahnbachtalsperrenverband
- 53721 Siegburg
- Germany
- Technische Universität Dresden
- Chair of Water Supply Engineering
| | - W. Uhl
- Norwegian Institute for Water Research (NIVA)
- 0349 Oslo
- Norway
- Technische Universität Dresden
- Chair of Water Supply Engineering
| | - H. Börnick
- Technische Universität Dresden
- Institute of Water Chemistry
- 01062 Dresden
- Germany
| | - E. Worch
- Technische Universität Dresden
- Institute of Water Chemistry
- 01062 Dresden
- Germany
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18
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Jungreuthmayer C, Steppert P, Sekot G, Zankel A, Reingruber H, Zanghellini J, Jungbauer A. The 3D pore structure and fluid dynamics simulation of macroporous monoliths: High permeability due to alternating channel width. J Chromatogr A 2015; 1425:141-9. [DOI: 10.1016/j.chroma.2015.11.026] [Citation(s) in RCA: 28] [Impact Index Per Article: 3.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/29/2015] [Accepted: 11/07/2015] [Indexed: 10/22/2022]
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19
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Rodriguez-Illera M, Janssen AE, Boom RM. Channeled monoliths for selective recovery of a lacto-tripeptide from a crude hydrolyzate. Sep Purif Technol 2015. [DOI: 10.1016/j.seppur.2015.10.014] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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20
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Rodriguez-Illera M, Boon MA, Boom RM, Janssen AE. Comparison of structured adsorbents for the adsorptive isolation of food ingredients from large streams. Chem Eng Res Des 2015. [DOI: 10.1016/j.cherd.2015.04.020] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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21
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Ribeiro RPPL, Grande CA, Rodrigues AE. Electric Swing Adsorption for Gas Separation and Purification: A Review. SEP SCI TECHNOL 2014. [DOI: 10.1080/01496395.2014.915854] [Citation(s) in RCA: 40] [Impact Index Per Article: 4.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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22
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Shafeeyan MS, Wan Daud WMA, Shamiri A. A review of mathematical modeling of fixed-bed columns for carbon dioxide adsorption. Chem Eng Res Des 2014. [DOI: 10.1016/j.cherd.2013.08.018] [Citation(s) in RCA: 161] [Impact Index Per Article: 16.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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23
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Chauveau R, Grévillot G, Marsteau S, Vallières C. Values of the mass transfer coefficient of the linear driving force model for VOC adsorption on activated carbons. Chem Eng Res Des 2013. [DOI: 10.1016/j.cherd.2012.09.019] [Citation(s) in RCA: 31] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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24
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25
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Applications of high-order approximate models for unsteady-state diffusion and reaction in a catalyst. KOREAN J CHEM ENG 2013. [DOI: 10.1007/s11814-012-0188-8] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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26
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Lee J, Kim DH. Global approximations of unsteady-state adsorption, diffusion, and reaction in a porous catalyst. AIChE J 2013. [DOI: 10.1002/aic.14014] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
Affiliation(s)
- Jietae Lee
- Dept. of Chemical Engineering; Kyungpook National University; Taegu; 702-701; Korea
| | - Dong Hyun Kim
- Dept. of Chemical Engineering; Kyungpook National University; Taegu; 702-701; Korea
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27
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Wang G, Dou B, Wang J, Wang W, Hao Z. Adsorption properties of benzene and water vapor on hyper-cross-linked polymers. RSC Adv 2013. [DOI: 10.1039/c3ra41450g] [Citation(s) in RCA: 27] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022] Open
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28
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Kim DH, Lee J. High-order approximations for unsteady-state diffusion and reaction in slab, cylinder and sphere catalyst. KOREAN J CHEM ENG 2011. [DOI: 10.1007/s11814-011-0120-7] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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29
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Guan C, Yang C, Wang K. Adsorption kinetics of methane on a template-synthesized carbon powder and its pellet. ASIA-PAC J CHEM ENG 2011. [DOI: 10.1002/apj.428] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
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30
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Águeda VI, Crittenden BD, Delgado JA, Tennison SR. Effect of channel geometry, degree of activation, relative humidity and temperature on the performance of binderless activated carbon monoliths in the removal of dichloromethane from air. Sep Purif Technol 2011. [DOI: 10.1016/j.seppur.2011.01.036] [Citation(s) in RCA: 20] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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31
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32
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Crittenden BD, Camus O, Perera SP, Mays TJ, Sánchez-Liarte F, Tennison SR, Crezee E. Nonuniform channels in adsorbent monoliths. AIChE J 2010. [DOI: 10.1002/aic.12335] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
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33
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Bhandari DA, Bessho N, Koros WJ. Hollow Fiber Sorbents for Desulfurization of Natural Gas. Ind Eng Chem Res 2010. [DOI: 10.1021/ie100157w] [Citation(s) in RCA: 35] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Dhaval A. Bhandari
- School of Chemical and Biomolecular Engineering, Georgia Institute of Technology, 778 Atlantic Drive, Atlanta, Georgia 30332-0100
| | - Naoki Bessho
- School of Chemical and Biomolecular Engineering, Georgia Institute of Technology, 778 Atlantic Drive, Atlanta, Georgia 30332-0100
| | - William J. Koros
- School of Chemical and Biomolecular Engineering, Georgia Institute of Technology, 778 Atlantic Drive, Atlanta, Georgia 30332-0100
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34
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35
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Li G, Singh R, Li D, Zhao C, Liu L, Webley PA. Synthesis of biomorphic zeolite honeycomb monoliths with 16 000 cells per square inch. ACTA ACUST UNITED AC 2009. [DOI: 10.1039/b912329f] [Citation(s) in RCA: 21] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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36
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Mosca A, Hedlund J, Ridha FN, Webley P. Optimization of synthesis procedures for structured PSA adsorbents. ADSORPTION 2008. [DOI: 10.1007/s10450-008-9126-9] [Citation(s) in RCA: 27] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/27/2022]
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Jungbauer A, Hahn R. Polymethacrylate monoliths for preparative and industrial separation of biomolecular assemblies. J Chromatogr A 2008; 1184:62-79. [DOI: 10.1016/j.chroma.2007.12.087] [Citation(s) in RCA: 182] [Impact Index Per Article: 11.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 08/16/2007] [Revised: 12/04/2007] [Accepted: 12/19/2007] [Indexed: 11/28/2022]
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