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Budhi YW, Irawan HK, Fitri RA, Al Syifa Elgi Wibisono T, Restiawaty E, Miyamoto M, Uemiya S. Effect of Co-existing gases on hydrogen permeation through a Pd82-Ag18/α-Al 2O 3 membrane during transient start-up. Heliyon 2023; 9:e16979. [PMID: 37484284 PMCID: PMC10361031 DOI: 10.1016/j.heliyon.2023.e16979] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 04/22/2023] [Revised: 05/09/2023] [Accepted: 06/02/2023] [Indexed: 07/25/2023] Open
Abstract
The work aimed to study the influence of co-existing gaseous mixture (H2-N2-CO-CO2) on hydrogen permeation through the counter-current flow of a Pd82-Ag18/α-Al2O3 membrane during transient start-up at 350 °C and atmospheric pressure. The membrane was operated for an 8-h. Its performance was measured in terms of hydrogen flux and recovery. The results were mapped on Sieverts-Fick's line and showed a slight membrane deactivation because of the presence of N2 and CO2 in the feed gas. The membrane deactivation became more profound when CO was a constituent. The effect of the co-existing gases on the hydrogen flux, in increasing order, was CO > CO2>N2. The co-existing gases, if present as a significant fraction, induces dilution, concentration polarization, and inhibition over the membrane surface, decreases the membrane performance in term of hydrogen recovery, time lag during transient start-up, and deactivation. It is recommended that the start-up might be run using equimolar H2-N2 mixture.
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Affiliation(s)
- Yogi Wibisono Budhi
- Department of Chemical Engineering, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
- Research Center for Nanosciences and Nanotechnology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
- Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
| | - Hans Kristian Irawan
- Department of Chemical Engineering, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
| | - Raihan Annisa Fitri
- Department of Chemical Engineering, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
| | - Tareqh Al Syifa Elgi Wibisono
- Department of Chemical Engineering, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
| | - Elvi Restiawaty
- Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung 40132, Indonesia
- Department of Bioenergy Engineering and Chemurgy, Faculty of Industrial Technology, Institut Teknologi Bandung, Jl. Let. Jend. Purn. Dr. (HC) Mashudi No.1, West Java 45363, Indonesia
| | - Manabu Miyamoto
- Department of Chemistry and Biomolecular Science, Faculty of Engineering, Gifu University, 1-1 Yanagido, Gifu 501-1193, Japan
| | - Shigeyuki Uemiya
- Department of Chemistry and Biomolecular Science, Faculty of Engineering, Gifu University, 1-1 Yanagido, Gifu 501-1193, Japan
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Radmanesh F, Pilz M, Ansaloni L, Peters TA, Louradour E, van Veen H, Høvik D, Hempenius MA, Benes NE. Comparing amine- and ammonium functionalized silsesquioxanes for large scale synthesis of hybrid polyimide high-temperature gas separation membranes. J Memb Sci 2021. [DOI: 10.1016/j.memsci.2021.119524] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/20/2022]
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Assessment of Sieverts Law Assumptions and ' n' Values in Palladium Membranes: Experimental and Theoretical Analyses. MEMBRANES 2021; 11:membranes11100778. [PMID: 34677544 PMCID: PMC8540459 DOI: 10.3390/membranes11100778] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 09/01/2021] [Revised: 09/30/2021] [Accepted: 10/04/2021] [Indexed: 11/17/2022]
Abstract
Palladium and palladium alloy membranes are superior materials for hydrogen purification, removal, or reaction processes. Sieverts’ Law suggests that the flux of hydrogen through such membranes is proportional to the difference between the feed and permeate side partial pressures, each raised to the 0.5 power (n = 0.5). Sieverts’ Law is widely applied in analyzing the steady state hydrogen permeation through Pd-based membranes, even in some cases where the assumptions made in deriving Sieverts’ Law do not apply. Often permeation data are fit to the model allowing the pressure exponent (n) to vary. This study experimentally assessed the validity of Sieverts’ Law as hydrogen was separated from other gases and theoretically modelled the effects of pressure and temperature on the assumptions and hence the accuracy of the 0.5-power law even with pure hydrogen feed. Hydrogen fluxes through Pd and Pd-Ag alloy foils from feed mixtures (5–83% helium in hydrogen; 473–573 K; with and without a sweep gas) were measured to study the effect of concentration polarization (CP) on hydrogen permeance and the applicability of Sieverts’ Law under such conditions. Concentration polarization was found to dominate hydrogen transport under some experimental conditions, particularly when feed concentrations of hydrogen were low. All mixture feed experiments showed deviation from Sieverts’ Law. For example, the hydrogen flux through Pd foil was found to be proportional to the partial pressure difference (n ≈ 1) rather than being proportional to the difference in the square root of the partial pressures (n = 0.5), as suggested by Sieverts’ Law, indicating the high degree of concentration polarization. A theoretical model accounting for Langmuir adsorption with temperature dependent adsorption equilibrium coefficient was made and used to assess the effect of varying feed pressure from 1–136 atm at fixed temperature, and of varying temperature from 298 to 1273 K at fixed pressure. Adsorption effects, which dominate at high pressure and at low temperature, result in pressure exponents (n) values less than 0.5. With better understanding of the transport steps, a qualitative analysis of literature (n) values of 0.5, 0.5 < n < 1, and n > 1, was conducted suggesting the role of each condition or step on the hydrogen transport based on the empirically fit exponent value.
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Vermaak L, Neomagus HWJP, Bessarabov DG. Hydrogen Separation and Purification from Various Gas Mixtures by Means of Electrochemical Membrane Technology in the Temperature Range 100-160 °C. MEMBRANES 2021; 11:membranes11040282. [PMID: 33920305 PMCID: PMC8069315 DOI: 10.3390/membranes11040282] [Citation(s) in RCA: 11] [Impact Index Per Article: 3.7] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 03/16/2021] [Revised: 03/31/2021] [Accepted: 04/01/2021] [Indexed: 11/29/2022]
Abstract
This paper reports on an experimental evaluation of the hydrogen separation performance in a proton exchange membrane system with Pt-Co/C as the anode electrocatalyst. The recovery of hydrogen from H2/CO2, H2/CH4, and H2/NH3 gas mixtures were determined in the temperature range of 100–160 °C. The effects of both the impurity concentration and cell temperature on the separation performance of the cell and membrane were further examined. The electrochemical properties and performance of the cell were determined by means of polarization curves, limiting current density, open-circuit voltage, hydrogen permeability, hydrogen selectivity, hydrogen purity, and cell efficiencies (current, voltage, and power efficiencies) as performance parameters. High purity hydrogen (>99.9%) was obtained from a low purity feed (20% H2) after hydrogen was separated from H2/CH4 mixtures. Hydrogen purities of 98–99.5% and 96–99.5% were achieved for 10% and 50% CO2 in the feed, respectively. Moreover, the use of proton exchange membranes for electrochemical hydrogen separation was unsuccessful in separating hydrogen-rich streams containing NH3; the membrane underwent irreversible damage.
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Affiliation(s)
- Leandri Vermaak
- HySA Infrastructure Centre of Competence, Faculty of Engineering, Potchefstroom Campus, North-West University, Potchefstroom 2520, South Africa
- Correspondence: (L.V.); (D.G.B.)
| | - Hein W. J. P. Neomagus
- Centre of Excellence in Carbon Based Fuels, Faculty of Engineering, School of Chemical and Minerals Engineering, Potchefstroom Campus, North-West University, Potchefstroom 2520, South Africa;
| | - Dmitri G. Bessarabov
- HySA Infrastructure Centre of Competence, Faculty of Engineering, Potchefstroom Campus, North-West University, Potchefstroom 2520, South Africa
- Correspondence: (L.V.); (D.G.B.)
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Martinez-Diaz D, Martínez del Monte D, García-Rojas E, Alique D, Calles J, Sanz R. Comprehensive permeation analysis and mechanical resistance of electroless pore-plated Pd-membranes with ordered mesoporous ceria as intermediate layer. Sep Purif Technol 2021. [DOI: 10.1016/j.seppur.2020.118066] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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6
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Ansaloni L, Louradour E, Radmanesh F, van Veen H, Pilz M, Simon C, Benes NE, Peters TA. Upscaling polyPOSS-imide membranes for high temperature H2 upgrading. J Memb Sci 2021. [DOI: 10.1016/j.memsci.2020.118875] [Citation(s) in RCA: 7] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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7
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Peters TA, Stange M, Bredesen R. Flux-Reducing Tendency of Pd-Based Membranes Employed in Butane Dehydrogenation Processes. MEMBRANES 2020; 10:E291. [PMID: 33081363 PMCID: PMC7650750 DOI: 10.3390/membranes10100291] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 09/29/2020] [Revised: 10/12/2020] [Accepted: 10/14/2020] [Indexed: 11/20/2022]
Abstract
We report on the effect of butane and butylene on hydrogen permeation through thin state-of-the-art Pd-Ag alloy membranes. A wide range of operating conditions, such as temperature (200-450 °C) and H2/butylene (or butane) ratio (0.5-3), on the flux-reducing tendency were investigated. In addition, the behavior of membrane performance during prolonged exposure to butylene was evaluated. In the presence of butane, the flux-reducing tendency was found to be limited up to the maximum temperature investigated, 450 °C. Compared to butane, the flux-reducing tendency in the presence of butylene was severe. At 400 °C and 20% butylene, the flux decreases by ~85% after 3 h of exposure but depends on temperature and the H2/butylene ratio. In terms of operating temperature, an optimal performance was found at 250-300 °C with respect to obtaining the highest absolute hydrogen flux in the presence of butylene. At lower temperatures, the competitive adsorption of butylene over hydrogen accounts for a large initial flux penalty.
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Affiliation(s)
- Thijs A. Peters
- SINTEF Industry, P.O. Box 124 Blindern, N-0314 Oslo, Norway; (M.S.); (R.B.)
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9
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Fontana AD, Faroldi B, Cornaglia LM, Tarditi AM. Development of catalytic membranes over PdAu selective films for hydrogen production through the dry reforming of methane. MOLECULAR CATALYSIS 2020. [DOI: 10.1016/j.mcat.2018.07.018] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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10
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Di Marcoberardino G, Knijff J, Binotti M, Gallucci F, Manzolini G. Techno-Economic Assessment in a Fluidized Bed Membrane Reactor for Small-Scale H 2 Production: Effect of Membrane Support Thickness. MEMBRANES 2019; 9:membranes9090116. [PMID: 31500136 PMCID: PMC6780302 DOI: 10.3390/membranes9090116] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 08/06/2019] [Revised: 09/03/2019] [Accepted: 09/03/2019] [Indexed: 11/29/2022]
Abstract
This paper investigates the influence of the support material and its thickness on the hydrogen flux in Palladium membranes in the presence of sweep gas in fluidized bed membrane reactors. The analysis is performed considering both ceramic and metallic supports with different properties. In general, ceramic supports are cheaper but suffer sealing problems, while metallic ones are more expensive but with much less sealing problems. Firstly, a preliminary analysis is performed to assess the impact of the support in the permeation flux, which shows that the membrane permeance can be halved when the H2 diffusion through the support is considered. The most relevant parameter which affects the permeation is the porosity over tortuosity ratio of the porous support. Afterward, the different supports are compared from an economic point of view when applied to a membrane reactor designed for 100 kg/day of hydrogen, using biogas as feedstock. The stainless steel supports have lower impact on the hydrogen permeation so the required membrane surface area is 2.6 m2 compared to 3.6 m2 of the best ceramic support. This ends up as 5.6 €/kg H2@20bar and 6.6 €/kg H2@700bar for the best stainless steel support, which is 3% lower than the price calculated for the best ceramic support.
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Affiliation(s)
- Gioele Di Marcoberardino
- Department of Mechanical and Industrial Engineering, University of Brescia, 25123 Brescia, Italy
| | - Jasper Knijff
- Inorganic Membranes and Membrane Reactors, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612 AZ Eindhoven, The Netherlands
| | - Marco Binotti
- Politecnico di Milano, Department of Energy, 20156 Milano, Italy
| | - Fausto Gallucci
- Inorganic Membranes and Membrane Reactors, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612 AZ Eindhoven, The Netherlands
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11
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Performance of Pd-Based Membranes and Effects of Various Gas Mixtures on H2 Permeation. ENVIRONMENTS 2018. [DOI: 10.3390/environments5120128] [Citation(s) in RCA: 16] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
Abstract
H2 permeation and separation properties of two Pd-based composite membranes were evaluated and compared at 400 °C and at a pressure range of 150 kPa to 600 kPa. One membrane was characterized by an approximately 8 μm-thick palladium (Pd)-gold (Au) layer deposited on an asymmetric microporous Al2O3 substrate; the other membrane consisted of an approximately 11 μm-thick pure palladium layer deposited on a yttria-stabilized zirconia (YSZ) support. At 400 °C and with a trans-membrane pressure of 50 kPa, the membranes showed a H2 permeance of 8.42 × 10−4 mol/m2·s·Pa0.5 and 2.54 × 10−5 mol/m2·s·Pa0.7 for Pd-Au and Pd membranes, respectively. Pd-Au membrane showed infinite ideal selectivity to H2 with respect to He and Ar at 400 °C and a trans-membrane pressure of 50 kPa, while the ideal selectivities for the Pd membrane under the same operating conditions were much lower. Furthermore, the permeation tests for ternary and quaternary mixtures of H2, CO, CO2, CH4, and H2O were conducted on the Pd/YSZ membrane. The H2 permeating flux decreased at the conclusion of the permeation tests for all mixtures. This decline however, was not permanent, i.e., H2 permeation was restored to its initial value after treating the membrane with H2 for a maximum of 7 h. The effects of gas hourly space velocity (GHSV) and the steam-to-carbon (S/C) ratio on H2 permeation were also investigated using simulated steam methane reforming mixtures. It was found that H2 permeation is highest at the greatest GHSV, due to a decline in the concentration polarization effect. Variations in S/C ratio however, showed no significant effect on the H2 permeation. The permeation characteristics for the Pd/YSZ membrane were also investigated at temperatures ranging from 350 to 400 °C. The pre-exponential factor and apparent activation energy were found to be 5.66 × 10−4 mol/m2·s·Pa0.7 and 12.8 kJ/mol, respectively. Scanning Electron Microscope (SEM) and X-ray diffraction (XRD) analyses were performed on both pristine and used membranes, and no strong evidence of the formation of Pd-O or any other undesirable phases was observed.
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12
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Rahmanifard H, Vakili R, Plaksina T, Rahimpour MR, Babaei M, Fan X. On improving the hydrogen and methanol production using an auto-thermal double-membrane reactor: Model prediction and optimisation. Comput Chem Eng 2018. [DOI: 10.1016/j.compchemeng.2018.09.006] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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13
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Dalla Fontana A, Sirini N, Cornaglia LM, Tarditi AM. Hydrogen permeation and surface properties of PdAu and PdAgAu membranes in the presence of CO, CO2 and H2S. J Memb Sci 2018. [DOI: 10.1016/j.memsci.2018.06.001] [Citation(s) in RCA: 15] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/14/2022]
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14
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Jo YS, Lee CH, Kong SY, Lee KY, Yoon CW, Nam SW, Han J. Characterization of a Pd/Ta composite membrane and its application to a large scale high-purity hydrogen separation from mixed gas. Sep Purif Technol 2018. [DOI: 10.1016/j.seppur.2017.12.019] [Citation(s) in RCA: 12] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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15
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Modeling Fixed Bed Membrane Reactors for Hydrogen Production through Steam Reforming Reactions: A Critical Analysis. MEMBRANES 2018; 8:membranes8020034. [PMID: 29921794 PMCID: PMC6026897 DOI: 10.3390/membranes8020034] [Citation(s) in RCA: 15] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 04/30/2018] [Revised: 06/08/2018] [Accepted: 06/12/2018] [Indexed: 11/30/2022]
Abstract
Membrane reactors for hydrogen production have been extensively studied in the past years due to the interest in developing systems that are adequate for the decentralized production of high-purity hydrogen. Research in this field has been both experimental and theoretical. The aim of this work is two-fold. On the one hand, modeling work on membrane reactors that has been carried out in the past is presented and discussed, along with the constitutive equations used to describe the different phenomena characterizing the behavior of the system. On the other hand, an attempt is made to shed some light on the meaning and usefulness of models developed with different degrees of complexity. The motivation has been that, given the different ways and degrees in which transport models can be simplified, the process is not always straightforward and, in some cases, leads to conceptual inconsistencies that are not easily identifiable or identified.
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16
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Alimov V, Bobylev I, Busnyuk A, Notkin M, Peredistov E, Livshits A. Hydrogen transport through the tubular membranes of V-Pd alloys: Permeation, diffusion, surface processes and WGS mixture test of membrane assembly. J Memb Sci 2018. [DOI: 10.1016/j.memsci.2017.12.017] [Citation(s) in RCA: 13] [Impact Index Per Article: 2.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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17
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Lundin STB, Patki NS, Fuerst TF, Wolden CA, Way JD. Inhibition of hydrogen flux in palladium membranes by pressure–induced restructuring of the membrane surface. J Memb Sci 2017. [DOI: 10.1016/j.memsci.2017.04.025] [Citation(s) in RCA: 15] [Impact Index Per Article: 2.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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18
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Castro-Dominguez B, Mardilovich IP, Ma LC, Ma R, Dixon AG, Kazantzis NK, Ma YH. Integration of Methane Steam Reforming and Water Gas Shift Reaction in a Pd/Au/Pd-Based Catalytic Membrane Reactor for Process Intensification. MEMBRANES 2016; 6:membranes6030044. [PMID: 27657143 PMCID: PMC5041035 DOI: 10.3390/membranes6030044] [Citation(s) in RCA: 23] [Impact Index Per Article: 2.9] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 07/23/2016] [Revised: 09/02/2016] [Accepted: 09/09/2016] [Indexed: 12/03/2022]
Abstract
Palladium-based catalytic membrane reactors (CMRs) effectively remove H2 to induce higher conversions in methane steam reforming (MSR) and water-gas-shift reactions (WGS). Within such a context, this work evaluates the technical performance of a novel CMR, which utilizes two catalysts in series, rather than one. In the process system under consideration, the first catalyst, confined within the shell side of the reactor, reforms methane with water yielding H2, CO and CO2. After reforming is completed, a second catalyst, positioned in series, reacts with CO and water through the WGS reaction yielding pure H2O, CO2 and H2. A tubular composite asymmetric Pd/Au/Pd membrane is situated throughout the reactor to continuously remove the produced H2 and induce higher methane and CO conversions while yielding ultrapure H2 and compressed CO2 ready for dehydration. Experimental results involving (i) a conventional packed bed reactor packed (PBR) for MSR, (ii) a PBR with five layers of two catalysts in series and (iii) a CMR with two layers of two catalysts in series are comparatively assessed and thoroughly characterized. Furthermore, a comprehensive 2D computational fluid dynamics (CFD) model was developed to explore further the features of the proposed configuration. The reaction was studied at different process intensification-relevant conditions, such as space velocities, temperatures, pressures and initial feed gas composition. Finally, it is demonstrated that the above CMR module, which was operated for 600 h, displays quite high H2 permeance and purity, high CH4 conversion levels and reduced CO yields.
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Affiliation(s)
- Bernardo Castro-Dominguez
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Ivan P Mardilovich
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Liang-Chih Ma
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Rui Ma
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Anthony G Dixon
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Nikolaos K Kazantzis
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
| | - Yi Hua Ma
- Center of Inorganic Membrane Studies, Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.
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Zhang XL, Akamatsu K, Nakao SI. Hydrogen Separation in Hydrogen–Methylcyclohexane–Toluene Gaseous Mixtures through Triphenylmethoxysilane-Derived Silica Membranes Prepared by Chemical Vapor Deposition. Ind Eng Chem Res 2016. [DOI: 10.1021/acs.iecr.6b00898] [Citation(s) in RCA: 10] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Xiao-Liang Zhang
- Jiangxi
Inorganic Membrane Materials Engineering Research Center, College
of Chemistry and Chemical Engineering, Jiangxi Normal University, 99
Ziyang Ave, Nanchang 330022, P.R. China
- Department
of Environmental Chemistry and Chemical Engineering, School of Advanced
Engineering, Kogakuin University, 2665-1 Nakano-machi, Hachioji-shi, Tokyo 192-0015, Japan
| | - Kazuki Akamatsu
- Department
of Environmental Chemistry and Chemical Engineering, School of Advanced
Engineering, Kogakuin University, 2665-1 Nakano-machi, Hachioji-shi, Tokyo 192-0015, Japan
| | - Shin-ichi Nakao
- Department
of Environmental Chemistry and Chemical Engineering, School of Advanced
Engineering, Kogakuin University, 2665-1 Nakano-machi, Hachioji-shi, Tokyo 192-0015, Japan
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20
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Kim CH, Han JY, Kim NC, Ryi SK, Kim DW. Characteristics of dense palladium alloy membranes formed by nano-scale nucleation and lateral growth. J Memb Sci 2016. [DOI: 10.1016/j.memsci.2015.12.010] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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21
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Shoham Patrascu M, Sheintuch M. Multi-fuel scaled-down autothermal pure H2generator: Design and proof of concept. AIChE J 2016. [DOI: 10.1002/aic.15193] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/05/2022]
Affiliation(s)
| | - Moshe Sheintuch
- Dept. of Chemical Engineering; Technion-Israel Institute of Technology; Haifa 32000 Israel
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22
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Nekhamkina O, Sheintuch M. Approximate models of concentration-polarization in Pd-membrane separators. Fast numerical analysis. J Memb Sci 2016. [DOI: 10.1016/j.memsci.2015.11.027] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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23
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Li X, Li A, Lim CJ, Grace JR. Hydrogen permeation through Pd-based composite membranes: Effects of porous substrate, diffusion barrier and sweep gas. J Memb Sci 2016. [DOI: 10.1016/j.memsci.2015.10.037] [Citation(s) in RCA: 25] [Impact Index Per Article: 3.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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25
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Boon J, Pieterse J, van Berkel F, van Delft Y, van Sint Annaland M. Hydrogen permeation through palladium membranes and inhibition by carbon monoxide, carbon dioxide, and steam. J Memb Sci 2015. [DOI: 10.1016/j.memsci.2015.08.061] [Citation(s) in RCA: 32] [Impact Index Per Article: 3.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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26
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Sheintuch M. Can the permeance of a Pd-based membrane be predicted from first principles? Curr Opin Chem Eng 2015. [DOI: 10.1016/j.coche.2015.07.004] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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27
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28
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Maroño M, Barreiro M, Torreiro Y, Sánchez J. Performance of a hybrid system sorbent–catalyst–membrane for CO2 capture and H2 production under pre-combustion operating conditions. Catal Today 2014. [DOI: 10.1016/j.cattod.2013.11.003] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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29
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Pishahang M, Larring Y, McCann M, Bredesen R. Ca0.9Mn0.5Ti0.5O3−δ: A Suitable Oxygen Carrier Material for Fixed-Bed Chemical Looping Combustion under Syngas Conditions. Ind Eng Chem Res 2014. [DOI: 10.1021/ie500928m] [Citation(s) in RCA: 27] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Mehdi Pishahang
- SINTEF Materials and Chemistry, Sustainable Energy Technology Sector,
P.O. Box 124, Blindern, NO-0314 Oslo, Norway
| | - Yngve Larring
- SINTEF Materials and Chemistry, Sustainable Energy Technology Sector,
P.O. Box 124, Blindern, NO-0314 Oslo, Norway
| | - Michael McCann
- SINTEF Materials and Chemistry, Sustainable Energy Technology Sector,
P.O. Box 124, Blindern, NO-0314 Oslo, Norway
| | - Rune Bredesen
- SINTEF Materials and Chemistry, Sustainable Energy Technology Sector,
P.O. Box 124, Blindern, NO-0314 Oslo, Norway
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30
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Alimov V, Busnyuk A, Notkin M, Livshits A. Pd–V–Pd composite membranes: Hydrogen transport in a wide pressure range and mechanical stability. J Memb Sci 2014. [DOI: 10.1016/j.memsci.2014.01.053] [Citation(s) in RCA: 26] [Impact Index Per Article: 2.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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31
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Jordal K, Anantharaman R, Gruber A, Peters T, Henriksen PP, Berstad D, Bredesen R. GHGT-12 Performance of the IGCC with distributed feeding of H2 in the gas turbine burner. ACTA ACUST UNITED AC 2014. [DOI: 10.1016/j.egypro.2014.11.219] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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32
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Bifunctional palladium composite membrane for hydrogen separation and catalytic CO methanation. CHINESE JOURNAL OF CATALYSIS 2013. [DOI: 10.1016/s1872-2067(12)60636-6] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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33
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Lewis A, Kershner D, Paglieri S, Slepicka M, Way J. Pd–Pt/YSZ composite membranes for hydrogen separation from synthetic water–gas shift streams. J Memb Sci 2013. [DOI: 10.1016/j.memsci.2013.02.056] [Citation(s) in RCA: 28] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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34
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Gallucci F, Fernandez E, Corengia P, van Sint Annaland M. Recent advances on membranes and membrane reactors for hydrogen production. Chem Eng Sci 2013. [DOI: 10.1016/j.ces.2013.01.008] [Citation(s) in RCA: 370] [Impact Index Per Article: 33.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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35
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Nagy E, Nagy R, Dudas J. Separate Expression of Polarization Modulus and Enrichment by Mass Transport Parameters for Membrane Gas Separation. Ind Eng Chem Res 2013. [DOI: 10.1021/ie302264j] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Endre Nagy
- Research Institute of Chemical and Process Engineering, University of Pannonia, P.O. Box 158, H-8201 H Veszprém, Hungary
| | - Renáta Nagy
- Research Institute of Chemical and Process Engineering, University of Pannonia, P.O. Box 158, H-8201 H Veszprém, Hungary
| | - Jozsef Dudas
- Research Institute of Chemical and Process Engineering, University of Pannonia, P.O. Box 158, H-8201 H Veszprém, Hungary
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van Berkel F, Hao C, Bao C, Jiang C, Xu H, Morud J, Peters T, Soutif E, Dijkstra JW, Jansen D, Song B. Pd-membranes on their Way Towards Application for CO2-capture. ACTA ACUST UNITED AC 2013. [DOI: 10.1016/j.egypro.2013.05.204] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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37
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Sarić M, van Delft YC, Sumbharaju R, Meyer DF, de Groot A. Steam reforming of methane in a bench-scale membrane reactor at realistic working conditions. Catal Today 2012. [DOI: 10.1016/j.cattod.2012.04.009] [Citation(s) in RCA: 46] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/28/2022]
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38
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Svenum IH, Herron J, Mavrikakis M, Venvik H. Adsorbate-induced segregation in a PdAg membrane model system: Pd3Ag(111). Catal Today 2012. [DOI: 10.1016/j.cattod.2012.01.007] [Citation(s) in RCA: 35] [Impact Index Per Article: 2.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/28/2022]
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Acha E, Requies J, Barrio V, Cambra J, Güemez M, Arias P, van Delft Y. PdCu membrane applied to hydrogen production from methane. J Memb Sci 2012. [DOI: 10.1016/j.memsci.2012.04.038] [Citation(s) in RCA: 16] [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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Peters T, Kaleta T, Stange M, Bredesen R. Hydrogen transport through a selection of thin Pd-alloy membranes: Membrane stability, H2S inhibition, and flux recovery in hydrogen and simulated WGS mixtures. Catal Today 2012. [DOI: 10.1016/j.cattod.2011.12.028] [Citation(s) in RCA: 74] [Impact Index Per Article: 6.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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41
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42
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Influence of CO2 and H2O on the separation of hydrogen over two types of Pd membranes: Thin metal membrane and pore-filling-type membrane. J Memb Sci 2012. [DOI: 10.1016/j.memsci.2012.04.053] [Citation(s) in RCA: 11] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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43
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Peters T, Kaleta T, Stange M, Bredesen R. Development of thin binary and ternary Pd-based alloy membranes for use in hydrogen production. J Memb Sci 2011. [DOI: 10.1016/j.memsci.2011.08.050] [Citation(s) in RCA: 68] [Impact Index Per Article: 5.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/17/2022]
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44
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Magnone E, Jeon SI, Park JH, Fleury E. Relationship between microstructure and hydrogen permeation properties in the multiphase Ni21Ti23Nb56 alloy membranes. J Memb Sci 2011. [DOI: 10.1016/j.memsci.2011.09.014] [Citation(s) in RCA: 25] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/17/2022]
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Couling DJ, Prakash K, Green WH. Analysis of Membrane and Adsorbent Processes for Warm Syngas Cleanup in Integrated Gasification Combined-Cycle Power with CO2 Capture and Sequestration. Ind Eng Chem Res 2011. [DOI: 10.1021/ie200291j] [Citation(s) in RCA: 22] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/21/2022]
Affiliation(s)
- David J. Couling
- Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Room 66-270, Cambridge, Massachusetts, United States
| | - Kshitij Prakash
- Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Room 66-270, Cambridge, Massachusetts, United States
| | - William H. Green
- Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Room 66-270, Cambridge, Massachusetts, United States
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46
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De Falco M, Salladini A, Iaquaniello G. Reformer and membrane modules for methane conversion: experimental assessment and perspectives of an innovative architecture. CHEMSUSCHEM 2011; 4:1157-1165. [PMID: 21826798 DOI: 10.1002/cssc.201100009] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/11/2011] [Indexed: 05/31/2023]
Abstract
An innovative concept for steam methane reforming (SMR), based on reformer and membrane modules (RMMs), has been developed and tested to investigate its performance, in terms of feed conversion, on an industrial scale. A major benefit of the proposed RMM configuration is a shift of the chemical equilibrium of SMR reactions, achieved by removing the hydrogen produced at high temperature through the integration of highly selective palladium-based membranes, which enhances the yield of product. In this manner the process can operate at temperatures as low as 600-650 °C, compared to the 850-880 °C range used in conventional plants, and allows for the use of a low-temperature heat source. This Full Paper discusses experimental data on feed conversion at different operating parameters, gathered during 1000 h of testing, and processes these data to optimize the overall architecture, defining the maximum achievable feed conversion. An overall conversion of 59% is achieved with two-step reactions at a reforming temperature of 620 °C. A conversion as high as 90% can be obtained with a three-step architecture at 650 °C by properly extending the design parameters within reasonable limits.
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Affiliation(s)
- Marcello De Falco
- Faculty of Engineering, University Campus Bio-Medico of Rome, Via Alvaro del Portillo 21, 00128 Rome, Italy
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47
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On the high pressure performance of thin supported Pd–23%Ag membranes—Evidence of ultrahigh hydrogen flux after air treatment. J Memb Sci 2011. [DOI: 10.1016/j.memsci.2010.11.022] [Citation(s) in RCA: 71] [Impact Index Per Article: 5.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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50
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Li H, Dijkstra J, Pieterse J, Boon J, van den Brink R, Jansen D. Towards full-scale demonstration of hydrogen-selective membranes for CO2 capture: Inhibition effect of WGS-components on the H2 permeation through three Pd membranes of 44cm long. J Memb Sci 2010. [DOI: 10.1016/j.memsci.2010.07.029] [Citation(s) in RCA: 42] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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