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Heras F, Justicia J, Baeza JA, Gilarranz MA, Ferro VR. Energy and economic analysis of alternatives for the valorization of hydrogen rich stream produced in the aqueous phase reforming of pyrolysis bio-oil aqueous fraction. BIORESOURCE TECHNOLOGY 2024; 399:130572. [PMID: 38492651 DOI: 10.1016/j.biortech.2024.130572] [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: 01/10/2024] [Revised: 02/27/2024] [Accepted: 03/09/2024] [Indexed: 03/18/2024]
Abstract
Aqueous phase reforming has been explored for renewable H2 production from waste biomass. Promising results have been reported for pyrolysis bio-oil aqueous fractions (AFB), but economical assessments are needed to determine process feasibility, which requires both energy consumption minimization and optimal H2 valorization. This work compares different alternatives using process simulation and economic evaluation computational tools. Experimental results and a specific thermodynamic model are used to set mass balances. An adequate heat integration allows to reduce the process energy demand, covering the 100 % of the reactor duty. Optimal H2 unit cost is achieved if part of the produced H2 is valorized for energy self-covering and the rest is commercialized. Renewable H2 net production of c.a. 3.3 kgH2/m3 of treated AFB at a preliminary 1-2 €/kg unit cost is estimated, which can be considered as competitive with green H2, even though a case of diluted AFB is considered.
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Affiliation(s)
- Francisco Heras
- Department of Chemical Engineering, Universidad Autónoma de Madrid. Ciudad Universitaria de Cantoblanco, 28049 Madrid Spain.
| | - Jéssica Justicia
- Department of Chemical Engineering, Universidad Autónoma de Madrid. Ciudad Universitaria de Cantoblanco, 28049 Madrid Spain
| | - José A Baeza
- Department of Chemical Engineering, Universidad Autónoma de Madrid. Ciudad Universitaria de Cantoblanco, 28049 Madrid Spain
| | - Miguel A Gilarranz
- Department of Chemical Engineering, Universidad Autónoma de Madrid. Ciudad Universitaria de Cantoblanco, 28049 Madrid Spain
| | - Víctor R Ferro
- Department of Chemical Engineering, Universidad Autónoma de Madrid. Ciudad Universitaria de Cantoblanco, 28049 Madrid Spain
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2
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Nitrogen-containing carbon nanofibers as supports for bimetallic Pt-Mn catalysts in aqueous phase reforming of ethylene glycol. Catal Today 2023. [DOI: 10.1016/j.cattod.2023.114066] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 03/04/2023]
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3
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Huo J, Tessonnier JP, Shanks BH. Improving Hydrothermal Stability of Supported Metal Catalysts for Biomass Conversions: A Review. ACS Catal 2021. [DOI: 10.1021/acscatal.1c00197] [Citation(s) in RCA: 33] [Impact Index Per Article: 11.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/19/2022]
Affiliation(s)
- Jiajie Huo
- Department of Chemical and Biological Engineering, Iowa State University, Ames, Iowa 50011, United States
- Center for Biorenewable Chemicals, Iowa State University, Ames, Iowa 50011, United States
| | - Jean-Philippe Tessonnier
- Department of Chemical and Biological Engineering, Iowa State University, Ames, Iowa 50011, United States
- Center for Biorenewable Chemicals, Iowa State University, Ames, Iowa 50011, United States
| | - Brent H. Shanks
- Department of Chemical and Biological Engineering, Iowa State University, Ames, Iowa 50011, United States
- Center for Biorenewable Chemicals, Iowa State University, Ames, Iowa 50011, United States
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Huang Y, Zhang G, Zhang Q. Preparation of the WO X /MCM-41 Solid Acid Catalyst and the Catalytic Performance for Solketal Synthesis. ACS OMEGA 2021; 6:3875-3883. [PMID: 33585766 PMCID: PMC7876846 DOI: 10.1021/acsomega.0c05671] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 11/21/2020] [Accepted: 01/20/2021] [Indexed: 06/12/2023]
Abstract
In the present work, an efficient and stable WO X /MCM-41 solid acid catalyst was prepared by the wet impregnation method. The characterization of powder X-ray diffraction, transmission electron microscopy, ultraviolet-visible, H2 temperature-programmed reduction, X-ray photoelectron spectroscopy, NH3 temperature-programmed desorption, and N2 adsorption-desorption isotherms confirmed that the impregnation amount and calcination temperature of WO X speciation affected the dispersity and acidity of the resulting catalyst. This WO X /MCM-41 solid acid catalyst was subsequently applied in the ketalization reaction of glycerol and acetone to produce solketal. By catalyst screening and reaction condition optimization, WO X /MCM-41 obtained by impregnating 20 wt % and calcining at 350 °C exhibited the highest solketal yield and catalytic stability.
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5
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Zhou X, Liu CJ. Three-dimensional printing of porous carbon structures with tailorable pore sizes. Catal Today 2020. [DOI: 10.1016/j.cattod.2018.05.044] [Citation(s) in RCA: 19] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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6
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Negahdar L, Parlett CMA, Isaacs MA, Beale AM, Wilson K, Lee AF. Shining light on the solid–liquid interface: in situ/ operando monitoring of surface catalysis. Catal Sci Technol 2020. [DOI: 10.1039/d0cy00555j] [Citation(s) in RCA: 12] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/06/2023]
Abstract
Many industrially important chemical transformations occur at the interface between a solid catalyst and liquid reactants. In situ and operando spectroscopies offer unique insight into the reactivity of such catalytically active solid–liquid interfaces.
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Affiliation(s)
| | - Christopher M. A. Parlett
- Department of Chemical Engineering & Analytical Science
- The University of Manchester
- Manchester
- UK
- Diamond Light Source
| | | | | | - Karen Wilson
- Centre for Advanced Materials and Industrial Chemistry (CAMIC)
- School of Science
- RMIT University
- Melbourne
- Australia
| | - Adam F. Lee
- Centre for Advanced Materials and Industrial Chemistry (CAMIC)
- School of Science
- RMIT University
- Melbourne
- Australia
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7
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Lee K, Lee ME, Kim JK, Shin B, Choi M. Single-step hydroconversion of triglycerides into biojet fuel using CO-tolerant PtRe catalyst supported on USY. J Catal 2019. [DOI: 10.1016/j.jcat.2019.09.043] [Citation(s) in RCA: 19] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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8
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Jin M, Choi M. Hydrothermal deoxygenation of triglycerides over carbon-supported bimetallic PtRe catalysts without an external hydrogen source. MOLECULAR CATALYSIS 2019. [DOI: 10.1016/j.mcat.2019.110419] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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9
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Abstract
Biomass is an interesting candidate raw material for the production of renewable hydrogen. The conversion of biomass into hydrogen can be achieved by several processes. In particular, this short review focuses on the recent advances in glycerol reforming to hydrogen, highlighting the development of new and active catalysts, the optimization of reaction conditions, and the use of non-innocent supports as advanced materials for supported catalysts. Different processes for hydrogen production from glycerol, especially aqueous phase reforming (APR) and steam reforming (SR), are described in brief. Thermodynamic analyses, which enable comparison with experimental studies, are also considered. In addition, research advances in terms of life cycle perspective applied to support R&D activities in the synthesis of renewable H2 from biomass are presented. Lastly, also featured is an evaluation of the studies published, as evidence of the increased interest of both academic research and the industrial community in biomass conversion to energy sources.
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Di X, Lafaye G, Especel C, Epron F, Qi J, Li C, Liang C. Supported Co-Re Bimetallic Catalysts with Different Structures as Efficient Catalysts for Hydrogenation of Citral. CHEMSUSCHEM 2019; 12:807-823. [PMID: 30620120 DOI: 10.1002/cssc.201802744] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/26/2018] [Revised: 12/20/2018] [Indexed: 06/09/2023]
Abstract
Bimetallic Co-Re/TiO2 catalysts were developed for efficient citral hydrogenation. Bimetallic catalysts were prepared by co-impregnation (CI), successive-impregnation (SI), and surface redox method (SR). The arrangement between the Co and Re species on these systems was fully characterized using several techniques (TEM-energy-dispersive X-ray spectroscopy, H2 temperature-programmed reduction, temperature-programmed desorption, XRD, CO FTIR spectroscopy, model reaction of cyclohexane dehydrogenation), and their catalytic performances were evaluated for the selective hydrogenation of citral towards unsaturated alcohols. The Re and Co species are completely isolated in the CI sample, presenting a very limited Co-Re interaction. In SI samples, the metals coexist in a Janus-type structure with a concentration of Re around Co. Decoration/core-shell structures are observed for SR samples resulting from the redox exchange between the metallic surface of the parent Co/TiO2 catalyst and the Re7+ species of the modifier precursor salt. The contact degree between the two metals gradually increases as follows: Isolated structure (CI)<Janus-type structure(SI)<decoration/core-shell structure (SR). The unchanging structure of all SI samples independent of the Re loading leads to similar electron transfer, and the increase in Re content results in agglomeration of Re, thus decreasing the catalytic activity. Density-of-state (DOS) calculations prove that the high valence of Re is a disadvantage for the hydrogenation reaction. For SR samples, the increase of Re loading contributes to the electron transfer from Re to Co that is consistent with a change of structure from decoration to core-shell. The lack of directly accessible Co atoms for SR catalysts with fully coated structure decreases the efficiency of Re reduction. The presence of Co-Re interaction resulting from the close contact between metals plays a dominant role in the hydrogenation of citral. Nevertheless, an excessively high contact degree is unnecessary for citral hydrogenation once Co-Re interaction has formed.
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Affiliation(s)
- Xin Di
- Laboratory of Advanced Materials and Catalytic Engineering, Dalian University of Technology, No.2 Linggong Road, Dalian City, Liaoning Province, P.R. China
- Institut de Chimie des Milieux & Matériaux de Poitiers (IC2MP), Université de Poitiers, CNRS, 4 rue Michel Brunet, 86073, Poitiers, France
| | - Gwendoline Lafaye
- Institut de Chimie des Milieux & Matériaux de Poitiers (IC2MP), Université de Poitiers, CNRS, 4 rue Michel Brunet, 86073, Poitiers, France
| | - Catherine Especel
- Institut de Chimie des Milieux & Matériaux de Poitiers (IC2MP), Université de Poitiers, CNRS, 4 rue Michel Brunet, 86073, Poitiers, France
| | - Florence Epron
- Institut de Chimie des Milieux & Matériaux de Poitiers (IC2MP), Université de Poitiers, CNRS, 4 rue Michel Brunet, 86073, Poitiers, France
| | - Ji Qi
- Laboratory of Advanced Materials and Catalytic Engineering, Dalian University of Technology, No.2 Linggong Road, Dalian City, Liaoning Province, P.R. China
| | - Chuang Li
- Laboratory of Advanced Materials and Catalytic Engineering, Dalian University of Technology, No.2 Linggong Road, Dalian City, Liaoning Province, P.R. China
| | - Changhai Liang
- Laboratory of Advanced Materials and Catalytic Engineering, Dalian University of Technology, No.2 Linggong Road, Dalian City, Liaoning Province, P.R. China
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Liu S, Tamura M, Shen Z, Zhang Y, Nakagawa Y, Tomishige K. Hydrogenolysis of glycerol with in-situ produced H 2 by aqueous-phase reforming of glycerol using Pt-modified Ir-ReO x /SiO 2 catalyst. Catal Today 2018. [DOI: 10.1016/j.cattod.2017.07.025] [Citation(s) in RCA: 27] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/07/2023]
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12
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13
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Vaidya PD, Lopez-Sanchez JA. Review of Hydrogen Production by Catalytic Aqueous-Phase Reforming. ChemistrySelect 2017. [DOI: 10.1002/slct.201700905] [Citation(s) in RCA: 30] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Prakash D. Vaidya
- Department of Chemical Engineering; Institute of Chemical Technology, Nathalal Parekh Marg, Matunga; Mumbai- 400019 India
| | - Jose A. Lopez-Sanchez
- Stephenson's Institute for Renewable Energy; Department of Chemistry; The University of Liverpool; Liverpool L69 7ZD UK
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Bossola F, Pereira-Hernández XI, Evangelisti C, Wang Y, Dal Santo V. Investigation of the promoting effect of Mn on a Pt/C catalyst for the steam and aqueous phase reforming of glycerol. J Catal 2017. [DOI: 10.1016/j.jcat.2017.03.002] [Citation(s) in RCA: 32] [Impact Index Per Article: 4.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/20/2022]
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15
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Opris C, Cojocaru B, Gheorghe N, Tudorache M, Coman SM, Parvulescu VI, Duraki B, Krumeich F, van Bokhoven JA. Lignin Fragmentation onto Multifunctional Fe3O4@Nb2O5@Co@Re Catalysts: The Role of the Composition and Deposition Route of Rhenium. ACS Catal 2017. [DOI: 10.1021/acscatal.6b02915] [Citation(s) in RCA: 20] [Impact Index Per Article: 2.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Cristina Opris
- University of Bucharest, Department of Organic
Chemistry, Biochemistry and Catalysis, B-dul Regina Elisabeta 4-12, 030016 Bucharest, Romania
| | - Bogdan Cojocaru
- University of Bucharest, Department of Organic
Chemistry, Biochemistry and Catalysis, B-dul Regina Elisabeta 4-12, 030016 Bucharest, Romania
| | - Nicoleta Gheorghe
- National Institute of Materials Physics, Atomistilor 105b, 077125 Magurele-Ilfov, Romania
| | - Madalina Tudorache
- University of Bucharest, Department of Organic
Chemistry, Biochemistry and Catalysis, B-dul Regina Elisabeta 4-12, 030016 Bucharest, Romania
| | - Simona M. Coman
- University of Bucharest, Department of Organic
Chemistry, Biochemistry and Catalysis, B-dul Regina Elisabeta 4-12, 030016 Bucharest, Romania
| | - Vasile I. Parvulescu
- University of Bucharest, Department of Organic
Chemistry, Biochemistry and Catalysis, B-dul Regina Elisabeta 4-12, 030016 Bucharest, Romania
| | - Bahir Duraki
- ETH Zurich, Wolfgang Pauli
Strasse, 8093 Zürich, Switzerland
| | - Frank Krumeich
- ETH Zurich, Wolfgang Pauli
Strasse, 8093 Zürich, Switzerland
| | - Jeroen A. van Bokhoven
- ETH Zurich, Wolfgang Pauli
Strasse, 8093 Zürich, Switzerland
- Paul Scherrer Institute, 5232 Villigen, Switzerland
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