Closing the Gap: Towards a Fully Continuous and Self-Regulated Kolbe Electrosynthesis

被引:7
作者
Droegemueller, Patrick [1 ,3 ]
Stobbe, Tobias [1 ]
Schroeder, Uwe [2 ,3 ]
机构
[1] Tech Univ Carolo Wilhelmina Braunschweig, Inst Environm & Sustainable Chem, Hagenring 30, D-38106 Braunschweig, Germany
[2] Univ Greifswald, Inst Biochem, Felix Hausdorff Str 4, D-17489 Greifswald, Germany
[3] Tech Univ Carolo Wilhelmina Braunschweig, Cluster Excellence SE2A Sustainable & Energy Effic, Braunschweig, Germany
关键词
Chemostatic processes; Continuous electrosynthesis; Green chemistry; Kolbe reaction; Valeric acid; ELECTROLYSIS; CONVERSION; BIOMASS;
D O I
10.1002/cssc.202300973
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In this article, we address the transition of the Kolbe electrolysis of valeric acid (VA) to n-octane as an exemplary electrosynthesis process from a batch reaction to a continuous, self-regulated process. Based on a systematic assessment of chemical boundary conditions and sustainability aspects, we propose a continuous electrosynthesis including a simple product separation and electrolyte recirculation, as well as an online-pH-controlled VA feeding. We demonstrate how essential performance parameters such as product selectivity (S) and coulombic efficiency (CE) are significantly improved by the transition from batch to a continuous process. Thus, the continuous and pH-controlled electrolysis of a 1 M valeric acid, starting pH 6.0, allowed a constantly high selectivity of around 47 % and an average Coulomb efficiency about 52 % throughout the entire experimental duration. Under otherwise identical conditions, the conventional batch operation suffered from lower and strongly decreasing performance values (Sn-octane, 60min=10.4 %, Sn-octane, 240min=1.3 %; CEn-octane, 60min=7.1 %, CEn-octane, 240min=0.5 %). At the same time, electrolyte recirculation significantly reduces wastes and limits the use of electrolyte components. Untapping the full potential of electrosynthesis: by means of the Kolbe electrolysis, the transfer of electrochemical syntheses from batch to continuous operation is demonstrated to allow the target reactions to be carried out efficiently, sustainably and in a scalable and thus industrially relevant manner.image
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页数:9
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共 28 条
  • [1] KINETIC STUDY OF HOFER-MOEST REACTION
    ATHERTON, G
    FLEISCHM.M
    GOODRIDG.F
    [J]. TRANSACTIONS OF THE FARADAY SOCIETY, 1967, 63 (534P): : 1468 - &
  • [2] Applications of Flow Microreactors in Electrosynthetic Processes
    Atobe, Mahito
    Tateno, Hiroyuki
    Matsumura, Yoshimasa
    [J]. CHEMICAL REVIEWS, 2018, 118 (09) : 4541 - 4572
  • [3] Scalable Microreactor Concept for the Continuous Kolbe Electrolysis of Carboxylic Acids Using Aqueous Electrolyte
    Baumgarten, Nils
    Etzold, Bastian J. M.
    Magomajew, Juri
    Ziogas, Athanassios
    [J]. CHEMISTRYOPEN, 2022, 11 (10)
  • [4] Organic Electrosynthesis: From Laboratorial Practice to Industrial Applications
    Cardoso, David S. P.
    Sljukic, Biljana
    Santos, Diogo M. F.
    Sequeira, Cesar A. C.
    [J]. ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2017, 21 (09) : 1213 - 1226
  • [5] Organic Electrosynthesis Towards Sustainability: Fundamentals and Greener Methodologies
    Cembellin, Sara
    Batanero, Belen
    [J]. CHEMICAL RECORD, 2021, 21 (09) : 2453 - 2471
  • [6] Faraday M., 1834, PHIL T, V124, P55, DOI DOI 10.1098/RSTL.1834.0007
  • [7] Conversion of biomass to selected chemical products
    Gallezot, Pierre
    [J]. CHEMICAL SOCIETY REVIEWS, 2012, 41 (04) : 1538 - 1558
  • [8] Electrosynthesis in Extended Channel Length Microfluidic Electrolysis Cells
    Green, Robert A.
    Brown, Richard C. D.
    Pletcher, Derek
    [J]. JOURNAL OF FLOW CHEMISTRY, 2016, 6 (03) : 191 - 197
  • [9] Tapping Renewables: A New Dawn for Organic Electrosynthesis in Aqueous Reaction Media
    Harnisch, Falk
    Schroeder, Uwe
    [J]. CHEMELECTROCHEM, 2019, 6 (16) : 4126 - 4133
  • [10] SOLUBILITIES OF PROPENE, BUTANE, ISOBUTANE AND ISOBUTENE GASES IN NORMAL-OCTANE, CHLOROBENZENE AND NORMAL-BUTANOL SOLVENTS
    HAYDUK, W
    ASATANI, H
    MIYANO, Y
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1988, 66 (03) : 466 - 473