Nylon Intermediates from Bio‐Based Levulinic Acid
Use of ZrO2/SiO2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐, and 4‐pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydrofo...
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| Vydáno v: | Angewandte Chemie International Edition Ročník 58; číslo 11; s. 3486 - 3490 |
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| Hlavní autoři: | , , , , , , , |
| Médium: | Journal Article |
| Jazyk: | angličtina |
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Wiley Subscription Services, Inc
11.03.2019
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| Vydání: | International ed. in English |
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| ISSN: | 1433-7851, 1521-3773, 1521-3773 |
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| Abstract | Use of ZrO2/SiO2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐, and 4‐pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5‐formyl‐valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring‐closure to ϵ‐caprolactam in excellent yield had been reported before. The remaining mixture of 2‐ and 3‐MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield.
Green nylon: Use of 25 % ZrO2/SiO2 as catalyst allows the gas‐phase ring‐opening of bio‐based γ‐valerolactone with methanol to a mixture of methyl pentenoates containing 81 % of the 4‐isomer, which could be selectively hydroformylated from the mixture to methyl 5‐formyl‐valerate, an intermediate for ϵ‐caprolactam. The remaining isomers were converted into dimethyl adipate. |
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| AbstractList | Use of ZrO2 /SiO2 as a solid acid catalyst in the ring-opening of biobased γ-valerolactone with methanol in the gas phase leads to mixtures of methyl 2-, 3-, and 4-pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5-formyl-valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring-closure to ϵ-caprolactam in excellent yield had been reported before. The remaining mixture of 2- and 3-MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield.Use of ZrO2 /SiO2 as a solid acid catalyst in the ring-opening of biobased γ-valerolactone with methanol in the gas phase leads to mixtures of methyl 2-, 3-, and 4-pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5-formyl-valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring-closure to ϵ-caprolactam in excellent yield had been reported before. The remaining mixture of 2- and 3-MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield. Use of ZrO /SiO as a solid acid catalyst in the ring-opening of biobased γ-valerolactone with methanol in the gas phase leads to mixtures of methyl 2-, 3-, and 4-pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5-formyl-valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring-closure to ϵ-caprolactam in excellent yield had been reported before. The remaining mixture of 2- and 3-MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield. Use of ZrO2/SiO2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐, and 4‐pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5‐formyl‐valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring‐closure to ϵ‐caprolactam in excellent yield had been reported before. The remaining mixture of 2‐ and 3‐MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield. Green nylon: Use of 25 % ZrO2/SiO2 as catalyst allows the gas‐phase ring‐opening of bio‐based γ‐valerolactone with methanol to a mixture of methyl pentenoates containing 81 % of the 4‐isomer, which could be selectively hydroformylated from the mixture to methyl 5‐formyl‐valerate, an intermediate for ϵ‐caprolactam. The remaining isomers were converted into dimethyl adipate. Use of ZrO2/SiO2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐, and 4‐pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5‐formyl‐valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring‐closure to ϵ‐caprolactam in excellent yield had been reported before. The remaining mixture of 2‐ and 3‐MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield. Use of ZrO 2 /SiO 2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐, and 4‐pentenoate (MP) in over 95 % selectivity, containing a surprising 81 % of M4P. This process allows the application of a selective hydroformylation to this mixture to convert M4P into methyl 5‐formyl‐valerate (M5FV) with 90 % selectivity. The other isomers remain unreacted. Reductive amination of M5FV and ring‐closure to ϵ ‐caprolactam in excellent yield had been reported before. The remaining mixture of 2‐ and 3‐MP was subjected to an isomerising methoxycarbonylation to dimethyl adipate in 91 % yield. |
| Author | Amani, Hadis El Ouahabi, Fatima Kamer, Paul C. J. Kalevaru, Narayana V. Wohlrab, Sebastian de Vries, Johannes G. Tin, Sergey Marckwordt, Annemarie |
| Author_xml | – sequence: 1 givenname: Annemarie orcidid: 0000-0002-0337-5946 surname: Marckwordt fullname: Marckwordt, Annemarie organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 2 givenname: Fatima orcidid: 0000-0003-1175-1988 surname: El Ouahabi fullname: El Ouahabi, Fatima organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 3 givenname: Hadis orcidid: 0000-0002-5236-5875 surname: Amani fullname: Amani, Hadis organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 4 givenname: Sergey orcidid: 0000-0002-4324-6380 surname: Tin fullname: Tin, Sergey organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 5 givenname: Narayana V. orcidid: 0000-0003-2105-0907 surname: Kalevaru fullname: Kalevaru, Narayana V. email: Narayana.Kalevaru@catalysis.de organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 6 givenname: Paul C. J. orcidid: 0000-0002-9115-8844 surname: Kamer fullname: Kamer, Paul C. J. organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 7 givenname: Sebastian orcidid: 0000-0003-1407-7263 surname: Wohlrab fullname: Wohlrab, Sebastian organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock – sequence: 8 givenname: Johannes G. orcidid: 0000-0001-5245-7748 surname: de Vries fullname: de Vries, Johannes G. email: Johannes.devries@catalysis.de organization: Leibniz Institut für Katalyse e. V. an der Universität Rostock |
| BackLink | https://www.ncbi.nlm.nih.gov/pubmed/30650227$$D View this record in MEDLINE/PubMed |
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| Keywords | biomass heterogeneous catalysis homogeneous catalysis nylon rhodium |
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| Snippet | Use of ZrO2/SiO2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐,... Use of ZrO 2 /SiO 2 as a solid acid catalyst in the ring‐opening of biobased γ‐valerolactone with methanol in the gas phase leads to mixtures of methyl 2‐, 3‐,... Use of ZrO /SiO as a solid acid catalyst in the ring-opening of biobased γ-valerolactone with methanol in the gas phase leads to mixtures of methyl 2-, 3-, and... Use of ZrO2 /SiO2 as a solid acid catalyst in the ring-opening of biobased γ-valerolactone with methanol in the gas phase leads to mixtures of methyl 2-, 3-,... |
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| SubjectTerms | Amination biomass Caprolactam heterogeneous catalysis homogeneous catalysis Intermediates Isomers Levulinic acid Nylon rhodium Selectivity Silicon dioxide Vapor phases Zirconium dioxide |
| Title | Nylon Intermediates from Bio‐Based Levulinic Acid |
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