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WO2013082264A1 - Synthèse d'oléfines - Google Patents

Synthèse d'oléfines Download PDF

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Publication number
WO2013082264A1
WO2013082264A1 PCT/US2012/067027 US2012067027W WO2013082264A1 WO 2013082264 A1 WO2013082264 A1 WO 2013082264A1 US 2012067027 W US2012067027 W US 2012067027W WO 2013082264 A1 WO2013082264 A1 WO 2013082264A1
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Prior art keywords
muconic acid
ethylene
ester
cis
butadiene
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Inventor
Susan Schofer
Adam Safir
Roberto VAZQUEZ
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Amyris Inc
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Amyris Inc
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
    • C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
    • C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • C07C51/353—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by isomerisation; by change of size of the carbon skeleton
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/333—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • C07C2531/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • C07C2531/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24
    • C07C2531/34—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24 of chromium, molybdenum or tungsten

Definitions

  • Butadiene, acrylic acid and acrylates are produced commercially in large volume from petroleum-derived chemicals.
  • Described herein are methods of producing 1,3-butadiene, acrylic acid or one or more esters of acrylic acid, or both 1,3-butadiene and acrylic acid or one or more esters of acrylic acid from muconic acid or a derivative thereof.
  • Muconic acid used in the methods described herein may be derived from any source. Any one of cis,cis-muconic acid, cis,trans- muconic acid, and trans,trans-muconic acid, or any combination thereof may be used.
  • muconic acid is derived microbially from genetically modified organisms using renewable, non- fossil fuel carbon sources.
  • R OOC-CH CH 2 .
  • R is hydrogen, hydrocarbyl or substituted hydrocarbyl, for instance Ci_ 30 hydrocarbyl, and R is hydrogen, hydrocarbyl or substituted hydrocarbyl, for instance Ci_ 30 hydrocarbyl, and R is hydrogen, hydrocarbyl or substituted hydrocarbyl, for instance Ci_ 30 hydrocarbyl, and R is hydrogen, hydrocarbyl or substituted hydrocarbyl, for instance Ci_ 30 hydrocarbyl, and R is hydrogen, hydrocarbyl or substituted hydrocarbyl, for
  • Ci_ 3 o hydrocarbyl.
  • R and R are the same.
  • R and R are different.
  • ethylene is unsubstituted.
  • the reaction is catalyzed by any catalyst apparent to those of skill in the art, or mixtures thereof. Exemplary catalysts are described herein including, for instance, metathesis
  • the methods are also applicable to mixtures of
  • intermediates of such a reaction comprising, for instance,
  • 1,3-butadiene and acrylic acid by reacting muconic acid with ethylene in the presence of a metathesis catalyst under conditions sufficient to produce at least one of 1,3-butadiene and acrylic acid.
  • methods for producing at least one of 1,3-butadiene and an ester of acrylic acid by reacting an ester of muconic acid with ethylene in the presence of a metathesis catalyst under conditions sufficient to produce at least one of 1,3-butadiene and an ester of acrylic acid.
  • the muconic acid ester can be produced by any method apparent to those of skill in the art.
  • the methods comprise providing microbially-derived muconic acid, forming one or more of a cis,cis-muconic acid ester, a cis,trans-muconic acid ester, and a trans ,trans-muconic acid ester or a mixture thereof from the microbially-derived muconic acid, and reacting the one or more muconic acid esters with ethylene in the presence of a metathesis catalyst to form one or more acrylic acid esters.
  • Certain variations of the methods comprise providing microbially-derived muconic acid, forming one or more of a cis,cis-muconic acid ester, a cis,trans-muconic acid ester, and a trans,trans-muconic acid ester or a mixture thereof from the microbially-derived muconic acid, and reacting the one or more muconic acid esters with ethylene in the presence of a metathesis catalyst to form one or more acrylic acid esters and 1,3-butadiene.
  • Some methods comprise reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst in a reactor to produce gaseous reaction products in the reactor, and obtaining 1,3-butadiene from the gaseous reaction products.
  • the methods comprise withdrawing at least a portion of gaseous reaction products from the reactor during the reaction.
  • Certain variations of the methods comprise reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst in a reactor to produce one or more reaction products in a liquid phase in the reactor, and obtaining acrylic acid or an acrylic acid ester from the liquid phase.
  • the method may comprise withdrawing at least a portion of gaseous content in a head space during the reaction.
  • Some variations of the methods comprise reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst in a reactor to produce one or more reaction products in a gas phase in the reactor and one or more reaction products in a liquid phase in the reactor, obtaining 1,3-butadiene from the gaseous reaction products, and obtaining acrylic acid or an acrylate ester from the liquid phase.
  • the methods may comprise withdrawing at least a portion of the gaseous reaction products from the reactor during the reaction.
  • any suitable metathesis catalyst or combination of catalysts may be used.
  • the metathesis catalyst comprises ruthenium.
  • the catalyst is a second generation Grubbs catalyst or a second generation Hoveyda-Grubbs catalyst.
  • reactors for carrying out the methods and reactors comprising one or more of the reactants, intermediates and products described herein.
  • industrial chemicals, polymers, and oils derived from 1,3-butadiene made from the methods described herein
  • industrial chemicals, polymers and oils derived from acrylic acid or esters of acrylic acid made from the methods described herein.
  • acrylic acid, or acrylates are synthesized using microbially-derived muconic acid and optionally plant-derived ethylene, such industrial chemicals, polymers and oils may be synthesized with little or no carbon content originating from fossil fuels.
  • FIGURE 1 A provides a schematic diagram showing the synthesis of one mole
  • FIGURE IB shows a reaction mechanism, with an inset providing a GC-FID spectrum of reaction products detected in the head space showing a retention time consistent with that of 1,3 -butadiene, 1-butene and/or 2-butene. It should be noted that the GC-FID described for Examples 8-126 was used to prepare the inset, and the column cannot resolve 1,3- butadiene from butene.
  • FIGURE 2 depicts an experimental apparatus used to recover gaseous products from the reactor head space for Examples 2-7.
  • FIGURE 3 A provides a non-limiting example of a reactor that can be used to carry out methods described herein.
  • FIGURE 3B provides a non-limiting example of a reactor that can be used to carry out methods described herein.
  • FIGURE 4A shows a GC-FID spectrum for the liquid phase reaction mixture for
  • FIGURES 4B-4C shows GC-FID spectra of toluene comprising reaction products collected from the reactor head space for Example 2.
  • FIGURE 4D shows a GC-MS spectrum for the liquid phase reaction mixture of
  • FIGURE 4E shows a mass spectrum for the peak at 5.319 minutes (reference
  • FIG. 4D for the reaction mixture for Example 2 (upper trace), as compared with a mass spectrum of butyl acrylate standard obtained from NIST (lower trace).
  • FIGURE 4F shows a mass spectrum for the peak at 7.376 min (reference FIG.
  • FIGURE 4G shows a GC-MS spectrum of toluene comprising reaction products collected from the reactor head space for Example 2.
  • FIGURE 4H shows a mass spectrum for the peak at 2.432 minutes (reference
  • FIG. 4G for toluene comprising reaction products collected from the reactor head space for Example 2.
  • FIGURE 5A shows a GC-FID spectrum for the liquid phase reaction mixture for
  • FIGURES 5B-5D shows a GC-FID spectrum for toluene comprising reaction products collected from the reactor head space for Example 3.
  • FIGURE 5D includes overlays showing GC-FID spectra for toluene comprising reaction products collected from the reactor head space for Example 2, for a 1,3-butadiene standard, and for a sample from Example 3 co- injected with 1,3-butadiene.
  • FIGURE 5E shows a GC-MS spectrum for the liquid phase reaction mixture of
  • FIGURE 5F shows a mass spectrum for the peak at 5.316 minutes (reference
  • FIG. 5E for the liquid phase reaction mixture for Example 3 (upper trace), as compared with a mass spectrum of butyl acrylate standard obtained from NIST (lower trace).
  • FIGURE 5G shows GC-MS for spectra for toluene comprising reaction products collected from the reactor head space for Example 3.
  • FIGURE 5H shows a mass spectrum for the peak at 2.432 minutes (reference
  • FIG. 5G for toluene comprising reaction products collected from the reactor head space for Example 3.
  • FIGURE 6A shows a GC-FID spectrum for the liquid phase reaction mixture for
  • FIGURE 6B shows a GC-FID spectrum for a butyl acrylate standard (upper trace), and overlays of the GC-FID spectrum for the butyl acrylate standard and the GC-FID spectrum for the liquid phase reaction mixture of Example 6 (lower trace).
  • FIGURE 6C shows a GC-FID spectrum of CDCI 3 comprising reaction products collected from the reactor head space for Example 6.
  • FIGURE 6D shows a GC-MS spectrum for the liquid phase reaction mixture of
  • FIGURE 6E shows a mass spectrum for the peak at 5.316 minutes (reference
  • FIG. 6D for the liquid phase reaction mixture of Example 6 (upper trace), compared with that of a NIST butyl acetate standard (lower trace).
  • FIGURE 6F shows a GC-MS spectrum for CDCI 3 comprising reaction products collected from the reactor head space for Example 6.
  • FIGURE 6G shows a mass spectrum for the peak at 2.441 minutes (reference
  • FIG. 6F for CDCI 3 comprising reaction products collected from the reactor head space for Example 6.
  • FIGURE 6H shows a GC-MS spectrum for a 1,3-butadiene standard (upper trace), and a mass spectrum for the peak at 2.433 minutes (lower trace).
  • FIGURE 6I-6K show proton NMR spectra for CDCI 3 comprising reaction products collected from the reactor head space for Example 6. Note that the coupling constants inset into FIG. 6 J are literature values.
  • FIGURE 6L-6O show C 13 NMR spectra for CDC13 comprising reaction products collected from the reactor head space for Example 6.
  • FIGURE 7A shows GC-FID spectra for toluene comprising reaction products collected from the reactor head space for Example 7, and overlays of a GC-FID spectrum for a 1,3-butadiene standard, and a GC-FID spectrum for the sample for Example 7 co-injected with a 1,3-butadiene standard.
  • FIGURE 7B shows a GC-FID spectrum for a butyl acrylate standard (upper trace), and overlays of the GC-FID spectra for the butyl acrylate standard and the liquid phase reaction mixture for Example 7 (lower trace).
  • FIGURE 8 provides a graph of mol butyl acrylate formed as a function of mole di-n-butyl muconate converted for Examples 8-126.
  • the solid line indicates a slope of 2, in which 2 moles butyl acrylate are formed per mole di-n-butyl muconate converted.
  • Muconic acid is known to have three stereoisomers: cis,cis-muconic acid, trans ,trans-muconic acid, and cis,trans-muconic acid. Unless specifically indicated otherwise, "muconic acid” as used herein refers to any isomer, or any mixture thereof.
  • Cis,cis-muconic acid has the structure:
  • Cis,trans-muconic acid has the structure:
  • Trans,trans-muconic acid has the structure:
  • moconate ester and “muconate” are used interchangeably, and each term encompasses diesters and monoesters of muconic acid, and mixtures thereof.
  • R 1 can be any aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted.
  • R and R are each individually any aliphatic or aromatic hydrocarbyl
  • a symmetric diester is a diester in which R and R are the same.
  • An asymmetric diester is a diester in which R 1 and R 2 are different.
  • muconic acid esters any one of or any combination of three isomers may exist, cis,cis-muconic acid ester, cis,trans muconic acid ester, and trans,trans muconic acid ester. Muconic acid esters also encompass mixtures of the isomers.
  • Cis,cis-dialkyl muconate [(2Z,4Z-dialkyl hexa-2,4-dienedioate)] has the structure:
  • R can be aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted, for example any alkyl group (e.g., a C1-C30 alkyl group, such as a C1-C20 alkyl group or a C1-C10 alkyl group).
  • R n-butyl
  • cis,cis-dibutyl muconate [(2Z,4Z-dibutyl hexa-2,4- dienedioate)] has the structure:
  • Cis,trans-dialkyl muconate [(2Z,4E-dialkyl hexa-2,4-dienedioate)] has the
  • R can be any aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted, for example any alkyl group (e.g., a C1-C30 alkyl group, such as a C1-C20 alkyl group or a C1-C10 alkyl group).
  • alkyl group e.g., a C1-C30 alkyl group, such as a C1-C20 alkyl group or a C1-C10 alkyl group.
  • Trans,trans-dialkyl muconate ((2E,4E-dialkyl hexa-2,4-dienedioate)] has the structure:
  • R can be any aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted, for example any alkyl group (e.g., a C1-C30 alkyl group, such as a C1-C20 alkyl group or a C1-C10 alkyl group).
  • alkyl group e.g., a C1-C30 alkyl group, such as a C1-C20 alkyl group or a C1-C10 alkyl group.
  • Acrylic acid also known as 2-propenoic acid, has the structure:
  • Acrylic acid ester or “acrylate ester” or “acrylate” refers to an ester of acrylic acid having the structure: where R can be any aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted, for example any aliphatic or aromatic hydrocarbyl group that is unsubstituted or substituted.
  • ethenolysis of muconic acid or a muconic acid ester refers to a reaction between muconic acid or muconic acid ester and ethylene in the presence of a metathesis catalyst such that one or more cross-metathesis products between ethylene and muconic acid or between ethylene and a muconic acid ester are formed.
  • Ethylene can be unsubstituted or substituted with any substituting group described herein. In particular embodiments, ethylene is unsubstituted.
  • Hydrocarbyl refers to a group containing one or more carbon atom backbones and hydrogen atoms, and the group may optionally contain one or more heteroatoms. Where the hydrocarbyl group contains heteroatoms, the heteroatoms may form one or more functional groups known to one of skill in the art. Hydrocarbyl groups may contain cycloaliphatic, aliphatic, or aromatic groups or any combination thereof. Aliphatic segments may be straight or branched. Aliphatic and cycloaliphatic groups may include one or more double and/or triple carbon-carbon bonds.
  • hydrocarbyl groups include alkyl, alkenyl, alkynyl, aryl, cycloalkyl, cycloalkenyl, alkaryl and aralkyl groups. Cycloaliphatic groups may contain both cyclic moieties and noncyclic portions.
  • the hydrocarbyl group is a saturated or unsaturated, cyclic or acyclic, unsubstituted or substituted C 1 -C30 hydrocarbyl group (e.g., C 1 -C20 alkyl, C 1 -C20 alkenyl, C 1 -C20 alkynyl, cycloalkyl, aryl, aralkyl and alkaryl).
  • a substituted hydrocarbyl group can be substituted with any described moiety, including, but not limited to, one or more moieties selected from the group consisting of halogen (fluoro, chloro, bromo or iodo), alkyl, haloalkyl, hydroxyl, amino, alkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfonic acid, sulfate, phosphonic acid, phosphate, or phosphonate, either unprotected, or protected as necessary, as known to those skilled in the art, for example, as taught in Greene, et ah, Protective Groups in Organic Synthesis, John Wiley and Sons, Second Edition, 1991.
  • halogen fluoro, chloro, bromo or iodo
  • Alkyl refers to a group having the general formula C n H 2n+ i derived from a saturated, straight chain or branched aliphatic hydrocarbon, where n is an integer. In certain embodiments, n is from 1 to about 30, from 1 to about 20, or from 1 to about 10.
  • alkyl groups include Ci-Cs alkyl groups such as methyl, ethyl, propyl, isopropyl, 2- methylpropyl, 2-methylbutyl, 3-methylbutyl, 2,2,-dimethylpropyl, 2-methylpentyl, 3- methylpentyl, 4-methylpentyl, 2-2-dimethylbutyl, 3,3-dimethylbutyl, 2-ethylbutyl, n-butyl, isobutyl, tert-butyl, isopentyl, n-pentyl, neopentyl, n-hexyl, isohexyl, n-heptyl, isoheptyl, n- octyl, isooctyl, n-nonyl, isononyl, n-decyl and isodecyl.
  • An alkyl group may be unsubstituted, or may be un
  • the alkyl group is branched having 1,
  • Non-limiting examples of moieties with which the alkyl group can be substituted are selected from the group consisting of halogen (fluoro, chloro, bromo or iodo), hydroxyl, amino, alkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfonic acid, sulfate, phosphonic acid, phosphate, or phosphonate, either unprotected, or protected as necessary, as known to those skilled in the art, for example, as taught in Greene, et al. ,
  • Cycloaliphatic encompasses “cycloalkyl” and “cycloalkenyl.” Cycloaliphatic groups may be monocyclic or polycyclic. A cycloaliphatic group can be unsubstituted or substituted with one or more suitable substituents.
  • Cycloalkyl refers to a saturated carbocyclic mono- or bicyclic (fused or bridged) ring of 3-12 (e.g., 5-12) carbon atoms.
  • Non-limiting examples of cycloalkyl include C 3 -C 8 cycloalkyl groups, e.g., cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, and cyclooctyl groups and saturated cyclic and bicyclic terpenes. Cycloalkyl groups may be unsubstituted or substituted.
  • Cycloalkenyl refers to a non-aromatic carbocyclic mono- or bicyclic ring of 3 to 12 ⁇ e.g., 4 to 8) carbon atoms having one or more double bonds.
  • Non- limiting examples of cycloalkenyl include C 3 -C 8 cycloalkenyl groups such as cyclopropenyl, cyclobutenyl, cyclopentenyl, cyclohexenyl, cycloheptenyl, cyclooctenyl, and unsaturated cyclic and bicyclic terpenes. Cycloalkenyl groups may be unsubstituted or substituted.
  • Aryl refers to an organic radical derived from a monocyclic or polycyclic aromatic hydrocarbon by removing a hydrogen atom.
  • Non-limiting examples of the aryl group include phenyl, naphthyl, benzyl, or tolanyl group, sexiphenylene, phenanthrenyl, anthracenyl, coronenyl, and tolanylphenyl.
  • An aryl group can be unsubstituted or substituted with one or more suitable substituents.
  • the aryl group can be monocyclic or polycyclic. In some embodiments, the aryl group contains at least 6, 7, 8, 9, or 10 carbon atoms.
  • Non-limiting examples of moieties with which the aryl group can be substituted are selected from the group consisting of halogen (fluoro, chloro, bromo or iodo), hydroxyl, amino, alkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfonic acid, sulfate, phosphonic acid, phosphate, or
  • Numbers may vary by 1 percent, 2 percent, 5 percent, or, sometimes, 10 to 20 percent.
  • described herein are methods for synthesizing 1,3-butadiene, acrylic acid, acrylate esters and derivatives of 1,3-butadiene, acrylic acid, and acrylate esters.
  • the methods may be capable of producing about 2 moles of acrylic acid and one mole 1,3-butadiene per mole muconic acid starting material, about 2 moles acrylate ester and one mole 1,3-butadiene per mole muconic acid diester, or one mole acrylic acid, one mole acrylate ester and one mole 1,3- butadiene per mole muconic acid monoester.
  • microbially- derived muconic acid is used in the methods described herein.
  • FIG. 1 A A schematic of an exemplary reaction scheme employed in the methods described herein is provided in FIG. 1 A.
  • R may be H or any aliphatic or aromatic hydrocarbyl group, substituted or unsubstituted.
  • muconic acid is reacted with ethylene in the presence of a metathesis catalyst to produce at least one of 1,3-butadiene and acrylic acid. In some cases, both 1,3-butadiene and acrylic acid are produced.
  • the reaction conditions may be tuned so that about 2 moles of acrylic acid are produced per mole muconic acid consumed, or about 1 mole 1,3-butadiene is produced per mole muconic acid consumed, or about 2 moles acrylic acid and about 1 mole 1,3-butadiene are produced per mole muconic acid consumed.
  • a muconic acid ester is reacted with ethylene in the presence of a metathesis catalyst to produce at least one of 1,3-butadiene and an acrylate ester. In some cases, both 1,3-butadiene and an acrylate ester are produced.
  • the reaction conditions may be tuned so that about 2 moles of acrylate ester are produced per mole muconic acid ester consumed, or about 1 mole 1,3-butadiene is produced per mole muconic acid ester consumed, or about 2 moles acrylic acid ester and about 1 mole 1,3-butadiene are produced per mole muconic acid ester consumed.
  • the reaction scheme is illustrated with the cis,cis- isomer of the muconic acid or muconic acid ester in FIG. 1 A, the reaction may utilize any isomer or any combination of isomers (i.e., cis,cis- isomer, cis,trans- isomer, trans,trans- isomer, or any combination thereof).
  • reaction scheme is illustrated as using a symmetrical muconic acid diester in which both R groups are the same, variations exist in which a monoester of muconic acid is used, such that the reaction products are 1,3-butadiene, acrylic acid, and an acrylate ester, and other variations exist in which an asymmetric diester is used in which the two R groups are chemically different such that the reaction products are 1,3-butadiene, and 2 chemically different acrylate esters.
  • Some variations of the methods comprise synthesizing acrylic acid or an acrylate ester from muconic acid, muconic acid monoester, or muconic acid diester by reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst.
  • a method may further comprise providing microbially-derived muconic acid and optionally esterifying the microbially-derived muconic acid prior to reaction with ethylene.
  • Some variations of the methods comprise synthesizing 1,3-butadiene from muconic acid, muconic acid monoester, or muconic acid diester by reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst.
  • a method may further comprise providing microbially-derived muconic acid and optionally esterifying the microbially-derived muconic acid prior to reaction with ethylene.
  • the methods include contemporaneous synthesis of 1,3- butadiene and acrylic acid by reacting muconic acid with ethylene in the presence of a metathesis catalyst, or contemporaneous synthesis of 1,3-butadiene and one or more acrylate esters by reacting a muconic acid ester with ethylene in the presence of a metathesis catalyst.
  • the method may further comprise providing microbially-derived muconic acid and optionally esterifying the microbially-derived muconic acid prior to reaction with ethylene.
  • Muconic acid used in the methods described herein can be obtained from any viable source or prepared by any technique apparent to one of skill in the art.
  • muconic acid is derived from a microbial organism that has been modified to produce muconic acid.
  • Microbially-derived muconic acid may contain any one of or any combination of the cis,cis- , cis-trans- , and trans,trans- isomers of muconic acid.
  • the most prevalent isomer in microbially-derived muconic acid is cis,cis-muconic acid.
  • the most prevalent isomer in microbially-derived muconic acid is cis,trans-muconic acid.
  • the most prevalent isomer in microbially-derived muconic acid is trans ,trans-muconic acid.
  • the muconic acid present in a cell culture medium or fermentation broth used in the microbial synthesis may be used as is, purified, or isolated before undergoing metathesis reaction.
  • purification or isolation methods include extraction, washing, filtration, centrifuge, and combinations thereof.
  • muconic acid is microbially synthesized from readily available carbon sources capable of biocatalytic conversion to erythrose 4-phosphate (E4) and phosphoenolpyruvate (PEP) in microorganisms having a common pathway of aromatic amino acid biosynthesis.
  • Carbon sources used in the synthesis are advantageously renewable, being derived from starch, cellulose and sugars found, for example, in corn, sugar cane, sugar beets, wood pulp and other biomass.
  • One carbon source that can be used to make muconic acid is D- glucose.
  • a host microbial organism is selected such that it produces the precursor of a muconate pathway, either as a naturally produced molecule or as an engineered product that produces the precursor or increases production of the precursor naturally produced by the host organism.
  • an engineered organism is generated from a host that contains the enzymatic capability to synthesize muconate.
  • Increased synthesis or accumulation of muconate can be accomplished by overexpression of nucleic acids encoding one or more muconate pathway enzymes or proteins.
  • Engineered organisms may be designed to produce muconate through overexpression of any number of the nucleic acids encoding muconate biosynthetic pathway enzymes or proteins.
  • Non-limiting examples of pathways that can be used for microbial synthesis of muconic acid are provided in U.S. Pat. No. 5,616,496, International Patent application PCT/US2010/021894, International patent application PCT/US2011/020681, and International patent application PCT/US2010/044606, each of which is incorporated herein by reference in its entirety.
  • Host microbial organisms suitable for synthesizing muconic acid may be selected from genera possessing an endogenous common pathway of aromatic amino acid biosynthesis.
  • the host cells are recombinantly modified to produce the muconic acid, or a precursor thereof.
  • suitable host cells include any Archae, prokaryotic, or eukaryotic cell. Examples of an Archae cell include, but are not limited to those belonging to the genera: Aeropyrum, Archaeoglobus, Halobacterium, Methanococcus,
  • Methanobacterium Pyococcus, Sulfolobus, and Thermoplasma.
  • Archae strains include but are not limited to: Aeropyrum pernix, Archaeoglobus fulgidus, Methanococcus jannaschii, Methanobacterium thermoautotrophicum, Pyococcus abyssi, Pyococcus horikoshii, Thermoplasma acidophilum, Thermoplasma volcanium.
  • Examples of a procaryotic cell include, but are not limited to those belonging to the genera: Agrobacterium, Alicyclobacillus, Anabaena, Anacystis, Arthrobacter, Azobacter, Bacillus, Brevibacterium, Chromatium, Clostridium, Corynebacterium, Enterobacter, Erwinia, Escherichia, Lactobacillus, Lactococcus, Mesorhizobium, Methylobacterium, Microbacterium, Phormidium, Pseudomonas, Rhodobacter, Rhodopseudomonas, Pvhodospirillum, Rhodococcus, Salmonella, Scenedesmun, Serratia, Shigella, Staphlococcus, Strepromyces, Synnecoccus, and Zymomonas.
  • prokaryotic bacterial strains include but are not limited to: Bacillus subtilis, Bacillus amyloliquefacines, Brevibacterium ammoniagenes, Brevibacterium immariophilum, Clostridium beigerinckii, Enterobacter sakazakii, Escherichia coli, Lactococcus lactis, Mesorhizobium loti, Pseudomonas aeruginosa, Pseudomonas mevalonii, Pseudomonas pudica, Rhodobacter capsulatus, Rhodobacter sphaeroides, Rhodospirillum rubrum, Salmonella enterica, Salmonella typhi, Salmonella typhimurium, Shigella dysenteriae, Shigella flexneri, Shigella sonnei, Staphylococcus aureus, and the like.
  • non-pathogenic strains include but are not limited to: Bacillus subtilis, Escherichia coli, Lactibacillus acidophilus, Lactobacillus helveticus, Pseudomonas aeruginosa, Pseudomonas mevalonii, Pseudomonas pudita, Rhodobacter sphaeroides, Rodobacter capsulatus, Rhodospirillum rubrum, and the like.
  • Examples of eukaryotic cells include but are not limited to fungal cells.
  • fungal cell examples include, but are not limited to those belonging to the genera:
  • Candida Chrysosporium, Cryotococcus, Fusarium, Kluyveromyces, Neotyphodium, Neurospora, Penicillium, Pichia, Saccharomyces, Trichoderma and Xanthophyllomyces
  • eukaryotic strains include but are not limited to:
  • Pichia thermotolerans Pichia trehalophila, Pichia stipitis, Streptomyces ambofaciens,
  • Streptomyces aureofaciens Streptomyces aureus, Saccaromyces bayanus, Saccaromyces boulardi, Saccharomyces cerevisiae, Streptomyces fungicidicus, Streptomyces
  • non-pathogenic strains include but are not limited to: Fusarium graminearum, Fusarium venenatum, Pichia pastoris, Saccaromyces boulardi, and
  • GRAS Generally Regarded As Safe
  • strains include: Bacillus subtilis, Lactibacillus acidophilus, Lactobacillus helveticus, and Saccharomyces cerevisiae.
  • the strain has been designated by the Food and Drug Administration as Generally Regarded As Safe.
  • host organisms include mutant strains of Escherichia coli genetically engineered to express selected genes endogenous to Klebsiella pneumoniae and Acinetobacter calcoaceticus.
  • an E. coli mutant for use in making muconic acid is E. coli AB2834, an auxotrophic mutant that is unable to catalyze the conversion of
  • dehydoshikimate an intermediate along the common pathway of aromatic amino acid biosynthesis, into shikimic acid due to a mutation in the aroE locus which encodes the enzyme shikimate dehydrogenase.
  • the common pathway of aromatic amino acid biosynthesis produces the aromatic amino acids phenylalanine, tyrosine, and tryptophan in bacteria and plants.
  • the common pathway ends with the molecule chorismate, which is subsequently converted into phenylalanine, tyrosine, and tryptophan by three separate terminal pathways.
  • DHS dihydroxy-3-dehydroshikimate dehydratase
  • aroZ 3-dehydroshikimate dehydratase
  • action of this enzyme of DHS produces protocatechuate.
  • Protocatechuate is thereafter converted to catechol via the enzyme known as protocatechuate decarboxylase (aroY).
  • the catechol thus formed is converted to cis,cis-muconic acid by the action of the enzyme catechol 1 ,2-dixoygenase (catA).
  • the three enzymes (aroZ, aroY, and catA) catalyzing the biosynthesis of cis,cis- muconate from DHS can be expressed in a host cell using recombinant DNA comprising genes encoding these three enzymes under control of a suitable promoter. Carbon flow can be forced away from the pathway of aromatic amino acid synthesis and into the divergent pathway to produce cis,cis muconate. The cis,cis muconate thus formed can accumulate in the extracellular medium which can be separated from the cells by centrifuge, filtration, or any other method known in the art.
  • Muconic acid esters may be obtained from any source or prepared by any method apparent to those of skill in the art.
  • muconic acid esters are prepared by esterification of muconic acid. Any suitable esterification method known in the art may be used to obtain the desired monoester or diester.
  • Muconic acid may be contacted with an esterifying agent under conditions suitable to form the desired ester.
  • esterifying agents include alkanols (e.g., Ci-Cio alkanols), polyols, polyalkylene glycols having one or more hydroxyl groups and one or more ether groups, aryl alcohols (e.g.
  • muconic acid is contacted with one or more esterifying agents in the presence of one or more acids.
  • suitable acids include sulfuric acid, nitric acid, phosphoric acid, hydrochloric acid, p-toluene sulfonic acid, and Lewis acids.
  • the esterification reaction may be carried out in the presence of acid at an elevated temperature, e.g., about 50°C, 60°C, 70°C, 80°C, 90°C, 100°C, 110°C, 120°C, 130°C, 140°C, or 150°C.
  • muconic acid may be esterified by reacting with an alcohol in the presence of a base (e.g., pyridine, a tertiary amine, or aqueous NaOH).
  • a base e.g., pyridine, a tertiary amine, or aqueous NaOH.
  • the methods may comprise isomerizing the muconic acid or muconic acid ester prior to the metathesis reaction. In some instances, it may be desired to isomerize muconic acid to form predominantly the cis,cis- isomer, the cis,trans- isomer, or the trans,trans isomer.
  • muconic acid produced via microbial synthesis may be the cis,cis-muconic acid isomer or a mixture of cis,cis-muconic acid and cis,trans- muconic acid, and it may be desired to isomerize the cis,cis muconic acid (or ester) to form cis,trans muconic acid or trans,trans muconic acid (or ester), or to isomerize cis,trans muconic acid to form cis,cis-muconic acid or trans,trans-muconic acid before the metathesis reaction. Isomerization may occur using any suitable isomerization conditions and appropriate isomerization conditions and catalysts (if needed).
  • the cis,cis- isomer can be isomerized to the cis,trans- isomer in boiling water without a need for a catalyst.
  • iodine is used as a catalyst for isomerization, and in some variations iodine-catalyzed photochemical isomerization of cis,cis- or cis,trans- isomers to trans,trans- isomers can be used.
  • Non-limiting examples of methods for isomerizing muconic acid are provided in International Patent Publication WO 2010/148063 and in Elvidge J A et al., Journal of the Chemical Society, Chemical Society, Letchworth, GB, 1 January 1950 (1950-01-01), pages 2235-2241, each of which is incorporated by reference herein in its entirety. It should be understood that esterification of muconic acid may occur prior to isomerization to form desired isomers, or isomerization to form desired isomers may occur prior to esterification.
  • R and R may independently be H or any hydrocarbyl group, with the proviso that R and R
  • R and R are not both H.
  • R and R are the same, and in other cases, R and R are different.
  • 1,3-butadiene is formed.
  • one or more acrylate esters are formed.
  • both 1,3-butadiene and one or more acrylate esters are formed.
  • R and R are Ci-Cio alkyl groups.
  • R and R are Ci-Cio alkyl groups.
  • R and R may be selected from the group consisting of methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, t-butyl, n-pentyl, isopentyl, 2-methylpentyl, 3-methylpentyl, 2-ethylbutyl, n-hexyl, isohexyl, 2-methylhexyl, 3-methylhexyl, 4-methylhexyl, n-heptyl, isoheptyl, 2-methylheptyl, 3- methylheptyl, 4-methylheptyl, 5-methylheptyl, 2-ethylhexyl, 3-ethylhexyl, 4-ethylhexyl, 5- ethylhexyl, 6-ethylhexyl, n-octyl, isooctyl, 2-methyloctyl, 3-methyloctyl, 4-methyl
  • dimethyl muconate is reacted with ethylene in the presence of a metathesis catalyst to form 1,3-butadiene and/or methyl acrylate.
  • diethyl muconate is reacted with ethylene in the presence of a metathesis catalyst to form 1,3-butadiene and/or ethyl acrylate.
  • di-n- propyl muconate is reacted with ethylene in the presence of a metathesis catalyst to form 1,3- butadiene and/or propyl acrylate.
  • di-n-butyl muconate is reacted with ethylene in the presence of a metathesis catalyst to form 1,3-butadiene and/or n-butyl acrylate.
  • the reactions are catalyzed.
  • the catalyst can be any catalyst deemed suitable by the practitioner of skill.
  • the catalyst is a metathesis catalyst, or a mixture thereof.
  • Exemplary catalysts are described in the sections below. Reaction conditions such as temperature, pressure, reaction time, solvent, amount of reactants, amount of catalyst, and so forth, are within the skill of the practitioner in the art. Exemplary conditions are provided herein.
  • any suitable metathesis catalyst, or any suitable combination of catalysts useful for metathesis may be used.
  • metathesis catalysts include metal carbene catalysts based on transition metals, such as ruthenium, osmium, nickel, tungsten, osmium, chromium, rhenium, or molybdenum wherein at least one ligand or complexing agent is coordinated with or bound to the metal atom.
  • ligands include phosphines, halides, and stabilized carbenes. It should be understood that some catalysts include more than one metal, and in some cases one or more metal-containing co-catalysts is used.
  • a metathesis catalyst is selected that favors production of the desired ethenolysis reaction products over side reactions such as self-metathesis.
  • Self- metathesis occurs when a substrate-bound catalyst reacts with another substrate molecule rather than ethylene, or ethylene reacts with another ethylene molecule instead of a substrate molecule.
  • a metathesis catalyst and reaction conditions are selected to favor kinetically controlled product ratios over thermodynamically controlled product ratios.
  • a metathesis catalyst based on ruthenium is used.
  • ruthenium-based metathesis catalysts include: ruthenium carbene complexes such as phosphine-containing or phosphine-free ruthenium carbene species which may or may not contain carbene-containing ligands; phosphine-containing or phosphine-free ether-tethered ruthenium alkylidene derivatives; stable 16-electron ruthenium carbene complexes; ruthenium carbene species having ligands comprising Lewis bases such as pyridine; ruthenium benzylidene complexes; and ruthenium trichlorides prepared from late transition metal salts.
  • ruthenium-based catalysts include dichloro-3,3-diphenylvinylcarbene- bis(trycyclohexylphosphine)ruthenium(II)bis(tricyclohexylphosphine)benzylidene ruthenium dichloride, bis(tricyclohexylphosphine benzylidene ruthenium dibromide,
  • L and L' refer to electron-donating moieties
  • X refers to mono-anionic moieties (e.g., halides such as chlorides, bromides, iodides), and one alkylidene group
  • RG refers to H or an aliphatic or aromatic group or a group containing one or more heteroatoms.
  • both L and L' are phosphines (e.g., trialkyl phosphines, triaryl phosphines, diarylalkyl phosphines) (first generation Grubbs catalysts).
  • one of L,L' is a phosphine group, and the other of L, L' is a saturated N-heterocyclic carbene (second generation Grubbs catalysts).
  • the methods employ a first generation Grubbs catalyst, or a variant or derivative thereof.
  • a first generation Grubbs catalyst or a variant or derivative thereof.
  • the methods employ a second generation Grubbs catalyst, or a variant or derivative thereof.
  • One exemplary second generation Grubbs catalyst also known as [l,3-bis-(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro
  • a catalyst dichloro[l,3-bis(2-methylphenyl)-2- imidazolidinylidene](2-isopropoxyphenylmethylene)ruthenium(II) having structure (4) is used:
  • a catalyst dichloro[l,3-bis(2,6-isopropylphenyl)-2- imidazolidinylidene](2-isopropoxyphenylmethylene)ruthenium(II) having structure (5) is used:
  • a catalyst dichloro[l,3-bis(2,6-isopropylphenyl)-2- imidazolidinylidene](benzylidene)(tricyclohexylphosphine)ruthenium(II) and structure (6) is used:
  • a catalyst dichloro[l,3-bis(2,4,6-trimethylphenyl)-2- imidazolidinylidene][(tricyclohexylphosphoranyl)methylidene]ruthenium(II) tetrafluoroborate and having structure (11) is used:
  • a catalyst dichloro[l,3-bis(2,4,6-trimethylphenyl)-2- imidazolidinylidene][3-(2-pyridinyl)propylidene]ruthenium(II)and having structure (12) is used:
  • a catalyst dichloro[l,3-Bis(2-methylphenyl)-2- imidazolidinylidene](benzylidene)(tricyclohexylphosphine)ruthenium(II) and having formula (13) is used:
  • a Hoveyda-Grubbs catalyst or a variant or derivative thereof is used.
  • one exemplary 1 st generation Hoveyda-Grubbs catalyst is dichloro(o- isopropoxyphenylmethylene)(tricyclohexylphosphine)ruthenium(II) having structure (14); and one exemplary 2 nd generation Hoveyda-Grubbs catalyst is (l,3-Bis-(2,4,6-trimethylphenyl)-2- imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium having structure (15):
  • cyclic (alkyl)(amino)carbene (CAAC) ruthenium catalysts are used.
  • a metathesis catalyst having structure (16) may be used:
  • a catalyst [l,3-bis(2,6-di-i-propylphenyl)-4,5- dihydroimidazol-2-ylidene]-[2-i-propoxy-5-(trifiuoroacetamido)phenyl]methylene ruthenium(II) dichloride, having structure (17) is used:
  • a catalyst l,3-Bis(2,4,6-trimethylphenyl)-4,5- dihydroimidazol-2-ylidene[2-(i-propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methylene ruthenium(II) dichloride, having structure (19) is used:
  • a catalyst tricyclohexylphosphine[4,5-dimethyl-l,3-bis(2,4,6- trimethylphenyl)imidazol-2-ylidene] [2-thienylmethylene]ruthenium(II) dichloride, having structure (20) is used:
  • a catalyst tricyclohexylphosphine[ 1 ,3-bis(2,4,6- trimethylphenyl)imidazol-2-ylidene] [2-thienylmethylene]ruthenium(II) dichloride, having structure (21) is used:
  • a catalyst tricyclohexylphosphine[ 1 ,3-bis(2,4,6- trimethylphenyl)imidazol-2-ylidene] [3 -phenyl- 1 H-inden- 1 -ylidene]ruthenium(II) dichloride, having structure (22) is used:
  • N-aryl,N-aryl N-heterocyclic carbene (NHC) ruthenium metathesis catalysts are used.
  • N-aryl,N-alkyl N-heterocyclic carbene (NHC) ruthenium metathesis catalysts are used.
  • Non-limiting examples of N-aryl, N-alkyl NHC ruthenium metathesis catalysts are provided in R.M. Thomas et al., J. Am. Chem. Soc. 2011, 133, 7490-7496, which is incorporated by reference herein in its entirety.
  • a Schrock metathesis catalyst or a variant or derivative thereof is used.
  • a Schrock-Hoveyda metathesis catalyst or a variant or derivative thereof is used.
  • a molybdenum-based catalyst is used.
  • a molybdenum alkoxyimidoalkylidene catalyst may be used.
  • a catalyst 2,6- Diisopropylphenylimido-neophylidene[(S)-(-)-BIPHEN]molybdenum(VI), having structure (23) is used:
  • a catalyst tris(N-tert-butyl-3,5- dimethylanilino)molybdenum(III), having structure (24) is used:
  • a ligand or other stabilizing compound may be added to the metathesis reaction mixture to stabilize the catalyst and/or to modify the distribution of products.
  • ligands or stabilizing compounds that can be added to the metathesis reaction include trialkylphosphines (e.g., tricyclohexylphosphine, tricyclopentylphosphine); triphenylphosphine; diarylalkylphines such as diphenylcylohexylphosphine; pryidines such as 2,6-dimethylpyridine or 2,4,6-trimethylpyridine; phosphine oxides; and phosphinites.
  • trialkylphosphines e.g., tricyclohexylphosphine, tricyclopentylphosphine
  • triphenylphosphine diarylalkylphines such as diphenylcylohexylphosphine
  • pryidines such as 2,6-dimethylpyr
  • the quantity of metathesis catalyst that is used relative to the amount of muconic acid or muconic acid ester may be any quantity that provides for desired products at a desired yield in a desired reaction time.
  • the ratio moles muconic acid or muconate:moles catalyst is about 10: 1 or greater, about 20: 1 or greater, about 30: 1 or greater, about 40: 1 or greater, about 50: 1 or greater, about 100: 1 or greater, about 500: 1 or greater, about 1000: 1 or greater, about 5000: 1 or greater, about 10,000: 1 or greater, about 50,000: 1 or greater, about 100,000: 1 or greater, or even higher.
  • the catalyst is present at an amount such that the ratio moles muconic acid or muconate:moles catalyst is less than about
  • the metathesis catalyst is homogeneous, meaning the catalyst is dissolved in a liquid reaction mixture.
  • Homogeneous catalyst loadings may be in a range from about 0.000001 mol% to about 10 mol%, from about 0.00001 mol% to about 10 mol%, from about 0.0001 mol% to about 10 mol%, from about 0.0001 mol% to about 10 mol%, from about 0.001 mol% to about 10 mol%, from about 0.01 mol% to about 10 mol%, from about 0.02 mol % to about 10 mol %, from about 0.05 mol% to about 10 mol%, from about 1 mol% to about 10 mol %, from about 2 mol% to about 10 mol%, from about 0.01mol% to about 5 mol%, from about 0.02mol% to about 5 mol%, from about 0.05mol% to about 5
  • a homogeneous catalyst loading is about 0.000001 mol%, 0.000005 mol%, 0.00001 mol%, 0.00005 mol%, 0.0001 mol%, 0.0005 mol%, 0.001 mol%, 0.005 mol%, 0.01 mol%, 0.02 mol%, 0.05 mol%, 0.1 mol%, 0.2 mol%, 0.5 mol%, 1 mol%, 1.5 mol%, 2 mol%, 2.5 mol%, 3 mol%, 3.5 mol%, 4 mol%, 4.5 mol%, 5 mol%, 5.5 mol%, 6 mol%, 6.5 mol%, 7 mol%, 7.5 mol%, 8 mol%, 8.5 mol%, 9 mol%, 9.5 mol%, or 10 mol%.
  • the metathesis catalyst is heterogeneous, e.g., bound to, deposited on, or otherwise supported on any catalyst support known in the art.
  • Use of a heterogeneous catalyst may simplify recovery of the catalyst (e.g., for recycling), increase catalyst strength, and reduce catalyst loss.
  • Non-limiting examples of catalyst supports include silicas, aluminas, silica- aluminas, aluminosilicates, including zeolites and other crystalline porous aluminosilicates, titanias, titanosilicates, zirconia, magnesium oxide, carbon, and reticulated cross-linked polymeric resins, such as functionalized cross-linked polystyrenes (e.g., chloromethyl- functionalized cross-linked polystyrenes). Any suitable method may be used to deposit a catalyst onto a support. Non-limiting techniques include impregnation, ion-exchange, deposition-precipitation, and vapor deposition. In some cases, the catalyst is chemically bound to a support through one or more covalent bonds. Methods for chemically binding
  • organometallic complexes to polymeric supports is known, and is described for example in S.B. Roscoe et al, J. Polymer Science: Part A: Polymer Chem., 2000, 38, 2979-2992 and in M.
  • any suitable loading of the catalyst on a support may be used to provide the desired reactivity, reaction rate, and reaction products.
  • the catalyst may be loaded onto a support in an amount in a range between about 0.01 wt% and 50 wt%, in a range between about 0.05 wt% and 20 wt%, in a range between about 1 wt% and 10 wt%, where wt % is based on the total weight of the catalyst and support.
  • a catalyst loading may be about 0.01 wt%, 0.05 wt%, 1 wt%, 2 wt%, 3 wt%, 4 wt%, 5 wt%, 6 wt %, 7 wt %, 8 wt %, 9 wt%, 10 wt%, 11 wt%, 12 wt%, 13 wt%, 14 wt %, 15 wt %, 20 wt %, 25 wt%, 30 wt%, 35 wt %, 40 wt%, 45 wt %, or 50 wt %.
  • reaction temperatures may be in a range from about 0°C to about 100°C, or from about 20°C to about 100°C, or from about 30°C to about 80°C. In some variations, the reaction temperature is about 30°C, 35°C, 40°C, 45°C, 50°C, 55°C, 60°C, 65°C, 70°C, 75°C or 80°C. Reactions may be carried out at neutral pH, or at a pH that is acidic or basic.
  • Any suitable solvent may be used, e.g., dichloromethane, toluene, dichloroethane, alcohols, water, other aqueous solutions, alcohol/water mixtures, and the like.
  • esterification of muconic acid prior to the metathesis reaction is carried out so that a desired acrylate results.
  • esterification of muconic acid is carried out to make a muconic acid ester that is soluble in solvents in which the metathesis catalyst is soluble.
  • sonication is used to aid in solubilizing one or both of the muconic acid or ester and the metathesis catalyst.
  • the metathesis reaction can be carried out in a closed reactor with an excess of ethylene.
  • the pressure of ethylene in the reactor can be kept at any level at which the reaction proceeds to provide a desired product mix.
  • the ethylene pressure can be kept at a pressure in a range from about 0.3 bar to about 100 bar, or from about 0.5 bar to about 50 bar, or from about 1 bar to about 50 bar, or from about 5 bar to about 50 bar, or from about 5 bar to about 40 bar, or from about 10 bar to about 40 bar.
  • the ethylene pressure is about 1 bar, 5 bar, 10 bar, 15 bar, 20 bar, 25 bar, 30 bar, 35 bar, 40 bar, 45 bar, or 50 bar.
  • the metathesis reaction is carried out at a temperature in a range from about 30°C to about 80°C and 10-20 bar ethylene pressure. In some variations, the metathesis reaction is carried out at a temperature in a range from about 30°C to about 80°C and 20-30 bar ethylene pressure. In some variations, the metathesis reaction is carried out at a temperature in a range from about 30°C to about 80°C and 30-40 bar ethylene pressure.
  • reaction time can be any time that is long enough to convert a desired amount of starting material to produce a desired product mix, without being so long that undesired secondary reactions involving reaction products occur.
  • Reaction times may depend on catalyst choice, temperature, solvent, type of reactor (e.g., batch or continuous) and/or pressure. In certain variations for batch reactions, reaction times are in a range from about 0.2 hours to about 24 hours, or from about 0.2 hours to about 10 hours, or from about 0.2 hours to about 6 hours (e.g., about 0.2, 0.5, 1, 1.5, 2, 2.5, 3, 4, 5, or 6 hours).
  • reaction conditions and metathesis catalyst can be selected so that about 2 moles acrylic acid are produced per mole muconic acid reactant, or 2 moles acrylate are produced per mole muconic acid ester reactant.
  • reaction conditions and catalyst can be selected so that about 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9 or 2 moles acrylic acid or acrylate are produced per mole reactant.
  • reaction conditions and metathesis catalyst can be selected so that more than one mole acrylic acid or acrylate is produced per mole reactant. In some cases, acrylic acid or an acrylate is produced but no detectable amount of 1,3 -butadiene is produced.
  • reaction conditions and metathesis catalyst are selected so that about 1 mole 1,3- butadiene is produced per mole muconic acid or muconic acid ester reactant. In some variations, reaction conditions and catalyst are selected so that about 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, or 1 mol 1,3-butadiene is produced per mole muconic acid or muconic acid ester reactant. In some cases, 1,3-butadiene is produced but no detectable amount of acrylic acid or acrylate is produced.
  • reaction conditions and metathesis catalyst are selected so that about 2 moles acrylic acid and about 1 mole 1,3-butadiene are produced per mole muconic acid.
  • reaction conditions and catalyst are selected so that about 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9 or 2 moles acrylic acid or acrylate and about 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, or 1 mole 1,3-butadiene are produced per mol muconic acid or muconic acid ester.
  • Examples 2-6 herein illustrate reactions in which both 1,3-butadiene and an acrylate was produced. Because the 1,3-butadiene trapped in a cooled solvent to aid in those Examples 2-6, no quantification of the amount of 1,3-butadiene produced was completed.
  • FIG. 8 illustrates many Examples in which the ratio of moles butyl acrylate produced:moles dibutyl muconate consumed is greater than 1 , many Examples in which the ratio of moles butyl acrylate produced:moles dibutyl muconate consumed is greater than 1.5, and several Examples in which the ratio of moles butyl acrylate produced:moles dibutyl muconate consumed is about 2.
  • the data in FIG. 8 indicates that an ethylene pressure of about 20 - 40 bar (e.g., about 25 bar) promotes formation of butyl acrylate for several metathesis catalysts.
  • the methods comprise obtaining gaseous reaction products
  • Some methods comprise extracting at least a portion of gaseous species in the reactor head space during the course of the reaction. By removing at least a portion of the gaseous reaction products from the head space, the reaction may be driven further to produce more 1,3-butadiene, and/or undesired side reactions (such as undesired secondary reactions or self-metathesis of 1,3- butadiene, undesired secondary reactions or self-metathesis of the penta-2,4-dieneoate intermediate, or reverse reactions) may be inhibited.
  • undesired side reactions such as undesired secondary reactions or self-metathesis of 1,3- butadiene, undesired secondary reactions or self-metathesis of the penta-2,4-dieneoate intermediate, or reverse reactions
  • any suitable scheme and mechanism may be employed to remove at least a portion of the reactor head space during the reaction.
  • contents of the head space are periodically or intermittently removed by opening a valve to a connected lower pressure vessel during the course of the reaction.
  • at least a portion of the contents of the head space is removed by periodically or intermittently evacuating or pumping out the head space during the course of the reaction.
  • a portion of the contents of the reactor head space is continuously or periodically or intermittently bled out of the reactor during the course of the reaction, and an appropriate amount of ethylene is pumped in continuously, periodically, or intermittently to maintain a desired ethylene pressure in the reactor.
  • reactors suitable for carrying out the methods described herein.
  • FIG. 3A One non-limiting example of a reactor that can be used to carry out the reactions described herein using a homogeneous catalyst is shown in FIG. 3A.
  • the liquid phase reaction mixture in the closed reactor comprises solvent, reactant (muconic acid or muconic acid ester), and metathesis catalyst.
  • Ethylene can be directed into the head space (or optionally bubbled into the solvent) using appropriate fixtures until the desired pressure is reached.
  • At least a portion of the contents of the head space (including gaseous reaction products such as 1,3 -butadiene) is allowed to exit from or is extracted from the head space using known techniques.
  • the removal of head space contents can be done in any manner, e.g., on a continuous basis, periodically, or intermittently.
  • the contents of the head space that are removed can then be directed into a separator that is capable of separating ethylene from reaction products such as 1,3 -butadiene.
  • a separator that is capable of separating ethylene from reaction products such as 1,3 -butadiene.
  • Any suitable separator may be used, e.g., a distillation apparatus, a cold trap at a temperature cold enough to liquefy desired reaction products such as 1,3-butadiene but warm enough such that ethylene remains gaseous and can be removed from the separator.
  • Ethylene recovered from the separator can be recycled back into the reactor for reuse.
  • acrylic acid or acrylate reaction products can be isolated from the liquid phase reaction mixture using any known technique. Another example of a reactor is shown in FIG. 3B.
  • one or more of the reaction products is used as it is made in a subsequent chemical reaction.
  • 1,3-butadiene may be reacted with a dienophile, or used in a polymerization reaction while it is still in the reactor or as it is extracted from the reactor.
  • acrylic acid or an acrylate ester may be used in a polymerization reaction while it is still in the reactor or as it is extracted from the reaction mixture.
  • Regular depletion of the desired reaction products may drive the reaction forward and inhibit undesired side reactions, reverse reactions, or secondary reactions.
  • Scenarios in which butadiene, acrylic acid or acrylate are used as they are made or imminently thereafter (before being purified or stored) may be useful if the metathesis reactions described herein are used as a step in part of a larger industrial process (e.g., functionalization, oligomerization or polymerization).
  • the metathesis reactions described herein may be a step or production module within a larger batchwise or continuous industrial process.
  • microbial synthesis of muconic acid may also be included as an upstream step or production module, which optionally feeds into an
  • esterification step or module which feeds into a metathesis reaction to produce 1,3 -butadiene, acrylic acid, or an acrylate, and each of these products is directed into one or more downstream steps or production modules for making industrial chemicals, polymers, oils and the like.
  • reactor configuration (batch mode, continuous, or flow through) may be used to carry out the methods described herein.
  • the 1,3 -butadiene, acrylic acid and one or more acrylic acid esters can be used for any purpose apparent to those of skill in the art. Accordingly, also disclosed herein are industrial chemicals, polymers and oils made using 1,3-butadiene made by any of the methods described herein. For example, a wide variety of butadiene homopolymers or butadiene copolymers may be made using as a monomer or comonomer 1,3-butadiene synthesized from muconic acid or a muconic acid ester using the methods described herein.
  • microbially-derived muconic acid can be used to make butadiene, which in turn, can be used to make industrial chemicals, homopolymers or copolymers of the butadiene, or oils.
  • industrial chemicals, polymers, and oils can be made using acrylic acid or acrylates made by any of the methods described herein.
  • acrylic acid or acrylates made by any of the methods described herein.
  • a wide variety of polymers can be made that incorporate acrylic acid or acrylates made by the methods described herein.
  • microbially-derived muconic acid can be used to make acrylic acid or an acrylate, which in turn, can be used to make industrial chemicals, homopolymers or copolymers of the acrylic acid or acrylate.
  • ethylene derived from plant sources may be used in the metathesis reactions.
  • 1,3-butadiene, acrylic acid, or acrylates are synthesized using microbially- derived muconic acid and optionally plant-derived ethylene
  • such industrial chemicals, polymers and oils may be synthesized with little or no carbon content originating from fossil fuels.
  • chemicals or polymers comprising at least about 30%, at least 40%, at least 50%), at least 60%>, at least 70%>, at least 80%>, at least 90%>, or about 100% carbons originating from a non-fossil fuel carbon source.
  • the number of carbons originating from non-fossil fuel carbon sources can be measured using radiocarbon analysis, e.g., according to any method described in ASTM D6866 - 11 "Standard Test Methods for Determining the Biobased Content of Solid, Liquid, and Gaseous Samples Using Radiocarbon Analysis," which is incorporated herein by reference in its entirety.
  • Certain methods comprise optionally providing microbially-derived muconic acid, optionally esterifying the muconic acid to form an ester of muconic acid, reacting the muconic acid or ester of muconic acid with ethylene in the presence of a metathesis catalyst to form at least one of 1,3-butadiene and acrylic acid, or at least one of 1,3 -butadiene and an acrylate ester at a pressure in a range from about 2 bar to about 50 bar ethylene, and a temperature in a range from about 0°C to about 100°C.
  • the metathesis catalyst comprises ruthenium.
  • the metathesis catalyst comprises a Grubbs catalyst.
  • the methods comprise reacting muconic acid or a muconic acid ester with ethylene in the presence of a metathesis catalyst at a catalyst loading of about 0.005mol% to about 10 mol% (e.g., 0.001 mol% to about 10 mol%, about 0.005 mol% to about 10 mol%, about 0.05 mol% to about 10 mol%, about 0.5mol% to about 5 mol%, about 1 mol% to about 5 mol%, or about 2 mol% to about 5 mol%) at a temperature in a range from about 0°C to about 100°C (e.g., about 20°C to about 100°C, about 20°C to about 80°C, or about 30°C to about 80°C) and an ethylene pressure in a range from about 1 bar to about 100 bar (e.g., about 1 bar to about 80 bar, about 1 bar to about 50 bar, about 5 bar to about 50 bar, or about 5 bar to about 40 bar) to form 1,3-but
  • the catalyst comprises ruthenium.
  • the catalyst is selected from the group consisting of dichloro[l,3-bis(2-methylphenyl)-2-imidazolidinylidene](2- isopropoxyphenylmethylene)ruthenium(II), (l,3-Bis-(2,4,6-trimethylphenyl)-2- imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium, and [ 1 ,3-bis-(2,4,6- trimethylphenyl)-2-imidazolidinylidene]dichloro
  • 2,4-hexadiene is used as the substrate instead of muconic acid or a muconic acid ester.
  • 2,4-hexadiene is observed to react with ethylene in the presence of a metathesis catalyst to form propylene and 1,3-butadiene.
  • a metathesis catalyst e.g., Gl
  • essentially all of the 2,4-hexadiene is converted.
  • Table 1 provides metathesis catalysts used in the Examples.
  • TCI T2358 Tris(N-tert-butyl-3,5-dimethylanilino)molybdenum(III) Mo Horn. T2358
  • GC-FID is carried out using an Agilent GC-FID equipped with an HP-1 column. The temperature is held at 60°C for 3 minutes, ramped at 20°C/min to
  • the carrier gas is hydrogen.
  • GC-MS is carried out using an Agilent GC-MS equipped with an HP-1 column and an MSD detector. The temperature is held at 50°C for 3 minutes, ramped at 25°C/min to 200°C, ramped at 20°C/min to 320°C, and held at 320°C for 5 minutes.
  • the inlet temperature is 250°C, and the carrier gas is helium.
  • a JEOL ECX 400 (400 MHz) spectrometer is used.
  • EXAMPLE 1 Preparation of cis,cis-di-n-butyl muconate from microbially- derived cis,cis-muconic acid.
  • the product was an oil that was adsorbed onto 900g of silica gel. 1L hexanes was added to the flask to ensure uniform adsorption onto silica gel, then solvent was removed by rotovap. The solid silica gel was loaded onto a fritted funnel with 1kg dry silica and the product was eluted with hexanes. The product fractions were combined and solvent removed via rotovap. The resulting oil was adsorbed onto silica gel again, and loaded into a 2kg silica gel column. The produce was eluted with hexane slowly. TLC was used as a test method for product detection. The product fractions were combined and solvent removed by rotovap.
  • Example 2 (RV-650-12), 8.6037g di-n-butyl muconate (prepared as in
  • Example 1 and having about 80% of the cis,cis- isomer, 15%> of the cis,trans- isomer, and 5%> of the trans,trans- isomer by GC-MS and NMR) were dissolved in 8.00 mL toluene (1.08g/ml) and dried over molecular sieves.
  • 0.4321 g 2 nd generation Grubbs catalyst (Sigma- Aldrich catalog number 569747) was dissolved in 12.72 ml toluene dried over molecular sieves to prepare a 0.04 M solution.
  • the head space of the reactor was connected to a gas recovery system (GRS) as shown in FIG. 1 and described as follows.
  • the head space of the reactor was connected via a valve to 2-150ml stainless steel reservoirs connected in series.
  • the outlet of the second stainless steel reservoir was connected via a valve and directed via a needle directed through a rubber septum and the tip of the needle was submerged in 10 ml toluene contained in a 40-ml glass vial cooled to a temperature that is below the boiling point of 1,3-butadiene (-4°C) but is above the boiling point of ethylene (-104°C).
  • the cooling of the vial is accomplished in this Example by immersion in a dry ice/acetone bath at -78°C.
  • the assembled reactor was removed from the glove box and the screws on the reactor head were tightened.
  • the Hastelloy reactor including its associated GRS was installed on a Parr 5000 multiple reactor system, to which was also connected a thermocouple, a pressure transducer, and ethylene line. The system was subjected to 3-cycles of house vacuum/nitrogen back-fill flush while stirring at 300 rpm. Following flushing, the whole system was left under vacuum.
  • the GRS was isolated from the reactor using a valve and the reactor was filled with ethylene to achieve a pressure of 250-290 psi (17- 20 bar). The reactor was heated to 60°C and stirring was increased to 1000 rpm. After 30 minutes the reactor head space was released into the GRS.
  • the reactor was again isolated using a valve, re-pressurized with ethylene and the reaction continued.
  • the contents of the GRS were allowed to slowly bubble through toluene at -78 °C.
  • the latter process was repeated after 50, 70, 90, and 110 minutes (for a total of 5 releases of the reactor head space).
  • heating was discontinued and the reactor head space was completely emptied into the GRS, then bubbled through toluene at -78 °C; and 8 microliters 4-tert-butyl catechol (TBC) solution (0.17 g/mL in methanol) was added to the toluene, which was subsequently analyzed by GC-FID using dodecane as an internal standard.
  • TBC 4-tert-butyl catechol
  • the toluene was stored at -20 °C.
  • the reactor was disassembled, the reaction mixture quenched with 1 mL of 2-propanol,10 microliters of TBC solution (0.17 g/mL in methanol) was added, and the reaction mixture was analyzed by GC-FID using dodecane as an internal standard.
  • % conversion ⁇ 1- [(final area di-n-butyl muconate)/(fmal area dodecane)]/[(initial area di-n-buty muconate)/(initial area dodecane)] ⁇ x 100%.
  • FIG. 4A GC-FID for the liquid phase reaction mixture is shown in FIG. 4A.
  • FIG. 4B-4C GC-FID of the cooled toluene that was used to trap gaseous reaction products from the head space are shown in FIG. 4B-4C.
  • FIG. 4C shows overlaid spectra of GC-FID of the toluene used to trap gaseous reaction products from the head space on the day of the reaction and on the day following the reaction, and a spectrum of a 1,3-butadiene standard taken using the same equipment and conditions as used for analysis of the products of this reaction.
  • peaks obtained from the toluene containing the reaction products were not observed to shift over a day.
  • the peak at 1.835 min is believed to be due to ethylene, which decreases in area %> over a day.
  • the toluene sample shows a peak at 1.876-1.877 minutes, which is consistent with that of the 1,3-butadiene standard at 1.878 minutes.
  • the toluene sample also shows a shoulder at 1.864 minutes. The shoulder at 1.864 minutes is attributed to a side product, and is thought to be 1-butene or 2-butene.
  • FIGS. 4D-4F GC-MS spectra of the reaction mixture are shown in FIGS. 4D-4F.
  • FIG. 4D shows the entire spectrum.
  • FIG. 4E shows the m/z profile for the peak at 5.314 minutes, compared against that of a standard m/z profile for 2-propenoic acid, butyl ester (butyl acrylate) obtained from a standards database managed by NIST (National Institute of Standards and Technology). By this analysis, the peak at 5.314 minutes in the GC-MS is consistent with butyl acrylate (Quality 78).
  • FIG. 4F shows the m/z scan for the peak at 7.376 min, which is attributed to n-butyl penta-2,4-dienoate.
  • the ratio (mol muconate starting material) :(mol butyl acrylate) was determined to be 1.88 by GC-FID using an internal dodecane standard.
  • the initial ratio of the amount of cis,cis- isomer to the amount of trans,trans- isomer in the di-n-butyl muconate was 6.31 by GC-FID, and the ratio was 7.32 for the muconate that was left unreacted, indicating that the rates of reaction for these isomers were similar.
  • FIG. 4G The GC-MS spectra of the toluene used to trap the gaseous reaction products from the reactor head space is shown in FIG. 4G.
  • FIG. 4H shows the m/z scan for the peak at 2.432 minutes.
  • the GC-MS for 1,3-butadiene and m/z scan for the peak eluting at 2.440 minutes is shown in FIG. 6H.
  • the GC-MS for the toluene incorporating the head space reaction products for Example 2 may indicate the presence of 1,3-butadiene, 1-butene, and/or 2- butene.
  • Example 3 (RV-650-13) was conducted as in Example 2.
  • FIG. 5 A shows a GC-
  • FIG. 5B shows a GC-FID spectrum for toluene used to trap gaseous reaction products from the head space.
  • FIGS. 5C-5D shows overlaid spectra of GC-FID of the toluene used to trap gaseous reaction products from the head space on the day of the reaction and on the day following the reaction, and a spectrum of a 1,3-butadiene standard taken using the same equipment and conditions as used for analysis of the products of this reaction. As shown in FIGS. 5C-5D, peaks obtained from the toluene containing the reaction products were not observed to shift over a day.
  • the peak at 1.835 min is believed to be due to ethylene, which decreases in area % over a day.
  • the toluene sample shows a peak at 1.876-1.877 minutes, which is consistent with that of the 1,3-butadiene standard at 1.878 minutes.
  • the toluene sample does not clearly exhibit a shoulder at 1.864 minutes that may be attributable to 1-butene or 2-butene.
  • FIG. 5E shows a GC-MS spectrum for the reaction mixture of Example 3.
  • 5F shows m/z scans for the peak at 5.316 minutes as compared with that of 2-propenoic acid, butyl ester (butyl acrylate) from a standards database managed by NIST. By this comparison, the peak at 5.316 minutes is consistent with butyl acrylate (Quality 83).
  • FIGS. 5G-5H GC-MS spectra of the toluene used to trap the gaseous reaction products from the reactor head space is shown in FIGS. 5G-5H.
  • FIG. 51 shows a m/z scan for the peak at 2.432 minutes.
  • the GC-MS for 1,3-butadiene and m/z scan for the peak eluting at 2.440 minutes is shown in FIG. 6H.
  • the GC-MS for the toluene incorporating the head space reaction products for Example 3 may indicate the presence of 1,3-butadiene, 1-butene, and/or 2- butene.
  • GC-FID and GC-MS analysis of the reaction products for Examples 4-5 were similar to those for Example 2.
  • GC-FID and GC-MS indicated the presence of butyl acrylate in the liquid phase reaction mixture.
  • GC-FID of the toluene used to trap gaseous reaction products from the head space exhibited a peak at 1.876-1.877 minutes (consistent with the presence of 1,3-butadiene), and a shoulder at 1.864 minutes (side product that may be attributable to 1-butene or 2-butene).
  • Example 4 (RV-650-21) was carried out as Example 2, except that the amounts of muconate reactant was increased to 3.00g (11.8 mmol, 2.997 mL of a solution made by dissolving 12.0094g di-n-butyl muconate in 12.0 mL toluene and dried over molecular sieves), 6.0 mL toluene was used, 1.0 mL (4.4 mmol) dodecane was used, 5.90 mL catalyst solution (0.04 M solution) was used, the ethylene pressure in the reactor was 250 psi (17.2 bar), and the solvent in the receiving vial for the gaseous reaction products from the head space was 2.5 mL CDCI 3 cooled to -43°C using a dry ice/acetonitrile bath.
  • Example 5 (RV-650-22) was carried out as Example 4.
  • EXAMPLE 6 (RV-650-17): Di-n-butyl muconate reacted with ethylene using homogeneous metathesis catalyst at 30°C, 150 psi.
  • Example 6 the procedure as in Example 2 was followed except the reaction was scaled up so that the amounts of muconate reactant was increased to 5.00g (19.7mmol, 4.63 mL of a solution made by dissolving 8.6037g di-n-butyl muconate in 8.0 mL toluene and dried over molecular sieves), 10.0 mL toluene was used, 2.23 mL dodecane used was used, 9.83 mL catalyst solution (0.04 M) was used, the ethylene pressure in the reactor was reduced to 150 psi (10.3 bar), and the temperature was reduced to 30°C, the solvent present in the receiving vial for the gaseous reaction products from the head space was 3.5 ml CDCI 3 and the bath used to cool the CDCI 3 through which the gaseous reaction products were bubbled was dry ice/acetonitrile at -43°C.
  • the CDCI 3 in the receiving was stabilized with 10 microliters TBC solution (0.17 g/mL methanol).
  • the reaction mixture was stabilized with 50 microliters TBC solution.
  • the % conversion was 32.3%.
  • the initial ratio of cis,cis-di-n-butyl muconate:cis,trans-di-n-butyl muconate was 6.83; the ratio of cis,cis di-n-butyl muconate:cis,trans-di-n-butyl muconate in the unreacted muconate following the reaction was 7.47.
  • FIG. 6A shows a GC-FID spectrum of the liquid phase reaction mixture.
  • FIG. 6B shows a GC-FID spectrum of a butyl acrylate standard (upper trace) and an overlay of the GC- FID spectra for the butyl acrylate standard and the liquid phase reaction products (lower trace).
  • FIG. 6C shows a GC-FID spectrum of the CDCI 3 used to trap gaseous reaction products from the head space.
  • FIG. 6C shows a peak at 1.884 minutes that is consistent with 1,3-butadiene and a shoulder at about 1.872 minutes that may be a side product attributable to 1-butene or 2- butene.
  • FIG. 6D provides a GC-MS spectrum for the liquid phase reaction mixture.
  • FIG. 6E shows a m/z scan for the peak at 5.316 minutes, which is consistent with a m/z scan for a standard of butyl acrylate obtained from NIST shown in the lower trace of FIG. 6E (Quality 72).
  • FIG. 6F shows a GC-MS spectrum for the CDCI 3 used to trap the gaseous reaction products from the head space.
  • FIG. 6G shows a m/z scan for the peak at 2.441 minutes.
  • FIG. 6H provides a GC-MS for a standard of 1,3-butadiene in the upper trace and a m/z scan for the peak at 2.443 minutes in the lower trace.
  • FIGS. 6L-6N The NMR was carried out in CDC1 3 at 5°C using a 400MHz JEOL ECX 400 spectrometer. As shown in FIGS. 6I-6J, the sample shows the presence of 1,3-butadiene that has been obtained from the head space of the reactor using the gas recovery system. The peak at
  • the peak at 122.957ppm is likely attributable to ethylene, based on estimated peak from ChemDraw® software.
  • the peaks at 137.65ppm and 117.647ppm are attributed to 1,3-butadiene, based on reference spectra available at Sigma- Aldrich.
  • the peaks at 137.5ppm, 117.479ppm, 26.653ppm, and 13.065ppm are attributed to 1-butene, based on estimates from ChemDraw® software.
  • EXAMPLE 7 (RV-650-5A) was carried out as in Example 2, except that the
  • FIG. 7A shows a GC-FID spectrum of toluene comprising reaction products in the receiving vial collected from the head space of the reactor. Also shown in FIG.
  • FIG. 7A is a GC-FID spectrum for a 1 ,3-butadiene standard, and a GC-FID spectrum for toluene comprising the head space reaction products co-injected with 1,3-butadiene.
  • FIG. 7A shows a GC-FID spectrum of a butyl acrylate standard (upper trace).
  • FIG. 7B also provides a GC-FID spectrum of the liquid phase reaction products overlaid with that of the butyl acrylate standard, indicating the presence of butyl acrylate.
  • Example 7 the head space reaction product of Example 7 is consistent with the side product observed in Examples 2-6, which may be 1- butene and/or 2-butene.
  • GC-FID for the liquid phase reaction mixture of Example 7 shows the presence of butyl acrylate, which is consistent with Examples 2-6.
  • EXAMPLES 8-126 Etheno lysis reaction carried out using homogeneous metathesis catalysts at 10-40 bar ethylene and 30°C-80°C.
  • TEFLON® tube containing a magnetic stir bar was loaded with 127 microliter (0.5 mmol) of cis,cis-di-n-butyl muconate having a purity of about 80% of the cis,cis isomer (as prepared in Example 1) and 200 microliters of an anhydrous toluene stock solution containing 0.025 mmol (5 mol%) of Hoveyda-Grubbs 2 nd generation metathesis catalyst (available from Sigma- Aldrich), made by dissolving 94 mg catalyst in 1200 microliters of anhydrous toluene. To this mixture was added 673 microliters of anhydrous toluene to reach a total liquid reaction volume of 1000 microliters.
  • the TEFLON® tube was capped with a TEFLON® septum and tightly sealed before transfer out of the glove box.
  • the reactor was flushed three times with 35 bar of nitrogen and three times with 20 bar of ethylene before it was brought to the desired ethylene pressure of 10 bar (145 psi). Then the reactor was placed in a pre-heated aluminum mantle of 30°C and stirred for 4 hours. After cooling to room temperature the headspace of the reactor was sampled for GC-FID analysis. Then the reactor was opened and the mixture was diluted with 4 ml of isopropyl alcohol containing 2.5 wt% tetradecane as a standard. 500 microliters of the resulting mixture was used for GC-MS analysis of the liquid phase. The head space was sampled for GC- FID analysis. For GC-MS, a Thermo Trace GC with FID detection and DSQ II mass
  • the start temperature was 60°C, with a hold time of 1 minute, then a first ramp at 10°C/min to 150°C, with a hold time of 1 minute, and a second ramp at 60°C/min to 250°C, with a hold time of 2 minutes.
  • the injection temperature was 250°C, and a split flow at 200 ml/min was used.
  • the carrier flow rate was 2 ml/min.
  • the FID temperature was 275°C.
  • the injection volume was 0.5 microliter.
  • the front channel was a 2m PBQ backflush column and a 23m PBQ analytical column with FID.
  • the middle channel was a 2m PBQ backflush column and a 23m PBQ analytical column with a thermal conductivity detector (TCD).
  • TCD thermal conductivity detector
  • the back channel was a 2m PBQ backflush column and a 8m Molsieve analytical column with a TCD.
  • the front channel was run at 80 kPa, 10 ml/min, 70°C, 20 seconds.
  • the middle channel was run at 70kPa, 20 ml/min, 60°C, 14 seconds.
  • BD 1,3 -butadiene and/or butene (1-butene and/or 2-butene)
  • BA butyl acrylate
  • MuBuE di-n-butyl muconate
  • PD n- butyl penta-2,4-dienoate
  • PR propylene
  • HD hexa-2,4-diene
  • tr trace
  • sub. substrate
  • the column labeled GC-FID refers to species detected in the reaction head space using GC-FID as described above, in addition to ethylene.
  • the column labeled GC-MS refers to species detected in the reaction liquid phase (in addition to solvent, internal standard and substrate) using GC-MS as described above, "mmol MuBuE left” is measured using the tetradecane standard.
  • the column labeled “% conv.” refers to the % conversion of the MuBuE ⁇ (l-[fmal amount of MuBuE)/(initial amount of MuBuE)]xl00% ⁇ .
  • the catalysts were screened in blocks of 12 experiments, with each block including a blank experiment that was run without a catalyst but with reactants. The total area of the reactant peaks in the blank, as measured by GC-MS, was used as a reference for the other experiments in the block to calculate % conversion.
  • the amount of MuBuE reactant remaining after the reaction was calculated directly from a calibration line of the reactant relative to the external standard tetradecane.
  • Examples 31 -54 were conducted as in Example 11 , except that the pressure was increased to 40 bar. Results are shown in Table 4.
  • Examples 55-78 were conducted as in Example 11, except that the temperature was increased to 55°C and the pressure was increased to 25 bar. Results are shown in Table 5.
  • Examples 79-102 were conducted as in Example 11, except that the temperature was increased to 80°C. Results are shown in Table 6.
  • Examples 103-126 were conducted as in Example 11, except that the temperature was increased to 80°C and the pressure was increased to 40 bar. Results are shown in Table 7. Table 7. Experimental results for di-n-butyl muconate reacted with ethylene in the presence of a homogeneous metathesis catalyst at 80°C and 40 bar
  • Example 127 was carried out as in Example 11, except heterogeneous catalysts were used, and pressure and temperature were varied as described below.
  • heterogeneous catalysts prepared in-house three metal containing stock solutions were made according to the following recipes. To make a rhenium stock solution, 2160.6 mg ammonium perrhenate(VII) (having a metal w/w of 0.694258) was added to 50000 microliters water to result in a stock solution having 30 mg metal/mL. To the Re-stock a few drops of 65% HNO 3 were added.
  • the support (commercial gamma-alumina) was impregnated using the respective stock solutions by Incipient Wetness (IWI) or dilution (DIL) for at least 24 h.
  • IWI Incipient Wetness
  • DIL dilution
  • the catalysts were dried in porcelain cups under air as follows. The temperature was ramped to 80°C at 2°C/min, with a 2 hour hold at 80°C, followed by a temperature ramp to 110°C at 2°C/min, with a 2 hour hold at 110°C, followed by a ramp to 525°C at 5°C/min, with a 24 hour hold at 525°C.
  • catalyst 44-0083 showed the presence of BA and PD by GC-MS in the liquid phase reaction mixture and BD in the reactor head space when reacted at 30°C, 10 bar (5% conversion of di-n-butyl muconate), 30°C, 40 bar (5% conversion of di-n-butyl muconate), 55°C, 25 bar (7% conversion), and 80°C, 10 bar (6%> conversion).

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Abstract

L'invention concerne des procédés de préparation de 1,3-butadiène et d'un ou de plusieurs parmi l'acide acrylique et des esters de l'acide acrylique à partir d'acide muconique ou d'un de ses dérivés.
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US9850192B2 (en) 2012-06-08 2017-12-26 Cj Cheiljedang Corporation Renewable acrylic acid production and products made therefrom
WO2019022083A1 (fr) * 2017-07-24 2019-01-31 国立研究開発法人理化学研究所 Décarboxylase et procédé de production d'un composé hydrocarboné insaturé mettant en œuvre ladite décarboxylase
US10786064B2 (en) 2010-02-11 2020-09-29 Cj Cheiljedang Corporation Process for producing a monomer component from a genetically modified polyhydroxyalkanoate biomass

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