EP2880010A1 - Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante - Google Patents

Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante

Info

Publication number
EP2880010A1
EP2880010A1 EP13756629.5A EP13756629A EP2880010A1 EP 2880010 A1 EP2880010 A1 EP 2880010A1 EP 13756629 A EP13756629 A EP 13756629A EP 2880010 A1 EP2880010 A1 EP 2880010A1
Authority
EP
European Patent Office
Prior art keywords
acid
process according
reaction
diol
oxidative cleavage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP13756629.5A
Other languages
German (de)
English (en)
French (fr)
Inventor
Marc Lemaire
Estelle METAY
Marc Sutter
Julien DEBRAY
Yann Raoul
Nicolas DUGUET
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Oleon
Centre National de la Recherche Scientifique CNRS
Universite Claude Bernard Lyon 1 UCBL
Avril SARL
Original Assignee
Interoleagineuse d' Assistance et de Developpement (SIA) Ste
Oleon
Centre National de la Recherche Scientifique CNRS
Universite Claude Bernard Lyon 1 UCBL
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Interoleagineuse d' Assistance et de Developpement (SIA) Ste, Oleon, Centre National de la Recherche Scientifique CNRS, Universite Claude Bernard Lyon 1 UCBL filed Critical Interoleagineuse d' Assistance et de Developpement (SIA) Ste
Publication of EP2880010A1 publication Critical patent/EP2880010A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • C07C51/367—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by introduction of functional groups containing oxygen only in singly bound form
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/23—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/31—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C53/00—Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen
    • C07C53/126—Acids containing more than four carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C55/00—Saturated compounds having more than one carboxyl group bound to acyclic carbon atoms
    • C07C55/02—Dicarboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C55/00—Saturated compounds having more than one carboxyl group bound to acyclic carbon atoms
    • C07C55/02—Dicarboxylic acids
    • C07C55/18—Azelaic acid
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
    • C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
    • C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
    • C07D317/12—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, directly attached to ring carbon atoms

Definitions

  • the invention relates to a process for preparing carboxylic acids, more particularly carboxylic acids having one or two acid functions, by oxidative cleavage of at least one diol or an epoxide.
  • the oxidizing cleavage of olefins can generally be carried out in one or two stages, either directly from olefins, or following a hydroxylation step or prior epoxidation of these compounds.
  • the document FR2086521 describes, in this sense, the oxidative cleavage of various vicinal diols, including the diol of oleic acid, with potassium monopersulfate and in the presence of a catalytic amount of nickel (20mol%). This technology uses nickel salts and remains toxic to the environment.
  • US Pat. No. 4,006,173 discloses a continuous cleavage process using cobalt or ruthenium complexes under an atmosphere having pure oxygen and in the presence of a solvent.
  • WO2008 / 138892 and WO2011 / 080296 both disclose a process for preparing monocarboxylic acids and triglycerides in the presence of solvent.
  • the subject of the present invention is a process for preparing a carboxylic acid, or an aldehyde, by oxidative cleavage of at least one olefin, a vicinal diol, or an epoxide, the reaction being carried out in the presence a catalyst, an oxidant and in the absence of a solvent.
  • the invention has the advantage of not using solvents. This makes it possible to reduce the costs of the reaction, to limit the risk of pollution of the environment and the danger of the reaction.
  • the invention also allows the preparation of aldehydes or preferably carboxylic acids in a single step or by combining in the same reactor the dihydroxylation step and the oxidative cleavage step when the reaction is conducted directly from olefins.
  • the subject of the invention is a process for preparing a carboxylic acid, by oxidative cleavage of at least one vicinal diol, or an epoxide, the reaction being carried out in the presence of a catalyst, a oxidizing and without added solvent.
  • the oxidative cleavage reaction is preferably carried out on vicinal diols or on pure epoxides, this making it possible to obtain acids which also have a high degree of purity.
  • the purity of the product obtained can thus be greater or equal to 95% by weight, preferably greater than or equal to 99%.
  • solvents organic compounds comprising at least one carbon atom and inorganic carbon-free compounds which have the capacity to dissolve or dilute at least one of the products used or obtained by the process of the invention.
  • absence of solvent must be understood in its most common sense as not excluding the presence of a minimal amount of solvent, or "trace”. Such an amount may for example be quantified as less than or equal to 10% by weight of the reaction medium, preferably less than 1%, or even less than 0.1%.
  • the oxidative cleavage reaction used in the process of the invention is therefore advantageously carried out in the absence of a solvent, that is to say without adding any organic solvent or inorganic solvent, including water, to the solvent. any of the steps of the method. It makes it possible to obtain at least one, and preferably two, compounds such as carboxylic acids, aldehydes or other compounds comprising oxygen such as oxacycloalkanes. The production of carboxylic acids is particularly envisaged.
  • carboxylic acid is meant any compound having a structure of varied nature, linear, branched or cyclic, having at least one carboxylic acid function.
  • aldehyde any compound having a structure of varied nature, linear, branched or cyclic, having at least one aldehyde function.
  • the reaction is conducted under an atmosphere comprising oxygen, the oxygen then being the oxidizer of the reaction.
  • the reaction is conducted in the presence of air, or a gaseous mixture comprising oxygen in a proportion similar to air as well as inert gases, the oxygen included in the air being the oxidant of the reaction.
  • air or a gaseous mixture comprising oxygen in a proportion similar to air as well as inert gases, the oxygen included in the air being the oxidant of the reaction.
  • oxygen in the air is less hazardous and avoids the need for additional product additions that may be toxic or difficult to control or recycle.
  • a particular aspect of the invention is therefore a process using no other oxidant than air or an equivalent mixture in danger.
  • the reaction is carried out in the presence of a catalyst based on ruthenium, cerium, palladium, iron, copper, nickel, rhenium, manganese, rhodium, cobalt, vanadium or molybdenum. , gold, tungsten, lead, platinum or a mixture of these metals.
  • a catalyst based on ruthenium, cerium, palladium, iron, copper, nickel, rhenium, manganese, rhodium, cobalt, vanadium or molybdenum. , gold, tungsten, lead, platinum or a mixture of these metals.
  • the catalyst is of formula M (OH) x / Support, in which M is a metal as defined above, x is an integer from 0 to 8, and wherein the support is selected from carriers conventionally used in heterogeneous catalysis.
  • M is a metal as defined above
  • x is an integer from 0 to 8
  • the support is selected from carriers conventionally used in heterogeneous catalysis.
  • the metal M may be deposited on alumina, zirconia, coal, silica, a zeolite or a mixture thereof.
  • the catalyst is chosen from low-toxicity catalysts and easy recycling. It is also advantageous to use a catalyst in solid form, or heterogeneous, during the process according to the invention.
  • M is a metal chosen from the group consisting of palladium, iron, copper, nickel, rhenium, manganese, rhodium, platinum, vanadium, molybdenum, gold, tungsten, lead and a mixture thereof.
  • the catalyst used is advantageously a catalyst based on ruthenium, iron, copper or palladium.
  • x is a number, whole or not, ranging from 1 to 8, more particularly from 1 to 4 and preferably from 1 to 3.
  • the catalyst used is a ruthenium / alumina catalyst of formula Ru (OH) x / Al 2 O 3 .
  • the proportion of catalyst used is from 0.001% to 50% by mole relative to the substrate and / or from 0.001% to 50% by mass relative to the support.
  • the proportion of catalyst is from 0.01% to 50% by mole relative to the substrate and / or from 0.01% to 50% by mass relative to the support.
  • the metal used is ruthenium, iron, copper or palladium.
  • the catalyst load used can range from 0.1 to 100 ppm (mass). Preferably it is chosen from 1 to 50 ppm, more particularly from 5 to 15 ppm, for example 10 ppm.
  • the reaction is carried out at a pressure of 10 -3 mbar at 15 bar, preferably at 4 -10 bar, more preferably 8 bar ⁇ 0.2.
  • the reaction is conducted at a temperature of 0 ° C to 200 ° C, preferably 90 ° C to 160 ° C, more preferably 90 to 110 ° C.
  • the olefin used in the reaction comprises at least 10 carbon atoms, preferably from 10 to 30 carbon atoms, and has the following formula (I):
  • the diol used comprises at least 10 carbon atoms, preferably from 10 to 30 carbon atoms, preferably from 1 to 24 carbon atoms, and has the following formula (II):
  • p is an integer from 1 to 6, preferably from 1 to 3;
  • n is an integer from 1 to 28, even more preferably from 1 to 12;
  • alkyl or hydroxyalkyl group having from 1 to 27 carbon atoms, preferably from 1 to 12,
  • R 1 and R 2 together form an alkylene group - (CH 2 ) m - in which m 'is an integer between 2 and 10, preferably between 2 and 6, and
  • R 3 and R 4 together form a bond -O- (epoxide), or each represent a hydroxyl group.
  • alkyl group is meant here a linear or branched, preferably linear, saturated hydrocarbon chain.
  • hydroxyalkyl group is meant herein an alkyl group of which at least one of the hydrogen atoms is replaced by a hydroxyl group (-OH).
  • the process according to the invention is generally useful for the oxidative cleavage of diols derived from monounsaturated or polyunsaturated acids and their derivatives, such as, for example, the corresponding fatty acid esters, in particular long-chain esters (having a number greater than 10 carbon atoms, preferably 10 to 30 carbon atoms), preferably originating from natural sources and in particular from oleaginous plants, for example, soybean oil, sunflower oil, rapeseed oil, linseed oil, olive oil, castor oil, peanut oil, or Palm oil.
  • mono-unsaturated acid By way of example of mono-unsaturated acid, mention may be made of myristoleic acid (9-tetradecenoic acid), palmitoleic acid (9-hexadecenoic acid), oleic acid (9-octadecenoic acid), ricinoleic acid (12-hydroxy-9-octadecenoic acid), gadoleic acid (11-eicosenoic acid), erucic acid (13-docosenoic acid), nervonic acid (15-tetracosenoic acid).
  • polyunsaturated acid By way of example of polyunsaturated acid, mention may be made of linoleic acid (9,12-octadecadienoic acid), alpha-linolenic acid (9,12,15-octadecatrienoic acid), gamma linolenic acid (6,9,12-octadecatrienoic acid), di-homo-gamma-linolenic acid (8,11,14-eicosatrienoic acid), arachidonic acid (5,8,11,14-eicosatetraenoic acid), timnodonic acid (5,8,11,14,17-eicosapentaenoic acid), cervonic acid (4,7,10,13,16,19-docosahexaenoic acid).
  • This process can also be applied to dimeric or trimeric compounds derived from the dimerization or trimerization of fatty acids or esters of fatty acids present in rapeseed, flax, olive, castor or peanut oils.
  • This process is particularly suitable for the oxidative cleavage of the diol of oleic acid (compound of formula I above in which p and n are 1, R 1 is a group - (CH 2 ) 6 -CH 3 , R 2 represents a group - (CH 2 ) 7-COOH and R 3 and R 4 represents an alcohol function) in pelargonic acid and azelaic acid.
  • the starting material used in the process according to the invention may advantageously be a mixture of compounds, for example a mixture of olefins, in particular a mixture of fatty acids or of their hydroxylated derivatives.
  • This method is also useful for the oxidative cleavage of diols derived from cyclic alkenes and in particular the cyclohexene diol which makes it possible to prepare adipic acid whose industrial use for the manufacture of nylon is well known.
  • R 1 and R 2 represents a group - (CH 2 ) m --CO 2 A (A representing a hydrogen atom or an alkyl group having from 1 to 4 carbon atoms and m, an integer of 1 to 26, preferably 5 and 9) and the other substituent represents an alkyl group having from 1 to 27 carbon atoms, preferably from 1 to 12, preferably from 5 to 9,
  • A representing a hydrogen atom or an alkyl group having from 1 to 4 carbon atoms and m, an integer of 1 to 26, preferably 5 and 9
  • the other substituent represents an alkyl group having from 1 to 27 carbon atoms, preferably from 1 to 12, preferably from 5 to 9
  • the oxidative cleavage of the Formula (I) results in a mixture of mono-carboxylic acid and dicarboxylic acid. This is the case, for example, when the starting material is oleic acid and a mixture of pelargonic acid and azelaic acid is obtained.
  • the oxidative cleavage can also lead to a mixture of monocarboxylic acid and half ester. This is the case when the starting material is an alkyl oleate and a mixture of pelargonic acid and mono-alkyl azelate is obtained.
  • the oxidative cleavage leads to a mixture of dicarboxylic acids. or even to a single di-carboxylic acid when the starting diol is symmetrical, that is to say when Ri represents a group - (CH 2 ) -C0 2 A and R 2 represents a group - (CH 2 ) - C0 2 A, with n equal to 1.
  • the starting diol corresponds to formula (I) in which:
  • n is an integer between 6 and 9 and A represents a hydrogen atom or an alkaline cation
  • R 2 represents:
  • n which is identical in R 1 and R 2 , is an integer between 6 and 9 and A represents a hydrogen atom or an alkaline cation; and p is preferably 1.
  • the starting material is a ⁇ -unsaturated or ⁇ -dihydroxy fatty acid, that is to say a fatty acid consisting of or comprising an acyclic carbon chain, which comprises an unsaturation, or a vicinal double hydroxylation in end of the chain such as methyl 9-decenoate and the corresponding dihydroxy compound.
  • the starting material is oleic acid and / or 9,10-dihydroxystearic acid.
  • the process comprises a further prior step of hydroxylation of the olefin used.
  • This step can be carried out by the use of electrophilic oxidants, such as potassium permanganate or osmium tetroxide, or by the hydrolysis of oxacyclopropanes (epoxides). It advantageously makes it possible to purify the diol obtained and to carry out the oxidative cleavage reaction according to the process of the invention on a purified diol which leads to obtaining carboxylic acids with a high degree of purity.
  • the process according to the invention makes it possible to obtain a dicarboxylic acid, a dialdehyde and / or an aldehyde / acid, saturated or not.
  • the process makes it possible to obtain an aldehyde or even more advantageously an unsaturated carboxylic acid.
  • Such compounds can be obtained for example by the use of unsaturated vicinal diols as starting materials. These can optionally be obtained by selective epoxidation of an olefin having several unsaturations.
  • the process according to the invention allows the preparation of a dicarboxylic acid.
  • it allows the preparation of a monocarboxylic acid and a dicarboxylic acid.
  • the carboxylic acid obtained has the following formula (II):
  • n, n 'and n are identical or different, chosen independently of each other, from 0 to 10,
  • A is a hydrogen atom, a carboxylic acid function - (COOH), and
  • said carboxylic acid having 2 to 16 carbon atoms, preferably 3 to 12 carbon atoms, preferentially 5, 6, 7, 8, 9 or 10 carbon atoms.
  • the reaction products obtained from oleic acid, its diol or epoxide derivative are pelargonic acid and azelaic acid.
  • An advantageous aspect of the process is a conversion rate to carboxylic acid and / or high aldehyde, in particular greater than 90% and more particularly greater than 99%.
  • Another advantageous aspect is a mass yield of bifunctional compounds, such as dicarboxylic acids, dialdehydes or aldehydes / acids, greater than 35%, preferably greater than 40%.
  • the diol used is cyclohexane diol and, preferably, the process according to the invention makes it possible to obtain adipic acid.
  • the carboxylic acid or aldehyde is obtained in a single reaction step.
  • the resulting mixture is then heated at 40 ° C for 8 h and then allowed to stand at room temperature overnight.
  • the oil is mixed in 150 mL of 1N potassium hydroxide (KOH) and then heated at 90 ° C for 1 hour.
  • KOH potassium hydroxide
  • the pH is adjusted to 2 of this solution by adding concentrated hydrochloric acid (37% by weight).
  • the oily phase obtained is separated using a dropping funnel and is washed with 100 ml of water. 59 g of an oil are obtained.
  • this oil is recrystallized from hexane and pure 9,10-dihydroxystearic acid is obtained in the form of a white solid.
  • Alumina (2 g) is added in powder form (after calcination at 550 ° C. for 3 hours) in an aqueous solution of RuCl 3 at room temperature (8.3 mM). After 15 minutes, the pH is adjusted to 13 by adding a solution of NaOH (1 M).
  • BCD 2 g (13.7 mmol) of 9,10-dihydroxystearic acid are added in the presence of 1 mol% of Ru (OH) x / Al 2 O 3 (1 x x 3 3 ) in an autoclave.
  • the mixture is brought to 150 ° C. for 15 h under 8 bar of air pressure. After 15 hours, the reaction medium is diluted in 10 ml of methanol and then filtered.
  • the filtrate obtained is esterified fatty acids not suitable for this type of analysis.
  • 100 mg of Amberlyst® dry, Ref 79291 STREM chemicals are added to the filtrate and refluxed for two hours.
  • the medium is then filtered to remove Amberlyst® (dry, ref 79291, STREM chemicals), and the filtrate is evaporated under reduced pressure.
  • the expected ester mixture is then obtained for analysis with a quantitative yield (2.34 g) of a mixture having the same proportions of pelargonic acid and azelaic acid in ester form.
  • the mixture is then heated at 140 ° C. for 18 hours under 8 bar of air pressure. After 15 hours, the reaction medium is diluted in 10 ml of methanol and then filtered. After evaporation of the organic phase, we obtain 2 g of products.
  • the product F is thus obtained with a selectivity greater than 90%, which corresponds to the aldehyde obtained by oxidative cleavage of the diol protected by the diol itself.
  • the Ru (OH) x / Al 2 O 3 catalyst is identical to that used in Examples 1 and
  • the mixture is then heated to 150 ° C. for 15 h under 8 bar of air pressure. After 15h, the reaction medium is diluted in 40 mL of methanol and filtered. For analytical purposes, the filtrate is then esterified. For this, 400 mg of Amberlyst 15 (STREM chemicals) are added to the filtrate obtained, which is refluxed for two hours.
  • Amberlyst 15 STREM chemicals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
EP13756629.5A 2012-07-31 2013-07-30 Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante Withdrawn EP2880010A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1257421A FR2994178B1 (fr) 2012-07-31 2012-07-31 Procede de preparation d'un acide carboxylique ou d'un aldehyde
PCT/FR2013/051842 WO2014020281A1 (fr) 2012-07-31 2013-07-30 Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante

Publications (1)

Publication Number Publication Date
EP2880010A1 true EP2880010A1 (fr) 2015-06-10

Family

ID=46852295

Family Applications (1)

Application Number Title Priority Date Filing Date
EP13756629.5A Withdrawn EP2880010A1 (fr) 2012-07-31 2013-07-30 Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante

Country Status (6)

Country Link
US (1) US9359280B2 (zh)
EP (1) EP2880010A1 (zh)
CN (1) CN104640833A (zh)
FR (1) FR2994178B1 (zh)
MY (1) MY173010A (zh)
WO (1) WO2014020281A1 (zh)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016183769A1 (en) * 2015-05-18 2016-11-24 Rhodia Operations Process for oxidation of alcohols using oxygen-containing gases
EP3713908B1 (en) 2017-11-22 2023-06-28 Novamont S.p.A. Production of carboxylic acids from vicinal diols
CN109942407B (zh) * 2019-04-16 2022-04-01 中国日用化学研究院有限公司 一种合成9，10-二羟基十八碳硬脂酸的方法
FR3100809B1 (fr) 2019-09-16 2023-06-02 Demeta Procédé de coupure oxydante d'oléfines utilisant comme catalyseur un halooxodiperoxométallate
KR102303532B1 (ko) * 2020-01-08 2021-09-23 애경유화주식회사 펠라르곤산 및 아젤라인산의 제조방법
WO2023114896A1 (en) * 2021-12-16 2023-06-22 Illumina Cambridge Limited Methods for metal directed cleavage of surface-bound polynucleotides

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2086521A5 (en) 1970-04-01 1971-12-31 Air Liquide Carboxylic acids prepn by oxidative cleavage of alpha-glycols
DE2106913A1 (en) 1971-02-13 1972-09-07 Oxidn of vicinal diols - to yield carboxylic acids in high purity
DE2314454A1 (de) * 1973-03-23 1974-10-03 Henkel & Cie Gmbh Verfahren zur kontinuierlichen herstellung von carbonsaeuren
IT1256989B (it) 1992-10-29 1995-12-27 Novamont Spa Procedimento per la preparazione di acidi carbossilici o loro esteri mediante scissione ossidativa di acidi grassi insaturi o loro esteri.
ITMI20051779A1 (it) 2005-09-23 2007-03-24 Novamont Spa Processo migliorato per la produzione di derivati di acidi carbossilici saturi
ITMI20070953A1 (it) 2007-05-10 2008-11-11 Novamont Spa Processo di scissione catalitica di oli vegetali
CA2777706C (en) * 2009-10-13 2015-12-01 University Of Central Florida Research Foundation, Inc. Oxidative cleavage of unsaturated carboxylic acids
IT1397379B1 (it) * 2009-12-30 2013-01-10 Novamont Spa Processo continuo per la produzione di derivati di acidi carbossilici saturi
IT1397378B1 (it) * 2009-12-30 2013-01-10 Novamont Spa Processo continuo di scissione ossidativa di oli vegetali
FR2957074B1 (fr) 2010-03-05 2012-04-27 Organisation Nationale Interprofessionnelle Des Graines Et Fruits Oleagineux O N I D O L Procede de preparation d'acides carboxyliques par coupure oxydante d'un diol vicinal

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
None *
See also references of WO2014020281A1 *

Also Published As

Publication number Publication date
MY173010A (en) 2019-12-18
US20150210623A1 (en) 2015-07-30
CN104640833A (zh) 2015-05-20
FR2994178A1 (fr) 2014-02-07
WO2014020281A1 (fr) 2014-02-06
FR2994178B1 (fr) 2015-08-07
US9359280B2 (en) 2016-06-07

Similar Documents

Publication Publication Date Title
CA2573638C (fr) Procede de co-production d`olefines et de diesters ou de diacides a partir de corps gras insatures
WO2014020281A1 (fr) Procede de preparation d'un acide carboxylique à partir d'un diol ou d'un epoxyde par coupure oxydante
EP2785676B1 (fr) Procede de coupure de chaines grasses insaturees
EP2097431B1 (fr) Complexes catalytiques a base de ruthenium et utilisation de tels complexes pour la metathese d'olefines
EP2542518B1 (fr) Procede de preparation d'acides carboxyliques par coupure oxydante d'un diol vicinal
Louis et al. Sustainable route to methyl-9-hydroxononanoate (polymer precursor) by oxidative cleavage of fatty acid methyl ester from rapeseed oil
CA2841161C (fr) Procede de synthese d'acides omega-fonctionnalises a partir d'acides ou d'esters gras
KR20160005904A (ko) 에스톨라이드 화합물 및 그 제조방법
EP2794543B1 (fr) Procédé de scission moléculaire oxydative d'un composé gras
EP2867196A1 (fr) Procédé de synthèse d'acides insaturés biosourcés
US11406968B2 (en) Mixed oxides for the oxidative cleavage of lipids using oxygen to afford mono- and di-carboxylic acids
FR2972191A1 (fr) Procede de preparation d'une composition tensioactive a base de bio-tensioactifs non-ioniques d'origine naturelle
EP3463647B1 (en) Mixed oxides for the oxidative cleavage of lipids using oxygen to afford mono- and di-carboxylic acids
EP4031554A1 (fr) Procede de coupure oxydante d'olefines utilisant comme catalyseur un halooxodiperoxometallate
FR2960874A1 (fr) Procede de fabrication d'esters alcooliques a partir de triglycerides et d'alcools au moyen de catalyseurs heterogenes a base de metallophosphates azotes
FR3104580A1 (fr) Procede d’esterification par adsorbsion
WO2010066959A1 (fr) Composition catalytique et procede de metathese de corps gras insature.
BE598331A (zh)
FR3003254A1 (fr) Procede de preparation de diols vicinaux
FR2970250A1 (fr) Procede de fabrication d'esters alcooliques a partir de triglycerides et d'alcools au moyen de catalyseurs heterogenes a base de phosphates de metaux de transition du groupe 13

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20150126

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAX Request for extension of the european patent (deleted)
RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: AVRIL

Owner name: UNIVERSITE CLAUDE BERNARD LYON 1

Owner name: CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE

Owner name: OLEON

17Q First examination report despatched

Effective date: 20180502

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20190717