WO2002000576A1 - Procede pour transferer des groupes alkylidene sur des composes organiques - Google Patents
Procede pour transferer des groupes alkylidene sur des composes organiques Download PDFInfo
- Publication number
- WO2002000576A1 WO2002000576A1 PCT/EP2001/005541 EP0105541W WO0200576A1 WO 2002000576 A1 WO2002000576 A1 WO 2002000576A1 EP 0105541 W EP0105541 W EP 0105541W WO 0200576 A1 WO0200576 A1 WO 0200576A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- microreactor
- organic
- compound
- alkylidene group
- group transfer
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 58
- 125000001118 alkylidene group Chemical group 0.000 title claims abstract description 48
- 150000002894 organic compounds Chemical class 0.000 title claims abstract description 25
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 24
- 150000001336 alkenes Chemical class 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 16
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011541 reaction mixture Substances 0.000 claims abstract description 8
- -1 alkyl compound Chemical class 0.000 claims description 23
- 238000006243 chemical reaction Methods 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 16
- 150000001733 carboxylic acid esters Chemical class 0.000 claims description 15
- 150000002596 lactones Chemical class 0.000 claims description 14
- 150000003857 carboxamides Chemical class 0.000 claims description 12
- 150000002576 ketones Chemical class 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 11
- 229910052723 transition metal Inorganic materials 0.000 claims description 10
- 150000003624 transition metals Chemical class 0.000 claims description 10
- 125000001931 aliphatic group Chemical group 0.000 claims description 8
- 125000003118 aryl group Chemical group 0.000 claims description 8
- 150000003254 radicals Chemical class 0.000 claims description 8
- 230000003068 static effect Effects 0.000 claims description 7
- 239000010936 titanium Substances 0.000 claims description 7
- 125000001072 heteroaryl group Chemical group 0.000 claims description 5
- 238000011065 in-situ storage Methods 0.000 claims description 5
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 claims description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical group [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 229910052736 halogen Inorganic materials 0.000 claims description 4
- 238000004128 high performance liquid chromatography Methods 0.000 claims description 4
- 239000003446 ligand Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical group Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 4
- 229910052725 zinc Inorganic materials 0.000 claims description 4
- 239000011701 zinc Chemical group 0.000 claims description 4
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 claims description 3
- ZSWFCLXCOIISFI-UHFFFAOYSA-N endo-cyclopentadiene Natural products C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 claims description 3
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 2
- 150000005840 aryl radicals Chemical class 0.000 claims description 2
- YNBJMIXWGPOBGE-UHFFFAOYSA-N carbanide;cyclopenta-1,3-diene;titanium(4+) Chemical compound [CH3-].[CH3-].[Ti+4].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 YNBJMIXWGPOBGE-UHFFFAOYSA-N 0.000 claims description 2
- FJBFPHVGVWTDIP-UHFFFAOYSA-N dibromomethane Chemical compound BrCBr FJBFPHVGVWTDIP-UHFFFAOYSA-N 0.000 claims description 2
- 125000000219 ethylidene group Chemical group [H]C(=[*])C([H])([H])[H] 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims description 2
- 229910052735 hafnium Inorganic materials 0.000 claims description 2
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 claims description 2
- 125000000654 isopropylidene group Chemical group C(C)(C)=* 0.000 claims description 2
- 125000000547 substituted alkyl group Chemical group 0.000 claims description 2
- 229910052726 zirconium Inorganic materials 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- 238000006276 transfer reaction Methods 0.000 description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 239000000758 substrate Substances 0.000 description 5
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical group C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 4
- 239000012965 benzophenone Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- JJNHBFYGCSOONU-UHFFFAOYSA-M carbanide;cyclopenta-1,3-diene;dimethylaluminum;titanium(4+);chloride Chemical compound [CH3-].[Ti+3]Cl.C[Al]C.C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 JJNHBFYGCSOONU-UHFFFAOYSA-M 0.000 description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 3
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 125000001570 methylene group Chemical group [H]C([H])([*:1])[*:2] 0.000 description 2
- 125000002950 monocyclic group Chemical group 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 125000001424 substituent group Chemical group 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- ZMYIIHDQURVDRB-UHFFFAOYSA-N 1-phenylethenylbenzene Chemical group C=1C=CC=CC=1C(=C)C1=CC=CC=C1 ZMYIIHDQURVDRB-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 150000008365 aromatic ketones Chemical class 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 150000004292 cyclic ethers Chemical class 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 150000003997 cyclic ketones Chemical class 0.000 description 1
- WJTCGQSWYFHTAC-UHFFFAOYSA-N cyclooctane Chemical compound C1CCCCCCC1 WJTCGQSWYFHTAC-UHFFFAOYSA-N 0.000 description 1
- 239000004914 cyclooctane Substances 0.000 description 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 125000003367 polycyclic group Chemical group 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B37/00—Reactions without formation or introduction of functional groups containing hetero atoms, involving either the formation of a carbon-to-carbon bond between two carbon atoms not directly linked already or the disconnection of two directly linked carbon atoms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0093—Microreactors, e.g. miniaturised or microfabricated reactors
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/207—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms from carbonyl compounds
- C07C1/2072—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms from carbonyl compounds by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/0095—Control aspects
- B01J2219/00984—Residence time
Definitions
- the present invention relates to a method for transferring alkylidene groups to organic compounds.
- the object of the present invention is therefore to provide a process for transferring alkylidene groups to organic compounds which avoids the disadvantages mentioned above.
- This process should in particular be able to be carried out in a simple, reproducible manner with increased safety for humans and the environment and with good yields, and the reaction conditions should be very easy to control.
- This object is surprisingly achieved by the process according to the invention for transferring alkylidene groups to organic compounds, in which at least one organic compound in liquid or dissolved form is mixed with at least one alkylidene group transfer reagent in liquid or dissolved form in at least one microreactor , reacts during a residence time and the olefin thus obtained is optionally isolated from the reaction mixture.
- individual organic compounds or mixtures of at least two of these compounds can be reacted by the process claimed. Only one organic compound is preferably reacted in each case in the process according to the invention.
- a microreactor in the sense of the invention is a reactor with a volume ⁇ 1000 ⁇ l in which the liquids and / or solutions are intimately mixed at least once.
- the volume of the microreactor is preferably ⁇ 100 ⁇ l, particularly preferably ⁇ 50 ⁇ l.
- the microreactor is preferably produced from thin, interconnected silicon structures.
- the microreactor is preferably a miniaturized flow reactor, particularly preferably a static micromixer.
- the microreactor is very particularly preferably a static micromixer, as described in the patent application with the international publication number WO 96/30113, which is hereby introduced as a reference and is considered part of the disclosure.
- Such a microreactor has small channels in which liquids and / or chemicals are present Compounds are mixed together by the kinetic energy of the flowing liquids and / or solutions.
- the channels of the microreactor preferably have a diameter of 10 to 1000 ⁇ m, particularly preferably 20 to 800 ⁇ m and very particularly preferably 30 to 400 ⁇ m.
- the liquids and / or solutions are preferably pumped into the microreactor in such a way that they flow through it at a flow rate of 0.01 ⁇ l / min to 100 ml / min, particularly preferably 1 ⁇ l / min to 1 ml / min.
- the microreactor can preferably be tempered.
- the microreactor is preferably connected via an outlet to at least one retention zone, preferably a capillary, particularly preferably a temperature-controlled capillary.
- the liquids and / or solutions are passed into this residence zone or capillary after they have been mixed in the microreactor in order to extend their residence time.
- the residence time in the sense of the invention is the time between the mixing of the starting materials and the working up of the resulting reaction solution for the analysis or isolation of the desired product (s).
- the required residence time in the process according to the invention depends on various parameters, such as, for example, the temperature or the reactivity of the starting materials. It is possible for the person skilled in the art to adapt the dwell time to these parameters and thus to achieve an optimal reaction course.
- the residence time of the reaction solution in the system used comprising at least one microreactor and optionally a residence section, can be set by selecting the flow rate of the liquids and / or solutions used.
- the reaction mixture is likewise preferably passed through two or more microreactors connected in series. The result of this is that the residence time is increased even at an increased flow rate and the components used in the alkylidene group transfer reaction are reacted in such a way that an optimum product yield of the desired olefin (s) is achieved.
- reaction mixture is passed through two or more microreactors arranged in parallel in order to increase the throughput.
- the number and the arrangement of the channels in one or more microreactor (s) are varied in such a way that the residence time is increased, so that here too, with an increased flow rate, an optimal yield of the desired olefin (s) is achieved.
- the residence time of the reaction solution in the microreactor is preferably ⁇ 15 hours, preferably ⁇ 3 hours, particularly preferably ⁇ 1 hour.
- the process according to the invention can be carried out in a very wide temperature range, which is essentially due to the temperature resistance of the materials used for the construction of the microreactor, if appropriate the residence zone, and further constituents, such as, for example, connections and seals, and the physical properties Properties of the solutions and / or liquids used is limited.
- the process according to the invention is preferably carried out at a temperature of from -100 to +100 ° C., preferably from -40 to + 50 ° C., particularly preferably from 0 to +25 ° C.
- the process according to the invention can be carried out either continuously or batchwise. It is preferably carried out continuously.
- the course of the reaction of the alkylidene group transfer reaction in the process according to the invention can be followed and, if necessary, regulated using various analytical methods known to the person skilled in the art.
- the course of the reaction is preferably followed by chromatography, particularly preferably by high-pressure liquid chromatography, and, if necessary, regulated.
- the control of the reaction is significantly improved compared to known methods.
- the olefin (s) formed is / are optionally isolated.
- the olefin (s) formed is / are preferably isolated from the reaction mixture by extraction. All organic compounds known to the person skilled in the art as substrates of alkylidene group transfer reactions can be used as organic compounds in the process according to the invention.
- the organic compounds are preferably selected from ketones, lactones, carboxylic acid esters, carboxamides or a mixture of at least two of these compounds.
- ketones known to the person skilled in the art which are suitable as substrates for alkylidene group transfer reactions can be used as ketones. This also includes aliphatic, vinylogenic, aromatic and heteroaromatic ketones.
- lactones known to the person skilled in the art which are suitable as substrates for alkylidene group transfer reactions can be used as lactones. This also includes aliphatic, vinylogenic, aromatic and heteroaromatic lactones.
- Carboxylic acid esters are used which are suitable as substrates for alkylidene group transfer reactions. This also includes aliphatic, vinylogenic, aromatic and heteroaromatic carboxylic acid esters.
- Carboxamides are used which are suitable as substrates for alkylidene group transfer reactions. This also includes aliphatic, vinylogenic, aromatic and heteroaromatic carboxamides.
- aliphatic ketones, lactones, carboxylic acid esters and carboxylic acid amides are also understood to mean saturated, unsaturated and branched ketones, lactones, carboxylic acid esters and carboxylic acid amides as well as cyclic ketones, carboxylic acid esters and carboxylic acid amides, which may also be substituted.
- vinylogenic ketones, lactones, carboxylic esters and carboxamides are understood to mean ketones, lactones, carboxylic esters and carboxamides which have a double bond in the ⁇ position to the carbonyl group.
- aromatic ketones, lactones, carboxylic acid esters and carboxamides also include ketones, lactones, carboxylic esters and carboxamides and / or their derivatives which have a monocyclic and / or polycyclic homoaromatic backbone or a corresponding partial structure, e.g. in the form of substituents.
- heteroaromatic ketones, lactones, carboxylic esters and carboxamides also include ketones, lactones, carboxylic esters and carboxamides and / or their derivatives which have at least one monocyclic and / or polycyclic heteroaromatic backbone or a corresponding partial structure, e.g. in the form of substituents.
- These heteroaromatic basic structures or partial structures particularly preferably comprise at least one oxygen and / or nitrogen and / or sulfur atom.
- alkylidene group transfer reagents in the process according to the invention all known to those skilled in the art for Alkylidene group transfer reactions suitable alkylidene group transfer reagents or a mixture of at least two of these reagents can be used.
- Alkylidene group transfer reagents for the purposes of the invention also include alkylidene group transfer reagents formed in situ, i.e. Alkylidene group transfer reagents that are formed immediately before or during the alkylidene group transfer reaction.
- the alkylidene group transfer reagent [(cyclopentadienyl) 2 Ti (CH 2 ) (CI) Al (CH3) 2] (“Tebbe reagent”), a biscyclopentadienyltitanium dialkyl compound, is an alkyl compound
- Transition metal an alkylidene compound of a transition metal or a mixture of at least two of these compounds.
- Dimethyltitanocene can preferably be used as the biscyclopentadienyltitanium dialkyl compound.
- the alkylidene compound of a transition metal which can optionally also be generated in situ, at least one compound of the general formula (I),
- n an integer from 1 to 9, preferably from 1 to 6, particularly preferably 1 or 2, depending on the ligand (s) L and the transition metal M,
- radicals R are an organic radical, preferably an optionally substituted alkyl or aryl radical,
- M is a transition metal, preferably titanium, zirconium or hafnium, particularly preferably titanium
- radicals L identical or different, an organic or inorganic ligand, preferably a cyclopentandienyl radical or a pentamethylcyclopentadienyl radical
- alkylidene group transfer reagent is generated in situ, this can preferably be achieved by a mixture of a compound of the general formula R 1 -CH 2 -X, in which R 1 is an organic radical or a halogen radical and X is a halogen -Rest means zinc and titanium tetrachloride, are particularly preferably generated by a mixture of methylene bromide, zinc and titanium tetrachloride.
- the molar ratio of the alkylidene group transfer agent (s) to the organic compound (s) in the process according to the invention depends on the reactivity of the organic compound (s) used and the reactivity of the alkylidene (s) used.
- Group transfer reagent (ien) The alkylidene group transfer reagent (s) and the organic compound (s) are preferably used in an equimolar ratio.
- the alkylidene group transfer reagent (s) is / are used in a 2-fold to 20-fold molar excess, particularly preferably in a 3-fold to 15-fold, very particularly preferably in a 4-fold to 10-fold excess, based on the organic compound (s) used.
- the selectivity of the reaction itself depends on a number of other parameters, e.g. the concentration of the reagents used, e.g. the temperature, the type of alkylidene group transfer agent used or the residence time. It is possible for the person skilled in the art to adapt the various parameters to the respective reaction in such a way that the desired olefin (s) is (are) obtained.
- the organic compounds and alkylidene group transfer reagents used are either themselves liquid or are in dissolved form. If either the alkylidene group transfer reagent or the organic compound itself is already liquid, these can optionally also be used as solvents for the respective other reaction component. If these are not already in liquid form, they must be dissolved in a suitable solvent before the process according to the invention is carried out become.
- Preferred solvents are halogenated solvents, particularly preferably dichloromethane, chloroform, 1, 2-dichloroethane or 1, 1, 2,2-tetrachloroethane, straight-chain, branched or cyclic paraffins, particularly preferably pentane, hexane, heptane, octane, cyclopentane, cyclohexane, Cycloheptane or cyclooctane or straight-chain, branched or cyclic ethers, particularly preferably diethyl ether, methyl tert-butyl ether, tetrahydrofuran or dioxane, aromatic solvents, particularly preferably toluene, xylenes, ligroin or phenyl ether, N-containing heterocyclic solvents, particularly preferably pyridine or N -Methylpyrrolidone, or a mixture of at least two of the solvents mentioned above.
- the risk to humans and the environment from escaping chemicals is considerably reduced and thus leads to increased safety when handling hazardous substances.
- the transfer of alkylidene groups to organic compounds by the process according to the invention also enables better control of the reaction conditions, e.g. Reaction time and temperature than is possible in the conventional processes.
- the risk of explosions in the case of very strongly exothermic alkylidene group transfer reactions is significantly reduced in the process according to the invention.
- the temperature can be individually selected and kept constant in each volume element of the system.
- the course of the reaction of the alkylidene group transfer reactions can be regulated very quickly and precisely in the process according to the invention.
- the olefins can thus be obtained in very good and reproducible yields.
- the process according to the invention also has the advantage that oxidation-sensitive organic compounds and alkylidene group transfer reagents, which are usually in a protective gas atmosphere must be handled, can be used in the process according to the invention without a protective gas atmosphere.
- a methylene group was transferred to benzophenone using the Tebbe reagent in a static micromixer (Ilmenau University of Technology, Faculty of Mechanical Engineering, Dr.-Ing. Norbert Schwesinger, P.O.Box 100565, D-98684, Ilmenau) with a size of 40 mm x 25 mm x 1 mm, which had a total of 11 mixing stages with a volume of 0.125 ⁇ l each.
- the total pressure loss was approximately 1000 Pa.
- the static micromixer was through an outlet and an omnifit
- the experimental set-up was calibrated for the dependence of the residence time on the pump flow rate before the reaction was carried out.
- the dwell time was set to 15 seconds.
- the reactions were followed using a Merck Hitachi LaChrom HPLC instrument.
- the benzophenone was completely converted to 1,1-diphenylethylene after just 15 seconds.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002505327A JP2004501879A (ja) | 2000-06-28 | 2001-05-16 | アルキリデン基を有機化合物に転移させるための方法 |
EP01933970A EP1296915A1 (fr) | 2000-06-28 | 2001-05-16 | Procede pour transferer des groupes alkylidene sur des composes organiques |
AU2001260303A AU2001260303A1 (en) | 2000-06-28 | 2001-05-16 | Method for transferring alkylidene groups to organic compounds |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2000131380 DE10031380A1 (de) | 2000-06-28 | 2000-06-28 | Verfahren zur Übertragung von Alkyliden-Gruppen auf organischen Verbindungen |
DE10031380.9 | 2000-06-28 |
Publications (1)
Publication Number | Publication Date |
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WO2002000576A1 true WO2002000576A1 (fr) | 2002-01-03 |
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Family Applications (1)
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PCT/EP2001/005541 WO2002000576A1 (fr) | 2000-06-28 | 2001-05-16 | Procede pour transferer des groupes alkylidene sur des composes organiques |
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EP (1) | EP1296915A1 (fr) |
JP (1) | JP2004501879A (fr) |
AU (1) | AU2001260303A1 (fr) |
DE (1) | DE10031380A1 (fr) |
WO (1) | WO2002000576A1 (fr) |
Cited By (15)
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AT501927A1 (de) * | 2005-05-23 | 2006-12-15 | Dsm Fine Chem Austria Gmbh | Verfahren zur durchführung von reaktionen unter beteiligung von carbokationen |
US7754206B2 (en) | 2000-08-03 | 2010-07-13 | The Regents Of The University Of Michigan | Method for treating cancer using a Notch4 ligand antagonist |
US7919092B2 (en) | 2006-06-13 | 2011-04-05 | Oncomed Pharmaceuticals, Inc. | Antibodies to notch receptors |
US8088617B2 (en) | 2007-01-24 | 2012-01-03 | Oncomed Pharmaceuticals, Inc. | Antibodies that bind the glutamate ligand binding region of Notch1 |
US8226943B2 (en) | 2008-07-08 | 2012-07-24 | Oncomed Pharmaceuticals, Inc. | Antibodies to notch receptors |
US8324361B2 (en) | 2005-10-31 | 2012-12-04 | Oncomed Pharmaceuticals, Inc. | Nucleic acid molecules encoding soluble frizzled (FZD) receptors |
US8507442B2 (en) | 2008-09-26 | 2013-08-13 | Oncomed Pharmaceuticals, Inc. | Methods of use for an antibody against human frizzled receptors 1, 2. 5, 7 or 8 |
US8551789B2 (en) | 2010-04-01 | 2013-10-08 | OncoMed Pharmaceuticals | Frizzled-binding agents and their use in screening for WNT inhibitors |
US8834875B2 (en) | 2010-01-13 | 2014-09-16 | Oncomed Pharmaceuticals, Inc. | Notch1 binding agents and methods of use thereof |
US9132189B2 (en) | 2008-07-08 | 2015-09-15 | Oncomed Pharmaceuticals, Inc. | Notch1 binding agents and methods of use thereof |
US9157904B2 (en) | 2010-01-12 | 2015-10-13 | Oncomed Pharmaceuticals, Inc. | Wnt antagonists and methods of treatment and screening |
US9168300B2 (en) | 2013-03-14 | 2015-10-27 | Oncomed Pharmaceuticals, Inc. | MET-binding agents and uses thereof |
US9266959B2 (en) | 2012-10-23 | 2016-02-23 | Oncomed Pharmaceuticals, Inc. | Methods of treating neuroendocrine tumors using frizzled-binding agents |
US9359444B2 (en) | 2013-02-04 | 2016-06-07 | Oncomed Pharmaceuticals Inc. | Methods and monitoring of treatment with a Wnt pathway inhibitor |
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WO2016104755A1 (fr) * | 2014-12-25 | 2016-06-30 | 旭硝子株式会社 | Procédé de production d'un dérivé de dihydropyrazinone |
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Also Published As
Publication number | Publication date |
---|---|
JP2004501879A (ja) | 2004-01-22 |
DE10031380A1 (de) | 2002-01-10 |
AU2001260303A1 (en) | 2002-01-08 |
EP1296915A1 (fr) | 2003-04-02 |
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