JP2005068102A - Method for producing cyclic ketone - Google Patents
Method for producing cyclic ketone Download PDFInfo
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- JP2005068102A JP2005068102A JP2003302460A JP2003302460A JP2005068102A JP 2005068102 A JP2005068102 A JP 2005068102A JP 2003302460 A JP2003302460 A JP 2003302460A JP 2003302460 A JP2003302460 A JP 2003302460A JP 2005068102 A JP2005068102 A JP 2005068102A
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- perfluoroalkylsulfonyl
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- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 150000003997 cyclic ketones Chemical class 0.000 title abstract description 9
- 239000002841 Lewis acid Substances 0.000 claims abstract description 9
- 150000001450 anions Chemical group 0.000 claims abstract description 9
- 150000007517 lewis acids Chemical class 0.000 claims abstract description 9
- 125000001072 heteroaryl group Chemical group 0.000 claims abstract description 8
- 239000007983 Tris buffer Substances 0.000 claims abstract description 5
- 125000004429 atom Chemical group 0.000 claims abstract description 5
- 230000007935 neutral effect Effects 0.000 claims abstract description 5
- 230000003197 catalytic effect Effects 0.000 claims abstract description 4
- 229910052735 hafnium Inorganic materials 0.000 claims abstract description 4
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 4
- 229910052738 indium Inorganic materials 0.000 claims abstract description 4
- 229910021645 metal ion Inorganic materials 0.000 claims abstract description 4
- 125000002950 monocyclic group Chemical group 0.000 claims abstract description 4
- 125000004433 nitrogen atom Chemical group N* 0.000 claims abstract description 4
- 125000004430 oxygen atom Chemical group O* 0.000 claims abstract description 4
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract description 4
- 125000004434 sulfur atom Chemical group 0.000 claims abstract description 4
- LGRLWUINFJPLSH-UHFFFAOYSA-N methanide Chemical compound [CH3-] LGRLWUINFJPLSH-UHFFFAOYSA-N 0.000 claims abstract description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract 2
- -1 halogen anion Chemical group 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 125000003118 aryl group Chemical group 0.000 claims description 10
- HYGWNUKOUCZBND-UHFFFAOYSA-N azanide Chemical compound [NH2-] HYGWNUKOUCZBND-UHFFFAOYSA-N 0.000 claims description 4
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 claims description 3
- 229910052797 bismuth Inorganic materials 0.000 claims description 3
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 3
- 229910052733 gallium Inorganic materials 0.000 claims description 3
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 claims description 3
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 claims description 3
- 125000003367 polycyclic group Chemical group 0.000 claims description 3
- 229910052717 sulfur Inorganic materials 0.000 claims description 3
- 125000004390 alkyl sulfonyl group Chemical group 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 10
- 239000000126 substance Substances 0.000 abstract description 5
- 239000003905 agrochemical Substances 0.000 abstract description 3
- 150000001336 alkenes Chemical class 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000003446 ligand Substances 0.000 abstract description 3
- 239000004973 liquid crystal related substance Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002685 polymerization catalyst Substances 0.000 abstract description 3
- 150000001408 amides Chemical class 0.000 abstract 1
- 239000003814 drug Substances 0.000 abstract 1
- 150000002367 halogens Chemical class 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 238000007363 ring formation reaction Methods 0.000 description 12
- 239000002253 acid Substances 0.000 description 8
- QNXSIUBBGPHDDE-UHFFFAOYSA-N indan-1-one Chemical class C1=CC=C2C(=O)CCC2=C1 QNXSIUBBGPHDDE-UHFFFAOYSA-N 0.000 description 7
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 5
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- XMIIGOLPHOKFCH-UHFFFAOYSA-N 3-phenylpropionic acid Chemical compound OC(=O)CCC1=CC=CC=C1 XMIIGOLPHOKFCH-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 238000004817 gas chromatography Methods 0.000 description 4
- 239000011968 lewis acid catalyst Substances 0.000 description 4
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000001735 carboxylic acids Chemical class 0.000 description 3
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical group O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 3
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 2
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 2
- 239000000543 intermediate Substances 0.000 description 2
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 2
- 150000004672 propanoic acids Chemical class 0.000 description 2
- 235000019260 propionic acid Nutrition 0.000 description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- GETTZEONDQJALK-UHFFFAOYSA-N (trifluoromethyl)benzene Chemical compound FC(F)(F)C1=CC=CC=C1 GETTZEONDQJALK-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- 125000004973 1-butenyl group Chemical group C(=CCC)* 0.000 description 1
- 125000001637 1-naphthyl group Chemical group [H]C1=C([H])C([H])=C2C(*)=C([H])C([H])=C([H])C2=C1[H] 0.000 description 1
- 125000006017 1-propenyl group Chemical group 0.000 description 1
- 125000000530 1-propynyl group Chemical group [H]C([H])([H])C#C* 0.000 description 1
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- 125000003682 3-furyl group Chemical group O1C([H])=C([*])C([H])=C1[H] 0.000 description 1
- 125000001397 3-pyrrolyl group Chemical group [H]N1C([H])=C([*])C([H])=C1[H] 0.000 description 1
- 125000001541 3-thienyl group Chemical group S1C([H])=C([*])C([H])=C1[H] 0.000 description 1
- 229910052772 Samarium Inorganic materials 0.000 description 1
- 229910052769 Ytterbium Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000003342 alkenyl group Chemical group 0.000 description 1
- 125000004414 alkyl thio group Chemical group 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000000748 anthracen-2-yl group Chemical group [H]C1=C([H])C([H])=C2C([H])=C3C([H])=C([*])C([H])=C([H])C3=C([H])C2=C1[H] 0.000 description 1
- 125000005110 aryl thio group Chemical group 0.000 description 1
- 125000004104 aryloxy group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 125000004093 cyano group Chemical group *C#N 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- XHQZXHMRBXBPEL-UHFFFAOYSA-N eaton reagent Chemical compound CS(O)(=O)=O.O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 XHQZXHMRBXBPEL-UHFFFAOYSA-N 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- DQYBDCGIPTYXML-UHFFFAOYSA-N ethoxyethane;hydrate Chemical compound O.CCOCC DQYBDCGIPTYXML-UHFFFAOYSA-N 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000003402 intramolecular cyclocondensation reaction Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 150000002736 metal compounds Chemical group 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 125000002816 methylsulfanyl group Chemical group [H]C([H])([H])S[*] 0.000 description 1
- 125000001624 naphthyl group Chemical group 0.000 description 1
- 125000005010 perfluoroalkyl group Chemical group 0.000 description 1
- 125000000951 phenoxy group Chemical group [H]C1=C([H])C([H])=C(O*)C([H])=C1[H] 0.000 description 1
- 125000003356 phenylsulfanyl group Chemical group [*]SC1=C([H])C([H])=C([H])C([H])=C1[H] 0.000 description 1
- 229920000137 polyphosphoric acid Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- KZUNJOHGWZRPMI-UHFFFAOYSA-N samarium atom Chemical compound [Sm] KZUNJOHGWZRPMI-UHFFFAOYSA-N 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 238000010898 silica gel chromatography Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 125000003944 tolyl group Chemical group 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- NAWDYIZEMPQZHO-UHFFFAOYSA-N ytterbium Chemical compound [Yb] NAWDYIZEMPQZHO-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Abstract
Description
本発明は、医農薬、オレフィン重合触媒の配位子、液晶材料の合成中間体として有用な環状ケトン類の製造方法に関するものである。 The present invention relates to a method for producing a cyclic ketone useful as a pharmaceutical or agricultural chemical, a ligand for an olefin polymerization catalyst, or a synthetic intermediate for a liquid crystal material.
3−アリールプロピオン酸類の分子内環化により環状ケトン類を製造する方法は、多数報告されている。ところが、これらの方法は、通常、カルボン酸を一旦酸塩化物に変換させた後、塩化アルミニウム等を用いて環化させる二段階法を採用するものである(特許文献1−2参照)。また、3−アリールプロピオン酸類を直接脱水環化反応させる製法も報告されているが、いずれも1当量以上の過剰量の酸反応剤を必要とする方法であるため、多量の廃酸が発生するという問題を抱えている。例えば、ポリリン酸(特許文献3,非特許文献1、2参照)、メタンスルホン酸(非特許文献3参照)、メタンスルホン酸−五酸化リン混合物(非特許文献2,4参照)を溶媒量用いる方法が知られている。さらに最近、その環化反応にゼオライトが触媒作用を有するという報告があるものの(非特許文献5参照)、目的物の収率が低いという欠点がある。 Many methods for producing cyclic ketones by intramolecular cyclization of 3-arylpropionic acids have been reported. However, these methods usually employ a two-stage method in which carboxylic acid is once converted into an acid chloride and then cyclized with aluminum chloride or the like (see Patent Document 1-2). In addition, production methods in which 3-arylpropionic acids are directly subjected to a dehydration cyclization reaction have been reported. However, since all of these methods require an excess amount of an acid reactant of 1 equivalent or more, a large amount of waste acid is generated. Have a problem. For example, polyphosphoric acid (see Patent Document 3, Non-Patent Documents 1 and 2), methanesulfonic acid (see Non-Patent Document 3), and methanesulfonic acid-phosphorus pentoxide mixture (see Non-Patent Documents 2 and 4) are used in an amount of solvent. The method is known. More recently, although there is a report that zeolite has a catalytic action in the cyclization reaction (see Non-Patent Document 5), there is a disadvantage that the yield of the target product is low.
本発明は、従来の技術における上記した問題を解消するためになされたものである。すなわち、本発明の目的は、医農薬、オレフィン重合触媒の配位子、液晶材料の合成中間体として有用な環状ケトン類を、環境汚染を引き起こす化学物質の発生を抑制して、安価にかつ容易に高収率で得ることのできる方法を提供することにある。 The present invention has been made to solve the above-described problems in the prior art. That is, the object of the present invention is to reduce the production of chemical ketones that cause environmental pollution by reducing the use of chemicals and agricultural chemicals, ligands for olefin polymerization catalysts, and cyclic ketones that are useful as synthetic intermediates for liquid crystal materials. It is another object of the present invention to provide a method that can be obtained in a high yield.
本発明者らは、前記課題を解決すべく鋭意研究を重ねた結果、ある種のルイス酸を少量添加することにより、3位が芳香環で置換されたプロピオン酸類の脱水環化反応が速やかに進行し環状ケトンが高収率で得られることを見出し、これらの事実に基づいて本発明を完成させるに至った。 As a result of intensive studies to solve the above-mentioned problems, the inventors of the present invention have made it possible to rapidly carry out the dehydration cyclization reaction of propionic acids in which the 3-position is substituted with an aromatic ring by adding a small amount of a certain Lewis acid. It has been found that cyclic ketones can be obtained in high yield, and the present invention has been completed based on these facts.
すなわち、本発明は、一般式(I)
MXm・Ln (II)
(式中、Mはビスマス、ガリウム、インジウム、ハフニウム、希土類元素から選ばれる金属イオンを示す。Xはハロゲンアニオン、パーフルオロアルキルスルホナートアニオン、ビス(パーフルオロアルキルスルホニル)アミドアニオン、トリス(パーフルオロアルキルスルホニル)メチドアニオンから選ばれるアニオンを示す。Lは配位力のある中性分子を示す。mは金属Mの原子価数であり、nは0〜10の整数である。)
で表されるルイス酸の触媒量と反応させることによる、一般式(III)
MXm · Ln (II)
(In the formula, M represents a metal ion selected from bismuth, gallium, indium, hafnium, and rare earth elements. X represents a halogen anion, a perfluoroalkylsulfonate anion, a bis (perfluoroalkylsulfonyl) amide anion, and tris (perfluoro). Alkylsulfonyl) represents an anion selected from methide anions, L represents a neutral molecule having a coordinating power, m is a valence number of metal M, and n is an integer of 0 to 10.)
By reacting with a catalytic amount of Lewis acid represented by the general formula (III)
本発明によれば、特定のルイス酸を少量用いることにより、芳香環を有するプロピオン酸類の脱水環化反応が速やかに進行し、各種の環状ケトン類、特にインダノン類を容易に高収率で得ることができ、また、用いるルイス酸が少ないから、廃酸の排出を抑制できるものである。 According to the present invention, by using a small amount of a specific Lewis acid, the dehydration cyclization reaction of propionic acids having an aromatic ring proceeds rapidly, and various cyclic ketones, particularly indanones are easily obtained in high yield. In addition, since less Lewis acid is used, discharge of waste acid can be suppressed.
本発明の製法に原料として用いられる前記一般式(I)で表されるカルボン酸は、3位が芳香環基または複素芳香環基で置換されたプロピオン酸類骨格を有するものであり、置換基R1〜R4は、いずれも本発明の環化反応に悪影響を及ぼさないものであれば、特に制限されるものではない。 The carboxylic acid represented by the general formula (I) used as a raw material in the production method of the present invention has a propionic acid skeleton in which the 3-position is substituted with an aromatic ring group or a heteroaromatic ring group, and the substituent R 1 to R 4 are not particularly limited as long as they do not adversely affect the cyclization reaction of the present invention.
一般式(I)中のR1〜R4は、プロピオン酸骨格のアルキレン鎖に結合する環化反応に関与しない基であって、例えば、水素原子、ハロゲン原子、メチル、エチル、プロピル、t−ブチルなどのアルキル基、メトキシ、エトキシなどのアルコキシ基、エステル基、シアノ基などが挙げられる。
また、一般式(I)において環Aは、単環もしくは縮合多環の芳香環基または複素芳香環基であり、それらの環を構成する原子には、1個以上の窒素原子(N)、酸素原子(O)またはイオウ原子(S)を含んでいてもよく、また環が反応に関与しない基で置換されていてもよい。ただし、これらの芳香環基または複素芳香環基は一般式(I)に示すように、プロピオン酸部位が直接結合した炭素原子に結合する2つの原子のうち少なくとも1つには水素原子が結合した炭素原子でなければならない。
R 1 to R 4 in the general formula (I) are groups that do not participate in the cyclization reaction bonded to the alkylene chain of the propionic acid skeleton, and include, for example, a hydrogen atom, a halogen atom, methyl, ethyl, propyl, t- Examples include alkyl groups such as butyl, alkoxy groups such as methoxy and ethoxy, ester groups, and cyano groups.
In general formula (I), ring A is a monocyclic or condensed polycyclic aromatic ring group or heteroaromatic ring group, and atoms constituting those rings include one or more nitrogen atoms (N), An oxygen atom (O) or a sulfur atom (S) may be contained, and the ring may be substituted with a group not participating in the reaction. However, as shown in the general formula (I), these aromatic ring groups or heteroaromatic ring groups have a hydrogen atom bonded to at least one of the two atoms bonded to the carbon atom to which the propionic acid moiety is directly bonded. Must be a carbon atom.
このような芳香環基または複素芳香環基Aの具体例としては、例えば、フェニル基、1−ナフチル基、5,6,7,8−テトラヒドロ−2−ナフチル基、2−アンスリル基、2−フェナンスリル基、1−ピレニル基、3−チエニル基、2−チアンスリル基、3−フリル基、2−キサンテニル基、3−ピロリル基、3H−インドール−2−イル基、6−キノリル基、2−カルバゾリル基などが挙げられる。また、その芳香環基または複素芳香環基Aに置換してもよい基の例としては、ハロゲン原子、メチル、エチル、プロピル、t−ブチルなどのアルキル基、ビニル、1−プロペニル、1−ブテニルなどのアルケニル基、エチニル、1−プロピニルなどのアルキニル基、フェニル、ナフチル、トリルなどのアリール基、メトキシ、エトキシなどのアルコキシ基、フェノキシなどのアリールオキシ基、メチルチオなどのアルキルチオ基、フェニルチオなどのアリールチオ基、パーフルオロアルキル基などが挙げられる。 Specific examples of such aromatic ring group or heteroaromatic ring group A include, for example, phenyl group, 1-naphthyl group, 5,6,7,8-tetrahydro-2-naphthyl group, 2-anthryl group, 2- Phenanthryl group, 1-pyrenyl group, 3-thienyl group, 2-thianthryl group, 3-furyl group, 2-xanthenyl group, 3-pyrrolyl group, 3H-indol-2-yl group, 6-quinolyl group, 2-carbazolyl group Group and the like. Examples of groups that may be substituted on the aromatic ring group or heteroaromatic ring group A include halogen atoms, alkyl groups such as methyl, ethyl, propyl, and t-butyl, vinyl, 1-propenyl, and 1-butenyl. Alkenyl groups such as ethynyl and 1-propynyl, aryl groups such as phenyl, naphthyl and tolyl, alkoxy groups such as methoxy and ethoxy, aryloxy groups such as phenoxy, alkylthio groups such as methylthio, arylthio such as phenylthio Group, perfluoroalkyl group and the like.
次に、本発明に触媒として用いられるルイス酸は、下記一般式(II)
MXm・Ln (II)
で表される金属化合物である。
一般式(II)において、Mは金属イオンであり、ビスマス、ガリウム、インジウム、ハフニウム及びスカンジウム、サマリウム、イッテルビウムなどの希土類元素から選ばれる。
また、アニオンXとしては、その共役酸が高い酸性度を示すものが好ましく、例えばハロゲンアニオン、パーフルオロアルキルスルホナートアニオン、ビス(パーフルオロアルキルスルホニル)アミドアニオン、トリス(パーフルオロアルキルスルホニル)メチドアニオンなどが挙げられる。
Next, the Lewis acid used as a catalyst in the present invention has the following general formula (II):
MXm · Ln (II)
It is a metal compound represented by these.
In the general formula (II), M is a metal ion and is selected from rare earth elements such as bismuth, gallium, indium, hafnium, scandium, samarium, and ytterbium.
The anion X is preferably one whose conjugate acid exhibits high acidity, such as a halogen anion, a perfluoroalkylsulfonate anion, a bis (perfluoroalkylsulfonyl) amide anion, a tris (perfluoroalkylsulfonyl) methide anion, etc. Is mentioned.
また、本発明の脱水環化反応に用いられるルイス酸触媒には、反応に悪影響を及ぼさない中性分子が配位していても差し支えない。この中性分子は一般式(II)におけるLであり、例えば水やジエチルエーテルなどのエーテル類が挙げられ、その数nは0〜10である。また、その反応に用いるルイス酸触媒の使用量は、いわゆる触媒量の少量でよく、化合物(I)に対し0.0001〜50モル%の範囲で実施できるが、あまりに少ないと反応が有利な速度で進行せず、また、あまりに多いと反応の経済性が悪くなるので、好ましくは0.01〜30モル%の範囲であり、より好ましくは0.05〜20モル%の範囲である。 Further, the Lewis acid catalyst used in the dehydration cyclization reaction of the present invention may be coordinated with neutral molecules that do not adversely influence the reaction. This neutral molecule is L in the general formula (II), and examples thereof include ethers such as water and diethyl ether, and the number n is 0 to 10. The amount of the Lewis acid catalyst used for the reaction may be a small amount of so-called catalyst amount, and can be carried out in the range of 0.0001 to 50 mol% with respect to the compound (I). However, if the amount is too large, the economical efficiency of the reaction is deteriorated, so the range is preferably 0.01 to 30 mol%, more preferably 0.05 to 20 mol%.
また、この反応は必ずしも溶媒を必要とするものではないが、溶媒を使用しても良い。使用しうる溶媒としては、芳香族炭化水素系、塩素化炭化水素系、ニトロ化炭化水素系、脂肪族炭化水素系などが挙げられるが、なかでも芳香族炭化水素系、ハロゲン化炭化水素系溶媒が好ましく、具体的には、トルエン、クロロベンゼン、1,2−ジクロロエタン、1,2−ジクロロベンゼン、α,α,α−トリフルオロトルエン等が例示される。
反応温度としては、あまりに低温では反応が有利な速度では進行せず、一方、あまりに高温では副反応が起こるとともに経済性も劣ることから、一般的には0〜350℃の範囲から選ばれ、好ましくは60〜280℃の範囲で実施される。
Further, this reaction does not necessarily require a solvent, but a solvent may be used. Solvents that can be used include aromatic hydrocarbons, chlorinated hydrocarbons, nitrated hydrocarbons, and aliphatic hydrocarbons. Among them, aromatic hydrocarbons and halogenated hydrocarbons are used. Specific examples include toluene, chlorobenzene, 1,2-dichloroethane, 1,2-dichlorobenzene, α, α, α-trifluorotoluene and the like.
As the reaction temperature, the reaction does not proceed at an advantageous rate at a very low temperature, while a side reaction occurs at a too high temperature and the economic efficiency is poor. Therefore, the reaction temperature is generally selected from the range of 0 to 350 ° C., preferably Is carried out in the range of 60-280 ° C.
反応生成混合物から所望の目的生成物を分離するには、溶媒抽出、再結晶、蒸留、クロマトグラフィーおよび昇華の通常の分離精製法を用いることにより容易に達成される。 Separation of the desired target product from the reaction product mixture is easily accomplished by using conventional separation and purification methods such as solvent extraction, recrystallization, distillation, chromatography, and sublimation.
以下、本発明を実施例によりさらに具体的に説明するが、本発明はこれらの実施例によって何ら限定されるものではない。
実施例1
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples.
Example 1
3−フェニルプロピオン酸37.5mg(0.25mmol)、Tb(OSO2CF3)37.6mg(mmol)及びドデカン20μl(GC分析の内部標準物質)をクロロベンゼン6ml中で混合し、これを密閉したガラス容器中、250℃の油浴で1.5時間加熱して環化反応を行った。反応終了後、ガスクロマトグラフィーで分析することにより1−インダノンが95%生成していることを確認した。その後、反応混合物をシリカゲルカラムクロマトグラフィーを用いて精製することにより1−インダノン27mg(82%)を得た。
実施例2〜21
37.5 mg (0.25 mmol) of 3-phenylpropionic acid, 7.6 mg (mmol) of Tb (OSO 2 CF 3 ) 3 and 20 μl of dodecane (internal standard for GC analysis) were mixed in 6 ml of chlorobenzene and sealed. The cyclization reaction was carried out by heating in an oil bath at 250 ° C. for 1.5 hours in the glass container. After completion of the reaction, it was confirmed by gas chromatography that 95% of 1-indanone was produced. Thereafter, the reaction mixture was purified using silica gel column chromatography to obtain 27 mg (82%) of 1-indanone.
Examples 2 to 21
実施例1における3−フェニルプロピオン酸の環化反応による1−インダノンの合成において、使用するルイス酸触媒の種類、触媒量、溶媒量、反応温度及び反応時間を、それぞれ表1に示すものに代えたこと以外は、実施例1と同様にして環化反応及び生成物の確認を行った。実施例1〜21で得られた結果を表1に示す。なお、表中の収率はガスクロマトグラフィーで分析し決定した値である。 In the synthesis of 1-indanone by cyclization of 3-phenylpropionic acid in Example 1, the kind of Lewis acid catalyst used, the amount of catalyst, the amount of solvent, the reaction temperature and the reaction time were changed to those shown in Table 1, respectively. Except that, the cyclization reaction and the product were confirmed in the same manner as in Example 1. The results obtained in Examples 1 to 21 are shown in Table 1. The yields in the table are values determined by analysis by gas chromatography.
各種3−アリールプロピオン酸類0.25mmolを、触媒としてTb(OSO2CF3)3を用い、クロロベンゼン6ml中250℃の油浴で加熱し環化反応を行った。それぞれの実施例に使用した原料化合物並びに得られた生成物の化学構造、触媒量、反応時間及び生成物の収率を、表2及び表3に示す。なお、表中の収率は単離収率であるが、括弧内にはガスクロマトグラフィーで分析し決定した値を示してある。 A cyclization reaction was carried out by heating 0.25 mmol of various 3-arylpropionic acids using Tb (OSO 2 CF 3 ) 3 as a catalyst in an oil bath at 250 ° C. in 6 ml of chlorobenzene. Tables 2 and 3 show the raw material compounds used in the respective examples and the chemical structures, catalyst amounts, reaction times and product yields of the obtained products. In addition, although the yield in a table | surface is an isolated yield, the value which analyzed and determined by gas chromatography is shown in a parenthesis.
本発明方法は、、各種アリールプロピオン酸類を1工程で脱水環化反応させて高収率で環状ケトン類を製造できること及びその反応を少量のルイス酸触媒を用いるのみで行うことができるものであり、環境汚染を軽減できる良好で簡易な製法であることから、工業的実施に有用な方法である。
In the method of the present invention, various arylpropionic acids can be subjected to a dehydration cyclization reaction in one step to produce cyclic ketones in a high yield, and the reaction can be carried out only by using a small amount of Lewis acid catalyst. Since it is a good and simple production method that can reduce environmental pollution, it is a useful method for industrial implementation.
Claims (2)
MXm・Ln (II)
(式中、Mはビスマス、ガリウム、インジウム、ハフニウム、希土類元素から選ばれる金属イオンを示す。Xはハロゲンアニオン、パーフルオロアルキルスルホナートアニオン、ビス(パーフルオロアルキルスルホニル)アミドアニオン、トリス(パーフルオロアルキルスルホニル)メチドアニオンから選ばれるアニオンを示す。Lは配位力のある中性分子を示す。mは金属Mの原子価数であり、nは0〜10の整数である。)
で表されるルイス酸の触媒量と反応させることによる、一般式(III)
MXm · Ln (II)
(In the formula, M represents a metal ion selected from bismuth, gallium, indium, hafnium, and rare earth elements. X represents a halogen anion, a perfluoroalkylsulfonate anion, a bis (perfluoroalkylsulfonyl) amide anion, and tris (perfluoro). Alkylsulfonyl) represents an anion selected from methide anions, L represents a neutral molecule having a coordinating power, m is a valence number of metal M, and n is an integer of 0 to 10.)
By reacting with a catalytic amount of Lewis acid represented by the general formula (III)
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JP2014525950A (en) * | 2011-07-08 | 2014-10-02 | ボレアリス エージー | catalyst |
US9630980B2 (en) | 2011-07-08 | 2017-04-25 | Borealis Ag | Asymmetrical ligands |
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