WO2006066436A1 - Cyclopropanation process - Google Patents
Cyclopropanation process Download PDFInfo
- Publication number
- WO2006066436A1 WO2006066436A1 PCT/CH2005/000763 CH2005000763W WO2006066436A1 WO 2006066436 A1 WO2006066436 A1 WO 2006066436A1 CH 2005000763 W CH2005000763 W CH 2005000763W WO 2006066436 A1 WO2006066436 A1 WO 2006066436A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- dibromomethane
- process according
- cyclopropanation
- mmol
- mol
- 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.)
- Ceased
Links
- NPGPPCSBEMHHCR-UHFFFAOYSA-N CC1(C)C(C)=CCC1CCO Chemical compound CC1(C)C(C)=CCC1CCO NPGPPCSBEMHHCR-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/42—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons homo- or co-oligomerisation with ring formation, not being a Diels-Alder conversion
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/36—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/86—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
- C07C2/861—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only halogen as hetero-atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/30—Preparation of carboxylic acid nitriles by reactions not involving the formation of cyano groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/32—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions without formation of -OH groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/16—Preparation of ethers by reaction of esters of mineral or organic acids with hydroxy or O-metal groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/18—Preparation of ethers by reactions not forming ether-oxygen bonds
- C07C41/30—Preparation of ethers by reactions not forming ether-oxygen bonds by increasing the number of carbon atoms, e.g. by oligomerisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C43/00—Ethers; Compounds having groups, groups or groups
- C07C43/02—Ethers
- C07C43/03—Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
- C07C43/04—Saturated ethers
- C07C43/115—Saturated ethers containing carbocyclic rings
-
- 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
- C07C67/343—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 by increase in the number of carbon atoms
- C07C67/347—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 by increase in the number of carbon atoms by addition to unsaturated carbon-to-carbon bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D313/00—Heterocyclic compounds containing rings of more than six members having one oxygen atom as the only ring hetero atom
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/02—Systems containing only non-condensed rings with a three-membered ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/06—Systems containing only non-condensed rings with a five-membered ring
- C07C2601/08—Systems containing only non-condensed rings with a five-membered ring the ring being saturated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/06—Systems containing only non-condensed rings with a five-membered ring
- C07C2601/10—Systems containing only non-condensed rings with a five-membered ring the ring being unsaturated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2602/00—Systems containing two condensed rings
- C07C2602/02—Systems containing two condensed rings the rings having only two atoms in common
- C07C2602/14—All rings being cycloaliphatic
- C07C2602/18—All rings being cycloaliphatic the ring system containing six carbon atoms
Definitions
- This invention relates to a process of preparing cyclopropanated compounds.
- a common cyclopropanation reaction is the Simmons-Smith reaction (see Simmons, H. E; Cairns, T. L.; Vladuchick, S. A.; Hoiness, C. M. Org. React. (N. Y.) 1973, 20, 1 - 131), which utilises diiodomethane and Zn(Cu).
- the invention therefore provides a process for the cyclopropanation of a substituted alkene, comprising the reaction of the alkene with a carbenoide, generated from dibromomethane and a tri-(C 2 - C 8 )-alkyl aluminium compound in the presence of a catalytic amount of a metal compound selected from the group consisting of Lewis acids other than tri-(C 2 - C 8 )-alkyl aluminium compounds, metallocenes and metal carbonyl complexes.
- catalytic amount is meant an amount of less than one molar equivalent of metal compound with more than one molar equivalent of reactant with the result that more than one molar equivalent of product is obtained.
- This method not only gives good yields of the product but is also free from the generation of zinc- and copper-containing residues.
- the advantage gained by the metal compounds is that the reaction rate of the cyclopropanation reaction is enhanced, thus allowing the use of less dibromomethane and trialkyl aluminum as well as a significantly decreased reaction temperatures.
- the C 2 - C 8 alkyl moieties may include alkanes, substituted alkanes, cycloalkanes and substituted cycloalkanes.
- the (C 2 - C 8 ) alkyl aluminium compound is preferably triisobutyl aluminium (TIBA).
- the method is applicable to electron-rich alkenes.
- alkenes include mono-, di- , tri- or tetra-substituted alkenes.
- the substituents may be selected from saturated and unsaturated alkyl and aryl groups, which themselves may be substituted with functional groups, such as (but not limited to) acids, esters, alcohols, ethers, allyl alcohols, allyl ethers, amines, allyl amines, imines, alkenes, aldehydes, cyclopropanes and ketones.
- Alkenes with which the invention works especially well are alkenes bearing at least three substituents including alkenes embedded in ring structures with ring sizes of 3 to 20 carbon- or hetero- atoms, which rings themselves can be substituted, for example, with the same substituents as hereinabove described.
- alkenes that undergo the cyclopropanation reaction of this invention including combinations of reactive alkenes and unreactive alkenes in the same molecule, include those with the following structures:
- alkenes may also include in the same molecule alkene moieties that are not electron-rich or alkenes that contain functional groups in their allylic position, which undergo complex formation with the alkyl aluminium compound, e.g.
- alkenes sterically against cyclopropanation.
- unreactive alkenes are allylic alcohols, allylic amines, as well as electron-deficient alkenes such as conjugated carbonyl compounds, conjugated nitriles, conjugated imines and conjugated oximes. If these unreactive alkenes are combined in the same molecule with electron-rich reactive ones, only the latter will undergo cyclopropanation, with high chemoselectivity.
- the metal compounds whose presence is essential to the working of the invention are selected from the group consisting of metallocenes, metal carbonyl complexes and Lewis acids other than tri-(C 2 - C 8 )-alkyl aluminium compounds.
- metallocenes metal carbonyl complexes
- Lewis acids other than tri-(C 2 - C 8 )-alkyl aluminium compounds One or more of these metal compounds can be used.
- tri-(C 2 - C 8 )-alkyl aluminium compounds are themselves weak Lewis acids, it has been found that they alone do not give the benefits of the invention, and when Lewis acids are desired as the metal compounds, Lewis acids other than these tri-(C 2 - C 8 )-alkyl aluminium compounds must be added.
- Examples of efficient Lewis acids include FeCl 2 and FeCl 3 , which are preferably used at a concentration of 0.01 - 30%, preferably 1 - 10%, with respect to the alkene to be cyclopropanated (the starting material).
- Examples of efficient metallocenes are those with at least one cyclopentadienyl-ligand, e.g. cyclopentadienyltitanium trichloride CpTiCl 3 or cyclopentadienyliron dicarbonyl dimer [CpFe(CO) 2 ] 2 , which are used at the concentrations hereinabove described.
- An example of a metal carbonyl complex is iron pentacarbonyl Fe(CO) 5 .
- the addition has the advantage of allowing the reaction to be carried out in less dibromomethane, typically 20 molar equivalents instead of 30 eq, and at lower temperatures, thus increasing the margin of safety, because above 85°C an exothermic decomposition of the reaction mass is possible.
- this reaction proceeds as follows:
- the excess dibromomethane is recovered.
- a recovery reduces costs and makes the process more industrially viable. The recovery is carried out by the steps of:
- recovery may be achieved.by the following steps:
- reaction mixture is added to aqueous base (preferably 25% NaOH) at a temperature of from -10° - 0°C.
- aqueous base preferably 25% NaOH
- Isobutane is cleaved from the isobutyl aluminium reagent and remains liquefied in the target vessel.
- the resulting two-phase mixture is slowly and under stirring warmed to room temperature. This causes the release of gaseous isobutane, which is collected in a cooling device;
- phase separation and addition of isopropanol to the organic phase the organic phase is dried azeotropically and the excess dibromomethane is evaporated under reduced pressure 5 and finally purified by distillation.
- the process described in this invention permits the cyclopropanation of electron-rich olefins in a cheap and efficient manner.
- the aluminium- and iron-containing wastes are environmentally of relatively low concern, the solvent dibromomethane can be recycled, and the collected 10 isobutane can be used for other purposes or can be burned.
- the process has many uses, including the relatively easy and inexpensive manufacture of flavour and fragrance ingredients.
- Campholene alcohol (EP 0 116 903) (8 g, 50 mmol) in dibromomethane (72 ml) is treated under cooling (10° - 2O 0 C) with neat TIBA (6.5 ml, 25 mmol) via syringe. After 15 min stirring anhydrous FeCl 3 (0.5 g, 3 mmol) is added followed by neat TIBA (39 ml, 0.15 mol).
- Example 2 trans-[ 1 -Methyl-2-(l ,2,2,5-tetramethyl-bicyclo[3.1.0]hex-3-ylmethyl)-cyclopropyl]methanol.
- the mixture is stirred for 4.5 h at 25 0 C, then cooled to -10° - 0 0 C and pumped via double needle on to cooled (-10° - O 0 C) 25% NaOH. Under stirring (Caution ! the biphasic mixture is 5 slowly warmed to room temperature. The evolving isobutane is collected in a cooling trap at -78 0 C. The phases are separated. The organic phase is washed with 4% oxalic acid, then with cone. NaHCO 3 until pH ⁇ 8. Isopropanol (HO g, 1.8 mol) is added to the organic phase and the water is removed azeotropically under reduced pressure.
- To Nor-Radjaldehyde (US 4,052,341) (192 g, 1 mol) is added at 0 0 C and stirring neat DIBAH (179 ml, 1 mol) via double needle, The solution is stirred for 30 min at.25°C ⁇ Dibromomethane, (2.1 1, 30 mol) is added and the solution heated to 6O 0 C, where neat TIBA (595 g, 3 mol) is 25 added over 2 h via double-needle. The reaction temperature is maintained by slight external cooling at 65 - 75°C for another 2 - 4 h, until complete conversion is detected by GC.
- Example 2 In comparison with Example 1, it can be seen that, without FeCl 3 , more TIBA and dibromomethane are required and that a higher reaction temperature is necessary. The use of FeCl 3 allows a better, more economic process.
- Linalool 5-(2,2-Dimethyl-cyclopropyl)-3-methyl-pent-l- en-3-ol
- FeCl 3 (0.5 g, 3 mmol) is added under stirring to 6-Methyl-hept-5-en-2-one (6.3 g, 50 mmol) in dibromomethane (70 ml, 1 mol) at 10° - 20°C, followed by slow addition of neat TIBA (38 ml, 0.15 mol) at this temperature. The mixture is stirred for 7 h at 25 0 C, then poured carefully on to 25% NaOH at -10° - 0°C. Work-up as described in example 1 and distillation (bp 50 0 C / 0.07 Torr) gives 4.8 g (67%) of a colorless oil (80% GC-purity, dr - 1:1).
- the analytical data (NMR, MS, IR) are consistent with the ones described in the literature (Perraud, R; Arnaud, P. Bull. Chem. Soc. Chim. Fr. 1968, 1540 - 1542).
- GC/MS 210 (0.1%, M + ), 195 (4%, [M - 15] + ), 153 (10%), 136 (35%), 82 (45%), 55 (100%).
- IR (film) 2925 (m), 2869 (m), 1719 (s), 1648 (m), 1453 (m), 10 1366 (m), 1219 (m), 1147 (s), 1042 (m), 970 (w), 859 (w).
- Example 13 Cyclopropanation of NirvanolideTM: ezs-3-Methyl-6-oxa-bicyclo[13.1.0]hexadecan-7-one.
- Example 14 trans-3 -(2-Ethoxymethyl-2-methyl-cyclopropylmethyl)- 1 ,2,2-trimethyl-bicyclo- [3.1. OJhexane.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Pyrane Compounds (AREA)
- Catalysts (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/722,121 US7777084B2 (en) | 2004-12-24 | 2005-12-20 | Cyclopropanation process |
| CN2005800445502A CN101087745B (zh) | 2004-12-24 | 2005-12-20 | 环丙烷化法 |
| JP2007547143A JP5301162B2 (ja) | 2004-12-24 | 2005-12-20 | シクロプロパン化の方法 |
| MX2007007354A MX2007007354A (es) | 2004-12-24 | 2005-12-20 | Proceso de ciclopropanacion. |
| EP05815490A EP1828087B1 (en) | 2004-12-24 | 2005-12-20 | Cyclopropanation process |
| BRPI0519352-4A BRPI0519352B1 (pt) | 2004-12-24 | 2005-12-20 | processos de ciclopropanação de um alqueno substituído, bem como de fabricação de uma essência ou ingrediente de fragrância |
| DE602005011481T DE602005011481D1 (de) | 2004-12-24 | 2005-12-20 | Cyclopropanierungsverfahren |
| IL183550A IL183550A (en) | 2004-12-24 | 2007-05-30 | Cyclopropanation process |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB0428294.3 | 2004-12-24 | ||
| GB0428294A GB0428294D0 (en) | 2004-12-24 | 2004-12-24 | Process |
| GB0517584.9 | 2005-08-30 | ||
| GB0517584A GB0517584D0 (en) | 2005-08-30 | 2005-08-30 | Process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2006066436A1 true WO2006066436A1 (en) | 2006-06-29 |
Family
ID=35811622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CH2005/000763 Ceased WO2006066436A1 (en) | 2004-12-24 | 2005-12-20 | Cyclopropanation process |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US7777084B2 (enExample) |
| EP (1) | EP1828087B1 (enExample) |
| JP (1) | JP5301162B2 (enExample) |
| KR (1) | KR20070089195A (enExample) |
| AT (1) | ATE416153T1 (enExample) |
| BR (1) | BRPI0519352B1 (enExample) |
| DE (1) | DE602005011481D1 (enExample) |
| ES (1) | ES2318571T3 (enExample) |
| IL (1) | IL183550A (enExample) |
| MX (1) | MX2007007354A (enExample) |
| WO (1) | WO2006066436A1 (enExample) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1712538B1 (en) * | 2005-04-14 | 2011-07-27 | International Flavors & Fragrances, Inc. | Cyclopropanated macrocyclic ketone |
| US8450533B2 (en) | 2007-08-21 | 2013-05-28 | Givaudan Sa | Cyclopropanation process |
| CN115181013A (zh) * | 2022-07-22 | 2022-10-14 | 北京先通国际医药科技股份有限公司 | 修饰脂肪酸型pet试剂前体关键中间体的制备方法及其用途 |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB0621805D0 (en) * | 2006-11-03 | 2006-12-13 | Givaudan Sa | Organic compounds |
| ES2869279T3 (es) | 2015-08-06 | 2021-10-25 | Int Flavors & Fragrances Inc | Ciclopropanación de alquenos sustituidos |
| JP6091028B1 (ja) * | 2015-11-11 | 2017-03-08 | 花王株式会社 | シクロプロパン化合物 |
| WO2022058018A1 (en) | 2020-09-18 | 2022-03-24 | Symrise Ag | Cyclopropanated sandalwood type compounds |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0801049A2 (en) * | 1996-04-09 | 1997-10-15 | Givaudan-Roure (International) S.A. | Cyclopentanebutanol derivatives as odorants |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06184051A (ja) * | 1992-12-22 | 1994-07-05 | Sagami Chem Res Center | 光学活性置換シクロプロピルアルカン酸誘導体およびその製造中間体 |
| JPH0753423A (ja) * | 1993-08-12 | 1995-02-28 | Sagami Chem Res Center | 光学活性シクロプロパン誘導体の製造法 |
| JPH07233175A (ja) * | 1994-02-22 | 1995-09-05 | Sagami Chem Res Center | 金属置換シクロプロピルメタノール誘導体の不斉製造法 |
| ES2222859T3 (es) * | 1996-04-09 | 2005-02-16 | Givaudan Sa | Derivados de ciclopentenbutanol. |
| JPH101446A (ja) * | 1996-06-14 | 1998-01-06 | Mitsubishi Chem Corp | 共役ジオレフィンの環化二量化方法 |
| JP3991625B2 (ja) * | 2001-06-26 | 2007-10-17 | 日本ゼオン株式会社 | シクロプロパン化合物および香料組成物 |
| GB0428306D0 (en) * | 2004-12-24 | 2005-01-26 | Givaudan Sa | Compound |
-
2005
- 2005-12-20 EP EP05815490A patent/EP1828087B1/en not_active Expired - Lifetime
- 2005-12-20 KR KR1020077014234A patent/KR20070089195A/ko not_active Withdrawn
- 2005-12-20 DE DE602005011481T patent/DE602005011481D1/de not_active Expired - Lifetime
- 2005-12-20 JP JP2007547143A patent/JP5301162B2/ja not_active Expired - Fee Related
- 2005-12-20 ES ES05815490T patent/ES2318571T3/es not_active Expired - Lifetime
- 2005-12-20 AT AT05815490T patent/ATE416153T1/de not_active IP Right Cessation
- 2005-12-20 WO PCT/CH2005/000763 patent/WO2006066436A1/en not_active Ceased
- 2005-12-20 US US11/722,121 patent/US7777084B2/en not_active Expired - Fee Related
- 2005-12-20 BR BRPI0519352-4A patent/BRPI0519352B1/pt not_active IP Right Cessation
- 2005-12-20 MX MX2007007354A patent/MX2007007354A/es active IP Right Grant
-
2007
- 2007-05-30 IL IL183550A patent/IL183550A/en not_active IP Right Cessation
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0801049A2 (en) * | 1996-04-09 | 1997-10-15 | Givaudan-Roure (International) S.A. | Cyclopentanebutanol derivatives as odorants |
Non-Patent Citations (2)
| Title |
|---|
| EDWIN C. FRIEDRICH: "Regioselectivity and Solvent Effects in Cyclopropanation of Alkadienes", J. ORG. CHEM., vol. 56, 1991, pages 2202 - 2205, XP002369365 * |
| KEJI MARUOKA ET AL.: "Trialkylaluminium-Alkylidene Iodide. A Powerful Cyclopropanation Agent with Unique Selectivity", J. ORG. CHEM., vol. 50, 1985, pages 4412 - 4414, XP002369364 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1712538B1 (en) * | 2005-04-14 | 2011-07-27 | International Flavors & Fragrances, Inc. | Cyclopropanated macrocyclic ketone |
| US8450533B2 (en) | 2007-08-21 | 2013-05-28 | Givaudan Sa | Cyclopropanation process |
| CN115181013A (zh) * | 2022-07-22 | 2022-10-14 | 北京先通国际医药科技股份有限公司 | 修饰脂肪酸型pet试剂前体关键中间体的制备方法及其用途 |
| CN115181013B (zh) * | 2022-07-22 | 2023-08-08 | 北京先通国际医药科技股份有限公司 | 修饰脂肪酸型pet试剂前体关键中间体的制备方法及其用途 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5301162B2 (ja) | 2013-09-25 |
| BRPI0519352A2 (pt) | 2009-01-20 |
| IL183550A (en) | 2010-12-30 |
| ATE416153T1 (de) | 2008-12-15 |
| US20080275256A1 (en) | 2008-11-06 |
| JP2008525324A (ja) | 2008-07-17 |
| ES2318571T3 (es) | 2009-05-01 |
| DE602005011481D1 (de) | 2009-01-15 |
| EP1828087B1 (en) | 2008-12-03 |
| IL183550A0 (en) | 2007-09-20 |
| EP1828087A1 (en) | 2007-09-05 |
| BRPI0519352B1 (pt) | 2015-09-15 |
| US7777084B2 (en) | 2010-08-17 |
| KR20070089195A (ko) | 2007-08-30 |
| MX2007007354A (es) | 2007-07-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Ballini et al. | Nitroaldol (Henry) reaction catalyzed by amberlyst A-21 as a far superior heterogeneous catalyst. | |
| US6521771B2 (en) | Use of zinc treated with metal hydride in organometallic synthesis | |
| Negishi et al. | Strictly regiocontrolled α-monosubstitution of cyclic carbonyl compounds with alkynyl and alkyl groups via Pd-catalyzed coupling of cyclic α-iodoenones with organozincs | |
| US20100267988A1 (en) | Processes for preparing intermediate compounds useful for the preparation of cinacalcet | |
| JP2008538101A (ja) | ジアリールフェノキシアルミニウム化合物 | |
| CN110950776A (zh) | 有机碱催化丙烯腈水合制备3-羟基丙腈的方法 | |
| EP1828087B1 (en) | Cyclopropanation process | |
| JPWO2001087817A1 (ja) | 2−アルキル−2−アダマンチルエステルの製造方法 | |
| TWI576338B (zh) | (Meth) acrylic acid adamantyl ester | |
| CN101087745B (zh) | 环丙烷化法 | |
| KR20010074521A (ko) | 3-하이드록시프로피오니트릴의 제조방법 | |
| JP2009298715A (ja) | 高純度2’−トリフルオロメチルプロピオフェノンの製造方法 | |
| JP5816037B2 (ja) | 3,3,3−トリフルオロプロパノール類の製造方法 | |
| JP2014001154A (ja) | 2−アルケニルエーテル化合物の製造方法 | |
| US20110004028A1 (en) | Process for production of dialcohol, process for production of allylhalide compound, and allylchloride compound | |
| WO2012133108A1 (ja) | 2-アルケニルエーテル化合物の製造方法 | |
| JP4182300B2 (ja) | 2−フルオロシクロプロパンカルボン酸のシス/トランス異性体混合物の分離方法 | |
| JP4286694B2 (ja) | 新規なグリニャール試薬及びそれを用いた脂肪族アルキニルグリニャール化合物の製造方法 | |
| CN121554366A (zh) | 一种以有机酸-含氮碱复合催化体系制备γ,δ-不饱和酮的方法 | |
| JP2011213661A (ja) | 1−アルキリデンインダン類の製造方法 | |
| TWI665182B (zh) | 製備α-官能化酮的方法 | |
| KR101154504B1 (ko) | 하이드록시알킬 (메타)아크릴레이트 반응에서의 촉매분리방법 | |
| JP2006008636A (ja) | 含フッ素アクリル酸エステルの製造方法 | |
| US9090533B2 (en) | Process for producing 4-cyclohexyl-2-methyl-2-butanol | |
| CN114401938A (zh) | 用于由烯烃制备环丙基化合物的改进方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KN KP KR KZ LC LK LR LS LT LU LV LY MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| WWE | Wipo information: entry into national phase |
Ref document number: 2005815490 Country of ref document: EP |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 183550 Country of ref document: IL |
|
| WWE | Wipo information: entry into national phase |
Ref document number: MX/a/2007/007354 Country of ref document: MX |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 200580044550.2 Country of ref document: CN Ref document number: 2007547143 Country of ref document: JP Ref document number: 1020077014234 Country of ref document: KR |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2787/CHENP/2007 Country of ref document: IN |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| WWP | Wipo information: published in national office |
Ref document number: 2005815490 Country of ref document: EP |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 11722121 Country of ref document: US |
|
| ENP | Entry into the national phase |
Ref document number: PI0519352 Country of ref document: BR |