WO1985002181A1 - Preparation of cyclic-keto-acids - Google Patents
Preparation of cyclic-keto-acids Download PDFInfo
- Publication number
- WO1985002181A1 WO1985002181A1 PCT/US1983/001810 US8301810W WO8502181A1 WO 1985002181 A1 WO1985002181 A1 WO 1985002181A1 US 8301810 W US8301810 W US 8301810W WO 8502181 A1 WO8502181 A1 WO 8502181A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- keto
- cyclic
- bromoalkane
- alcohol
- acids
- Prior art date
Links
- 238000002360 preparation method Methods 0.000 title description 6
- -1 alkaline earth metal inorganic base Chemical class 0.000 claims abstract description 16
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 12
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 11
- 239000002904 solvent Substances 0.000 claims abstract description 10
- 239000003513 alkali Substances 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 5
- 230000003197 catalytic effect Effects 0.000 claims abstract description 4
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 4
- 150000002367 halogens Chemical class 0.000 claims abstract description 4
- 239000001257 hydrogen Substances 0.000 claims abstract description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 14
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical group [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- 150000001242 acetic acid derivatives Chemical class 0.000 claims description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 4
- CPRMKOQKXYSDML-UHFFFAOYSA-M rubidium hydroxide Chemical compound [OH-].[Rb+] CPRMKOQKXYSDML-UHFFFAOYSA-M 0.000 claims description 4
- MQIKJSYMMJWAMP-UHFFFAOYSA-N dicobalt octacarbonyl Chemical group [Co+2].[Co+2].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-] MQIKJSYMMJWAMP-UHFFFAOYSA-N 0.000 claims description 3
- CYNYIHKIEHGYOZ-UHFFFAOYSA-N 1-bromopropane Chemical compound CCCBr CYNYIHKIEHGYOZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 150000002823 nitrates Chemical class 0.000 claims description 2
- 150000007529 inorganic bases Chemical class 0.000 claims 1
- 150000003871 sulfonates Chemical class 0.000 claims 1
- 150000001728 carbonyl compounds Chemical class 0.000 abstract description 6
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 description 16
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 12
- DCAYPVUWAIABOU-UHFFFAOYSA-N hexadecane Chemical compound CCCCCCCCCCCCCCCC DCAYPVUWAIABOU-UHFFFAOYSA-N 0.000 description 12
- CBFCDTFDPHXCNY-UHFFFAOYSA-N icosane Chemical compound CCCCCCCCCCCCCCCCCCCC CBFCDTFDPHXCNY-UHFFFAOYSA-N 0.000 description 12
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 12
- LQERIDTXQFOHKA-UHFFFAOYSA-N nonadecane Chemical compound CCCCCCCCCCCCCCCCCCC LQERIDTXQFOHKA-UHFFFAOYSA-N 0.000 description 12
- RZJRJXONCZWCBN-UHFFFAOYSA-N octadecane Chemical compound CCCCCCCCCCCCCCCCCC RZJRJXONCZWCBN-UHFFFAOYSA-N 0.000 description 12
- YCOZIPAWZNQLMR-UHFFFAOYSA-N pentadecane Chemical compound CCCCCCCCCCCCCCC YCOZIPAWZNQLMR-UHFFFAOYSA-N 0.000 description 12
- IIYFAKIEWZDVMP-UHFFFAOYSA-N tridecane Chemical compound CCCCCCCCCCCCC IIYFAKIEWZDVMP-UHFFFAOYSA-N 0.000 description 12
- RSJKGSCJYJTIGS-UHFFFAOYSA-N undecane Chemical compound CCCCCCCCCCC RSJKGSCJYJTIGS-UHFFFAOYSA-N 0.000 description 12
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 10
- NDJKXXJCMXVBJW-UHFFFAOYSA-N heptadecane Chemical compound CCCCCCCCCCCCCCCCC NDJKXXJCMXVBJW-UHFFFAOYSA-N 0.000 description 10
- BGHCVCJVXZWKCC-UHFFFAOYSA-N tetradecane Chemical compound CCCCCCCCCCCCCC BGHCVCJVXZWKCC-UHFFFAOYSA-N 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000002253 acid Substances 0.000 description 9
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 7
- 230000007062 hydrolysis Effects 0.000 description 6
- 238000006460 hydrolysis reaction Methods 0.000 description 6
- ZCYXXKJEDCHMGH-UHFFFAOYSA-N nonane Chemical compound CCCC[CH]CCCC ZCYXXKJEDCHMGH-UHFFFAOYSA-N 0.000 description 6
- BKIMMITUMNQMOS-UHFFFAOYSA-N normal nonane Natural products CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 6
- 229940038384 octadecane Drugs 0.000 description 6
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- 238000005810 carbonylation reaction Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- JPJALAQPGMAKDF-UHFFFAOYSA-N selenium dioxide Chemical compound O=[Se]=O JPJALAQPGMAKDF-UHFFFAOYSA-N 0.000 description 4
- MSXVEPNJUHWQHW-UHFFFAOYSA-N 2-methylbutan-2-ol Chemical compound CCC(C)(C)O MSXVEPNJUHWQHW-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 150000001298 alcohols Chemical class 0.000 description 3
- 150000001340 alkali metals Chemical class 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 230000006315 carbonylation Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- LCSYJVAKMPOJIB-UHFFFAOYSA-N 2-cyclopropyl-2-oxoacetic acid Chemical compound OC(=O)C(=O)C1CC1 LCSYJVAKMPOJIB-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- PCLIMKBDDGJMGD-UHFFFAOYSA-N N-bromosuccinimide Chemical compound BrN1C(=O)CCC1=O PCLIMKBDDGJMGD-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- NQRYJNQNLNOLGT-UHFFFAOYSA-N Piperidine Chemical compound C1CCNCC1 NQRYJNQNLNOLGT-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 150000001733 carboxylic acid esters Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000004292 cyclic ethers Chemical class 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012429 reaction media Substances 0.000 description 2
- 150000003431 steroids Chemical class 0.000 description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- LSXKDWGTSHCFPP-UHFFFAOYSA-N 1-bromoheptane Chemical compound CCCCCCCBr LSXKDWGTSHCFPP-UHFFFAOYSA-N 0.000 description 1
- MNDIARAMWBIKFW-UHFFFAOYSA-N 1-bromohexane Chemical compound CCCCCCBr MNDIARAMWBIKFW-UHFFFAOYSA-N 0.000 description 1
- YZWKKMVJZFACSU-UHFFFAOYSA-N 1-bromopentane Chemical compound CCCCCBr YZWKKMVJZFACSU-UHFFFAOYSA-N 0.000 description 1
- UFDFFEMHDKXMBG-UHFFFAOYSA-N 2-acetamidoprop-2-enoic acid Chemical class CC(=O)NC(=C)C(O)=O UFDFFEMHDKXMBG-UHFFFAOYSA-N 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- YXHKONLOYHBTNS-UHFFFAOYSA-N Diazomethane Chemical compound C=[N+]=[N-] YXHKONLOYHBTNS-UHFFFAOYSA-N 0.000 description 1
- MFESCIUQSIBMSM-UHFFFAOYSA-N I-BCP Chemical compound ClCCCBr MFESCIUQSIBMSM-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 150000001264 acyl cyanides Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 229940061720 alpha hydroxy acid Drugs 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000009615 deamination Effects 0.000 description 1
- 238000006481 deamination reaction Methods 0.000 description 1
- 238000006114 decarboxylation reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- OTGHWLKHGCENJV-UHFFFAOYSA-N glycidic acid Chemical class OC(=O)C1CO1 OTGHWLKHGCENJV-UHFFFAOYSA-N 0.000 description 1
- 150000004795 grignard reagents Chemical class 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000004715 keto acids Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- PPFNAOBWGRMDLL-UHFFFAOYSA-N methyl 2-ethoxyacetate Chemical compound CCOCC(=O)OC PPFNAOBWGRMDLL-UHFFFAOYSA-N 0.000 description 1
- 230000000269 nucleophilic effect Effects 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- UCUUFSAXZMGPGH-UHFFFAOYSA-N penta-1,4-dien-3-one Chemical class C=CC(=O)C=C UCUUFSAXZMGPGH-UHFFFAOYSA-N 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 125000001273 sulfonato group Chemical class [O-]S(*)(=O)=O 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
Definitions
- the present invention relates to a process for the carbonylation of a functionalized 1-bromoalkane to form a cyclic-keto-carboxylic acid as the predominant product.
- R represents hydrogen or a monovalent alkyl radical which can be either straight chain or branched containing from 1 to 20 carbon atoms
- X - 1, 3, 4 or 5 can be prepared by carbonylating a functionalized 1-bromoalkane of the general formula:
- R and X are as defined above and Y is a leaving group, preferably a halogen, in a liquid solvent medium, with carbon monoxide at a pressure of from 300 to 3000 psig in the presence of a catalytic amount of a metal carbonyl compound and an alkali or an alkaline earth metal inorganic base.
- R is hydrogen or a monovalent alkyl radical which can be either straight chain or branched containing from 1 to about 20 carbon atoms
- X ⁇ 1, 3, 4 or 5 and Y is a suitable leaving group,preferably the halogens viz.,
- a few exemplary materials of this type include l-bromo-3-chloro-or 3-bromopropane, butane, pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, heptadecane, octadecane, nonadecane, eicosane, and the like; l-bromo-5-chloro- or 5-bromo- pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, hepta ⁇ decane, octadecane, nonadecane, eicosane, and
- a particularly useful reactant is l-bromo-3-chloropropane from which cyclopropyl- glyoxylic acid (a precursor for the synthesis of steroids) is produced by the process of the present invention.
- the reaction is carried out in the presence of a mixture of water and alcohol as a reaction medium.
- the alcohols employed for the reaction may be straight-chain, branched or cyclic, and preferably contain up to 6 carbon atoms.
- Methanol, ethanol, propanol, isopropanol, n-butanol, isobutanol, tert- butanol, and tert-amyl alcohol may be mentioned as examples.
- Cyclic ethers such as tetrahydrofuran, also may be used.
- a particularly preferred solvent alcohol is tert-butanol.
- Mixtures containing 10% to 90% by weight of water and 90% to 10% by weight of alcohol generally are used.
- Preferred mixtures contain 307. to 80% by weight water and 70% to 20% by weight alcohol.
- the reaction takes place in the presence of a basic substance suitably an alkali or an alkaline earth metal hydroxide employing a metal carbonyl compound-
- a basic substance suitably an alkali or an alkaline earth metal hydroxide employing a metal carbonyl compound-
- the 1-bromoalkane undergoes reaction with the carbon monoxide and basic substance whereby the salt of the desired cyclic-keto-carboxylic acid is formed from which the cyclic-keto-carboxylic acid is isolated after acidification in a known manner. It is believed that the salt of the keto acid is formed first followed by intramolecular nucleophilic dis ⁇ placement under the alkaline conditions of the reaction medium to form the cyclic keto acid.
- suitable basic agents which can be used in the practice of the process include: LiOH, NaOH, KOH, RbOH, Ca(0H) 2 , Ba(0H) 2 and Mg(0H) 2 .
- LiOH and Ca(0H) 2 are particularly preferred. Yields of cyclic-keto-carboxylic acids of up to approximately 62% can be obtained using Ca(0H) 2 as the basic substance and a solvent medium of tert-butanol and water.
- the amount of basic agent used can vary within wide limits.
- the molar ratio of the alkali metal or alkaline earth metal base to 1-bromoalkane reactant is preferably 10:1 to 1:1.
- metal carbonyl compounds as carbonylation catalysts.
- These catalysts include particularly metal carbonyls such as iron pentacarbonyl, dicobalt-octa- carbonyl and nickel-tetracarbonyl, or their salts sjjch as, for example, the calcium, potassium or sodium salts thereof. Dicobalt-octacarbonyl is very particularly suited.
- These catalysts can be added to the medium in the solid state or .in the form of solutions in the solvent used for the carbonylation reaction.
- the molar percentage of the metal carbonyl compound to the 1-bromoalkane reactant is preferably from 0.1 to 25%.
- the concentration of the 1-bromoalkane used in the reaction solvent is not critical and can vary within wide limits. Thus, it can be between 1 and 307. by weight, based on the weight of the solvent, however, it is possible to go outside of these limits without disadvantage.
- the present process is advantageously carried out by bringing the mixture consisting of the 1-bromoalkane reactant, the metal carbonyl catalyst and the alkali or alkaline earth metal base, suspended in the mixture of water and alcohol, into contact, under nitrogen, in a suitable pressure-resistant reactor equipped with a stirrer, with a large excess of carbon monoxide (amount greater than 2 moles of carbon monoxide per mole of the
- OM starting 1-bromoalkane reactant introduced at the desired pressure and temperature, in accordance with techniques suitable for bringing about the reaction between a liquid phase and a gas phase.
- the carbonylation reaction is carried out at ⁇ a temperature in the range of from 30 C. to 150 C, preferably from 50°C. to 100°C, over a period of time of from 3 to 60 hours, typically 3 to 20 hours.
- the reaction takes place at elevated * carbon monoxide pressures which may range from 300 psig to 3000 psig. Preferably, the reaction takes place at a pressure in the range of 500 psig to 1000 psig.
- the carbon monoxide may contain or be mixed with an inert gas, such as nitrogen.
- the product mix ⁇ ture is filtered, resulting in the alkali metal or alkaline earth metal salt of the cyclic-keto-carboxylic acid being separated from the liquid, reaction components as the main solid component.
- the filtrate contains the remainder of the alkali or alkaline earth metal salt of the cyclic-keto-carboxylic acid, and, where unbranched alcohols are used, also esters in addition to unreacted 1-bromoalkane as well as acid and alcohol products from the starting 1-bromoalkane.
- the metal salt of the cyclic-keto-carboxylic acid is acidified with a dilute acid, such as hydrochloric acid, so as to displace the cyclic-keto-carboxylic acid from its alkali or alkaline earth metal salt.
- lower alkyl esters of the cyclic-ket ⁇ - carboxylic acid products of the present invention c.an be prepared by esterifying the cyclic-keto-carboxylic acid product according to conventional esterification tech ⁇ niques employing lower aliphatic alkanol and acid catalysts such as, for example, BF , BF ⁇ HC1, or BF ⁇ MeOH, B 3 Et 2 0 or diazomethane at suitable reaction conditions.
- Example 1 Into a 300 ml autoclave were charged 7.87 g (50 mmoles) of l-chloro-3-bromopropane and 70 ml of t-BuOH. Next, 0.682 g (2 mmoles) of Co 2 (C0)g were added under CO, and then a mixture of 7.4 g (100 mmoles) of lime and 30 ml of H 2 0 were added. After 850 psi CO was charged to the autoclave, the reaction mixture was heated to 80°C over a period of time of approximately 1 hour and held at that temperature for 15 hours. The CO uptake stopped after 11 hours.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Cyclic-keto-acids of the general formula (I), wherein R is hydrogen or a monovalent alkyl radical which can be either straight chain or branched having from 1 to 20 carbon atoms and X = 1, 3, 4 or 5, are prepared by reacting a functionalized 1-bromoalkane of the formula (II), wherein R and X are as defined above and Y is a leaving group, preferably the halogens, in a liquid solvent medium with carbon monoxide at elevated temperature and pressure in the presence of a catalytic amount of a metal carbonyl compound and an alkali or an alkaline earth metal inorganic base.
Description
PREPARATION OF CYCLIC-KETO-AC1DS
The present invention relates to a process for the carbonylation of a functionalized 1-bromoalkane to form a cyclic-keto-carboxylic acid as the predominant product.
The practical value of such acids and their esters is that they can be used in the synthesis of pharmaceuticals, such as steroids, and for preparing herbicides. The preparation of α-keto-carboxylic acids and their derivatives has been the subject of a large number of investigations. According to Rodd, The Chemistry of Carbon Compounds (1952 edition), Vol. 1, pages 227-229, the following methods of preparation are available: gentle oxidation of -hydroxyacids containing a secondary hydroxyl group, or by the enzymatic deamination of α-ainino-acids; hydrolysis of an acyl cyanide; hydrolysis of α-oximino-esters; from glycidic acid esters on treatment with benzene saturated with boron trifluoride; from a,β-dibromocarboxylic acids by forming a piperidine addition compound followed by hydrolysis;
from α-keto-acetals by ultraviolet irradiation in the presence of N-bromosuccinxmide; from α-bromomethyIke ones by boiling with selenium dioxide in absolute methanol or ethanol; β from carboxylic acid esters by oxidation with selenium dioxide; permanganate oxidation of vinyl ketones; from carboxylic acid esters by condensation with oxalic ester followed by decarboxylation; from aldehydes via 5-alkylidene-2-thio- oxazolid-4-ones or by reaction with methyl ethoxyacetate; hydrolysis of azlactones or acetamido-acrylic acids; hydrolysis of the reaction product of Grignard reagents on diethyl-oxamic ester; oxidation of α-hydroxyacid esters containing two α-hydrogen atoms by N-bromosuccinimide in carbon tetrachloride to β-bromo-α-keto-acid esters; and by the action of alkali on the dimethane- sulphonates and ditoluene-j>-sulphonates of α, &-dihydroxy-carboxylic acids. Methods for preparing arylpyruvic acids also are known. For example, U. S. Pat. No. 4,152,352 discloses
the preparation of an arylpyruvic acid by reacting an arylmethyl halide in a liquid solvent medium with carbon monoxide at pressures of 5 to 200 bars in the presence of a catalytic amount of a metal carbonyl compound and an alkaline earth metal inorganic base. Further, I . Patent Application 2,026,478A discloses that alkali metal salts of an arylpyruvic acid can be prepared by reacting an arylmethyl halide, carbon monoxide and an alkali metal base in the presence of a metal carbonyl compound as catalyst and in the presence of an alcohol or cyclic ether as solvent.
The cobalt-catalyzed carbonylation of secondary benzyl halides to give either monocarbonyl or double carbonyl insertion or coupling of organic halides is reported by E. Francalanci e_t. ^. , Journal of Electroanalytical Chemistry, 1982, pp. 59-70.
It has now been found that cyclic-keto-acids of the general formula:
-OH
in which R represents hydrogen or a monovalent alkyl radical which can be either straight chain or branched containing from 1 to 20 carbon atoms, and X - 1, 3, 4 or 5 can be prepared by carbonylating a functionalized 1-bromoalkane of the general formula:
where R and X are as defined above and Y is a leaving group, preferably a halogen, in a liquid solvent medium, with carbon monoxide at a pressure of from 300 to 3000 psig in the presence of a catalytic amount of a metal carbonyl compound and an alkali or an alkaline earth metal inorganic base.
The functionalized 1-bromoalkane reactants suitable for use in the present process are well known in the art as are methods for their preparation and, as defined above, are of the general formula:
R-CH(CHR) CH9Br I X L
when R is hydrogen or a monovalent alkyl radical which can be either straight chain or branched containing from 1 to about 20 carbon atoms, X β 1, 3, 4 or 5 and Y is a
suitable leaving group,preferably the halogens viz.,
* iodine, bromine and most preferably chlorine. Other suitable leaving groups, such as, for example, nitrates, sulfonates and acetates also may be used with the proviso that under the reaction conditions of the instant process, hydrolysis does not become a major competing reaction with the resultant production of unwanted alcohols as the major product. A few exemplary materials of this type include l-bromo-3-chloro-or 3-bromopropane, butane, pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, heptadecane, octadecane, nonadecane, eicosane, and the like; l-bromo-5-chloro- or 5-bromo- pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, hepta¬ decane, octadecane, nonadecane, eicosane, and the like; l-bromo-6-chloro- or 6-bromohexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, heptadecane, octadecane, nonadecane, eicosane and the like; l-bromo-7-chloro- or 7-bromoheptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, heptadecane, octadecane, nonadecane, eicosane, and the like; the nitrate,
sulfonate and acetate esters of l-bromo-3-hydroxy- propane, butane, pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetra¬ decane, pentadecane, hexadecane, heptadecane, octa- decane, nonadecane, eicosane and the like; the nitrate, sulfonate and acetate esters of l-bromo-5-hydroxy- pentane, hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, hexadecane, heptadecane, octadecane, nonadecane, eicosane and so forth. A particularly useful reactant is l-bromo-3-chloropropane from which cyclopropyl- glyoxylic acid (a precursor for the synthesis of steroids) is produced by the process of the present invention. The reaction is carried out in the presence of a mixture of water and alcohol as a reaction medium. Preferably, the alcohols employed for the reaction may be straight-chain, branched or cyclic, and preferably contain up to 6 carbon atoms. Methanol, ethanol, propanol, isopropanol, n-butanol, isobutanol, tert- butanol, and tert-amyl alcohol may be mentioned as examples. Cyclic ethers, such as tetrahydrofuran, also may be used. A particularly preferred solvent alcohol is tert-butanol. Mixtures containing 10% to 90% by weight of water and 90% to 10% by weight of alcohol
generally are used. Preferred mixtures contain 307. to 80% by weight water and 70% to 20% by weight alcohol. The reaction takes place in the presence of a basic substance suitably an alkali or an alkaline earth metal hydroxide employing a metal carbonyl compound- During the reaction, the 1-bromoalkane undergoes reaction with the carbon monoxide and basic substance whereby the salt of the desired cyclic-keto-carboxylic acid is formed from which the cyclic-keto-carboxylic acid is isolated after acidification in a known manner. It is believed that the salt of the keto acid is formed first followed by intramolecular nucleophilic dis¬ placement under the alkaline conditions of the reaction medium to form the cyclic keto acid. Specific examples of suitable basic agents which can be used in the practice of the process include: LiOH, NaOH, KOH, RbOH, Ca(0H)2, Ba(0H)2 and Mg(0H)2. LiOH and Ca(0H)2 are particularly preferred. Yields of cyclic-keto-carboxylic acids of up to approximately 62% can be obtained using Ca(0H)2 as the basic substance and a solvent medium of tert-butanol and water.
The amount of basic agent used can vary within wide limits. In general, the molar ratio of the alkali metal or alkaline earth metal base to 1-bromoalkane reactant is preferably 10:1 to 1:1.
In the process described herein, it is preferred to use metal carbonyl compounds as carbonylation catalysts. These catalysts include particularly metal carbonyls such as iron pentacarbonyl, dicobalt-octa- carbonyl and nickel-tetracarbonyl, or their salts sjjch as, for example, the calcium, potassium or sodium salts thereof. Dicobalt-octacarbonyl is very particularly suited. These catalysts can be added to the medium in the solid state or .in the form of solutions in the solvent used for the carbonylation reaction. The molar percentage of the metal carbonyl compound to the 1-bromoalkane reactant is preferably from 0.1 to 25%. The concentration of the 1-bromoalkane used in the reaction solvent is not critical and can vary within wide limits. Thus, it can be between 1 and 307. by weight, based on the weight of the solvent, however, it is possible to go outside of these limits without disadvantage.
The present process is advantageously carried out by bringing the mixture consisting of the 1-bromoalkane reactant, the metal carbonyl catalyst and the alkali or alkaline earth metal base, suspended in the mixture of water and alcohol, into contact, under nitrogen, in a suitable pressure-resistant reactor equipped with a stirrer, with a large excess of carbon monoxide (amount greater than 2 moles of carbon monoxide per mole of the
OM
starting 1-bromoalkane reactant) introduced at the desired pressure and temperature, in accordance with techniques suitable for bringing about the reaction between a liquid phase and a gas phase. The carbonylation reaction is carried out at^ a temperature in the range of from 30 C. to 150 C, preferably from 50°C. to 100°C, over a period of time of from 3 to 60 hours, typically 3 to 20 hours.
In general, the reaction takes place at elevated * carbon monoxide pressures which may range from 300 psig to 3000 psig. Preferably, the reaction takes place at a pressure in the range of 500 psig to 1000 psig. The carbon monoxide may contain or be mixed with an inert gas, such as nitrogen. On completion of the reaction, the product mix¬ ture is filtered, resulting in the alkali metal or alkaline earth metal salt of the cyclic-keto-carboxylic acid being separated from the liquid, reaction components as the main solid component. The filtrate contains the remainder of the alkali or alkaline earth metal salt of the cyclic-keto-carboxylic acid, and, where unbranched alcohols are used, also esters in addition to unreacted 1-bromoalkane as well as acid and alcohol products from the starting 1-bromoalkane. In a further process step, the metal salt of the cyclic-keto-carboxylic acid is acidified with a dilute
acid, such as hydrochloric acid, so as to displace the cyclic-keto-carboxylic acid from its alkali or alkaline earth metal salt.
If desired, lower alkyl esters of the cyclic-ketό- carboxylic acid products of the present invention c.an be prepared by esterifying the cyclic-keto-carboxylic acid product according to conventional esterification tech¬ niques employing lower aliphatic alkanol and acid catalysts such as, for example, BF , BF~ HC1, or BF~ MeOH, B 3 Et20 or diazomethane at suitable reaction conditions.
The following example illustrates the invention.
Example 1 Into a 300 ml autoclave were charged 7.87 g (50 mmoles) of l-chloro-3-bromopropane and 70 ml of t-BuOH. Next, 0.682 g (2 mmoles) of Co2(C0)g were added under CO, and then a mixture of 7.4 g (100 mmoles) of lime and 30 ml of H20 were added. After 850 psi CO was charged to the autoclave, the reaction mixture was heated to 80°C over a period of time of approximately 1 hour and held at that temperature for 15 hours. The CO uptake stopped after 11 hours. After centrifugation, the solid was rinsed once with a 20 ml portion of a 50:50 t-butanol/water solution and then acidified with 150 ml of HC1 solution containing 100 mmoles of HC1. The free acid was extracted from the aqueous solution
with diethyl ether (2 x 120 ml) to give a 62% yield ι of cyclopropylglyoxylic acid based on proton NMR data with internal standard.
OMP
Claims
1. A process for the production of cyclic-keto- acids of the general formula:
where R is hydrogen or a monovalent alkyl radical which can be either straight chain or branched having from 1 to 20 carbon atoms and X = 1, 3, 4 or 5 which comprises reacting a functionalized 1-bromoalkane of the formula:
R-CH(CHR) CH Br I x Δ Y where R and X are as defined above and Y represents a leaving group, in a liquid solvent medium, with carbon monoxide at elevated temperature and pressure in the presence of a catalytic amount of a metal carbonyl com¬ pound and an alkali or an alkaline earth metal inorganic base.
2. The process as claimed in Claim 1 in which the functionalized 1-bromoalkane is l-bromo-3-chloro- or 3-bromopropane.
3. The process as claimed in Claim 1 in which the leaving group is selected from the halogens, nitrates, sulfonates or acetates.
4 The process as claimed in Claim 1 in which the carbon monoxide pressure is from 300 to 3000 psig.
5. The process as claimed in Claim 1 in which the reaction is carried out at a temperature of from
30°C. to 150°C.
6. The process as claimed in Claim 1 in which the inorganic base is selected from LiOH, NaOH, KOH, RbOH, Ca(0H)2, Ba(0H)2 or Mg(0H)2.
7. The process as claimed in Claim 1 in which the metal carbonyl is dicobalt-octacarbonyl.
8. The process as claimed in Claim 1 in which the liquid solvent medium is a mixture of water and alcohol.
9. The process as claimed in Claim 8 in which the alcohol is tert-butanol.
10. The process as claimed in Claim 8 in which the alcohol is isopropanol.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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JP50007883A JPS61500429A (en) | 1983-11-15 | 1983-11-15 | Production method of cyclic keto acid |
PCT/US1983/001810 WO1985002181A1 (en) | 1983-11-15 | 1983-11-15 | Preparation of cyclic-keto-acids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/US1983/001810 WO1985002181A1 (en) | 1983-11-15 | 1983-11-15 | Preparation of cyclic-keto-acids |
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WO1985002181A1 true WO1985002181A1 (en) | 1985-05-23 |
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PCT/US1983/001810 WO1985002181A1 (en) | 1983-11-15 | 1983-11-15 | Preparation of cyclic-keto-acids |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US6002359A (en) * | 1997-06-13 | 1999-12-14 | Trw Inc. | Antenna system for satellite digital audio radio service (DARS) system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2874186A (en) * | 1954-12-08 | 1959-02-17 | Sinclair Refining Co | Carbonylation of saturated hydrocarbons |
US3665034A (en) * | 1968-04-25 | 1972-05-23 | Maruzen Oil Co Ltd | Process for the production of carboxylic acids |
US3816488A (en) * | 1968-08-15 | 1974-06-11 | Monsanto Co | Increasing the selectivity and yield in the production of carboxylic acids |
US4152352A (en) * | 1975-01-09 | 1979-05-01 | Rhone-Poulenc Industries | Process for the carbonylation of aralkylhalides |
GB2026478A (en) * | 1978-06-26 | 1980-02-06 | Dynamit Nobel Ag | Process for producing alkali metal salts of aryl pyruvic acids |
-
1983
- 1983-11-15 WO PCT/US1983/001810 patent/WO1985002181A1/en unknown
- 1983-11-15 JP JP50007883A patent/JPS61500429A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2874186A (en) * | 1954-12-08 | 1959-02-17 | Sinclair Refining Co | Carbonylation of saturated hydrocarbons |
US3665034A (en) * | 1968-04-25 | 1972-05-23 | Maruzen Oil Co Ltd | Process for the production of carboxylic acids |
US3816488A (en) * | 1968-08-15 | 1974-06-11 | Monsanto Co | Increasing the selectivity and yield in the production of carboxylic acids |
US4152352A (en) * | 1975-01-09 | 1979-05-01 | Rhone-Poulenc Industries | Process for the carbonylation of aralkylhalides |
GB2026478A (en) * | 1978-06-26 | 1980-02-06 | Dynamit Nobel Ag | Process for producing alkali metal salts of aryl pyruvic acids |
Non-Patent Citations (2)
Title |
---|
Journal of Electroanalytical Chemistry 1982, Francilanci et al, pages 59-70 * |
The Chemistry of Carbon Compounds, Vol. 1, 1952, Robb, pages 227-229 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6002359A (en) * | 1997-06-13 | 1999-12-14 | Trw Inc. | Antenna system for satellite digital audio radio service (DARS) system |
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