WO2011016409A1 - アルコール化合物の製造方法 - Google Patents
アルコール化合物の製造方法 Download PDFInfo
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- WO2011016409A1 WO2011016409A1 PCT/JP2010/062995 JP2010062995W WO2011016409A1 WO 2011016409 A1 WO2011016409 A1 WO 2011016409A1 JP 2010062995 W JP2010062995 W JP 2010062995W WO 2011016409 A1 WO2011016409 A1 WO 2011016409A1
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- 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
- C07C29/128—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by alcoholysis
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Definitions
- the present invention relates to an alcohol compound production method for producing an alcohol compound from an amide compound or an amine compound.
- amide compounds exist in nature, and many of them are difficult to synthesize by organic synthesis.
- further synthesis development of amide compounds is limited by functional groups of the compounds. Therefore, if raw material compounds that can be developed in organic synthesis can be produced from these amide compounds, it is expected that a new path will be opened for the synthesis development of pharmaceuticals, intermediate raw materials and chemical raw materials.
- a large number of amine compounds exist naturally in amino acids and the like, and the establishment of a functional group conversion method is expected to expand the range of synthetic development of pharmaceuticals, intermediate raw materials and chemical raw materials. For example, it is conceivable to obtain an alcohol compound from these amide compounds and amine compounds.
- Patent Document 1 describes a method of producing methyl 6-hydroxycaproate by reacting nylon 6 with methanol in a supercritical state.
- Patent Document 2 describes a method for producing a fluorine-containing benzyl alcohol derivative by reacting a fluorine-containing benzylamine derivative with an acid and an alkali nitrite.
- Patent Documents 1 and 2 have a problem that the yield of the obtained alcohol compound is not always sufficient. Then, this invention aims at providing the manufacturing method of the alcohol compound which can obtain an alcohol compound with a high yield from an amide compound or an amine compound.
- the present inventors have made an amide compound or an amine compound by allowing a supercritical alcohol to act on the amide compound or amine compound in the presence of a carboxylic acid derivative. It has been found that an alcohol compound can be obtained from the compound in a high yield. That is, the present invention is a method for producing an alcohol compound, wherein an alcohol compound is obtained by allowing a supercritical alcohol to act on an amide compound or an amine compound in the presence of a carboxylic acid derivative.
- examples of the amide compound used as a raw material include amide compounds represented by Chemical Formula 1.
- R 1 is a hydrocarbon group having 1 to 50 carbon atoms, preferably 1 to 36 carbon atoms. Specifically, methyl group, ethyl group, n-propyl group, i-propyl group, n- Examples thereof include linear or branched alkyl groups such as butyl group, i-butyl group, n-pentyl group, i-pentyl group, hexyl group and octyl group, and aromatic alkyl groups such as benzyl group. Are an octyl group and a benzyl group.
- R 2 is hydrogen or a hydrocarbon group having 1 to 50 carbon atoms, preferably 1 to 36 carbon atoms, specifically, a linear or branched alkyl group such as hydrogen, methyl group, or ethyl group. Examples thereof include hydrogen and methyl group.
- R 3 includes a hydrocarbon group having 1 to 50 carbon atoms, preferably 1 to 36 carbon atoms, and more preferably 1 to 24 carbon atoms.
- R 1 and R 2 may be bonded to form a ring.
- the formed ring is a 3- to 50-membered ring, preferably a 4- to 24-membered ring, preferably a 7-membered ring or a 13-membered ring.
- amide compounds include N-dodecyloctanoic acid amide, N, N-dimethylformamide, N, N-diethylformamide, N, N-di-i-propylformamide, N, N-dibutylformamide, N , N-dipentylformamide, N, N-dioctylformamide, N-methyl, N-stearylformamide, ⁇ -caprolactam, ⁇ -laurolactam, and cyclic amides such as N-methylcaprolactam.
- N-dodecyloctanoic acid amide, ⁇ -caprolactam and ⁇ -laurolactam are preferable.
- the amide bond is substituted with a hydroxyl group by cutting the bond on the amino group side that forms the amide bond. 2 can be obtained.
- N-dodecyloctanoic acid amide is used as a starting compound, 1-dodecanol can be obtained.
- examples of amine compounds used as raw materials include aliphatic primary amines, aliphatic secondary amines, aliphatic tertiary amines, aromatic amines, diamine compounds, and cyclic amine compounds. Can be mentioned.
- R 3 has the same meaning as in Chemical Formula 1
- R 4 and R 5 are hydrogen or a hydrocarbon group having 1 to 24 carbon atoms, preferably 1 to 18 carbon atoms, more preferably 1 to 12 carbon atoms.
- R 4 and R 5 are hydrogen or a hydrocarbon group having 1 to 24 carbon atoms, preferably 1 to 18 carbon atoms, more preferably 1 to 12 carbon atoms.
- R 4 and R 5 are hydrogen or a hydrocarbon group having 1 to 24 carbon atoms, preferably 1 to 18 carbon atoms, more preferably 1 to 12 carbon atoms.
- R 4 and R 5 are hydrogen or a hydrocarbon group having 1 to 24 carbon atoms, preferably 1 to 18 carbon atoms, more preferably 1 to 12 carbon atoms.
- amine compounds include methylamine, ethylamine, propylamine, butylamine, pentylamine, hexylamine, heptylamine, octylamine, nonylamine, decylamine, undecylamine, dodecylamine, tridecylamine, tetradecylamine.
- Primary amines such as pentadecylamine, cetylamine and benzylamine, secondary amines such as N-methyldodecylamine and dibenzylamine, and tertiary amines such as N, N-dimethyldodecylamine and tribenzylamine.
- Preferred are dodecylamine, hexylamine, benzylamine, dibenzylamine, and tribenzylamine.
- the amine compound represented by Chemical Formula 3 when used as a raw material compound, the amino group is substituted with a hydroxyl group, and the alcohol compound represented by Chemical Formula 2 can be obtained.
- dodecylamine when used as a raw material compound, 1-dodecanol can be obtained.
- cyclic amide compound examples include cyclic amines shown in Chemical formula 5.
- n is an integer of 2 to 12, more preferably 6 to 12, and hydrogen bonded to each carbon is substituted with another functional group as long as the reaction in the alcohol production method according to the present invention is not inhibited. May be.
- cyclic amine compounds include hexamethyleneimine, heptamethyleneimine, octamethyleneimine, dodecamethyleneimine and the like. Preferred are hexamethyleneimine, heptamethyleneimine, octamethyleneimine, and dodecamethyleneimine.
- diamine compound examples include diamines shown in Chemical formula 7.
- n is an integer of 2 to 12, preferably 6 to 12, and hydrogen bonded to each carbon is substituted with other functional groups as long as the reaction in the alcohol production method according to the present invention is not inhibited. May be.
- diamine compounds include hexamethylene diamine and dodecamethylene diamine. Preferred is hexamethylene diamine.
- the method for producing an alcohol compound according to the present invention is a novel method for producing an alcohol compound from an amide compound or an amine compound. For example, it may open a new path for the synthesis development of pharmaceuticals, intermediate raw materials, and chemical products. it can.
- Examples of the alcohol used for producing the alcohol compound according to the present invention include methanol, ethanol, 1-propanol (n-propanol), 2-propanol, (isopropanol), allyl alcohol, 1-butanol (n-butanol), 2- Butanol (sec-butanol), 2-methyl-1-propanol (isobutanol), 2-methyl-2-propanol (t-butanol), 3-buten-2-ol, crotyl alcohol, cyclopropanemethanol, 3- Buten-1-ol, 2-methyl-2-propen-1-ol, 3-butyn-1-ol, 2-butyn-1-ol, 3-butyn-2-ol, 1-pentanol (n-penol Thanol), 2-pentanol (sec-amyl alcohol), 3-pentanol, 2- Tyl-1-butanol, 2-methyl-2-butanol, 3-methyl-2-butanol, 3-methyl-1-butano
- the number of carbons of these alcohols is not particularly limited, but primary alcohols are preferable, and chain fatty acids having 1 to 6 carbon atoms such as methanol, ethanol, n-propanol, n-butanol, n-pentanol, and n-hexanol.
- a group alcohol is more preferable, and methanol is particularly preferable.
- These alcohols can be brought into a supercritical state by, for example, heating and pressurizing these alcohols or heating them in a sealed state.
- the critical temperature and critical pressure of main alcohols are as shown in Table 1.
- the reaction temperature is, for example, 200 to 400 ° C., preferably 220 to 330 ° C., particularly preferably 250 ° C. or higher.
- the pressure is 5 to 40 MPaG (G represents a gauge pressure), preferably 8 MPaG or more.
- the amide compound or amine compound, the alcohol and the carboxylic acid derivative may be mixed at the same time, and then the alcohol may be brought into a supercritical state by heating or the like. These may be added to the amide compound or amine compound in a supercritical state.
- the reaction time of the amide compound or amine compound and the alcohol is preferably 5 minutes to 48 hours, more preferably 0.5 hours to 24 hours, still more preferably 1 hour. ⁇ 6 hours.
- the ratio of the amide compound or the amine compound to the total weight of the alcohol acting on the amide compound or the amine compound is preferably more than 0 and 50% by weight or less, more preferably 0.5 to 30% by weight, and more preferably 3 to 10% by weight. % Is particularly preferred.
- the carboxylic acid derivative used in the method for producing an alcohol compound according to the present invention is not particularly limited, but carboxylic acid or carboxylic acid ester is preferable.
- carboxylic acid examples include aliphatic carboxylic acids and aromatic carboxylic acids.
- the aliphatic carboxylic acid is an aliphatic carboxylic acid having 1 to 12 carbon atoms, preferably an aliphatic carboxylic acid having 2 to 8 carbon atoms, and specifically includes acetic acid, propionic acid, butyric acid, methoxyacetic acid, pentane.
- the acid include caproic acid, heptanoic acid, octanoic acid, lactic acid, and glycolic acid, and acetic acid, lactic acid, glycolic acid, and octanoic acid are preferable.
- aromatic carboxylic acid examples include terephthalic acid, isophthalic acid, orthophthalic acid, trimellitic acid, benzoic acid, cresolic acid, naphthoic acid, naphthalenedicarboxylic acid, and benzoic acid is preferable.
- the ester of carboxylic acid is an ester of the above aliphatic carboxylic acid or aromatic carboxylic acid, linear or branched having 1 to 50 carbon atoms, preferably 1 to 36 carbon atoms, more preferably 1 to 24 carbon atoms. And an ester with an alkyl alcohol in the form of a ring. Specific examples include methyl acetate, methyl glycolate, and methyl propionate.
- the amount of the carboxylic acid derivative used is preferably 1 to 1000% by weight, particularly preferably 71 to 1270% by weight, based on the amide compound or amine compound.
- reaction rate will fall or the yield of a hydroxycarboxylic acid derivative will fall.
- Examples of the reaction apparatus used in the present invention include a cylindrical tank with a stirrer and a tubular reaction tank.
- the reaction format may be either a continuous method or a batch method.
- the amide compound or amine compound, the carboxylic acid derivative and the alcohol can be separately supplied to the reaction apparatus, but those previously mixed may be supplied to the reaction apparatus.
- the reaction solution containing the alcohol compound obtained by the method for producing an alcohol compound according to the present invention the alcohol and the carboxylic acid derivative that have acted on the amide compound or the amine compound are separated and removed by flash distillation or the like. When an alcohol compound with high purity is desired, it is further purified by distillation under reduced pressure or the like.
- the reactor is composed of stainless steel (SUS316) piping (outer diameter 3/8 inch, inner diameter 7.53 mm, length 23 cm) and caps at both ends (SS-600-C manufactured by Swagelok), and has a volume of 10 mL.
- SUS316 stainless steel
- An electric furnace manufactured by ADVANTEC: DRD360DA
- GC-2014 manufactured by Shimadzu Corporation was used.
- the yield of the produced target alcohol was calculated based on [mol amount of produced target alcohol] / [mol amount of charged amide compound or amine compound] ⁇ 100.
- Example 1 N-dodecyloctanoic acid amide (0.30 g), methanol (4.00 g), and methyl octoate (0.64 g) as a carboxylic acid derivative were added to a 10 mL-volume piping reactor, and the mixture was sealed with nitrogen at room temperature. .
- the reactor was put into an electric furnace heated to 330 ° C. and reacted for 3 hours (pressure 34.0 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and cyclododecanol as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis.
- the integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1-dodecanol was 62%.
- Example 2 The same procedure as in Example 1 was carried out except that methyl acetate (0.38 g) was used as the carboxylic acid derivative (pressure 33.0 MPa). As a result, the yield of 1-dodecanol was 57%.
- Example 3 The same procedure as in Example 1 was performed except that methyl propionate (0.45 g) was used as the carboxylic acid derivative (pressure 33.0 MPa). As a result, the yield of 1-dodecanol was 62%.
- Example 4 The same operation as in Example 1 was performed except that the carboxylic acid derivative was changed to lactic acid (0.46 g) (pressure 33.1 MPa). As a result, the yield of 1-dodecanol was 66%.
- Example 5 The same procedure as in Example 1 was carried out except that the carboxylic acid derivative was changed to benzoic acid (0.62 g) (pressure 34.0 MPa). As a result, the yield of 1-dodecanol was 67%.
- Example 6 The same operation as in Example 8 was performed except that the carboxylic acid derivative was changed to glycolic acid (0.38 g) (pressure 32.8 MPa). As a result, the yield of 1-dodecanol was 67%.
- Comparative Example 1 The same operation as in Example 6 was performed except that the carboxylic acid derivative was changed to no addition (pressure 28.0 MPa). As a result, the yield of 1-dodecanol was 19%.
- Example 7 A 10 mL capacity pipe reactor (outside diameter 3/8 inch, inside diameter 7.53 mm, length 23 cm) was charged with N-dodecyloctanoic acid amide (0.30 g), methanol (3.00 g), acetic acid (0.60 g). And purged with nitrogen at room temperature and sealed. The reactor was put into an electric furnace heated to 330 ° C. and reacted for 3 hours (pressure 24.0 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and cyclododecanol as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis.
- the integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1-dodecanol was 67%.
- Example 8 N-dodecyloctanoic acid amide (0.30 g), methanol (3.01 g), and methyl acetate (0.76 g) were added to a pipe reactor with a volume of 10 mL, and the mixture was sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 330 ° C. and reacted for 3 hours (pressure 24.4 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and cyclododecanol as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1-dodecanol was 64%.
- Example 9 N-dodecyloctanoic acid amide (0.30 g), methanol (3.01 g), and lactic acid (0.46 g) were added to a pipe reactor having a volume of 10 mL, and sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 300 ° C. and reacted for 3 hours (pressure 18.0 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and cyclododecanol as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1-dodecanol was 57%.
- Example 10 N-dodecyloctanoic acid amide (0.3 g), acetic acid (0.30 g) and methanol (3.0 g) were added to a pipe reactor having a volume of 10 mL, and the mixture was sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 300 ° C. (pressure 17.8 MPa), and the change with time was measured. For the measurement, cyclododecanol was weighed as the obtained reaction mixture and an internal standard substance, and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield of 1-dodecanol was determined from the prepared calibration curve table. These results are shown in Table 2.
- Example 11 To a 10 mL capacity pipe reactor, dodecylamine (0.19 g), octanoic acid (0.14 g) and methanol (4.0 g) as carboxylic acid derivatives were added and sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 330 ° C. and reacted for 4 hours (pressure 28.1 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. The obtained reaction mixture and cyclododecanol as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1-dodecanol was 53%.
- Comparative Example 2 The same operation as in Example 11 was carried out except that the carboxylic acid derivative was changed to no addition (pressure 26.2 MPa). As a result, the yield of 1-dodecanol was 4%.
- Example 12 Benzylamine (0.10 g), methanol (3.02 g), and glycolic acid (0.38 g) were added to a 10 mL capacity pipe reactor, and sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 270 ° C. and reacted for 160 minutes (pressure 10.7 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. Hexanol was weighed as an internal standard substance and the obtained reaction mixture, and used as an analytical sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of benzyl alcohol was 72%.
- Example 13 The reaction was performed in the same manner as in Example 12 except that the reaction temperature was 300 ° C. and the reaction time was 120 minutes (pressure 14.5 MPa). As a result, the yield of benzyl alcohol was 71%.
- Example 14 The same procedure as in Example 12 was performed except that the amount of glycolic acid added was 0.071 g and the reaction time was 360 minutes (pressure 10.8 MPa). As a result, the yield of benzyl alcohol was 77%.
- Example 15 The same procedure as in Example 14 was carried out except that acetic acid (1.27 g) was used as the carboxylic acid derivative (pressure 10.7 MPa). As a result, the yield of benzyl alcohol was 65%.
- Comparative Example 3 The same operation as in Example 14 was carried out except that the carboxylic acid derivative was not added (pressure 10.6 MPa). As a result, the yield of benzyl alcohol was 3%.
- Example 16 Dibenzylamine (0.10 g), methanol (3.00 g), and glycolic acid (0.38 g) were added to a 10 mL capacity pipe reactor, and sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 300 ° C. and reacted for 1 hour (pressure 14.5 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. Hexanol was weighed as an internal standard substance and the obtained reaction mixture, and used as an analytical sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of benzyl alcohol was 83%.
- Comparative Example 4 The same operation as in Example 16 was performed except that the carboxylic acid derivative was not added (pressure 14.5 MPa). As a result, the yield of benzyl alcohol was 20%.
- Example 17 Tribenzylamine (0.10 g), methanol (3.01 g), and glycolic acid (0.38 g) were added to a 10 mL capacity pipe reactor, and sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 270 ° C. and reacted for 6 hours (pressure 10.7 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. Hexanol was weighed as an internal standard substance and the obtained reaction mixture, and used as an analytical sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of benzyl alcohol was 33%.
- Example 18 Hexamethyleneimine (0.11 g), methanol (3.01 g), and glycolic acid (0.23 g) were added to a 10 mL capacity pipe reactor, and sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 250 ° C. and reacted for 6 hours (pressure 8.8 Mpa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1,6-hexanediol was 42%.
- Example 19 The same procedure as in Example 18 was carried out except that the amount of glycolic acid added was 0.77 g (pressure 8.9 MPa). As a result, the yield of 1,6-hexanediol was 41%.
- Example 20 The reaction was performed in the same manner as in Example 19 except that the reaction temperature was 270 ° C. and the reaction time was 100 minutes (pressure 10.8 MPa). As a result, the yield of 1,6-hexanediol was 37%.
- Example 21 The reaction was performed in the same manner as in Example 19 except that the reaction temperature was 300 ° C. and the reaction time was 1 hour (pressure 14.7 MPa). As a result, the yield of 1,6-hexanediol was 36%.
- Example 22 The same operation as in Example 18 was performed except that lactic acid (1.14 g) was used as the carboxylic acid derivative (pressure 8.6 MPa). As a result, the yield of 1,6-hexanediol was 38%.
- Example 23 The same operation as in Example 18 was performed except that benzoic acid (1.23 g) was used as the carboxylic acid derivative (pressure 8.6 MPa). As a result, the yield of 1,6-hexanediol was 31%.
- Example 24 Heptamethyleneimine (0.10 g), methanol (3.00 g), and glycolic acid (0.20 g) were added to a pipe reactor with a volume of 10 mL, and the mixture was sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 300 ° C. and reacted for 140 minutes (pressure 14.5 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. Benzyl alcohol was weighed as the obtained reaction mixture and internal standard substance, and used as an analytical sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1,7-heptanediol was 61%.
- Example 25 The reaction was performed in the same manner as in Example 25 except that the reaction temperature was 250 ° C. and the reaction time was 240 minutes (pressure 8.6 MPa). As a result, the yield of 1,7-heptanediol was 48%.
- Example 26 The reaction was performed in the same manner as in Example 25 except that the reaction temperature was 270 ° C. and the reaction time was 360 minutes (pressure 10.7 MPa). As a result, the yield of 1,7-heptanediol was 52%.
- Example 27 Octamenimine (0.10 g), methanol (3.00 g), and glycolic acid (0.18 g) were added to a pipe reactor with a volume of 10 mL, and the mixture was sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 300 ° C. and reacted for 4 hours (pressure 14.5 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1,8-octanediol was 54%.
- Example 28 The reaction was performed in the same manner as in Example 28 except that the reaction temperature was 250 ° C. and the reaction time was 360 minutes (pressure 8.7 MPa). As a result, the yield of 1,8-octanediol was 52%.
- Example 29 The reaction was performed in the same manner as in Example 28 except that the reaction temperature was 270 ° C. and the reaction time was 300 minutes (pressure 10.7 MPa). As a result, the yield of 1,8-octanediol was 54%.
- Example 30 Dodecamethyleneimine (0.10 g), methanol (3.00 g), and glycolic acid (0.12 g) were added to a pipe reactor having a volume of 10 mL, and sealed with nitrogen at room temperature. The reactor was put into an electric furnace heated to 300 ° C. and reacted for 240 minutes (pressure 14.5 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. The obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1,12-dodecanediol was 56%.
- Example 31 1,6-Hexanediamine (0.10 g), methanol (3.00 g), and glycolic acid (0.20 g) were added to a 10 mL capacity pipe reactor, and sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 270 ° C. and reacted for 160 minutes (pressure 10.6 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of 1,6-hexanediol was 43%.
- Example 32 ⁇ -Caprolactam (0.10 g), methanol (3.00 g), and glycolic acid (0.23 g) were added to a pipe reactor with a volume of 10 mL, and sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 300 ° C. and reacted for 180 minutes (pressure 14.6 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected.
- the obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis. The integrated value was calculated by gas chromatography analysis, and the yield was determined from the prepared calibration curve table. As a result, the yield of methyl hydroxyhexanoate was 41.2%.
- Example 33 ⁇ -laurolactam (0.10 g), methanol (3.00 g) and glycolic acid (0.23 g) were added to a pipe reactor with a volume of 10 mL, and the mixture was sealed with nitrogen at room temperature.
- the reactor was put into an electric furnace heated to 300 ° C. and reacted for 240 minutes (pressure 14.6 MPa). Thereafter, the reactor was taken out of the electric furnace, rapidly cooled with a cold water bath, and the reaction was stopped. After confirming that the reactor was sufficiently cooled, the reaction mixture was taken out with methanol and collected. The obtained reaction mixture and anisole as an internal standard substance were weighed and used as an analysis sample for gas chromatography analysis.
- the integrated value was calculated by gas chromatography analysis, and the yield was determined from a calibration curve table prepared using ⁇ -laurolactam as the factor of methyl hydroxydodecanoate. As a result, the yield of methyl hydroxydodecanoate was 67.7%.
Abstract
Description
500mL二口フラスコにドデシルアミン(18.69g)、DMAP(N,N-ジメチル-4-アミノピリジン)(3.67g)、を加え窒素置換を行った。次いで、これにジクロロメタン(150mL)と炭酸カリウム(16.67g)を加えた。このフラスコを氷浴により冷却した状態でジクロロメタン(150mL)とオクタン酸クロリド(17.94g)を混合させた溶液の滴下を行った。滴下終了後、室温に昇温し4時間反応を行った。反応終了はガスクロマトグラフィーにて確認し、飽和塩化アンモニウム水溶液を50mL加えた。10分間撹拌した後、ジクロロメタン(100mL)により抽出を行い、得られた有機相を1M塩酸水溶液(50mL)、飽和炭酸水素ナトリウム水溶液(50mL)、飽和食塩水(50mL)で洗浄した。溶媒の減圧留去をエバポレーターにて行い、ジクロロメタン-ヘキサンにて再結晶を行った。目的のN-ドデシルオクタン酸アミドの収率は、ドデシルアミン基準で89%(20.13g、89.42mmol)であった。
容積10mLの配管反応器に、N-ドデシルオクタン酸アミド(0.30g)、メタノール(4.00g)、カルボン酸誘導体としてオクタン酸メチル(0.64g)を加え、室温で窒素置換を行い密閉した。反応器を330℃に加熱した電気炉に投入し、3時間反応させた(圧力34.0MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1-ドデカノールの収率は62%であった。
カルボン酸誘導体として酢酸メチル(0.38g)に変更した以外は、実施例1と同様に行った(圧力33.0MPa)。その結果、1-ドデカノールの収率は57%であった。
カルボン酸誘導体としてプロピオン酸メチル(0.45g)に変更した以外は、実施例1と同様に行った(圧力33.0MPa)。その結果、1-ドデカノールの収率は62%であった。
カルボン酸誘導体として乳酸(0.46g)に変更した以外は、実施例1と同様に行った(圧力33.1MPa)。その結果、1-ドデカノールの収率は66%であった。
カルボン酸誘導体として安息香酸(0.62g)に変更した以外は、実施例1と同様に行った(圧力34.0MPa)。その結果、1-ドデカノールの収率は67%であった。
カルボン酸誘導体としてグリコール酸(0.38g)に変更した以外は、実施例8と同様に行った(圧力32.8MPa)。その結果、1-ドデカノールの収率は67%であった。
カルボン酸誘導体を無添加に変更した以外は、実施例6と同様に行った(圧力28.0MPa)。その結果、1-ドデカノールの収率は19%であった。
容積10mLの配管反応器(外径3/8インチ、内径7.53mm、長さ23cm)に、N-ドデシルオクタン酸アミド(0.30g)、メタノール(3.00g)、酢酸(0.60g)を加え、室温で窒素置換を行い密閉した。反応器を330℃に加熱した電気炉に投入し、3時間反応させた(圧力24.0MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1-ドデカノールの収率は67%であった。
容積10mLの配管反応器に、N-ドデシルオクタン酸アミド(0.30g)、メタノール(3.01g)、酢酸メチル(0.76g)を加え、室温で窒素置換を行い密閉した。反応器を330℃に加熱した電気炉に投入し、3時間反応させた(圧力24.4MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1-ドデカノールの収率は64%であった。
容積10mLの配管反応器に、N-ドデシルオクタン酸アミド(0.30g)、メタノール(3.01g)、乳酸(0.46g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、3時間反応させた(圧力18.0MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1-ドデカノールの収率は57%であった。
容積10mLの配管反応器に、N-ドデシルオクタン酸アミド(0.3g)、酢酸(0.30g)、メタノール(3.0g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し(圧力17.8MPa)、経時変化を測定した。測定は、得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から1-ドデカノールの収率を求めた。これらの結果を表2に示す。
容積10mLの配管反応器に、ドデシルアミン(0.19g)、カルボン酸誘導体としてオクタン酸(0.14g)、メタノール(4.0g)を加え、室温で窒素置換を行い密閉した。反応器を330℃に加熱した電気炉に投入し、4時間反応させた(圧力28.1MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてシクロドデカノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1-ドデカノールの収率は53%であった。
カルボン酸誘導体を無添加に変更した以外は、実施例11と同様に行った(圧力26.2MPa)。その結果、1-ドデカノールの収率は4%であった。
容積10mLの配管反応器に、ベンジルアミン(0.10g)、メタノール(3.02g)、グリコール酸(0.38g)を加え、室温で窒素置換を行い密閉した。反応器を270℃に加熱した電気炉に投入し、160分間反応させた(圧力10.7MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてヘキサノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、ベンジルアルコールの収率は72%であった。
反応温度を300℃とし、反応時間を120分とした以外は、実施例12と同様に行った(圧14.5MPa)。その結果、ベンジルアルコールの収率は71%であった。
グリコール酸の添加量を0.071gとし、反応時間を360分とした以外は、実施例12と同様に行った(圧力10.8MPa)。その結果、ベンジルアルコールの収率は77%であった。
カルボン酸誘導体として酢酸(1.27g)とした以外は、実施例14と同様に行った(圧力10.7MPa)。その結果、ベンジルアルコールの収率は65%であった。
カルボン酸誘導体を添加しなかった以外は、実施例14と同様に行った(圧力10.6MPa)。その結果、ベンジルアルコールの収率は3%であった。
容積10mLの配管反応器に、ジベンジルアミン(0.10g)、メタノール(3.00g)、グリコール酸(0.38g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、1時間反応させた(圧力14.5MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてヘキサノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、ベンジルアルコールの収率は83%であった。
カルボン酸誘導体を添加しなかった以外は、実施例16と同様に行った(圧力14.5MPa)。その結果、ベンジルアルコールの収率は20%であった。
容積10mLの配管反応器に、トリベンジルアミン(0.10g)、メタノール(3.01g)、グリコール酸(0.38g)を加え、室温で窒素置換を行い密閉した。反応器を270℃に加熱した電気炉に投入し、6時間反応させた(圧力10.7MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてヘキサノールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、ベンジルアルコールの収率は33%であった。
容積10mLの配管反応器に、ヘキサメチレンイミン(0.11g)、メタノール(3.01g)、グリコール酸(0.23g)を加え、室温で窒素置換を行い密閉した。反応器を250℃に加熱した電気炉に投入し、6時間反応させた(圧力8.8Mpa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1,6-ヘキサンジオールの収率は42%であった。
グリコール酸の添加量を0.77gとした以外は、実施例18と同様に行った(圧力8.9MPa)。その結果、1,6-ヘキサンジオールの収率は41%であった。
反応温度を270℃とし、反応時間を100分とした以外は、実施例19と同様に行った(圧力10.8MPa)。その結果、1,6-ヘキサンジオールの収率は37%であった。
反応温度を300℃とし、反応時間を1時間とした以外は、実施例19と同様に行った(圧力 14.7MPa)。その結果、1,6-ヘキサンジオールの収率は36%であった。
カルボン酸誘導体として乳酸(1.14g)とした以外は、実施例18と同様に行った(圧力8.6MPa)。その結果、1,6-ヘキサンジオールの収率は38%であった。
カルボン酸誘導体として安息香酸(1.23g)とした以外は、実施例18と同様に行った(圧力8.6MPa)。その結果、1,6-ヘキサンジオールの収率は31%であった。
容積10mLの配管反応器に、ヘプタメチレンイミン(0.10g)、メタノール(3.00g)、グリコール酸(0.20g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、140分間反応させた(圧力14.5MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてベンジルアルコールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1,7-ヘプタンジオールの収率は61%であった。
反応温度を250℃とし、反応時間を240分とした以外は、実施例25と同様に行った(圧力8.6MPa)。その結果、1,7-ヘプタンジオールの収率は48%であった。
反応温度を270℃とし、反応時間を360分とした以外は、実施例25と同様に行った(圧力 10.7MPa)。その結果、1,7-ヘプタンジオールの収率は52%であった。
容積10mLの配管反応器に、オクタメチレンイミン(0.10g)、メタノール(3.00g)、グリコール酸(0.18g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、4時間反応させた(圧力14.5MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1,8-オクタンジオールの収率は54%であった。
反応温度を250℃とし、反応時間を360分とした以外は、実施例28と同様に行った(圧力 8.7MPa)。その結果、1,8-オクタンジオールの収率は52%であった。
反応温度を270℃とし、反応時間を300分とした以外は、実施例28と同様に行った(圧力 10.7MPa)。その結果、1,8-オクタンジオールの収率は54%であった。
容積10mLの配管反応器に、ドデカメチレンイミン(0.10g)、メタノール(3.00g)、グリコール酸(0.12g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、240分間反応させた(圧力14.5MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1、12-ドデカンジオールの収率は56%であった。
容積10mLの配管反応器に、1、6-ヘキサンジアミン(0.10g)、メタノール(3.00g)、グリコール酸(0.20g)を加え、室温で窒素置換を行い密閉した。反応器を270℃に加熱した電気炉に投入し、160分間反応させた(圧力10.6MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、1,6-ヘキサンジオールの収率は43%であった。
容積10mLの配管反応器に、ε-カプロラクタム(0.10g)、メタノール(3.00g)、グリコール酸(0.23g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、180分間反応させた(圧力14.6MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、作成した検量線表から収量を求めた。その結果、ヒドロキシヘキサン酸メチルの収率は41.2%であった。
容積10mLの配管反応器に、ω-ラウロラクタム(0.10g)、メタノール(3.00g)、グリコール酸(0.23g)を加え、室温で窒素置換を行い密閉した。反応器を300℃に加熱した電気炉に投入し、240分間反応させた(圧力14.6MPa)。その後、反応器を電気炉より取り出し、冷水浴により急冷却し、反応を停止した。反応器が十分に冷却されたのを確認したのち、メタノールで反応混合物を取り出し捕集した。得られた反応混合物と内部標準物質としてアニソールをはかりとり、ガスクロマトグラフィー分析の分析試料とした。ガスクロマトグラフィー分析により積分値を算出、ヒドロキシドデカン酸メチルのファクターはω-ラウロラクタムのものを用いて作成した検量線表から収量を求めた。その結果、ヒドロキシドデカン酸メチルの収率は67.7%であった。
Claims (6)
- アミド化合物又はアミン化合物にカルボン酸誘導体の存在下で超臨界状態のアルコールを作用させることによって、アルコール化合物を得ることを特徴とするアルコール化合物の製造方法。
- 前記カルボン酸誘導体は、カルボン酸又はカルボン酸のエステルであることを特徴とする請求項1乃至5いずれか記載のアルコール化合物の製造方法。
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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JP2011525874A JP5713404B2 (ja) | 2009-08-05 | 2010-08-02 | アルコール化合物の製造方法 |
EP10806408.0A EP2463262A4 (en) | 2009-08-05 | 2010-08-02 | PROCESS FOR PRODUCING ALCOHOL COMPOUND |
US13/389,059 US8993814B2 (en) | 2009-08-05 | 2010-08-02 | Method for producing alcohol compound |
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JPH11292831A (ja) * | 1998-04-10 | 1999-10-26 | Nippon Shokubai Co Ltd | N−アルキルアミン類の製造方法およびこれに用いる触媒 |
JPH11343338A (ja) * | 1998-06-02 | 1999-12-14 | Toray Ind Inc | α,ω−アミノカルボン酸の製造方法及びラクタムの重合方法 |
JP2000086583A (ja) | 1998-09-17 | 2000-03-28 | Asahi Glass Co Ltd | 含フッ素ベンジル誘導体の製造方法 |
JP2002148253A (ja) * | 2000-11-08 | 2002-05-22 | Sumitomo Chem Co Ltd | ポリアミド系樹脂の分析方法 |
JP2003096032A (ja) * | 2001-09-27 | 2003-04-03 | Sumitomo Chem Co Ltd | ジフェニルアミン類の製造方法 |
JP2005232170A (ja) * | 2004-02-19 | 2005-09-02 | Goldschmidt Gmbh | アミノ酸エステルおよびその酸付加塩を調製するための方法 |
WO2007088756A1 (ja) * | 2006-01-31 | 2007-08-09 | Yamaguchi University | 6-ヒドロキシカプロン酸エステルの製造方法及びトリアルキルアミンの製造方法 |
WO2008096568A1 (ja) * | 2007-02-06 | 2008-08-14 | Yamaguchi University | 12-ヒドロキシドデカン酸エステルの製造方法及びトリアルキルアミンの製造方法 |
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CN1726010A (zh) * | 2002-12-19 | 2006-01-25 | 巴克斯特国际公司 | 使用超临界流体制备组合药物制剂的方法 |
-
2010
- 2010-08-02 US US13/389,059 patent/US8993814B2/en not_active Expired - Fee Related
- 2010-08-02 EP EP10806408.0A patent/EP2463262A4/en not_active Withdrawn
- 2010-08-02 JP JP2011525874A patent/JP5713404B2/ja active Active
- 2010-08-02 WO PCT/JP2010/062995 patent/WO2011016409A1/ja active Application Filing
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JPH11292831A (ja) * | 1998-04-10 | 1999-10-26 | Nippon Shokubai Co Ltd | N−アルキルアミン類の製造方法およびこれに用いる触媒 |
JPH11343338A (ja) * | 1998-06-02 | 1999-12-14 | Toray Ind Inc | α,ω−アミノカルボン酸の製造方法及びラクタムの重合方法 |
JP2000086583A (ja) | 1998-09-17 | 2000-03-28 | Asahi Glass Co Ltd | 含フッ素ベンジル誘導体の製造方法 |
JP2002148253A (ja) * | 2000-11-08 | 2002-05-22 | Sumitomo Chem Co Ltd | ポリアミド系樹脂の分析方法 |
JP2003096032A (ja) * | 2001-09-27 | 2003-04-03 | Sumitomo Chem Co Ltd | ジフェニルアミン類の製造方法 |
JP2005232170A (ja) * | 2004-02-19 | 2005-09-02 | Goldschmidt Gmbh | アミノ酸エステルおよびその酸付加塩を調製するための方法 |
WO2007088756A1 (ja) * | 2006-01-31 | 2007-08-09 | Yamaguchi University | 6-ヒドロキシカプロン酸エステルの製造方法及びトリアルキルアミンの製造方法 |
WO2008096568A1 (ja) * | 2007-02-06 | 2008-08-14 | Yamaguchi University | 12-ヒドロキシドデカン酸エステルの製造方法及びトリアルキルアミンの製造方法 |
Non-Patent Citations (1)
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See also references of EP2463262A4 |
Also Published As
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JP5713404B2 (ja) | 2015-05-07 |
US8993814B2 (en) | 2015-03-31 |
US20120157707A1 (en) | 2012-06-21 |
EP2463262A1 (en) | 2012-06-13 |
JPWO2011016409A1 (ja) | 2013-01-10 |
EP2463262A4 (en) | 2014-07-09 |
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