WO2012023546A1 - 水素または重水素の製造方法およびそれを利用した有機化合物の水素化または重水素化 - Google Patents
水素または重水素の製造方法およびそれを利用した有機化合物の水素化または重水素化 Download PDFInfo
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- C07C5/08—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
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Definitions
- the present invention relates to a method for producing hydrogen or deuterium using a mechanochemical reaction and to hydrogenation or deuteration of an organic compound using the method.
- hydrogen is expected to be an alternative energy because it does not emit exhaust gas other than water, such as particulate matter and carbon dioxide, even if it is burned.
- Stacked hydrogen vehicles are on sale, and are used for rocket fuel and fuel cells.
- this hydrogen is produced in large quantities as a by-product of hydrocarbon steam reforming and partial oxidation (hydrocarbon gas decomposition method).
- methane gas in natural gas, paraffins, ethylene / propylene, etc. are reacted with water vapor using nickel as a catalyst at a high temperature to form hydrogen and carbon monoxide.
- carbon dioxide and hydrogen gas are reacted.
- hydrogen generated as a by-product of seawater electrolysis in the soda and salt industries may be used.
- the hydrogenation reaction in which an organic compound is reacted with hydrogen is a reaction widely used in organic synthetic chemistry, and many useful compounds are produced by this method.
- There are many known hydrogenation reactions such as reactions using alkali metals, reactions using metal hydrides or metal hydrogen complexes, reactions using diborane or hydrazine, and reactions using catalytic hydrogenation. Yes.
- the method using an alkali metal, metal hydride, metal hydrogen complex, diborane, hydrazine, etc. has a problem that the cost of the reaction reagent to be used is high, and that they are dangerous. In addition, there is a problem that it is necessary to use a special metal catalyst even in a method using catalytic hydrogenation.
- the present invention has been made in view of the above circumstances, and without requiring a large-scale apparatus, can be easily obtained without using a method for easily obtaining hydrogen, without using an expensive reaction reagent or a special catalyst. It is an object of the present invention to provide a method capable of performing a hydrogenation reaction.
- the inventors of the present invention have conducted many experiments on organic synthesis reactions, and have found that the organic compound added is hydrogenated by reacting the organic compound and water in a specific reaction system. It was also found that hydrogen gas is generated when the above reaction is carried out only with water. Furthermore, the present invention was completed by confirming that deuteration of organic compounds and generation of deuterium gas can be carried out using heavy water instead of water.
- the present invention is a method for producing hydrogen or deuterium, characterized in that water or heavy water is subjected to a mechanochemical reaction in the presence of a catalytic metal.
- the present invention is also a method for producing a hydrogenated or deuterated organic compound, characterized in that an organic compound and water or heavy water are subjected to a mechanochemical reaction in the presence of a catalytic metal.
- the present invention is a method for hydrogenating or deuterating an organic compound, wherein a mechanochemical reaction is performed between the organic compound and water or heavy water in the presence of a catalytic metal.
- the present invention is a method for dehalogenating a halogen-containing organic compound, characterized by causing a mechanochemical reaction between a halogen-containing organic compound and water or heavy water in the presence of a catalytic metal.
- the method for producing hydrogen or deuterium of the present invention it is possible to obtain hydrogen or deuterium from water or heavy water without requiring a large-scale device and causing problems such as waste.
- hydrogenation or deuterium can be easily performed without using an expensive reaction reagent or catalyst. It is possible to obtain a modified organic compound.
- an organic compound deuterated by a method for producing a deuterated organic compound or a method for deuterating an organic compound is useful as a label compound.
- a drug composed of a known organic compound is deuterated, the medicinal effect may be increased.
- the dehalogenation method of the present invention it is possible to easily dehalogenate an organic compound having a halogen without using an expensive reaction reagent or catalyst.
- this method can be used to detoxify organic compounds having halogens harmful to the human body such as polychlorinated biphenyl (PCB).
- PCB polychlorinated biphenyl
- invention relating to a method for producing hydrogen or deuterium of the present invention (hereinafter sometimes referred to as “first aspect invention”), invention relating to a method for producing a hydrogenated or deuterated organic compound (hereinafter referred to as “second aspect invention”)
- first aspect invention invention relating to a method for producing a hydrogenated or deuterated organic compound
- second aspect invention A method for hydrogenating or deuterating an organic compound (hereinafter sometimes referred to as “the third aspect invention”) and a dehalogenation method (hereinafter sometimes referred to as “the fourth aspect invention”), It is essential to cause a mechanochemical reaction in the presence of a catalytic metal.
- heavy water refers to hydrogen ( 1 H) isotopes of 2 H (D) and 3 H (T), oxygen ( 16 O) isotopes of 17 O and 18 O, and combinations thereof.
- D 2 O, T 2 O and the like can be mentioned.
- deuterium is hydrogen composed of an isotope of hydrogen, and examples thereof include D 2 and T 2 .
- deuteration is the replacement of part or all of hydrogen in normal hydrogenation with D or T.
- the mechanochemical reaction carried out in these inventions is carried out by increasing the activity of the reactant by mechanical energy such as impact and friction, and is usually carried out in an apparatus capable of performing a mechanochemical reaction.
- an apparatus capable of performing a mechanochemical reaction.
- an apparatus include a reactor equipped with a reaction vessel and a stirring medium for providing mechanical energy.
- a ball mill such as a planetary ball mill or a mixer mill, or a mixing device such as a shaker. Machine.
- This planetary ball mill device is a device that functions to uniformly mix or finely pulverize metal or ceramic powder, and is composed of a planetary ball mill reaction vessel body and an atmosphere control section. Then, after putting a metal or ceramic powder (a material to be crushed) and a ball as a stirring medium into the ball mill reaction vessel and setting it in the equipment, the ball mill reaction vessel is placed in the atmosphere control section. The powder is mixed and pulverized efficiently in a short time by revolving with the movement similar to the movement of the planet while rotating. In addition, since the entire planetary ball mill has a structure in which the atmosphere is controlled, it is possible to mix and pulverize powder that may be altered in air.
- reaction vessel used in the planetary ball mill apparatus and the stirring medium such as stainless steel, agate, alumina, tungsten carbide, chrome steel, zirconia, and silicon nitride.
- the thing formed with the material is mentioned.
- stainless steel which is an alloy of iron and chromium, nickel or the like, is preferable.
- the size of the container used in the planetary ball mill apparatus is not particularly limited, but is about 1 to 1,000 cm 3 .
- the size of the ball is not particularly limited, but the diameter is about 2 to 20 mm.
- particularly preferred planetary ball mills include, for example, a planetary ball mill quartet P-7 (manufactured by Friitch Germany), a planetary ball mill premium line-7 (manufactured by Frisch Germany), and a planetary ball mill. And ball mill PM-100 (manufactured by Lecce, Germany).
- the catalytic metal in order to cause the mechanochemical reaction in the presence of the catalytic metal, is used in the mechanochemical reaction system in an amount that exhibits catalytic action, for example, in an amount greater than 0.001 mol% with respect to water. It only needs to be present.
- the catalyst metal include transition metals such as palladium, iron, nickel, and chromium, and oxides thereof, preferably iron, iron (II) hydroxide, nickel, nickel (II) oxide, chromium, chromium oxide ( III), palladium and the like. These catalytic metals can be used alone or in combination of two or more.
- These catalytic metals may be added to the reaction vessel used for the mechanochemical reaction in the form of a wire or foil, or the reaction vessel, ball, stirring rod, etc. used for the mechanochemical reaction.
- the stirring medium may be contained, or the stirring medium may be plated.
- water or heavy water is selected from catalytic metals, preferably iron, iron hydroxide (II), chromium, chromium oxide (III). What is necessary is just to make mechanochemical reaction in presence of 1 type, or 2 or more types of catalyst metals.
- catalytic metals preferably iron, iron hydroxide (II), chromium, chromium oxide (III).
- a stirring medium is operated in the presence of a catalytic metal, and a mechanochemical reaction is performed to generate hydrogen or deuterium. Just do it.
- hydrogen or deuterium accumulated in the reaction vessel may be collected according to a conventional method.
- the first aspect of the invention is specifically performed using a planetary ball mill.
- water or heavy water of about 0.1 to 20% by mass (hereinafter simply referred to as “%”) of the vessel capacity is put into a reaction vessel of a planetary ball mill apparatus, and about 1 to 100 stirring media are added thereto.
- the catalyst metal is added in an amount of about 0.01 to 100 mol% based on the organic compound, and about 0.1 to 12 hours, preferably The stirring may be performed for about 0.5 to 6 hours, at about 400 to 1,200 rpm, preferably at 800 to 1,100 rpm.
- the conversion efficiency from water or heavy water to hydrogen or deuterium in the first aspect of the invention is about 20 to 100%, although it varies depending on the apparatus used, reaction conditions, and the like.
- Hydrogen or deuterium obtained by the first aspect of the invention described above can be used for power generation using cold fusion with fuel cells or deuterium.
- an organic compound and water or deuterium are mixed with a catalyst metal, preferably nickel, nickel (II) oxide, chromium. And mechanochemical reaction in the presence of one or more kinds of catalytic metals selected from chromium (III) oxide and palladium.
- a catalyst metal preferably nickel, nickel (II) oxide, chromium.
- mechanochemical reaction in the presence of one or more kinds of catalytic metals selected from chromium (III) oxide and palladium.
- an organic compound and water or heavy water are placed in a reaction vessel of an apparatus capable of performing the above mechanochemical reaction, a stirring medium is operated in the presence of a catalytic metal, a mechanochemical reaction is performed, and the organic compound is Hydrogenation or deuteration may be performed.
- the organic compound used in the second aspect of the invention is not particularly limited as long as it is an organic compound that is hydrogenated or deuterated.
- an unsaturated bond such as a double bond or a triple bond, an aldehyde group , Ketone groups, nitro groups, azido groups and other highly oxidized substituents, halogens and the like in the skeleton.
- the degree of hydrogenation or deuteration of the organic compound can be adjusted by the addition amount. If you want to increase the degree of hydrogenation or deuteration, add a large amount of water or heavy water, and if the degree of hydrogenation or deuteration may be low, you should conserve the amount of water or heavy water added. .
- the amount of water or heavy water added is greatly affected by the ease of hydrogenation or deuteration of the organic compound, and may be confirmed experimentally.
- the degree of hydrogenation or deuteration of the organic compound can be adjusted by controlling mechanical energy such as impact and friction in the mechanochemical reaction.
- the second aspect of the invention When the second aspect of the invention is carried out as described above, first, water or heavy water in the reaction vessel is converted to hydrogen or deuteration, whereby the organic compound is hydrogenated or deuterated.
- the conversion efficiency from the organic compound to the hydrogenated or deuterated organic compound in the second aspect of the invention is about 70 to 100%, although it varies depending on the apparatus used, reaction conditions, and the like.
- an unsaturated bond (double bond or triple bond) in the skeleton of the organic compound can be converted to a saturated bond, and a highly oxidized substituent (aldehyde group, ketone group, nitro group) Can be converted to a substituent having a low degree of oxidation (hydroxyalkyl group, hydroxy group, amino group), or the halogen in the halide can be removed to form a dehalogenated product.
- a highly oxidized substituent aldehyde group, ketone group, nitro group
- a substituent having a low degree of oxidation hydroxyalkyl group, hydroxy group, amino group
- any compound having the following basic skeleton can be converted into a corresponding reductant by hydrogenation or deuteration.
- the compound which can be hydrogenated or deuterated is illustrated below, the compound which can be hydrogenated or deuterated by 2nd aspect invention is not limited to these.
- the methyl group is described as representative of an alkyl group (functionalized fatty chain), and benzene or phenyl is an aryl group [functionalized aromatic ring (benzene, furan, pyro- And thiophene, etc.)]].
- Terminal alkyne methyl acetylene, ethynylbenzene Disubstituted alkyne: diphenylacetylene, dimethylacetylene, methylphenylacetylene ⁇ double bond-containing compound> Monosubstituted alkene: phenylethylene, methylethylene Disubstituted alkene: (E) -1,2-diphenylethylene, (Z) -1,2-diphenylethylene, (E) -1,2-dimethylethylene, (Z ) -1,2-dimethylethylene, 1,1-diphenylethylene, 1,1-dimethylethylene, 1-methyl-1-phenylethylene, (E) -1-methyl-2-phenylethylene, (Z) -1 -Methyl-2-phenylethylene trisubstituted alkene: 1,1,2-triphenylethylene, 1,1,2-trimethylethylene, 1,1-diphenyl-2-methylethylene, 1-phenyl-1
- a reaction vessel of the planetary ball mill apparatus is equipped with water or heavy water of about 0.1 to 20% of the vessel capacity, and 0.01 to Except for adding about 20% organic compound, it may be the same as the first aspect of the invention.
- the conversion efficiency from an organic compound to a hydrogenated or deuterated organic compound is about 70 to 100%, although it varies depending on the apparatus used, reaction conditions, and the like.
- the organic compound deuterated by the above-described second aspect of the invention is useful as a label compound used for structural analysis and elucidation of the mechanism.
- the drug efficacy may be increased.
- organic compound hydrogenation or deuteration method according to the third aspect of the present invention may be carried out in the same manner as in the second aspect of the present invention.
- the above-described dehalogenation method according to the fourth aspect of the present invention may be performed in the same manner as the second aspect of the present invention.
- this method can dehalogenate organic compounds having halogen harmful to the human body, such as polychlorinated biphenyl (PCB), and thus can be used for detoxifying these organic compounds.
- PCB polychlorinated biphenyl
- Example 1 Decomposition of water into hydrogen: Into a planetary ball mill container, 270 ⁇ L (15 mmol) of distilled water (Wako 046-16971) and a stainless ball (50 pieces) were put, then the cap was put on, and the planetary ball mill device was operated at 800 rpm for 6 hours. Rotated (reversed every 30 minutes) and stirred. After stirring, the container was opened and the gas in the container was ignited and burned. From this combustion phenomenon, the generation of hydrogen gas, which is a combustible gas, was confirmed. This reaction is shown by the following formula.
- Example 2 Hydrogenation reaction of diphenylacetylene (1) Synthesis of 1,2-diphenylethane (2) In a planetary ball mill container, 89.1 mg (0.50 mmol) of diphenylacetylene (1), 270 ⁇ L (15 mmol) of distilled water and stainless steel balls (50 pieces) ) was added, and the mixture was capped and rotated on a planetary ball mill for 12 hours at 800 rpm (reversed every 30 minutes) and stirred. After 12 hours, 10 mL of ethyl acetate was added to a ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 89.4 mg (0.49 mmol) of 1,2-diphenylethane (2). The yield was 98%.
- Example 3 Synthesis of 4-aminobenzophenone by hydrogenation of 4-azidobenzophenone: After adding 111.6 mg (0.50 mmol) of 4-azidobenzophenone (5), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls (50) to a planetary ball mill container, the cap was put on the planet, The mixture was rotated and stirred at 800 rpm (reversed every 30 minutes) for 12 hours in a mold ball mill apparatus. After 12 hours, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction product, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 87.7 mg (0.45 mmol) of 4-aminobenzophenone (6). The yield was 89%. This reaction is shown by the following formula.
- Example 4 Synthesis of 3-benzyloxy-4-methoxybenzyl alcohol and 3-hydroxy-4-methoxybenzyl alcohol by hydrogenation of 3-benzyloxy-4-methoxybenzaldehyde: After adding 121.1 mg (0.50 mmol) of 3-benzyloxy-4-methoxybenzaldehyde (7), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls to a planetary ball mill container, The mixture was rotated at 800 rpm (reversed every 30 minutes) with a planetary ball mill for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 5 Synthesis of 4-amino-1-methoxybenzene by hydrogenation reaction of 1-methoxy-4-nitrobenzene: To a planetary ball mill container, 76.6 mg (, 0.50 mmol) of 1-methoxy-4-nitrobenzene (10), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls (50) were added, and then the lid was closed. Then, it was rotated by a planetary ball mill apparatus at 800 rpm (reversed every 30 minutes) for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 48.2 mg (0.39 mmol) of 4-amino-1-methoxybenzene (11). The yield was 78%. This reaction formula is shown by the following formula.
- Example 7 Synthesis of methoxybenzene by hydrogenation of 4-chloro-1-methoxybenzene: To a planetary ball mill container was added 61.3 ⁇ L (0.50 mmol) of 4-chloro-1-methoxybenzene (14), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls (50), and then the lid was closed. Then, it was rotated by a planetary ball mill apparatus at 800 rpm (reversed every 30 minutes) for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain methoxybenzene (15). The conversion efficiency was 100%. This reaction is shown by the following formula.
- Example 8 Deuteration of diphenylacetylene using heavy water (D 2 O): In a planetary ball mill container, 89.1 mg (0.50 mmol) of diphenylacetylene (1), 272 ⁇ L (15 mmol) of heavy water (Cambridge Isotope Laboratories, Inc .: Cat. No. 15,188-2) and a stainless ball (50 Then, the cap was capped and rotated and stirred in a planetary ball mill for 12 hours at 800 rpm (reversed every 30 minutes). After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- D 2 O heavy water
- Example 9 Synthesis of 1-aminonaphthalene by hydrogenation reaction of 1-nitronaphthalene: To a planetary ball mill container, 86.6 mg (0.50 mmol) of 1-nitronaphthalene (17), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls (50) were added, then the cap was put on, and the planetary type was added. The mixture was rotated on a ball mill apparatus at 800 rpm (reversed every 30 minutes) for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 10 Synthesis of naphthalene by hydrogenation reaction of 1-chloronaphthalene: 1-Chloronaphthalene (19) 68.4 ⁇ L (0.50 mmol), distilled water 270 ⁇ L (15 mmol) and stainless steel balls (50 pieces) were added to a planetary ball mill container, and then the cap was capped to form a planetary type. The mixture was rotated on a ball mill apparatus at 800 rpm (reversed every 30 minutes) for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 11 Inhibition of hydrogenation reaction by tetracyanoquinodimethane (TCNQ): In a planetary ball mill container, 89.1 mg (0.50 mmol) of diphenylacetylene (1), 270 ⁇ L (15 mmol) of distilled water, 10.1 mg (0.05 mmol) of tetracyanoquinodimethane (TCNQ) and a stainless ball After adding (50 pieces), the lid was capped, and the mixture was rotated with a planetary ball mill for 12 hours at 800 rpm (reversed every 30 minutes) and stirred. In this system, the reaction did not proceed at all even when stirring was continued for 12 hours. The reason is presumed that this reaction proceeds via radicals. This reaction is shown by the following formula.
- Example 12 Synthesis of 4-aminobenzophenone by hydrogenation of 4-nitrobenzophenone: After adding 91.1 mg (0.50 mmol) of 4-nitrobenzophenone (21), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls to a planetary ball mill container, the cap was capped, and the planetary type The mixture was rotated on a ball mill apparatus at 800 rpm (reversed every 30 minutes) for 12 hours and stirred. After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. After concentrating the filtrate obtained by repeating this operation 5 times, 4-aminobenzophenone (22) and 4-aminobenzhydrol (23) were obtained in a ratio of 83:17 from 1 H NMR. This reaction is shown by the following formula.
- Example 13 Synthesis of 4-benzyloxybenzene by hydrogenation reaction of 4-benzyloxybromobenzene
- a planetary ball mill container 131.6 mg (0.50 mmol) of 4-benzyloxybromobenzene (24), 270 ⁇ L (15 mmol) of distilled water ) And stainless steel balls (50 pieces) were added, and the caps were capped and rotated on a planetary ball mill for 12 hours at 800 rpm (reversed every 30 minutes) and stirred. After 12 hours, 10 mL of ethyl acetate was added to a planetary ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 14 Hydrogenation reaction by adding palladium foil In a planetary ball mill container, 89.1 mg (0.50 mmol) of diphenylacetylene (1), 270 ⁇ L (15 mmol) of distilled water, 50 stainless balls and palladium foil (made by Aldrich) in the amounts shown in the table below. After the addition, the cap was capped, and the mixture was rotated with a planetary ball mill device at a speed shown in the table below at 800 rpm (reverse rotation every 30 minutes) and stirred. After stirring, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 15 Dechlorination reaction by adding palladium foil: In a planetary ball mill container, 148.5 mg (0.50 mmol) of 4-chlorododecyloxybenzene (28), 270 ⁇ L (15 mmol) of distilled water and palladium foil (1.9 mg (3.6 mol%)) and stainless steel ball (50 pieces), the cap was capped, and the mixture was rotated with a planetary ball mill for 12 hours at 800 rpm (reversed every 30 minutes) and stirred.After 12 hours, ethyl acetate was put into the ball mill container.
- Example 16 Hydrogenation reaction of diphenylacetylene To a planetary ball mill vessel, 1.34 g (7.5 mmol) of diphenylacetylene (1), 4.01 mL (225 mmol) of distilled water and stainless steel balls (25) were added, then the cap was put on, and the planet type Using a ball mill, the mixture was rotated for 6 hours at 650 rpm (reversed every 30 minutes) and stirred. After 6 hours, 200 ml of ethyl acetate was added to a ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate was concentrated to obtain a reaction product. This was confirmed by 1 H NMR.
- Example 17 Examination of hydrogen generation conditions: Into a planetary ball mill container, 270 ⁇ L (15 mmol) of distilled water (Wako 046-16971) and a stainless ball (50 pieces) were placed, then the cap was put on, and the planetary ball mill device was used for 400 hours. Rotate at ⁇ 1,000 rpm (reversed every 30 minutes) or 1,100 rpm (no reversal) for 0.3 hours and stir. The composition of the gas in the container after the stirring was analyzed by GC / TCD (manufactured by Shimadzu Corporation: GC-2014). The results are shown in Table 2.
- the method of the present invention is an extremely safe hydrogen generation method with little oxygen content.
- high-purity hydrogen can be generated and collected by previously evacuating the ball mill.
- Example 18 Synthesis of dodecane by hydrogenation of 6-dodecin: To a planetary ball mill container, 83.2 mg (0.50 mmol) of 6-dodecine (30), 270 ⁇ L (15 mmol) of distilled water and 50 stainless balls were added, and then the cap was closed. -Rotated at 800 rpm (reversed every 30 minutes) for 6 hours in a Lumil apparatus and stirred. After 6 hours, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 51.1 mg (0.30 mmol) of dodecane (31). The yield was 60%. This reaction is shown by the following formula.
- Example 19 Synthesis of 1-phenylethanol by hydrogenation reaction of 1-phenylethanone: To a planetary ball mill container, 1-phenylethanone (32) 60.1 mg (0.50 mmol), distilled water 270 ⁇ L (15 mmol) and stainless steel balls (50 pieces) were added, then the cap was put on, The mixture was rotated and stirred at 800 rpm (reversed every 30 minutes) in a mold ball mill apparatus for 6 hours. After 6 hours, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 42.8 mg (0.35 mmol) of 1-phenylethanol (33). The yield was 70%. This reaction is shown by the following formula.
- Example 20 Synthesis of 3-phenyl-1-propanol by hydrogenation of 3-phenyl-2-propen-1-ol: To a planetary ball mill vessel, add 67.1 mg (0.50 mmol) of 3-phenyl-2-propen-1-ol (34), 270 ⁇ L (15 mmol) of distilled water, and 50 stainless balls (50). After that, it was capped and rotated on a planetary ball mill for 6 hours at 800 rpm (reversed every 30 minutes) and stirred. After 6 hours, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 64.7 mg (0.475 mmol) of 3-phenyl-1-propanol (35). The yield was 95%. This reaction is shown by the following formula.
- Example 21 Synthesis of 1,3-dimethoxybenzene by hydrogenation of 1-chloro-3,5-dimethoxybenzene: To a planetary ball mill container, 86.3 mg (0.50 mmol) of 1-chloro-3,5-dimethoxybenzene (36), 45 ⁇ L (2.5 mmol) of distilled water, and 50 stainless balls were added. Then, it was covered and rotated at 1,100 rpm for 30 minutes in a planetary ball mill apparatus and stirred. After 30 minutes, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite. The filtrate obtained by repeating this operation 5 times was concentrated to obtain 36.6 mg (0.265 mmol) of 1,3-dimethoxybenzene (37). The yield was 53%. This reaction is shown by the following formula.
- Example 22 Synthesis of 3-phenyl-2,3-didetro-1-propanol by deuteration of 3-phenyl-2-propen-1-ol: To a planetary ball mill container, 67.1 mg (0.50 mmol) of 3-phenyl-2-propen-1-ol (34), 272 ⁇ L (15 mmol) of heavy water and 50 stainless balls were added. Then, it was covered, and it was rotated by a planetary ball mill device for 6 hours at 800 rpm (reversed every 30 minutes) and stirred. After 6 hours, 10 mL of ethyl acetate was added to the ball mill container to obtain a solution containing the reaction mixture, which was filtered through Celite.
- Example 23 Deuterium addition reaction of benzyl-4-bromophenyl ketone (39): (1) Synthesis of 1- (4-bromophenyl) -2,2-didetro-2-phenylethane (40) Into a planetary ball mill container, 137.6 mg of benzyl-4-bromophenyl ketone (39) (0.50 mmol), 272 ⁇ L of heavy water (15 mmol) and stainless steel balls (50 pieces) were added, then the caps were turned and rotated on a planetary ball mill device for 6 hours at 650 rpm (reversed every 30 minutes). , Stirred.
- hydrogen or deuterium can be easily generated without requiring a large-scale and complicated apparatus, and the hydrogen or deuterium can be obtained as a gas, or hydrogenated or deuterated. It can be used for reaction.
- the present invention can be advantageously used in a small-scale hydrogen or deuterium gas production apparatus, or in a simple organic compound hydrogenation or deuteration reaction apparatus.
Abstract
Description
<三重結合含有化合物>
末端アルキン体:メチルアセチレン、エチニルベンゼン
2置換アルキン体:ジフェニルアセチレン、ジメチルアセチレン、メチルフェニルアセチレン
<二重結合含有化合物>
1置換アルケン体:フェニルエチレン、メチルエチレン
2置換アルケン体:(E)-1,2-ジフェニルエチレン、(Z)-1,2-ジフェニルエチレン、(E)-1,2-ジメチルエチレン、(Z)-1,2-ジメチルエチレン、1,1-ジフェニルエチレン、1,1-ジメチルエチレン、1-メチル-1-フェニルエチレン、(E)-1-メチル-2-フェニルエチレン、(Z)-1-メチル-2-フェニルエチレン
3置換アルケン体:1,1,2-トリフェニルエチレン、1,1,2-トリメチルエチレン、1,1-ジフェニル-2-メチルエチレン、1-フェニル-1,2-ジメチルエチレン
4置換アルケン体:1,1,2,2-テトラフェニルエチレン、1,1,2,2-テトラメチルエチレン、1,1,2-トリフェニル-2-メチルエチレン、1,1-ジフェニル-2,2-ジメチルエチレン、1-フェニル-1,2,2-トリメチルエチレン、(E)-1,2-ジフェニル-1,2-ジメチルエチレン、(Z)-1,2-ジフェニル-1,2-ジメチルエチレン
芳香環:ベンゼン、ビフェニル、ピリジン、フラン、ピロ-ル、チオフェン、ナフタレン、キノリン、アントラセン、イミダゾ-ル、インド-ル、ベンゾフラン、オキサゾ-ル
<カルボニル基含有化合物*>
アルデヒド体:メチルアルデヒド、フェニルアルデヒド
ケトン体:ジメチルケトン、ジフェニルケトン、メチルフェニルケトン
イミン体:N-メチル-メチルイミン、N-フェニル-メチルイミン、N-メチル-ジメチルイミン、N-メチル-ジフェニルイミン、N-メチル-メチルフェニルイミン、N-フェニル-ジメチルイミン、N-フェニル-ジフェニルイミン、N-フェニル-メチルフェニルイミン、オキシム:N-ヒドロキシ-メチルイミン、N-ヒドロキシ-ジメチルイミン、N-ヒドロキシ-ジフェニルイミン、N-ヒドロキシ-メチルフェニルイミン
*:カルボニル基の酸素原子が他の原子や基に置換されたものを含む
<ニトロ基含有化合物>
ニトロ体:ニトロメタン、ニトロベンゼン
<アジド基含有化合物>
アジド体:アジ化メタン、アジ化ベンゼン
<ハロゲン含有化合物>
フッ素体:メチルフルオライド、フルオロベンゼン
クロロ体:メチルクロライド、クロロベンゼン
ブロモ体:メチルブロマイド、ブロモベンゼン
ヨウ素体:メチルヨ-ダイド、ヨ-ドベンゼン
<ベンジルエ-テル基含有化合物>
ベンジルエ-テル体:フェニルメチルオキシメタン、フェニルメチルオキシベンゼン
(水素化または重水素化される化合物) (還元体)
エチニルベンゼン エチルベンゼン
ジフェニルアセチレン 1,2-ジフェニルエタン
フェニルエチレン エチルベンゼン
(E)-1,2-ジフェニルエチレン 1,2-ジフェニルエタン
(Z)-1,2-ジフェニルエチレン 1,2-ジフェニルエタン
1,1-ジフェニルエチレン 1,1-ジフェニルエタン
フェニルアルデヒド ベンジルアルコ-ル
メチルフェニルケトン 1-フェニルエタノ-ル
ニトロベンゼン アミノベンゼン
アジ化ベンゼン アミノベンゼン
クロロベンゼン ベンゼン
フェニルメチルオキシベンゼン フェノ-ル
使用機器:ドイツ フリッチュ社製 遊星型ボ-ルミル
カルテットP-7
自転:公転比率=1:-2
ボ-ル:直径 5~6mm、材質 ステンレススチ-ル
容 器:内容量 12mL、材質 ステンレススチ-ル
ステンレススチ-ルの組成;
Fe(approx.) 67~70%、
C 0.12%、
Si 1%、
Mn 2%、
P 0.06%、
S 0.15~0.35%、
Cr 17~19%、
Ni 8~10%
<実施例16>
使用機器:ドイツ レッチェ社製 遊星型ボ-ルミル PM-100
自転:公転比率=1:-2
ボ-ル:直径 10mm、材質 ステンレススチ-ル
容 器:内容量 250mL、材質 ステンレススチ-ル
ステンレススチ-ルの組成;
Fe 82.925%、
Cr 14.5%、
Mn 1%、
Si 1%、
C 0.5%、
P 0.045%、
S 0.03%
<実施例17、21>
使用機器:ドイツ フリッチュ社製 遊星型ボ-ルミル
プレミアムライン-7
自転:公転比率=1:-2
ボ-ル:直径 5~6mm、材質 ステンレススチ-ル
容 器:内容量 20mL(実施例17)または
80mL(実施例21)
材質 ステンレススチ-ル
ステンレススチ-ルの組成;
Fe(approx.) 67~70%、
C 0.12%、
Si 1%、
Mn 2%、
P 0.06%、
S 0.15~0.35%、
Cr 17~19%、
Ni 8~10%
水の水素への分解:
遊星型ボ-ルミル容器に、蒸留水(Wako 046-16971)270μL(15mmol)と、ステンレスボ-ル(50個)を入れた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。攪拌終了後に容器を開封し、容器内のガスに点火したところ燃焼した。この燃焼現象から、可燃性ガスである水素ガスの生成を確認した。この反応は、下式で示される。
ジフェニルアセチレンの水素添加反応:
(1)1,2-ジフェニルエタン(2)の合成
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)89.1mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、1,2-ジフェニルエタン(2)89.4mg(0.49mmol)を得た。収率は、98%であった。
エタン(3)および1,2-ジシクロヘキシルエタン(4)の合成
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)89.1mg(0.50mmol)、蒸留水900μL(50mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、反応生成物を得た。これをGC/MSおよび1H NMRで確認したところ、1,2-ジフェニルエタン(2)、1-シクロヘキシル-2-フェニルエタン(3)および1,2-ジシクロヘキシルエタン(4)の混合物であった。この反応は下式で示される。
4-アジドベンゾフェノンの水素添加反応による4-アミノベンゾ
フェノンの合成:
遊星型ボ-ルミル容器に、4-アジドベンゾフェノン(5)111.6 mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、4-アミノベンゾフェノン(6)87.7mg(0.45mmol)を得た。収率は89%であった。この反応は下式で示される。
3-ベンジルオキシ-4-メトキシベンズアルデヒドの水素添加反応
による3-ベンジルオキシ-4-メトキシベンジルアルコ-ルならび
に3-ヒドロキシ-4-メトキシベンジルアルコ-ルの合成:
遊星型ボ-ルミル容器に、3-ベンジルオキシ-4-メトキシベンズアルデヒド(7)121.1mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、3-ベンジルオキシ-4-メトキシベンジルアルコ-ル(8)74.0mg(0.31mmol)および3-ヒドロキシ-4-メトキシベンジルアルコ-ル(9)6.9mg(0.05mmol)を得た。収率はそれぞれ61%および9%であった。この反応式は、下式で示される。なお、未反応の3-ベンジルオキシ-4-メトキシベンズアルデヒド(7)23.7mg(0.10mmol)を回収した。
1-メトキシ-4-ニトロベンゼンの水素添加反応による4-アミノ
-1-メトキシベンゼンの合成:
遊星型ボ-ルミル容器に、1-メトキシ-4-ニトロベンゼン(10)76.6mg(,0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、4-アミノ-1-メトキシベンゼン(11)48.2mg(0.39mmol)を得た。収率は78%であった。この反応式は、下式で示される。
4-エチニル-1-メトキシベンゼンの水素添加反応による4-エチ
ル-1-メトキシベンゼンの合成:
遊星型ボ-ルミル容器に、4-エチニル-1-メトキシベンゼン(12)64.8μL (0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、4-エチル-1-メトキシベンゼン(13)を47.0mg(0.35mmol)得た。収率は、69%であった。この反応式は、下式で示される。
4-クロロ-1-メトキシベンゼンの水素添加反応によるメトキシベ
ンゼンの合成:
遊星型ボ-ルミル容器に、4-クロロ-1-メトキシベンゼン(14)61.3μL(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、メトキシベンゼン(15)を得た。転換効率は100%であった。この反応は、下式で示される。
重水(D2O)を用いたジフェニルアセチレンの重水素化反応:
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)89.1mg(0.50mmol)、重水(Cambridge Isotope Laboratories, Inc.:Cat.No.15,188-2)272μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転、撹拌した。12時間経過後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、1,2-ジフェニル-1,1,2,2-テトラジュ-トロエタン(16)85.9mg(0.46mmol)を得た。収率は93%であった。なお、このものの構造は、1H NMR、GC/MSにより確認した。また、この反応は、下式で示される。
1-ニトロナフタレンの水素添加反応による1-アミノナフタレン
の合成:
遊星型ボ-ルミル容器に、1-ニトロナフタレン(17)86.6mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、1-アミノナフタレン(18)44.3mg(0.31mmol)を得た。収率は62%であった。転換収率は100%であったが、一部減圧留去したため、単離収率に低下が見られた。この反応は、下式で示される。
1-クロロナフタレンの水素添加反応によるナフタレンの合成:
遊星型ボ-ルミル容器に、1-クロロナフタレン(19)68.4μL(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、ナフタレン(20)を10.4mg(0.08mmol)得た。収率は16%であった。転換収率は100%であるが、一部減圧留去したため、単離収率に低下が見られた。この反応は、下式で示される。
テトラシアノキノジメタン(TCNQ)による水素添加反応抑制
効果:
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)89.1mg(0.50mmol)、蒸留水270μL(15mmol)、テトラシアノキノジメタン(TCNQ)10.1mg(0.05mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。この系では撹拌を12時間継続させても反応は全く進行しなかった。その理由は本反応がラジカル経由で進行すると推測される。この反応は、下式で示される。
4-ニトロベンゾフェノンの水素添加反応による4-アミノベンゾ
フェノンの合成:
遊星型ボ-ルミル容器に、4-ニトロベンゾフェノン(21)91.1mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、1H NMRより4-アミノベンゾフェノン(22)と4-アミノベンズヒドロ-ル(23)を83:17の比率で得た。この反応は、下式で示される。
4-ベンジルオキシブロモベンゼンの水素添加反応による4-ベンジ
ルオキシベンゼンの合成
遊星型ボ-ルミル容器に、4-ベンジルオキシブロモベンゼン(24)131.6mg( 0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、遊星型ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮後、1H NMRより4-ベンジルオキシブロモベンゼン(24)と4-ベンジルオキシベンゼン(25)を9:91の比率で得た。この反応は、下式で示される。
パラジウムホイル添加による水素添加反応:
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)89.1mg(0.50mmol)、蒸留水270μL(15mmol)、ステンレスボ-ル(50個)およびパラジウムホイル(Aldrich製)を下表の量で加えた後、蓋をし、遊星型ボ-ルミル装置で下表の時間、800rpm(30分毎に逆回転)で回転させ、撹拌した。撹拌後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、反応生成物を得た。これを1H NMRで確認したところ、シス-1,2-ジフェニルエチレン(26)、トランス-1,2-ジフェニルエチレン(27)および1,2-ジフェニルエタン(2)の混合物であった。これらの生成比率を下表の通りであった。この系ではパラジウムホイルを添加することにより、生成に要する時間の短縮や生成比率を改善することができた。また、この反応は下式で示される。
パラジウムホイル添加による脱塩素化反応:
遊星型ボ-ルミル容器に、4-クロロドデシルオキシベンゼン(28)148.5mg(0.50mmol)、蒸留水270μL(15mmol)およびパラジウムホイル(1.9mg(3.6mol%)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で12時間、800rpm(30分毎に反転)で回転させ、撹拌した。12時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮し、ドデシルオキシベンゼン(29)58.7mg(0.22mmol)を45%の収率で得た。転換効率は100%であった。この反応は下式で示される。
ジフェニルアセチレンの水素添加反応:
遊星型ボ-ルミル容器に、ジフェニルアセチレン(1)1.34g(7.5mmol)、蒸留水4.01mL(225mmol)およびステンレスボ-ル(25個)を加えた後、蓋をし、遊星型ボ-ルミルを用い、6時間、650rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト200mlを加え、反応混合物を含む溶液を得、これをセライト濾過した。濾液を濃縮し、反応生成物を得た。これを1H NMRで確認したところ、シス-1,2-ジフェニルエチレン(26)、トランス-1,2-ジフェニルエチレン(27)および1,2-ジフェニルエタン(2)の混合物を92:0:8の混合比で得た。収率は92%であった。また、この反応は下式で示される。
水素発生条件の検討:
遊星型ボ-ルミル容器に、蒸留水(Wako 046-16971)270μL(15mmol)と、ステンレスボ-ル(50個)を入れた後、蓋をし、遊星型ボ-ルミル装置で1時間、400~1,000rpm(30分毎に反転)または0.3時間、1,100rpm(反転なし)で回転させ、撹拌した。攪拌終了後の容器内のガスの組成をGC/TCD(島津製作所製:GC-2014)で分析した。その結果を表2に示した。
6-ドデシンの水素添加反応によるドデカンの合成:
遊星型ボ-ルミル容器に、6-ドデシン(30)83.2mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、ドデカン(31)51.1mg(0.30mmol)を得た。収率は、60%であった。この反応は下式で示される。
1-フェニルエタノンの水素添加反応による1-フェニルエタノ-ル
の合成:
遊星型ボ-ルミル容器に、1-フェニルエタノン(32)60.1mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、1-フェニルエタノ-ル(33)42.8mg(0.35mmol)を得た。収率は、70%であった。この反応は下式で示される。
3-フェニル-2-プロペン-1-オ-ルの水素添加による3-フェ
ニル-1-プロパノ-ルの合成:
遊星型ボ-ルミル容器に、3-フェニル-2-プロペン-1-オ-ル(34)67.1mg(0.50mmol)、蒸留水270μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、3-フェニル-1-プロパノ-ル(35)64.7mg(0.475mmol)を得た。収率は、95%であった。この反応は下式で示される。
1-クロロ-3,5-ジメトキシベンゼンの水素添加による1,3-ジ
メトキシベンゼンの合成:
遊星型ボ-ルミル容器に、1-クロロ-3,5-ジメトキシベンゼン(36)86.3mg(0.50mmol)、蒸留水 45μL(2.5mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で30分間、1,100rpmで回転させ、撹拌した。30分経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、1,3-ジメトキシベンゼン(37)36.6mg(0.265mmol)を得た。収率は、53%であった。この反応は下式で示される。
3-フェニル-2-プロペン-1-オ-ルの重水素添加による
3-フェニル-2,3-ジジュ-トロ-1-プロパノ-ルの
合成:
遊星型ボ-ルミル容器に、3-フェニル-2-プロペン-1-オ-ル(34)67.1mg(0.50mmol)、重水272μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、3-フェニル-2,3-ジジュ-トロ-1-プロパノ-ル(38)60.1mg(0.435mmol)を得た。2位、3位の重水素化率は50%で、収率は、87%であった。この反応は下式で示される。
ベンジル-4-ブロモフェニルケトン(39)の重水素添加反応:
(1)1-(4-ブロモフェニル)-2,2-ジジュ-トロ-2-フェニル
エタン(40)の合成
遊星型ボ-ルミル容器に、ベンジル-4-ブロモフェニルケトン(39)137.6mg(0.50mmol)、重水272μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、650rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、1-(4-ブロモフェニル)-2,2-ジジュ-トロ-2-フェニルエタン(40)128.9mg(0.465mmol)を得た。2位の重水素化率は77%で、収率は、93%であった。この反応は下式で示される。
エタン(40)および 2,2-ジジュ-トロ1,2-ジフェニルエ
タノン(41)の合成
遊星型ボ-ルミル容器に、ベンジル-4-ブロモフェニルケトン(39)137.6mg(0.50mmol)、272μL(15mmol)およびステンレスボ-ル(50個)を加えた後、蓋をし、遊星型ボ-ルミル装置で6時間、800rpm(30分毎に反転)で回転させ、撹拌した。6時間経過後、ボ-ルミル容器中にエチルアセテ-ト10mLを加え、反応混合物を含む溶液を得、これをセライト濾過した。この操作を5回繰り返して得られた濾液を濃縮したところ、1-(4-ブロモフェニル)-2,2-ジジュ-トロ-2-フェニルエタン(40)124.7mg(0.45mmol)および2,2-ジジュ-トロ1,2-ジフェニルエタノン(41)5.9mg(0.03mmol)を得た。2位の重水素化率はそれぞれ、96%および98%で、収率は、それぞれ90%および6%であった。この反応は下式で示される。
Claims (14)
- 水または重水を、触媒金属の存在下、メカノケミカル反応させることを特徴とする水素または重水素の製造方法。
- メカノケミカル反応を遊星型ボ-ルミルで行う請求項1記載の水素または重水素の製造方法。
- 触媒金属が、遷移金属の1種または2種以上である請求項1または2記載の水素または重水素の製造方法。
- 有機化合物と、水または重水とを、触媒金属の存在下、メカノケミカル反応させることを特徴とする水素化または重水素化有機化合物の製造方法。
- メカノケミカル反応を遊星型ボ-ルミルで行う請求項4記載の水素化または重水素化有機化合物の製造方法。
- 触媒金属が、遷移金属の1種または2種以上である請求項4または5記載の水素化または重水素化有機化合物の製造方法。
- 有機化合物が、ハロゲンを有する有機化合物であり、水素化または重水素化有機化合物が脱ハロゲン化有機化合物である請求項4~6の何れかに記載の水素化または重水素化有機化合物の製造方法。
- 有機化合物と、水または重水とを、触媒金属の存在下、メカノケミカル反応させることを特徴とする有機化合物の水素化または重水素化方法。
- メカノケミカル反応を遊星型ボ-ルミルで行う請求項8記載の有機化合物の水素化または重水素化方法。
- 触媒金属が、遷移金属の1種または2種以上である請求項8または9記載の有機化合物の水素化または重水素化方法。
- ハロゲンを有する有機化合物と、水または重水とを、触媒金属の存在下、メカノケミカル反応させることを特徴とするハロゲンを有する有機化合物の脱ハロゲン化方法。
- ハロゲンを有する有機化合物が、ポリ塩化ビフェニルである請求項11記載の脱ハロゲン化方法。
- メカノケミカル反応を遊星型ボ-ルミルで行う請求項11または12記載の脱ハロゲン化方法。
- 触媒金属が、遷移金属の1種または2種以上である請求項11~13の何れかに記載の脱ハロゲン化方法。
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JP2012529597A JP5480386B2 (ja) | 2010-08-18 | 2011-08-16 | 水素または重水素の製造方法およびそれを利用した有機化合物の水素化または重水素化 |
KR1020187000169A KR101899291B1 (ko) | 2010-08-18 | 2011-08-16 | 수소 또는 중수소의 제조 방법 |
US13/817,637 US8871980B2 (en) | 2010-08-18 | 2011-08-16 | Process for producing hydrogen or heavy hydrogens, and hydrogenation (protiation, deuteration or tritiation) of organic compounds using same |
KR1020137003211A KR101817820B1 (ko) | 2010-08-18 | 2011-08-16 | 수소 또는 중수소의 제조 방법 및 그것을 이용한 유기 화합물의 수소화 또는 중수소화 |
CN201180040072.3A CN103068721B (zh) | 2010-08-18 | 2011-08-16 | 氢或重氢的制造方法及利用该制造方法而进行的有机化合物的氢化或重氢化 |
BR112013003046A BR112013003046A2 (pt) | 2010-08-18 | 2011-08-16 | ''processo para produzir hidrogênio ou hidrogênios pesados, e hidrogenação (protiação, deuteração ou tritiação) de compostos orgnânicos utilizando os mesmos'' |
EP11818187.4A EP2607300B1 (en) | 2010-08-18 | 2011-08-16 | Process for hydrogenation of organic compounds using hydrogen or heavy hydrogen |
EP20166285.5A EP3689817A1 (en) | 2010-08-18 | 2011-08-16 | Process for producing hydrogen or heavy hydrogens, and hydrogenation (protiation, deuteration or tritiation) of organic compounds using same |
US14/459,673 US9676622B2 (en) | 2010-08-18 | 2014-08-14 | Process for producing hydrogen or heavy hydrogens, and hydrogenation (protiation, deuteration or tritiation) of organic compounds using same |
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US14/459,673 Continuation US9676622B2 (en) | 2010-08-18 | 2014-08-14 | Process for producing hydrogen or heavy hydrogens, and hydrogenation (protiation, deuteration or tritiation) of organic compounds using same |
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Cited By (3)
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WO2013121997A1 (ja) * | 2012-02-17 | 2013-08-22 | シオノケミカル株式会社 | 水素または重水素の製造方法、水素化または重水素化有機化合物の製造方法、有機化合物の水素化または重水素化方法、ハロゲンを有する有機化合物の脱ハロゲン化方法、メカノケミカル反応用ボ-ル |
WO2015115410A1 (ja) * | 2014-01-28 | 2015-08-06 | 株式会社日本触媒 | 水素化反応方法 |
JP2015532195A (ja) * | 2012-09-27 | 2015-11-09 | ホワイチャオ・チェン | 水蒸気分解用触媒、及びその製造方法、並びに水蒸気分解で得られた水素ガスの燃焼方法 |
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Also Published As
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US20140363369A1 (en) | 2014-12-11 |
CN103068721A (zh) | 2013-04-24 |
JPWO2012023546A1 (ja) | 2013-10-28 |
EP2607300A1 (en) | 2013-06-26 |
EP2607300A4 (en) | 2017-05-31 |
KR101899291B1 (ko) | 2018-09-14 |
CN105366638A (zh) | 2016-03-02 |
EP3689817A1 (en) | 2020-08-05 |
BR112013003046A2 (pt) | 2016-06-14 |
US8871980B2 (en) | 2014-10-28 |
TW201601994A (zh) | 2016-01-16 |
US20130150623A1 (en) | 2013-06-13 |
CN105366638B (zh) | 2018-01-09 |
JP5894117B2 (ja) | 2016-03-23 |
CN103068721B (zh) | 2016-01-13 |
TW201219299A (en) | 2012-05-16 |
KR20140002598A (ko) | 2014-01-08 |
TWI507355B (zh) | 2015-11-11 |
US9676622B2 (en) | 2017-06-13 |
EP2607300B1 (en) | 2020-05-13 |
JP5480386B2 (ja) | 2014-04-23 |
KR20180005741A (ko) | 2018-01-16 |
KR101817820B1 (ko) | 2018-01-11 |
JP2013176773A (ja) | 2013-09-09 |
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