Organic compounds -- part of the class 532-570 series – Organic compounds – Heterocyclic carbon compounds containing a hetero ring...
Reexamination Certificate
2002-05-31
2003-01-14
Qazi, Sabiha (Department: 1616)
Organic compounds -- part of the class 532-570 series
Organic compounds
Heterocyclic carbon compounds containing a hetero ring...
C549S531000
Reexamination Certificate
active
06506914
ABSTRACT:
TECHNICAL FIELD
The present invention relates to a process for producing an oxirane compound. More particularly, the present invention relates to a process for producing an oxirane compound in which the oxirane compound can be obtained with high selectivity and high yield by reacting an olefin with a hydroperoxide in the presence of a catalyst.
BACKGROUND ART
A process for obtaining an oxirane compound by reacting an olefin with a hydroperoxide in the presence of a catalyst is known. For example, in U.S. Pat. No. 4367342, a method of using a titanium-supported silica catalyst is described. In the conventional method, however, the selectivity and yield of oxirane compound as the intended material, were insufficient.
DISCLOSURE OF THE INVENTION
Under such conditions, the present inventors have intensively studied regarding a process for producing an oxirane compound having no problem as described above, and resultantly found that an oxirane compound can be obtained under high selectivity and high yield by reacting an olefin with a hydroperoxide using a catalyst obtained by a specific method, leading to completion of the invention.
Namely, the present invention relates to a process for producing an oxirane compound by reacting an olefin with a hydroperoxide in the presence of a catalyst, wherein the catalyst is obtained by gelling a silicon compound of the following formula (1) (silicon compound (1)), a silicon compound of the following formula (2) (silicon compound (2)) and a titanium compound in water, alcohol solvent or mixed solvent of water and alcohol, removing the solvent in the resulted gel by extraction with supercritical fluid, then, drying and silylating the resultant:
Si(OR
1
)
4
(1)
(R
2
)
m
Si(OR
3
)
4−m
(2)
(R
1
,R
2
and R
3
independently represent a hydrocarbon group having 1 to 20 carbon atoms and m represents an integer of 1 or 2.).
BEST MODE FOR CARRYING OUT THE INVENTION
As the olefin to be subjected to reaction, ethylene, propylene, 1-butene, 2-butene, isobutylene, butadiene, 1-pentene, isoprene, 1-hexene, 1-octane, 1-decene, cyclopentene, cyclohexene, styrene, allyl chloride, allyl alcohol and the like are exemplified.
As the hydroperoxide to be subjected to reaction, any of organic hydroperoxides and inorganic hydroperoxides can be used. As the organic hydroperoxide, ethylbenzene hydroperoxide, cumene hydroperoxide, t-butylhydroperoxide and the like are exemplified. As the inorganic hydroperoxide, hydrogen peroxide and the like are exemplified.
From the industrial standpoint, a process for producing propylene oxide from propylene and an organic hydroperoxide is important, and the catalyst according to the present invention can be suitably used in this reaction.
In the present invention, there is used a catalyst obtained by gelling a silicon compound of the following formula (1) (silicon compound (1)), a silicon compound of the following formula (2) (silicon compound (2)) and a titanium compound in water, an alcohol solvent or a mixed solvent of water and an alcohol, removing the solvent in the resulted gel by extraction with supercritical fluid, then, drying and silylating the resultant:
Si(OR
1
)
4
(1)
(R
2
)
m
Si(OR
3
)
4−m
(2)
wherein R
1
, R
2
and R
3
independently represent a hydrocarbon group having 1 to 20 carbon atoms. m represents an integer of 1 or 2. As the hydrocarbon group, a methyl group, ethyl group, propyl group, butyl group, phenyl group, benzyl group and the like are exemplified, and these hydrocarbon groups may be partially substituted with a hetero atom. Preferable are a methyl group, ethyl group, propyl group, butyl group and phenyl group which are easily available in industrial.
Specific preferable examples of the silicon compound (1) include tetramethyl orthosilicate, tetraethyl orthosilicate, tetrapropyl orthosilicate, tetraisopropyl orthosilicate, tetrabutyl orthosilicate and the like. Specific preferable examples of the silicon compound (2) include trimethoxymethylsilane, trimethoxyphenylsilane, dimethoxydimethylsilane, triethoxymethylsilane, triethoxyphenylsilane and the like.
The ratio of the mol number of the hydrocarbon group R
2
to the total mol number of the silicon compound (1) and silicon compound (2) is preferably from 5 to 95%, further preferably from 20 to 80%. When the ratio is too small, catalytic ability may decrease, on the other hand, when too large, gelling may not progress in catalysis synthesis.
As the titanium compound, titanium alkoxides, for example, tetramethyl orthotitanate, tetraethyl orthotitanate, tetrapropyl orthotitanate, tetraisopropyl orthotitanate, tetrabutyl orthotitanate, titanium diisopropoxide bis(acetylacetonate) and the like can be Exemplified.
Examples of alcohols as the solvent include methanol, ethanol, n-propanol, isopropanol, butanol, cyclohexanol, ethylene glycol and the like.
The catalyst in the present invention is prepared as described below. First, a silicon compound (1), a silicon compound (2) and a titanium compound are gelled in water, an alcohol solvent, or a mixed solvent of water and an alcohol. It is preferable to adjust so that the ratio of the mol number of the hydrocarbon group R
2
to the total mol number of the silicon. compound (1) and silicon compound (2) becomes 5 to 95%. The silicon compound (1) and silicon compound (2) may each be a mixture of two or more compounds. The molar ratio of a titanium compound used to the total mol number of the silicon compound (1) and silicon compound (2) is preferably from 0.0001 to 1. As the gelling method, the following methods are illustrated. That is, usually by adding an acid or alkali as a promoter into water, the alcohol solvent or the mixed solvent of water and alcohol containing a silicon compound (1), silicon compound (2) and titanium compound dissolved, hydrolysis and condensing reaction of the silicon compounds and titanium compound can be progressed, and finally, a gel which is a polymer condensate containing a Si—O—Ti bond can be obtained. The gelling reaction is usually conducted at temperatures from −30 to 100° C. Aging may also be effected to grow gelled solid. The aging is usually conducted at 0 to 200° C. within 180 hours. An acid or alkali is used as a promoter of the above-mentioned hydrolysis and condensing reaction, and use of an acid is preferable from the standpoint of the resulting catalytic ability. Examples of the acid include inorganic acids such as nitric acid, hydrochloric acid, sulfuric acid and the like and organic acids such as formic acid, acetic acid and the like, and examples of the alkali include sodium hydroxide, potassium hydroxide, ammonia and the like. The addition amount of this acid or alkali cannot be limited since it depends on the kinds of raw material compounds and gelling conditions, and it is preferable that the addition amount is generally in the range from 0.0001 to 100 mol based on 1 mol of silicon compounds.
The solvent in the resulted gel is removed by extraction with supercritical fluid. As the fluid, carbon dioxide, methanol, ethanol, propanol and the like are exemplified, and use of carbon dioxide is preferable since post treatment is easy and high catalytic ability is obtained. As the method of removal by extraction, the following methods are listed. Namely, the removal by extraction can be carried out by passing supercritical carbon dioxide through an autoclave charged with the gel under conditions for forming supercritical carbon dioxide, namely, at temperatures of about 31° C. or more and under pressure of about 7.3 MPa or more. For example, supercritical carbon dioxide fluid having a temperature of 31 to 100° C. and a pressure of 10 to 30 MPa can be used. By this operation, water, the alcohol solvent or mixed solvent of water and the alcohol incorporated into the gel can be removed by extraction.
After the above-mentioned extraction removal operation, drying and silylation are performed.
The drying is preferably conducted under reduced pressure or under gas flow of air, nitrogen or the like at 0 to 200° C
Stocker Carsten
Tsuji Junpei
Qazi Sabiha
Sumitomo Chemical Company Limited
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