PREPARATION OF EPOXIDATION CATALYST SOLUTION

24-10-1969 дата публикации
Номер:
FR0001583189A
Автор:
Принадлежит:
Контакты:
Номер заявки: 1583189D
Дата заявки: 29-12-1967

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MINISTRY

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THE INDUSTRIAL DEVELOPMENT

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SCIENTIFIC AND

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SERVICE

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iNTELLECTUAL INDUSTRIELLE PATENT of the P.V. On PROBLEMS it 134,216 No. 1.583.189 internation Classification has the: B 01 j // C 07 d

Chemical process for the preparation of catalyst.

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Society said: [...] INTERNATIONAL, INC. residing in the United States of America.

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Demanded 29 December 1967, to 1011 42m, to Paris.

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Issued by stopped 15 September 1969.

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(Bulletin official A property industrial, no. 43 of the 24 October 1969.) (Patent application deposited in the United States of America 3 January 1967,

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under the no. 606,535, on behalf of John m. Kollar.)

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The present invention relates to the preparation

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structure by the incorporation of

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inorganic forms of certain elementary and

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a hydroperoxide catalysts aralkyl, to

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produce a solution of catalyst

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for the production of compounds [...]. The In-

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prevention also relates to the use of the said solution-

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the purification catalyst for the production of compound^

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[...].

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The preparation method of catalyst solutions

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[...] of the of the invention deviates from the tech-

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nic front. For the production

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[...] compounds using [...] -

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organic oxides, reference is made to the patents

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belgian nbone 663,859, 665.082,644,090 657,838 and,

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which describe in detail the reaction conditions

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and catalytic materials used. A problem

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which has been in the prior art is the

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price of the catalyst employed. Be

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the shapes also be possible to use the least

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expensive catalyst, but difficulties have

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been encountered for obtaining an amount of

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lowest cost solution of the catalyst sufficient

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to be able to successfully conduct epoxidation.

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The invention provides a solution to this problem

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by permitting the use of forms of catalyst

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and inexpensive the solubilization of these forms

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to such a degree that the catalyst solutions

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resulting can be used for the production

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[...] compounds.

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An object of the invention is to provide a pro-

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supplied for the preparation of said solution a-

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the purification catalyst for use in

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epoxidation reactions employing hydro-

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aralkyl peroxides as epoxidation of agents.

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The invention also relates to the use of the

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solution to the production of compounds

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[...].

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According to the invention, are mixed forms [...] -

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[...] or elementary metals capable of in-

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9 210341 7-φ-

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take efficiently at the reaction of unsaturated olefinic compounds with hydroperoxides to produce compounds with a hydroperoxide [...] aralkyl, and the mixture is kept, during a practical time frame, at a temperature capable of providing a solution containing the epoxidation catalyst, this solution same suitable for use in the production of compounds [...] as previously described.

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Examples given below to [...] limiting is will further understand how the invention can be implemented.

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Example 1. - Is introduced a solution formed by 2.5% by weight of glycerol, 72.5 by weight of alpha-phenylethanol and 25% by weight of a 12% solution of ethylbenzene hydroperoxide in ethylbenzene in a suitable container. Are added to 50 grams of this solution 0.75 gram of molybdenum metal finely pulverized. The resulting mixture is maintained at a temperature of about 85 °C, while stirring, for five hours. After this period of time, the resulting solution contains 0.1% molybdenum form of a compound which is soluble. The entire hydroperoxide is decomposed, mainly [...].

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Is introduced 2 grams of the catalyst solution prepared as described above in a reactor, in conjunction with 16 grams of propylene, 74 grams ethylbenzene containing few percent of alpha-phenyl ethanol and 10 grams of ethylbenzene hydroperoxide. Is reacted mixture into the reactor for one hour at 120 °C, at a gauge pressure of about 35 kg/cm2. There is that the reaction mixture contains 2.9 grams of propylene oxide.

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The metals catalyst, used in elemental form or in the form of inorganic compounds or minerals, are [...] molybdenum, vanadium, tungsten, titanium, tantalum, the [...], the rhenium, selenium, chromium, zirconium, tellurium and uranium. These metals are used in the form of metal powder or inorganic compounds, including oxides, hydroxides, sulfides, chlorides, oxy-chlorides, fluorides, phosphates, andc. The preferred forms of compounds are oxides and acids these oxides by hydration.

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The solution in which the catalyst is dissolved may comprise the following components:

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Series Series desirable Preferred Series
Hydroperoxide [...] of-
[...], % by weight... 0,1-200,5-101,0-5,0
[...], . % by weight. 5-9920-8565-75
Solubilization agent,
% by weight0-401-102-5
[...], % by weight... remainderremainderremainder

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The catalyst mixture is maintained as inorganic or elemental and containing the hydroperoxide solution at temperatures generally between 25 and 200 °C, [...] between 50 and 100 °C, and preferably between 75 and 90 °C, while stirring or circulating otherwise, over a period generally of thirty minutes to ten hours and preferably four to six hours. At the end of this period, a solution is obtained containing the catalyst in the form of a dissolved compound, the solution suitable ideal for the catalytic production of a compound by reacting a compound [...] unsaturated olefin with a hydroperoxide [...].

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Aralkyl The hydroperoxides are derived from alpha-aralkyl preferably hydrocarbons of the general formula:

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Hh

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I I

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A-c-c-r "

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I I

R 'r' "

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wherein each of the substituents R ', R " and Rw may be hydrogen or an alkyl radical preferably having from one to twenty carbon atoms, and A is an aromatic ring. The aromatic ring A can be benzene, and it may be substituted by fluoro, chloro, bromo, nitro, alkoxyl, [...] or carboxy (or their esters). The core may have one or more side chains containing up to twelve carbon atoms each, these chains may be branched themselves. Hydroperoxides The alpha-aralkyl are of the formula:

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O-h

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I

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Oh

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I I

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A-c-c-r "

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I I

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R ' r "

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wherein R ', R ", R' " and A have the same meaning as previously. Exemplary, hydroperoxides include toluene, ethylbenzene, , cumene, of [...], of isobutylbenzene, tetralin, diisopropylbenzene, para- [...], ortho-xylene, meta-xylene, para- [...], of [...], andc. Preferred species are those derived from a cumene, i.e. the hydroxide of alpha- [...], and ethylbenzene, i.e. hydroxide [...].

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Solubilizing agents are, preferably, used to prepare the catalyst solutions according to the invention. By way of suitable solubilizing agents, include highly polar compounds type [...], the diketones, alcohols such as glycerin, andc.

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See patent mentioned above with respect to the complete description and reagents for epoxidation reaction conditions, as well as the percentage of catalyst, andc.

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Materials to non-olefinic unsaturation are epoxidized which the defined according to the invention include aliphatic and alicyclic substituted and unsubstituted, which can be hydrocarbons, esters, alcohols, ketones, ethers, andc. As preferred compounds, include those containing from two to thirty carbon atoms approximately, and preferably at least three carbon atoms. Include, as [...], ethylene, propylene, normal butylene, isobutylene, pentenes, the Methylpentenes, the normal [...], octenes, the dodecenes, cyclohexene, methylcyclohexene the, [...] butadiene, styrene, methylstyrene, the [...], the [...], the [...], andc. Olefins may be used having substituents containing halogen, oxygen, sulfur, andc. As substituted olefins of this type, include [...] alcohol, methallyl alcohol, cyclohexanol, [...] ether, methyl methacrylate, methyl oleate, the [...], [...] chloride, etc Generally, all epoxidized olefin materials by the method pre-





[...] used may also be epoxidized by the process of the invention, including non-saturation with up to several thousands of carbon atoms. Exemplary olefins, include linseed oil, olive oil, cottonseed oil, liquid resin glycerides, castor oil, corn oil, esters [...] unsaturated fatty acids, the solid or liquid polybutadiene, polyisoprene, the unsaturated copolymers of ethylene and propylene, including their terpolymers with cyclopentadiene, andc.

Examples specified given below will more preferably the manner in which the method of the present invention can be implemented.

Example 2. - Is heated a solution containing 85% by weight of alpha-methylbenzyl alcohol, 5% by weight of glycerol and 10% of an oxidation product of ethylbenzene containing 14.2% by weight of ethylbenzene hydroperoxide, in the presence of an excess of molybdenum dioxide, to 85 °C, for four hours. The effluent comprises approximately 8,000 PPM of soluble molybdenum.

The selectivity to propylene oxide is similar to that obtained in the example 1 with the above catalyst.

Example 3. Are treated 2- grams of vanadium metal powder with a solution comprising 15% oxidation product ethylbenzene (containing 12% by weight of ethylbenzene hydroperoxide), glycerin 3% and 82% alpha-methylbenzyl alcohol to 100 °C, for four hours, while vigorously agitating. In the solution about 1000 PPM soluble vanadium.

Is treated a mixture of epoxidation of hydroxide containing 10% ethylbenzene, a molar proportion of 5:1 between 1' allyl alcohol and ethylbenzene hydroperoxide, 0.4% vanadium (from the readying) and of ethylbenzene 110 °C for fifteen minutes. The selectivity in [...] is equal to 84% based on moles of ethylbenzene hydroperoxide and to 86 mole % based on the allyl alcohol. Level i The conversions' hydroperoxide and allyl alcohol are greater than 97% and equal to 19% respectively.

Example 4. - Is treated about 2 grams of metallic tungsten as described in the example 1, resulting in 650 PPM soluble tungsten.' The application of this catalyst to the epoxidation butene -1 is as follows: is treated a mixture formed by 7 moles of butene -1 per mole of ethylbenzene hydroperoxide and 150 PPM tungsten soluble catalyst, to 120 °, during 96 minutes. The oxide selectivity 1,2-butene is equal to 62% based on moles of the hydroperoxide, with a conversion to hydroperoxide equal to 99%.

Alterations can be made to the described modes of implementation, in the field of technical equivalents, without departing from the invention.

SUMMARY

1° A process for making a solution of catalyst for the reaction of hydroperoxide aralkyl compounds and non-saturation [...] to produce compounds [...], comprising mixing a metal catalyst, elemental form or in the form of inorganic compound, with a liquid of aralkyl hydroperoxide, in principle in the absence of non-olefinically unsaturated compound.

2° A process for making a solution of catalyst for the reaction of hydroperoxides of aralkyl compounds and non-olefinic unsaturation to produce compounds [...], comprising mixing a metal catalyst, elemental form or in the form of inorganic compound, with a liquid containing a hydroperoxide of aralkyl, at a temperature of from 40 to 200 °C, for a period of from fifteen minutes to twenty-four hours, the mixture is carried out in principle in the absence of non-olefinically unsaturated compound.

Society said: [...] INTERNATIONAL, INC.

For proxy:

Vault Cabinet [...]

Ia sale For booklets, be directed to [...] Nationale, 27, the street Convention, Paris (15 *).