专利摘要:
1495245 Carboxylation process MONTEDISON SpA 24 March 1976 [28 March 1975] 11916/76 Heading C2C A process for carboxylating a ketone, ester, nitroparaffin or nitrile substrate comprises reacting said substrate with CO 2 and an alkali metal phenate in a linear or cyclic ester, cyclic ether, cyclic sulphone, tertiary aliphatic or cycloaliphatic amine or a saturated or unsaturated heterocyclic base. The preferred reaction temperature is 40‹ to 60‹ C. The phenate may be prepared in situ from the corresponding phenol and alkali metal hydroxide and the water formed being eliminated azeotropically with excess solvent.
公开号:SU715016A3
申请号:SU762337708
申请日:1976-03-26
公开日:1980-02-05
发明作者:Боттаччио Джорджо;Паоло Чьюзоли Джан;Алпери Энзо;Марчи Марчелло;Лана Джулио
申请人:Монтэдисон С.П.А. (Фирма);
IPC主号:
专利说明:

The invention relates to methods for producing substituted carboxylic acids, for example, nitroacetic acid and fekylcyanoacetic acid, which are used in the production of solvents for cellulose nitrate, resins, varnishes, etc. The known methods for producing ketocarboxylic acids of the formula Rt-C-CH II O Bg R and R where H and R together form cycloalkylene rings, by carboxyplating the corresponding ketones with carbon dioxide in the presence of trimethylphenol alkali metal (or silica) in a polar solvent such as dimethylformamide or dimethylsulfonic acid. B yes, at O-100 ° C 1. Use of solvents smeshivayuipths with water complicates the separation and isolation of the desired product. Another method of producing ketocarboxylic acids is based on the interaction of cycloalkanoic hydroperoxides with aldehydes under redox conditions followed by extraction 2. The use of peroxides and the extraction, as well as separation and isolation of the desired product leads to a low yield (9-25%), as well as complicates the process because of the need to ensure explosion-free process. A method of producing substituted, in particular ketocarbopic, acids by carboxylation of the corresponding ketones having an active hydrogen atom, carbon dioxide and an alkali metal phenol is known. The ketocarboxylic mono- or di-acids of the aliphatic or araliphatic or cycloaliphatic series are obtained. The process is carried out at a temperature of about -100 ° C in an environment of bipolar aprotic solvents 3. Although a high conversion is achieved in this process (80-99%), the yield and purity of the target product do not achieve the same high performance due to the difficulty of separating displaced with water solvents. To simplify the process, according to method 4, under the same conditions and to obtain the same compounds, another solvent is used - aliphatic, aromatic or araliphatic) hydrogen, having a boiling point of 80-250 ° C.
This method is the closest technical solution to the one proposed. The process of carboxylation of the compounds of the general formula "1O CH-C-E3 or C — C where RI, R2-R4 RS is independently hydrogen, alkyl Cj- € 4, aryl; RI and RS together form a hydrocarbon chain of normal or branched structure; RE - alkyl GI-Ci2 aryl; O-alkyl, O-aryl, are carried out with carbon dioxide and a phenol of an alkali metal at a temperature of 20–100 ° C. As a phenol of an alkali metal, its mono-, di-, or trialkyl-substituted ones are used, and their molar ratio to the specified starting ketones is (1-4): 1 However, despite the relatively high selectivity, for example, for benzoyl acetic acid, 823%. Kozgaers is small (25.8%) to achieve high process productivity. The purpose of the invention is to increase the selectivity of the process with a higher conversion of the starting materials. This aim dostagaets in that the solvent is selected from the coupled meters group consisting of tetrahydrofuran, propylene carbonate, triethylamine, f -metilmorfoli sulfolane, dioxane, Ethyl acetate was, 8-picoline, metiletilpiridin, shtrobenzol, anisole, diphenyl ether zfir or diizoprogshlovga. It is advisable to use sodium o-tert-butyl-l-β-cresolate as an alkali metal phenol; the molar ratio of the phenol of the alkali metal to the initial ketone is 1-4: 1. According to the proposed method, I get nitroacetic, phenylcyanoacetic or substituted carboxylic acids of the general form K, -C-Ch-Soon (1) where СНН-; NZSO-; CN-; SbH5-.
7150164
Phenylacetonitrile or nitromethane or compounds of the general formula are used as starting compounds.
(2)
RI-C-CH-JZ
And I
Where RJ and Rj are as indicated; RE -N-. SNS-, i.e. compounds containing an active hydrogen atom. The process is conducted at a temperature of 40-60 ° C. All of these conditions provide better selectivity (up to 95%), greater conversion (up to 45%), greater solvent stability than a greater degree of regeneration is achieved, and low cost of solvents reduces the cost price of the target product. The method is carried out as follows. To the solution of phenol sodium and in a solvent previously saturated with carbon dioxide, while stirring at a given temperature, add the starting material, which is carboxylated in the established proportions; then the reaction mixture is stirred under carbon dioxide atmosphere until the reaction is complete. In the case of using acetone, water is added to the reaction mixture with vigorous stirring in an amount equimolar to the amount of the starting phenol. The sodium salts of acetoacetic and 3-ketoglutaric acids, which are formed in this case, together with sodium bicarbonate, obtained from an excess of phenol, are precipitated as crystals, and then filtered and washed with a solvent (benzene, petroleum ether, chloroform). The acid is then separated from the salt by acidification with dilute sulfuric acid, followed by extraction with ethyl ether. For other starting materials, the reaction mixture is diluted with an equal volume of water in the presence of carbon dioxide, after which the phenol, solvent and unreacted starting material are extracted with ether, the aqueous phase is acidified and the acid is extracted with ether. The table shows examples of the preparation of carboxylic acid substitutions for various starting materials and process conditions.

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权利要求:
Claims (4)
[1]
 t- "f 13 claims. The method of obtaining nitroacetic or phenylcyanoacetic or substituted carboxylic acids of the general formula R-C-CH-COOH where Ri is CH5-; OCHj-; R2-H-; CN-; CgHs-; by carboxylphenol phenylacetonitrile or nitromethane or compounds of the general formula C – C – CH – Bc (2) where RJ and R2 are the indicated values, Ra is H, CH 2– carbon dioxide and the phenolate of the base metal at a temperature of 40-60 ° C in a solvent medium. Distinguished by the fact that, in order to increase the selectivity of the process, a solvent from the group of tetrahydrofuran, propylene carbonate, triethylamine, N-methylmorpholine, 14 sulfolane, dioxane, ethyl acetate,-picolin, methyl ethyl pyridine, nitrobenzene is used as a solvent. anisole, diphenyl ether or diisopropyl ether 2. The method according to any one of the preceding claims, with the fact that o-tert, butyl-p-cresolate sodium is used as the phenol of the alkali metal. 3. A process according to claim 1, characterized in that the process uses the molar ratio of alkali metal phenol and compound of formula (2) equal to 1-4: 1. Sources of information taken into account in the examination 1. For the Germany, No. 1668378, cl. C 07 C 59/32, published 1973.
[2]
2. US patent number 3197488, cl. 260-3473, publ. 1965.
[3]
3.J.Bottaccio et al. Organic syntheses in solvents. Carboxylation with carbon dioxide in aprotic dipolar solvents. Gazzette Chemica Hafiana, 103, p. 105-116, 1973.
[4]
4. For the USSR, N 2118337 / 23-04, cl. C 07 C 59/32, 04/03/1974 (prototype).
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同族专利:
公开号 | 公开日
AU1236676A|1977-09-29|
BE840078A|1976-09-27|
US4032555A|1977-06-28|
DE2612577C2|1987-04-30|
JPS6032604B2|1985-07-29|
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NL7603018A|1976-09-30|
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FR2305422B1|1979-04-06|
NL185774C|1990-07-16|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

GB1145098A|1966-08-02|1969-03-12|Montedison Spa|Beta-ketoacids|
US3595907A|1968-12-18|1971-07-27|Texaco Inc|Carboxylation of indene|
US3658874A|1969-01-27|1972-04-25|Texaco Inc|Carboxylation of organic nitriles|IT1075720B|1977-03-03|1985-04-22|Montedison Spa|PROCESS FOR THE PREPARATION OF ALPHA-FORMYLACIDS AND THEIR DERIVATIVES|
US4508660A|1983-03-14|1985-04-02|E. I. Du Pont De Nemours And Company|Carbonylation of olefinically unsaturated nitriles and acids using a sulfone solvent|
US4730083A|1984-12-24|1988-03-08|Ciba-Geigy Corporation|Process for the preparation of 3,5-dialkyl-4-hydroxy benzoic acid|
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US5124477A|1988-12-14|1992-06-23|Kawasaki Steel Corporation|Process for preparing para-hydroxybenzoic acid|
US5807933A|1992-06-22|1998-09-15|The Mead Corporation|Carboxyl-containing phenolic resin developer and method of preparation|
FR2730731B1|1995-02-20|1997-04-04|Rhone Poulenc Chimie|CARBOXYLATION PROCESS OF AN AROMATIC ETHER|
EP0912482B1|1996-05-20|2001-03-21|E.I. Du Pont De Nemours And Company|Production of aromatic hydroxycarboxylic acids|
US6392090B1|1996-10-02|2002-05-21|Mitsui Chemicals, Inc.|Process for preparing hydroxybenzoic acids|
JP4191875B2|1999-07-30|2008-12-03|富士フイルム株式会社|Method for producing aromatic carboxylic acid compound|
US8188020B2|2003-12-22|2012-05-29|Chevron Oronite S.A.|Lubricating oil composition containing an alkali metal detergent|
US8187455B2|2008-07-18|2012-05-29|Socomer Nv.|Voltammetric technique to determine the individual concentration of different antioxidants of the same class|
DE102010009346A1|2010-02-20|2011-08-25|Fachhochschule Münster, 48565|Synthesizing isophorone-2-carboxylic acid from isophorone, comprises reducing isophorone to 3,5,5-trimethyl cyclohexanone, and carboxylating 3,5,5-trimethyl-cyclohexanone with carbon dioxide in the presence of diazabicycloundecene|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
IT21816/75A|IT1034702B|1975-03-28|1975-03-28|PROCESS FOR THE CARBOXYLATION OF ORGANIC SUBSTRATES WITH CARBON ANHYDERS.|
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