Process for the polymerization of diacrylate-substituted halogenated aromatic monomers
US-2016311948-A1 · Oct 27, 2016 · US
US9598345B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9598345-B2 |
| Application number | US-201614991393-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 8, 2016 |
| Priority date | Jul 12, 2013 |
| Publication date | Mar 21, 2017 |
| Grant date | Mar 21, 2017 |
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The present invention relates to a method for producing an unsaturated-acid ester or an unsaturated acid, containing a step of reacting a compound (1) represented by the following formula (1) with a compound represented by the following formula (2) (excluding the compound (1)) in the presence of a Lewis acid catalyst at a temperature of the boiling point of the compound (1) or higher and 350° C. or lower, thereby obtaining products including a compound represented by the following formula (3): (in formula (1) and formula (3), R 1 , R 2 and R 4 each independently may be hydrogen atom or an alkyl group, R 3 and R 5 each independently are hydrogen atom or a deuterium atom, and X is a halogen atom; in formula (2) and formula (3), R 6 may be hydrogen atom, an alkyl group or an aryl group, and R 7 is hydrogen atom or a deuterium atom).
Opening claim text (preview).
The invention claimed is: 1. A method for producing an unsaturated-acid ester or an unsaturated acid, the method comprising reacting a compound (1) of the formula (1) with a compound (2) of the formula (2), which is different from the compound of the formula (1), in the presence of a Lewis acid catalyst at a temperature within a range from 170° C. to 350° C., thereby obtaining a reaction product comprising a compound (3) of the formula (3) wherein R 1 , R 2 , and R 4 each independently are selected from the group consisting of a hydrogen atom, a deuterium atom, and an alkyl group which has a carbon number of from 1 to 3 and may be optionally substituted with a halogen atom and/or a deuterium atom, R 3 and R 5 each independently are selected from the group consisting of a hydrogen atom and a deuterium atom, and X is a chlorine atom, a fluorine atom, a bromine atom, or an iodine atom; R 6 —OR 7 (2), wherein R 6 is selected from the group consisting of a hydrogen atom, a deuterium atom, and an alkyl group which has a carbon number of from 1 to 11 and may be optionally substituted with a halogen atom and/or a deuterium atom, or an aryl group and may be optionally substituted with a halogen atom and/or a deuterium atom, and R 7 is a hydrogen atom or a deuterium atom; and wherein R 1 , R 2 , and R 4 are the same as defined with regard to the formula (1), and R 6 is the same as defined with regard to the formula (2); wherein the Lewis acid catalyst is at least one selected from the group consisting of ZnO—ZrO 2 , ZnO—Al 2 O 3 , ZnO—TiO 2 , In 2 O 3 —ZrO 2 , NiO—ZrO 2 , CoO—ZrO 2 , MnO—ZrO 2 , silica gel, γ-alumina, ZrO 2 , ZnO—SiO 2 , Zr PbO x , Al 2 O 3 —ZrO 2 , MgO—ZrO 2 , ZnO—Cr 2 O 3 , TiO 2 , and Zr—NiOx, and wherein the Lewis acid catalyst is fixed to a support. 2. The method according to claim 1 , wherein the Lewis acid catalyst is a solid acid. 3. The method according to claim 1 , wherein the reaction is conducted in a gas phase. 4. The method according to claim 1 , wherein an amount of the compound (2) is from 0.5 to 20 mol, per 1 mol of the compound (1). 5. The method according to claim 1 , wherein an amount of the compound (2) is from 1 to 10 mol, per 1 mol of the compound (1). 6. The method according to claim 1 , wherein an amount of the Lewis acid catalyst, per 1 mol of the compound (1) present in a reaction vessel, is from 0.001 to 1 mol. 7. The method according to claim 1 , wherein an amount of the Lewis acid catalyst, per 1 mol of the compound (1) present in a reaction vessel in a batch mode or per 1 mol of the compound (1) residing in a reaction vessel in a continuous mode, is from 0.01 to 0.2 mol. 8. The method according to claim 1 , wherein the reacting temperature is from 200 to 300° C. 9. The method according to claim 1 , wherein the reaction is conducted in a liquid phase. 10. The method according to claim 1 , wherein in the reaction a compound or gas which does not chemically react with starting materials and the reaction product is used as a solvent or a diluent gas, wherein the solvent is selected from the group consisting of pentane, hexane, heptane, petroleum ether, dimethyl ether, diethyl ether, tetrahydrofuran, 1,2-dimethyoxyethane, dichloromethane, chloroform, carbon tetrachloride, dichloroethane, acetic acid, benzoic acid, acetic anhydride, ethyl acetate, acetone, 2-butanone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, benzene, toluene, chlorobenzene, dichlorobenzene, benzonitrile, nitromethane, nitrobenzene, and a mixture thereof, and wherein the diluent gas is selected from the group consisting of nitrogen, helium, argon, and a mixture thereof. 11. The method according to claim 10 , wherein an amount of the solvent or the diluent gas is in a range that a concentration of the compound (1) is kept at 5% by mass or higher. 12. The method according to claim 1 , wherein the reaction is conducted in a continuous mode and a space velocity is from 1 to 500,000 h −1 . 13. The method according to claim 1 , wherein a reaction pressure is from 0 MPa to 10 MPa. 14. The method according to claim 1 , wherein a reaction pressure is from 0.05 MPa to 2 MPa. 15. The method according to claim 1 , wherein when the reacting is conducted in a batch mode, a reaction time is from 10 minutes to 12 hours, and when the reacting is conducted in a continuous mode, a reaction time is from 0.1 second to 60 minutes.
by reacting carboxylic acids or symmetrical anhydrides with ester groups or with a carbon-halogen bond (preparation from carboxylic acid halides C07C67/14) · CPC title
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