Method for continuously producing ketomalonic acid compound using flow reactor
The purpose of the present invention is to provide a method for continuously producing a ketomalonic acid compound such as a ketomalonic acid diester or a hydrate thereof, which is an industrially useful compound, on an industrial scale and in a safe and steady manner. The present invention relates to: a method in which a malonic acid diester, a carboxylic acid compound and a chlorous acid compound are used as raw material compounds, and these raw material compounds are mixed together to prepare a mixture and the mixture is supplied to a flow reactor continuously, thereby continuously producing a corresponding ketomalonic acid diester or a hydrate thereof; and a continuous production apparatus for performing the method.
1. A method for continuously producing a ketomalonic acid diester or a hydrate thereof, comprising:
step (A) mixing a malonic acid diester, a carboxylic acid compound, and a chlorous acid compound to obtain a mixed mixture;
step (B) supplying the mixed mixture to one or more tubular flow reactors; and
step (C) reacting the mixed mixture in the one or more tubular flow reactors to obtain a reaction mixture;
wherein the reaction mixture is continuously producing the ketomalonic acid diester or the hydrate thereof,
wherein the length of the tube of the one or more tubular flow reactor is from 9 m to 50 m,
wherein a temperature control part of the one or more tubular flow reactors controls the temperature of the one or more tubular flow reactors at 80° C. or higher.
2. The method according to claim 1 , wherein the chlorous acid compound is supplied to step (A) as an aqueous solution of a chlorous acid compound.
3. The method according to claim 1 , wherein the malonic acid diester or a mixture of the malonic acid diester and the carboxylic acid compound is supplied to step (A) in the absence of a solvent.
4. The method according to claim 1 , wherein the temperature control part is a bath and the bath is at a temperature of 80° C. or higher.
5. The method according to claim 1 , wherein the method further comprises:
step (D) aging the reaction mixture obtained in the step (C).
6. The method according to claim 5 , wherein the step (D) is performed in one or more second flow reactors.
7. The method according to claim 1 , wherein the method further comprises:
step (E) quenching the reaction by mixing a quench liquid with the reaction mixture obtained in the step (C).
8. The method according to claim 7 , wherein the step (E) is performed in one or more third tubular flow reactors.
9. The method according to claim 7 , wherein the quench liquid is an aqueous solution of a sulfite salt and/or an alkali metal hydroxide.
10. The method according to claim 1 , wherein the malonic acid diester is a malonic acid diester having chemical formula (1)
wherein, in the chemical formula (1), R may be the same as or different from each other and represents an alkyl group which optionally has substituent(s), a cycloalkyl group which optionally has substituent(s), an aromatic hydrocarbon group which optionally has substituent(s), or an aromatic heterocyclic group which optionally has substituent(s), or two Rs may bind to each other to form a ring with adjacent oxygen atoms.
11. The method according to claim 1 , wherein the ketomalonic acid diester is a ketomalonic acid diester having chemical formula (2)
wherein, in the chemical formula (2), R may be the same as or different from each other and represents an alkyl group which optionally has substituent(s), a cycloalkyl group which optionally has substituent(s), an aromatic hydrocarbon group which optionally has substituent(s), or an aromatic heterocyclic group which optionally has substituent(s), or two Rs may bind to each other to form a ring with adjacent oxygen atoms.
12. The method according to claim 1 , wherein the method is an industrial production method.
13. The method according to claim 5 , wherein the method further comprises:
step (E) quenching the reaction by mixing a quench liquid with the reaction mixture obtained in the step (D).
14. The method according to claim 13 , wherein the step (E) is performed in one or more third tubular flow reactors.
15. The method according to claim 13 , wherein the quench liquid is an aqueous solution of a sulfite salt and/or an alkali metal hydroxide.
16. The method according to claim 1 , wherein the malonic acid diester is a malonic acid diester having chemical formula (1)
wherein, in the chemical formula (1), R may be the same as or different from each other and represents an alkyl group which optionally has substituent(s), a cycloalkyl group which optionally has substituent(s), an aromatic hydrocarbon group which optionally has substituent(s), or an aromatic heterocyclic group which optionally has substituent(s), or two Rs may bind to each other to form a ring with adjacent oxygen atoms; and
wherein the ketomalonic acid diester is a ketomalonic acid diester having chemical formula (2)
wherein, in the chemical formula (2), R may be the same as or different from each other and represents an alkyl group which optionally has substituent(s), a cycloalkyl group which optionally has substituent(s), an aromatic hydrocarbon group which optionally has substituent(s), or an aromatic heterocyclic group which optionally has substituent(s), or two Rs may bind to each other to form a ring with adjacent oxygen atoms.