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Tube type continuous flow reaction device and preparation method of isopropyl acetoacetate

A technology of isopropyl acetoacetate and a reaction device, which is applied in the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds, can solve the problems of low synthesis yield, high cost, and expensive raw materials, and achieve reduction The effect of generation of side reactions, improvement of yield and content, and simplification of process operation

Inactive Publication Date: 2019-10-01
NANTONG ACETIC ACID CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] 1) is to adopt the transesterification method to carry out synthesis, adopts ethyl acetoacetate or methyl acetoacetate to carry out transesterification reaction with isopropanol under reflux state as raw material, obtains finished product isopropyl acetoacetate, and this technology reaction time is long, and yield The yield is low, the highest yield is 87%, and involves the recovery of solvent toluene, the cost is high;
[0013] 2) It is the Claisen ester condensation route, which needs to use expensive metal sodium, and is used for synthesis with low yield, and there are no mature industrial reports;
[0014] 3) is to adopt diketene and isopropanol under acid catalysis, reflux reaction prepares isopropyl acetoacetate, the highest yield of this method is 86.5%, and because the existence of acid, produce isopropyl ether secondary plant in the reaction process, to reaction The yield is greatly affected
[0015] All of the above processes have either expensive raw materials or low yields, and they are all intermittent reactions, and the reaction time is too long, which leads to higher production and preparation costs.

Method used

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  • Tube type continuous flow reaction device and preparation method of isopropyl acetoacetate
  • Tube type continuous flow reaction device and preparation method of isopropyl acetoacetate
  • Tube type continuous flow reaction device and preparation method of isopropyl acetoacetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] First, from the isopropanol metering tank 1 and the catalyst metering tank 6, through the metering pumps 4 and 5, the isopropanol and the catalyst are injected into the catalyst mixing section 7 according to a certain flow rate respectively, and after the two are mixed, start the diketene metering pump 3. Then inject the diketene and alcohol solution into the tubular continuous flow reactor 8 at a certain flow rate. The internal mixing unit structure of the tubular reactor is SV type, and the molar ratio of diketene and isopropanol is 1:1.01 , the catalyzer is diethylamine, and the consumption of catalyzer accounts for 0.05% of reactant gross mass, and reaction temperature is 140 ℃, and reaction residence time is 5min, and the reaction pressure is regulated by pressure regulating valve 9, and reaction pressure is 0.6MPa, and crude ester after reaction After being cooled to 35°C by the condenser 10, it flows into the crude ester buffer tank 12, and the low boilers in the ...

Embodiment 2

[0048]First, from the isopropanol metering tank 1 and the catalyst metering tank 6, through the metering pumps 4 and 5, the isopropanol and the catalyst are injected into the catalyst mixing section 7 according to a certain flow rate respectively, and after the two are mixed, start the diketene metering pump 3. Then inject the diketene and alcohol solution into the tubular continuous flow reactor 8 at a certain flow rate. The internal mixing unit structure of the tubular reactor is SX type, and the molar ratio of diketene and isopropanol is 1:1.05 , the catalyzer is triethylamine, and the consumption of catalyzer accounts for 0.13% of reactant gross mass, and reaction temperature is 105 ℃, and reaction residence time is 12min, and the reaction pressure is regulated by pressure regulating valve 9, and reaction pressure is 0.35MPa, and crude ester after reaction After being cooled to 40°C by the condenser 10, it flows into the crude ester buffer tank 12, and the low boilers in th...

Embodiment 3

[0050] First, from the isopropanol metering tank 1 and the catalyst metering tank 6, through the metering pumps 4 and 5, the isopropanol and the catalyst are injected into the catalyst mixing section 7 according to a certain flow rate respectively, and after the two are mixed, start the diketene metering pump 3. Then diketene and alcohol solution are poured into the tubular continuous flow reactor 8 at a certain flow rate. The internal mixing unit structure of the tubular reactor is SH type, and the molar ratio of diketene and isopropanol is 1:1.1 , the catalyst is aniline, the amount of the catalyst accounts for 0.2% of the total mass of the reactants, the reaction temperature is 120°C, the reaction residence time is 21min, the reaction pressure is regulated by the pressure regulating valve 9, the reaction pressure is 0.25MPa, and the crude ester is condensed after the reaction The device 10 is cooled to 45°C, and then flows into the buffer tank 12, the low boilers in the crud...

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Abstract

The invention provides a tube type continuous flow reaction device. The tube type continuous flow reaction device is characterized in that an isopropanol metering tank is connected with a catalyst mixing section through an isopropanol metering pump, and a catalyst metering tank is connected between the isopropanol metering tank and the catalyst mixing section; the other end of the catalyst mixingsection and a diketene metering tank are respectively connected with a tube type continuous flow reactor; the other end of the tube type continuous flow reactor is sequentially connected with a crudeester condenser, a crude ester buffer tank and a crude ester feeding pump; a pressure pump is arranged between the tube type continuous flow reactor and the crude ester condenser, and a hollow condenser is arranged on the crude ester buffer tank. The invention also provides a method using the tube type continuous flow reaction device to prepare the isopropyl acetoacetate. The tube type continuousflow reaction device has the advantages that a technology using the tube type continuous flow reactor to prepare the isopropyl acetoacetate is studied, so that the reaction staying time is greatly shortened, the side reaction is reduced, and the yield rate and content of the product are increased; furthermore, the difficulty in rectification separation is decreased, the production cost is reduced,and the safety risk in production is greatly decreased.

Description

technical field [0001] The invention relates to the field of chemical synthesis, in particular to a preparation device and a preparation method of isopropyl acetoacetate. Background technique [0002] Isopropyl acetoacetate [0003] Chinese name: isopropyl acetoacetate; [0004] English name: Isopropyl acetoacetate; [0005] Solubility: soluble in ethanol, chloroform, ether, toluene and other organic solvents; [0006] Molecular formula: C7H12O3; [0007] Molecular weight: 144.16; [0008] Melting point (℃): -27; [0009] Density (g / ml, 25 / 4°C): 0.993; [0010] Action and use: Isopropyl acetoacetate is an important pharmaceutical and pesticide intermediate, and it is mainly used in medicine as the intermediate of cardiovascular drug nimodipine and 2-(3-nitrobenzylidene) isopropyl acetoacetate Synthesis is also the basic raw material for the synthesis of organophosphorus insecticide-refenphos. [0011] Prior Art Synthetic Process: [0012] 1) is to adopt the transest...

Claims

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Application Information

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IPC IPC(8): C07C69/72C07C67/46C07C67/54
CPCC07C67/46C07C67/54C07C69/72
Inventor 庆九俞新南朱小刚刘芳
Owner NANTONG ACETIC ACID CHEM
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