Method for producing isopropylamine

A technology of isopropylamine and diisopropylamine, which is applied in the field of isopropylamine production, can solve the problems that diisopropylamine cannot be effectively converted into isopropylamine, the operation difficulty of the rectification system, and the increase of production cost, etc., and the method is simple, feasible, and considerable economic benefits , the effect of easy operation

A technology of isopropylamine and diisopropylamine, which is applied in the field of isopropylamine production, can solve the problems that diisopropylamine cannot be effectively converted into isopropylamine, the operation difficulty of the rectification system, and the increase of production cost, etc., and the method is simple, feasible, and considerable economic benefits , the effect of easy operation

CN101684073AActive Publication Date: 2010-03-31CHINA PETROLEUM & CHEM CORP +1

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for producing isopropylamine
  • Method for producing isopropylamine
  • Method for producing isopropylamine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] This example is used to illustrate that acetone, diisopropylamine, and isopropanol are converted into isopropylamine at different reaction temperatures.

[0032] In the laboratory, a fixed-bed reactor was used, and the isopropylamine catalyst produced by Beijing Research Institute of Chemical Industry was used, and the filling volume was 50 ml to carry out the gas phase reaction.

[0033] Experiment 1: Use acetone as raw material to carry out hydrogenation reaction to synthesize isopropylamine. The reaction conditions are: the volume space velocity of liquid acetone is 0.5h -1 , the pressure is normal pressure, the reaction temperature is 152°C, and the molar ratio of acetone:hydrogen:ammonia is 1:3:3. The test results are listed in Table 1.

[0034] Test 2: In order to simulate the material in the industrial plant, a mixture of 50 wt% of diisopropylamine and isopropanol is used as a raw material. In the presence of hydrogen, they react with ammonia and convert to isop...

Embodiment 2

[0039] This embodiment is used to explain the hydroamination reaction of the present invention with staged temperature control.

[0040] In order to simulate the segmental temperature control of the reactor in the industrial device, the reactor is divided into two sections in the laboratory, that is, two sections of beds, each section is filled with 50 ml of isopropylamine catalyst produced by Beijing Research Institute of Chemical Industry, and the temperature of the two sections is controlled respectively. Perform a gas phase reaction.

[0041] The feed is a mixture containing 75wt% acetone, 12.5wt% diisopropylamine and 12.5wt% isopropanol, and the liquid volume space velocity of acetone is 0.5h -1 . The reaction temperature of the first section bed is controlled at 152°C, the reaction temperature of the second section bed is controlled at 170°C, and the pressure is normal pressure, (acetone+diisopropylamine+isopropanol): hydrogen: the mol ratio of ammonia is 1:3:3. The c...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a method for producing isopropylamine, which belongs to the technical field of amine. To solve the problem that the prior isopropylamine industrial production device cannot effectively convert diisopropylamine into the isopropylamine, a reactor for an acetone hydroamination reaction performs the sectional control of the reaction temperature, the reaction temperature of a first section positioned at an inlet of the reactor is between 110 and 150 DEG C, and the reaction temperature of a downstream section is 5 to 30 DEG C higher than that of an upstream section which is adjacent to the downstream section. Along with the gradual reduction of the concentration of acetone along a bed, the reaction temperature is improved section by section, which is favorable for converting the diisopropylamine and isopropanol into the isopropylamine, thereby reducing the circulation of the diisopropylamine and the isopropanol, reducing energy consumption, and preventing the diisopropylamine from being gradually accumulated in a system so as not to need operating a diisopropylamine rectification system with difficult operation. The method is simple, feasible and easy to realize,and has considerable industrial application value and economic benefit.

Description

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
31 Mar 2010
Publication
CN101684073A