Technique for producing magnesium stearate by dry method and device
A technology of magnesium stearate and stearic acid, applied in carboxylate preparation, chemical/physical/physicochemical stationary reactors, organic chemistry, etc., can solve high production cost, long production cycle, high labor intensity, etc. Problems, to achieve the effect of low production efficiency, high storage and transportation costs, and large drying energy consumption
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0033] Embodiment 1: Reaction raw material: 40 kilograms of magnesium hydroxide, 310 kilograms of stearic acid, 12 kilograms of deionized water.
[0034] Put the stearic acid into the reaction vessel 4 through the feeding port 6, heat and stir for about 10 minutes, after the temperature rises to 50°C, put the magnesium hydroxide into it, and after fully stirring, pour 12kg of deionized water from the feeding port, and pass the gas The inlet and outlet pipeline port 7 is continuously fed with nitrogen, and the air in the reactor 4 is discharged from the top feed port 6. After gradually replacing the air in the reactor 4 with nitrogen, the valves of the feed port 6 and the gas inlet and outlet pipe port 7 are tightly closed. While stirring, gradually heat the reaction mass to between 80°C and 120°C. Keep the vapor pressure formed by the deionized water and the reaction water in the reactor 4 between 0 and 0.1 MPa. After reacting for about two hours, open the valve of the gas in...
Embodiment 2
[0035] Embodiment 2: Reaction raw materials: 28 kilograms of magnesium oxide, 200 kilograms of stearic acid, 14 kilograms of deionized water.
[0036] First, magnesium oxide is put into the reaction vessel 4 through the feeding port 6, stirred and added with deionized water, after the magnesium oxide and water are completely mixed, stearic acid is put into it, and nitrogen gas is constantly fed through the gas inlet and outlet pipe port 7, and the reaction vessel 4 The air is discharged from the top feeding port 6, and after gradually replacing the air in the reaction vessel 4 with nitrogen, close the feeding port 6 and the gas inlet and outlet pipe port 7 valves. While stirring, gradually heat the reaction mass to between 80°C and 120°C. Keep the vapor pressure formed by the deionized water and the reaction water in the reactor 4 between 0-0.1 MPa. After reacting for about two hours, open the valve of the gas inlet and outlet pipeline 7, and discharge the nitrogen, deionized...
Embodiment 3
[0039] Embodiment 3: as figure 1 , 2 As shown, the reaction device includes a reaction vessel 4, a feeding port 6 and a jacket 8, the motor 1 is connected with the speed reducer 2, the speed reducer 2 is connected with the gear transmission 3, and the gear transmission 3 is connected with the agitator 9 installed in the reaction vessel 4 , the stirrer 9 is 2, and reverse shear rotation, variable frequency speed regulation; The reaction vessel 4 is a pressure vessel, the top of the reaction vessel 4 is provided with a feeding port 6, a gas inlet and outlet pipe port 7 and a temperature measuring port 5, the reaction vessel A jacket 8 is set outside 4, a discharge port 10 is set under the reaction vessel 4, and a steam and cooling water inlet 11 and a steam and cooling water outlet 12 are set on the side of the jacket 8, which can be heated or cooled by steam or cooling water.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 