Method for preparing rare earth dilaurate

A technology of lauric acid and rare earth, applied in the preparation of carboxylate, organic chemistry and other directions, can solve the problems of high drying energy consumption, high consumption, low production efficiency, etc., achieve mild reaction conditions, improve reaction yield, and product color and luster excellent effect

Inactive Publication Date: 2009-04-29
扬州科宇化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] (1) Since the saponification metathesis reaction must be carried out at a slow speed under the condition of a relatively dilute reaction slurry, this leads to the disadvantages of large container equipment, low production efficiency, high energy consumption and water consumption in the metathesis process
[0004] (2) Due to the liquid-solid ratio of the reaction material with high reaction requirements, a large amount of water needs to be consumed for washing. Therefore, the metathesis process discharges a large amount of salty and organic waste water, which will pollute the environment and cause adverse effects. people's attention
[0005] (3) Saponification-lanthanum chloride double decomposition reaction has high water content in the filter cake and high energy consumption for drying

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] Inject 75L of water whose temperature is lower than the melting point of dilauric acid into a 100L normal-pressure reactor, start stirring, add 15kg of dilauric acid and 2.7kg of lanthanum hydroxide, heat up to 50°C and react at a constant temperature for 190min, and dry the reaction product with a centrifuge , After the filter cake is dispersed, it is dried according to the usual drying method and conditions to obtain the rare earth dilauric acid product.

Embodiment 2

[0016] Inject 80L of water whose temperature is lower than the melting point of dilauric acid into a 100L normal-pressure reactor, start stirring, put in 10kg of dilauric acid and 1.8kg of lanthanum hydroxide, heat up to 85°C and react at a constant temperature for 150min. The reaction product is dried by a centrifuge, and the filter cake is dispersed and dried according to the usual drying method and conditions to obtain the dilauric acid rare earth product.

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Abstract

The invention relates to a preparation method of dilaurate rare earth, belonging to the technical field of chemical synthesis. Under normal pressure, dilaurate, lanthanum hydroxide and medium water are stirred and mixed below the melting point of dilaurate; then the mixture is heated above the melting point of dilaurate for reaction; the product is dehydrated, dispersed and dried, and dilaurate rare earth is obtained; and the medium water can be recycled to avoid waste water discharge. The preparation method has the advantages of high productivity and obvious reduction of energy consumption and water consumption.

Description

technical field [0001] The invention relates to a preparation method of rare earth dilaurate, which belongs to the technical field of chemical synthesis. Background technique [0002] Rare earth dilaurate can be used as plastic stabilizer, lubricant, halogen absorber, cosmetic additive, etc. However, the current method for preparing rare earth dilauric acid is saponification of dilauric acid-lanthanum chloride double decomposition method. However, the double decomposition method has the following disadvantages: [0003] (1) Since the saponification metathesis reaction must be carried out at a slow rate under a relatively dilute reaction slurry condition, this leads to the disadvantages of large container equipment, low production efficiency, and high energy and water consumption in the metathesis process. [0004] (2) Due to the liquid-solid ratio of the reaction material with high reaction requirements, a large amount of water needs to be consumed for washing. Therefore, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C53/126C07C51/41
Inventor 王大年
Owner 扬州科宇化工有限公司
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