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Preparation process of calcium stearate

A calcium stearate and preparation process technology, which is applied in the field of calcium stearate preparation process, can solve the problems of long reaction time, environmental pollution, high energy consumption and water consumption, achieve low thermal stability requirements, and shorten reaction time , the effect of small steam consumption

Inactive Publication Date: 2019-01-11
南通诺佰恩化工科技有限公司
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  • Claims
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Problems solved by technology

The reaction conditions of the metathesis method are mild, but there are disadvantages such as poor product quality, high production cost, low production efficiency, high energy consumption and high water consumption, and a large amount of salty wastewater is discharged during the production of calcium stearate by the metathesis method, which has caused great harm to the environment. big pollution
The one-step synthesis of calcium stearate is to directly react calcium oxide or calcium hydroxide with stearic acid under certain conditions to generate calcium stearate. The current domestic one-step synthesis of calcium stearate needs to add a catalyst (hydrogen peroxide or ethanol) , because of ethanol in the drying process, there are potential safety hazards, the reaction time is long (1-3 hours), the product yield is low, and the assembly is high

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Embodiment Construction

[0011] The present invention will be further described below in conjunction with embodiment.

[0012] In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with specific embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, and are not intended to limit the present invention.

[0013] A kind of preparation technology of calcium stearate, comprises the following steps:

[0014] S1: First add 42 parts of water to the reactor, and when heated to 45°C with steam, add 1 part of calcium hydroxide and stir evenly, then add 7 parts of stearic acid and stir evenly;

[0015] S2: After stirring evenly, continue heating with steam until the temperature rises to 75-80°C;

[0016] S3: Through sampling analysis, after the material and water are clearly separated, the reaction ends;

[0017] S4:...

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Abstract

The invention discloses a preparation process of calcium stearate. The method comprises the following steps: S1: firstly adding 42 parts of water to a reaction kettle, heating the material to 45 DEG Cwith steam, adding 1 part of calcium hydroxide, stirring the material uniformly, and then adding 7 parts of stearic acid, and uniformly stirring the material; S2: after stirring evenly, continuouslyheating the material with the steam to the temperature of 75-80 DEG C; S3: after sampling analysis, obviously layering the material and water, and completing the reaction; and S4: separating the product from the raw material, and drying the product to obtain the calcium stearate product. The reaction temperature of the preparation process is low, the temperature is controlled at 75 to 80 DEG C, the steam consumption is small, and the reaction time is short, the normal reaction kettle material is about 800 kg, and the reaction time is about 20 minutes from feeding to ending of the reaction, which greatly shortens the reaction time. The calcium content, free acid and melting point of the calcium stearate obtained by the reaction of the invention can reach the standards of superior products,the reaction yield is high, and the by-product has no other products except water.

Description

technical field [0001] The invention relates to the technical field of calcium stearate processing equipment, in particular to a preparation process of calcium stearate. Background technique [0002] At present, the domestic production methods of calcium stearate mainly include double decomposition method, saponification method, one-step synthesis method and some special synthesis methods. The metathesis method is to take stearic acid as the main raw material, at an appropriate temperature, carry out heating and melting and saponification reaction with sodium hydroxide solution, and the generated sodium stearate and soluble calcium salt carry out metathesis reaction to generate calcium stearate. The metathesis method has mild reaction conditions, but there are disadvantages such as poor product quality, high production cost, low production efficiency, high energy consumption and high water consumption, and a large amount of salty wastewater is discharged during the productio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/41C07C53/126
CPCC07C51/412C07C53/126
Inventor 张亚明张智伟张春林王峰刘国威
Owner 南通诺佰恩化工科技有限公司
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