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Simple production process of feed additive calcium soap

A feed additive and fatty acid calcium technology, which is applied in the production process of fatty acid derivatives, can solve the problems of long construction period, complex equipment, and high infrastructure investment, and achieve the effects of simple operation, reduced material transfer, and reduced investment

Inactive Publication Date: 2005-01-19
安致和
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

To build a large-scale modern calcium stearate production base, not only the construction period is long, but also the infrastructure investment is high and the equipment is complicated

Method used

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  • Simple production process of feed additive calcium soap
  • Simple production process of feed additive calcium soap

Examples

Experimental program
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Effect test

Embodiment 1

[0010] Add 100 kilograms of fatty acids with 16 carbons to 20 carbons in the reactor 1, 600 kilograms of water to start the stirrer, maintain the temperature in the kettle to be 60 ℃ to 80 ℃, add 27 kilograms of sodium hydroxide solution with a concentration of 30%, and solid chlorination After stirring 21 kilograms of calcium for 6 to 10 minutes, slowly add 13 kilograms of sodium hydroxide solution with a concentration of 30%, and then stir for 30 minutes to stop stirring after the reaction is complete, insert the suction filter 2, and suck out the medium water to the negative pressure tank 3, Take out the suction filter 2, add 200 kg of washing water to the reaction kettle and stir for 3 minutes, then insert the suction filter 2 to suck out the washing water, take out the suction filter 2, start stirring to raise the temperature in the reaction 1 to 130℃~150℃ to vaporize the water Reactor mouth escapes, stop stirring, turn on the thick slurry pump 5, spray the molten material...

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Abstract

The invention relates to a simplified process for manufacturing fat acid derivatives which comprises, placing fatty acid and water in autoclave, starting agitating, charging aqueous alkali and solid phase calcium chloride, inserting suction filter to suck off the dielectric water, watering and stirring, water scrubbing, stopping agitation and sucking off wash water, agitating and elevating the temperature to 130-150 deg. C, making the water escape form autoclave mouth, drenching the molten substance into the open end product tower, thus obtaining granule end product on the tower bottom.

Description

(1) Technical field [0001] The invention relates to a production process of fatty acid derivatives (2) Background technology [0002] Calcium stearate was first used in industry as heat stabilizer and lubricant in non-toxic plastic products such as food packaging and medical appliances, waterproofing agent for textiles, thickener for grease and flat finish for paint. In recent years, a large number of researches and practices at home and abroad have proved that calcium fatty acid can also be used as a feed additive for ruminants, which can increase the milk production of cattle and sheep, improve the reproductive capacity of livestock and promote the health of livestock. If the use of fatty acid calcium as a feed additive is widely promoted, the cost of importing products from abroad will be relatively high due to the limited scale of domestic production. To build a large-scale modern calcium stearate production base, not only the construction period is long, but also the i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/41
Inventor 安致和
Owner 安致和
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