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Citric acid continuous cooling crystallization system and method thereof

A technology of cooling crystallization and citric acid, which is applied in the directions of heat exchange cooling crystallization, crystallization separation, solution crystallization, etc., can solve the problems of uneven particle size distribution of citric acid monohydrate crystal products, increased equipment and manual operations, and impact on product production costs. , to ensure continuity and stability, shorten cooling time, and improve the quality of crystal products

Inactive Publication Date: 2016-07-27
西安航天华威化工生物工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The crystallization kettle has a fast heat transfer on the wall and coil, which is easy to cause fouling and affect the heat transfer; the fouling needs to be cleaned after batch production, which reduces production efficiency
[0004] With the continuous expansion of industrialization scale, the equipment and manual operation required for the batch crystallization process of citric acid monohydrate are greatly increased. Due to the influence of unstable factors in manual operation, it is easy to cause uneven particle size distribution of citric acid monohydrate crystal products and crystal product aggregation. Serious knots and large batch-to-batch differences lead to increased difficulty in subsequent process separation, washing, and drying, which in turn affects the production cost of the final product

Method used

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  • Citric acid continuous cooling crystallization system and method thereof
  • Citric acid continuous cooling crystallization system and method thereof
  • Citric acid continuous cooling crystallization system and method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0064] This embodiment is used to illustrate the citric acid monohydrate crystal provided by the present invention and its production method.

[0065] The citric acid solution is heated and concentrated to 55°C through two-effect heat exchange, and the acidity of citric acid is 98g / 100ml, and then the citric acid concentrate is transported to the continuous cooling crystallization system for cooling and crystallization, and the temperature difference between the citric acid concentrate and the cooling medium is kept at 5°C, the circulation rate is 60 times the feed amount, maintain the temperature of the citric acid feed liquid in the crystallizer at 10°C, and keep the solid content of the citric acid crystal slurry in the crystallizer at 15%, circulate and cool in the crystallizer for 4 hours and pass through the outlet The material is discharged from the feed port, and the monohydrate citric acid crystal slurry is transported to the centrifuge for solid-liquid separation to o...

Embodiment 2

[0067] This embodiment is used to illustrate the citric acid monohydrate crystal provided by the present invention and its production method.

[0068] The citric acid solution is heated and concentrated to 60°C through two-effect heat exchange, and the acidity of citric acid is 105g / 100ml, and then the citric acid concentrate is transported to the continuous cooling crystallization system for cooling and crystallization, and the temperature difference between the citric acid concentrate and the cooling medium is kept at 8°C, the circulation rate is 100 times of the feed amount, maintain the temperature of the citric acid feed liquid in the crystallizer at 12°C, and keep the solid content of the citric acid crystal slurry in the crystallizer at 20%, circulate and cool in the crystallizer for 8 hours and pass through the outlet The material is discharged from the feed port. After the discharge, the monohydrate citric acid crystal slurry is transported to the centrifuge for solid-...

Embodiment 3

[0070] This embodiment is used to illustrate the citric acid monohydrate crystal provided by the present invention and its production method.

[0071] The citric acid solution is heated and concentrated to 65°C through two-effect heat exchange, and the acidity of citric acid is 109g / 100ml, and then the citric acid concentrate is transported to the continuous cooling crystallization system for cooling and crystallization, and the temperature difference between the citric acid concentrate and the cooling medium is maintained at 10°C, the circulation rate is 80 times the feed amount, maintain the temperature of the citric acid feed liquid in the crystallizer at 17°C, and keep the solid content of the citric acid crystal slurry in the crystallizer at 25%, circulate and cool in the crystallizer for 8 hours and then pass through the outlet The material is discharged from the feed port. After the discharge, the monohydrate citric acid crystal slurry is transported to the centrifuge fo...

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Abstract

The invention relates to a citric acid continuous cooling crystallization system and a method thereof. In an existing method of producing citric acid monohydrate crystal, intermittent processing equipment is used, product size distribution is uneven, a crystal product is agglutinated seriously, and difference between product batches is large. According to the crystallization method, a citric acid solution is heated and concentrated through two-effect heat exchange, then is input into a circulating pipeline composed of an indirect cooler and a cooling crystallizer through a feed pump and is continuously cooled for cooling crystallization in the circulating pipeline under the action of a circulating pump, and citric acid monohydrate slurry is obtained through cooling crystallization; the citric acid monohydrate slurry is discharged through a discharging pump, conveyed to a crystal slurry buffering tank to be buffered and then input into a centrifugal separation device for solid-liquid separation. According to the continuous cooling crystallization method, intermittent crystallization operation of using a crystallization kettle for feeding and discharging and conducting cooling in the kettle in the past is replaced, the feeding, discharging and cooling flow path is stabilized, continuity and stability of product quality can be effectively ensured, and production efficiency and product quality of citric acid monohydrate are greatly improved.

Description

technical field [0001] The invention belongs to the technical field of citric acid crystallization production, and in particular relates to a citric acid continuous cooling crystallization system and a method thereof. Background technique [0002] Citric acid has a mild and refreshing sour taste. It is widely used in the manufacture of various beverages, soft drinks, wine, candies, snacks, biscuits, canned juices, dairy products and other foods. It can also be used in chemical and textile industries, environmental protection, cosmetics and pharmaceutical industries. . [0003] At present, the main operation mode of producing citric acid monohydrate is intermittent cooling and crystallization, which specifically includes: heating and concentrating the purified citric acid solution, and then pouring the concentrated citric acid solution into multiple batch crystallization kettles respectively. The crystallization kettles are equipped with stirring, external jacket and In the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D9/02C07C51/43C07C59/265
CPCB01D9/0013B01D9/0059B01D2009/0086C07C51/43C07C59/265
Inventor 郭坤杜宏德刘胜梁恺张志上官菲菲张洪娇王辉
Owner 西安航天华威化工生物工程有限公司
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