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Evaporative crystallization system for continuously producing low-density crystal substances from mixed solution and process thereof

An evaporative crystallization, low-density technology, applied in solution crystallization, general layout of crystallization device, separation/purification of carboxylic acid compounds, etc., can solve problems such as poor product quality stability, difficult product specification control, product coalescence, etc. Achieve the effect of reducing labor intensity, facilitating production management, and stabilizing the crystallization process

Pending Publication Date: 2018-12-07
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

[0003] The batch crystallization process is suitable for small-scale production, and its characteristics are: the crystallization process is relatively simple, and the investment cost is relatively low, but the batch gap in the batch crystallization process is large, and it is difficult to realize automatic control, resulting in poor product quality stability and difficult control of product specifications ;With the continuous expansion of industrialization scale, the required process equipment and manual operation costs are greatly increased, and due to the influence of manual operation instability factors, the purity of crystal products is unstable, and the product coalescence is serious, which affects the quality and production cost of the final product

Method used

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  • Evaporative crystallization system for continuously producing low-density crystal substances from mixed solution and process thereof
  • Evaporative crystallization system for continuously producing low-density crystal substances from mixed solution and process thereof
  • Evaporative crystallization system for continuously producing low-density crystal substances from mixed solution and process thereof

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Effect test

Embodiment 1

[0051] This embodiment is used to illustrate the calcium propionate crystal provided by the present invention and its production method.

[0052]The calcium propionate raw material liquid is transported to the circulation pipeline of the evaporative crystallization system through the feed pipeline, and after being flashed and concentrated in the separation chamber of the heat exchange device 1 and the crystallization device 2-Oslo evaporative crystallizer, it enters the Oslo evaporation through the central downcomer The crystallization chamber of the crystallizer carries out crystal growth, and the liquid level in the crystallizer is controlled to be 30 cm lower than the feed port of the separation chamber, and the circulation amount of the crystallization process is controlled by the circulation device 3 to be 200 times of the feed amount, and the vacuum device 5 pipeline valve is adjusted The vacuum degree in the crystallizer is controlled by the opening degree to 20kPa, and ...

Embodiment 2

[0054] This embodiment is used to illustrate the calcium propionate crystal provided by the present invention and its production method.

[0055] The calcium propionate raw material liquid is transported to the circulation pipeline of the evaporative crystallization device through the feed pipeline, and after being flashed and concentrated in the separation chamber of the heat exchange device 1 and the crystallization device 2-DTB type evaporative crystallizer, it enters the DTB type evaporative crystallizer through the draft tube. The crystallization chamber of the evaporative crystallizer carries out crystal growth, and the liquid level in the crystallizer is controlled to be 10cm lower than the feed port of the separation chamber, and the circulation amount of the crystallization process is controlled to be 80 times of the feed amount through the circulation device 3, and the DTB type evaporative crystallizer is controlled The stirring rate is controlled by adjusting the val...

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Abstract

The invention relates to an evaporative crystallization system for continuously producing low-density crystal substances from a mixed solution and a process thereof. The evaporative crystallization system comprises a heat exchange unit, a crystallization apparatus and a circulating device, wherein the output end of the heat exchange unit is connected with the input end of the crystallization apparatus; the output end of the crystallization apparatus is connected with the input end of the heat exchange unit by virtue of the circulating device; the heat exchange unit and the crystallization apparatus are connected with a condensing unit and further connected with a vacuum unit; the crystallization apparatus is connected with a centrifugal device; and the filtrate output end of the centrifugal device is connected with the heat exchange unit. According to the evaporative crystallization system for continuously producing low-density crystal substances disclosed by the invention, the batch production manner of batch crystal kettle feeding, evaporating and discharging is replaced, the feeding and discharging balance is effectively controlled, the crystallization process is stable, the product quality is effectively ensured, the manual labor intensity is greatly reduced, and convenience is brought to production and management.

Description

technical field [0001] The invention belongs to the field of evaporative crystallization and food additives, and in particular relates to an evaporative crystallization system and a process for continuously producing low-density crystallization systems from mixed liquids. Background technique [0002] Crystallization is the process in which solid substances are precipitated from steam, solution or melt in the form of crystals. Many chemical industrial processes include crystallization as a basic unit operation. At present, the crystallization of low-density crystalline substances such as calcium propionate mostly adopts the batch crystallization method. During operation, firstly, the prepared material is transported to the crystallization kettle at one time through the feed pump, and the heating medium feed valve is opened to allow the heating medium to enter the jacket or inner coil; heat is exchanged through the outer jacket of the crystallization kettle or the inner coil ...

Claims

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Application Information

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IPC IPC(8): B01D9/02B01D1/30B01D1/00C07C51/43C07C53/122
CPCB01D1/00B01D1/0082B01D1/30B01D9/0022B01D9/0031B01D9/0059B01D9/0063C07C51/43B01D2009/0086C07C53/122
Inventor 刘胜郭坤曹芳利房晓玲上官菲菲张志王运芬
Owner 西安航天华威化工生物工程有限公司
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