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Calcium gluconate continuous crystallization system and process

A calcium gluconate, crystallization technology, applied in solution crystallization, sustainable manufacturing/processing, chemical industry, etc., can solve the problem of unclear description of continuous cooling crystallization system and process, large surface area of ​​surface cooler, low labor productivity, etc. problem, to avoid the phenomenon of inner wall structure, high energy utilization rate, and good energy saving effect.

Pending Publication Date: 2019-06-18
ENERGY RES INST OF SHANDONG ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The evaporation, concentration and crystallization link in the refining process is directly related to the production cost and product quality of the product. At present, the static crystallization process after rapid cooling in calcium gluconate crystallization accounts for more than 95% of the domestic calcium gluconate industry, which has high energy consumption and accounts for Large area, low degree of automation, low labor productivity and other problems, more importantly, uneven crystal size and difficult dehydration, which seriously affect the quality of the product
[0005] In the patent CN201810245150.7, a continuous cooling and rapid crystallization method of calcium gluconate is disclosed, which mainly includes the steps of dissolution, oxidation, concentration, filtration, decolorization, kinematic crystallization, and drying. This invention improves the preparation method of calcium gluconate Detailed description, but the description of the continuous cooling crystallization system and process is not clear
[0006] In the patent 201410543277.9, a vacuum flash cooling continuous crystallization device is disclosed. The main equipment used in this invention is a self-evaporator and a three-stage vacuum flash crystallizer for cooling and continuous crystallization. The self-evaporator needs to be connected to a cooling system and a surface cooler It occupies a large area and has low cooling efficiency. The system has disadvantages such as complex system and huge equipment.

Method used

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  • Calcium gluconate continuous crystallization system and process
  • Calcium gluconate continuous crystallization system and process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Such as figure 1 As shown, a calcium gluconate continuous crystallization system MVR evaporator ①, three-stage vacuum flash crystallizer ③, ⑥, ⑨, steam jet vacuum pump ④, ⑦, ⑩, mixing condenser, heat exchanger, slurry tank Centrifuges, granulators, dryers. Among them, the MVR evaporator ① is connected to the three-stage vacuum flash crystallizer ③, ⑥, ⑨ in sequence, and the lower part of each vacuum flash crystallizer ③, ⑥, ⑨ is connected to the forced circulation pump ②, ⑤, ⑧, and the upper part is connected to the steam jet vacuum pump. ④, ⑦, ⑩, the steam jet vacuum pump ④, ⑦, ⑩ are connected to the mixing condenser, the third-stage vacuum flash crystallizer ⑨ is connected to the centrifuge, and the centrifuge is connected to the granulator and the dryer in sequence.

[0058] Wherein, the specific structure of the vacuum flash crystallizer includes: an evaporation chamber 1 and a crystallization chamber 2, the evaporation chamber 1 is located above the crystallizati...

Embodiment 2

[0068] A concrete structure of a vacuum flash crystallizer for continuous crystallization of calcium gluconate comprises: an evaporation chamber 1 and a crystallization chamber 2, the evaporation chamber 1 is positioned above the crystallization chamber 2, and the evaporation chamber 1 top is provided with a shower device 3 and a second crystallization chamber. An exhaust port 5; the evaporation chamber 1 is a straight cylinder, and the crystallization chamber 2 is a conical structure; A feed port 7 and a discharge port 8; the bottom of the crystallization chamber is also provided with a vent 9, the bottom of the crystallization chamber 2 is connected with the forced circulation pump 4, and the top of the evaporation chamber 2 is connected with the steam jet vacuum pump ④,⑦ , ⑩ connected.

[0069] The operation method of the above-mentioned device is:

[0070] The supernatant of calcium gluconate is transported through the MVR evaporator ① to the multi-stage vacuum flash crys...

Embodiment 3

[0073] A concrete structure of a vacuum flash crystallizer for continuous crystallization of calcium gluconate comprises: an evaporation chamber 1 and a crystallization chamber 2, the evaporation chamber 1 is positioned above the crystallization chamber 2, and the evaporation chamber 1 top is provided with a shower device 3 and a second crystallization chamber. An exhaust port 5; the evaporation chamber 1 is a straight cylinder, and the crystallization chamber 2 is a conical structure; A feed port 7 and a discharge port 8; the bottom of the crystallization chamber is also provided with a vent 9, the bottom of the crystallization chamber 2 is connected with the forced circulation pump 4, and the top of the evaporation chamber 2 is connected with the steam jet vacuum pump ④,⑦ , ⑩ connected.

[0074] A support pipe 11 is provided between the inner circulation guide tube 10 and the crystallization chamber 2, which is a steel structure, and the inner circulation guide tube 10 is fi...

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Abstract

The invention relates to a calcium gluconate continuous crystallization system and process. The system comprises an MVR evaporator, a three-stage vacuum flash crystallizer, a steam jet vacuum pump, amixing condenser, a heat exchanger, a pulp tank, a centrifuge, a granulator and a drying machine. The process includes steps: feeding calcium gluconate supernatant into the MVR evaporator, concentrating until the material concentration reaches 50-52%, feeding into the multi-stage vacuum flash crystallizer for flash continuous cooling crystallization, allowing crystal paste to enter the slurry tankafter crystallization, centrifuging in the centrifuge to obtain a crystal material, cleaning impurities with pure water, granulating in the granulator, and drying through a boiling bed to obtain a finished product of calcium gluconate. The defect of intermittent crystallization is completely overcome, continuity in production and crystallization of calcium gluconate is realized, compact equipmentstructure and small floor area are realized, energy consumption and production cost are sharply reduced, operating efficiency is improved, and energy is saved by 40-50%. In addition, crystal particleforce uniformity, surface smoothness and product quality stability are realized.

Description

technical field [0001] The invention relates to the field of calcium gluconate crystallization, in particular to a vacuum flash cooling continuous crystallization system and process for calcium gluconate. Background technique [0002] The information disclosed in this background section is only intended to increase the understanding of the general background of the present invention, and is not necessarily taken as an acknowledgment or any form of suggestion that the information constitutes the prior art already known to those skilled in the art. [0003] Calcium gluconate has important uses in medicine, food, chemical industry, etc., especially in medicine, calcium gluconate helps bone formation, and maintains the normal and excitability of nerves and muscles, and has become the first choice for people to supplement calcium product. The production process of calcium gluconate is mainly composed of three parts: glucose oxidation to gluconic acid, gluconic acid and calcium n...

Claims

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Application Information

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IPC IPC(8): C07C59/105C07C51/41B01D9/02B01J2/16
CPCY02P20/10
Inventor 赵改菊孙荣峰王鲁元员冬玲耿文广
Owner ENERGY RES INST OF SHANDONG ACAD OF SCI