A continuous crystallization system and method for large particle nickel sulfate

A crystallization system, nickel sulfate technology, applied in crystallization separation, separation method, solution crystallization, etc., can solve the problems of unstable product performance index, large product difference, low production efficiency, etc., and achieve good product quality stability, particle size and Uniform, high-quality results

Active Publication Date: 2021-10-01
天津乐科节能科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Not only the production efficiency is very low, but also the operation is complicated and the labor intensity of the workers is high
At the same time, the intermittent operation mode also has the disadvantages of wide particle size distribution range, large product differences between batches, and unstable product performance indicators.
[0005] In recent years, some related companies have also directed their research to the continuous crystallization process of nickel sulfate. For example, the invention patent application CN202110167094.1 recently proposed by Huayou Cobalt Co., Ltd. is the latest patent on the continuous crystallization process of nickel sulfate, which records a continuous method of production The crystallization system and crystallization process of nickel sulfate, which introduces the fine-grain elimination cycle to improve the crystal size to a certain extent, realizes continuous production, but due to the relatively simple system structure, it lacks the recovery ratio of fine crystals in the fine-grain elimination cycle and The adjustment method of cutting particle size, and the relationship between dissolution rate and particle size are not considered, resulting in unsatisfactory effects. The average particle size of the product is only 800 μm, and from its attached Figure 4 According to the particle size distribution curve provided, the distribution curve has a trailing peak around 100 μm, and a certain proportion of fine particles are still mixed in the crystal product

Method used

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  • A continuous crystallization system and method for large particle nickel sulfate
  • A continuous crystallization system and method for large particle nickel sulfate
  • A continuous crystallization system and method for large particle nickel sulfate

Examples

Experimental program
Comparison scheme
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Embodiment 1

[0028]A continuous crystallization system of large-grained nickel sulfate comprises a main crystallizer, a classifier, a cooling unit, a dissolution unit and circulation equipment, the main crystallizer adopts an Oslo graded fluidized bed crystallizer, and the crystal bed area of ​​the main crystallizer is Inverted conical structure, the upper diameter is twice the lower diameter, there are upper and lower sets of overflow circulation outlets on the top and middle upper part of the crystal bed area, and a discharge port is provided at the bottom of the crystal bed area, and the overflow circulation outlet passes through The circulation equipment is connected with the classifier, and the classifier is provided with two outlets, the upper outlet is connected with the inlet of the main crystallizer circulating clear liquid, the corresponding circulation pipeline is provided with a feed port, and is connected with the feed pump, and the lower outlet is connected with the dissolution...

Embodiment 2

[0030] A continuous crystallization system for large particle nickel sulfate, comprising a main crystallizer, a classifier, a cooling unit, a dissolving unit and circulation equipment, the main crystallizer adopts a DTB graded fluidized bed crystallizer, and the crystal bed area of ​​the main crystallizer is Inverted conical structure, the upper diameter is three times the lower diameter, there are two sets of overflow circulation outlets on the top and middle upper part of the crystal bed area, and a discharge port is provided at the bottom of the crystal bed area, and the overflow circulation outlet passes through The circulation equipment is connected with the classifier, and the classifier is provided with two outlets, the upper outlet is connected with the inlet of the main crystallizer circulating clear liquid, the corresponding circulation pipeline is provided with a feed port, and is connected with the feed pump, and the lower outlet is connected with the dissolution uni...

Embodiment 3

[0032] A method for continuous crystallization of large-grain nickel sulfate adopts the continuous crystallization system of large-grain nickel sulfate described in Example 1. The front-end nickel sulfate raw material solution is concentrated to a liquid phase density of 1600kg / m 3 After entering the crystallization system through the feed pipeline, the effective volume of the main crystallizer is 50m 3 , control the rising velocity of the liquid phase in the main crystallizer at 2-4cm / s. The temperature in the main crystallizer is 40°C, the liquid phase temperature in the dissolution tank is set to be 5°C higher than the liquid phase temperature in the main crystallizer, the liquid phase residence time is 300S, and the liquid phase concentration and crystal suspension amount in the dissolution tank are monitored as the main crystallizer The upper and lower sets of overflow circulation outlets of the classifier and the adjustment signals of the upper and lower outlet valves o...

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Abstract

The invention discloses a large-grain nickel sulfate continuous crystallization system and method. The continuous crystallization system includes a main crystallizer, a classifier, a cooling unit, a dissolving unit and circulation equipment. The system reduces the number density of crystals in the main crystallizer by setting a fine-grain elimination cycle, and at the same time, the overflow magma is dissolved by the dissolving unit and returned to the crystal bed of the main crystallizer to provide supersaturation for the secondary growth of the remaining crystals. The nickel sulfate crystal obtained by adopting the continuous crystallization method of the present invention has a large particle size, the average particle size can reach more than 1500 μm, the particle size distribution is uniform, and the diameter distance is less than 0.6. Compared with the traditional batch process, it has high production efficiency, low labor intensity, stable product quality, and unit Advantages of low energy consumption.

Description

technical field [0001] The invention belongs to the technical field of industrial crystallization, and in particular relates to a continuous crystallization system and method of large-grain nickel sulfate. Background technique [0002] Nickel sulfate is an important inorganic salt chemical raw material, which is widely used in electroplating, battery materials, semiconductor materials, catalysts, metal coloring and other fields. Nickel sulfate products mainly exist in the form of hydrates, mainly including nickel sulfate hexahydrate and nickel sulfate heptahydrate. Studies have shown that when the temperature is lower than 31.5°C, the obtained crystal is nickel sulfate heptahydrate, and the nickel sulfate obtained above 53°C is β-type nickel sulfate hexahydrate. The performance of β-type nickel sulfate hexahydrate is unstable, and when the temperature is lower than 53°C, it will undergo crystal transformation to the more stable α-type nickel sulfate hexahydrate. The crysta...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D9/00B01D9/02
CPCB01D9/0031B01D9/0063
Inventor 夏君君于会满彭涛尹海蛟全晓宇唐昊刘莉
Owner 天津乐科节能科技有限公司
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