Production of electroplating-grade nickel aminosulfonate or electroplating-grade cobalt aminosulfonate through ion exchange method

An ion exchange method and a technology of nickel sulfamate, applied in the field of electroplating chemistry, can solve the problems such as the inability to realize continuous production, and achieve the effects of high strength, high content and high yield

Inactive Publication Date: 2016-04-27
江西核工业兴中科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

And this process cannot realize continuous production

Method used

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  • Production of electroplating-grade nickel aminosulfonate or electroplating-grade cobalt aminosulfonate through ion exchange method
  • Production of electroplating-grade nickel aminosulfonate or electroplating-grade cobalt aminosulfonate through ion exchange method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Ion exchange method produces electroplating grade nickel sulfamate, comprises the following steps:

[0045] Step 1: Resin Transformation

[0046] Sodium hydroxide is configured into a solution with a mass concentration of 5%. When the temperature drops below 40 degrees Celsius, the sodium hydroxide solution enters from the upper end of the ion exchange column at a speed of 2 meters per hour, and then the effluent solution is recovered for the following For the first configuration of lye, the amount of resin transformation sodium hydroxide solution is 2 times of resin volume;

[0047] Step Two: Wash

[0048] Use deionized water with a conductivity of less than 10μs / cm to enter from the upper end of the ion exchange column to wash the lye in the ion exchange column, and the washing water is recovered for the preparation of lye;

[0049] Step 3: Ion Exchange

[0050] Pass the nickel salt solution of any concentration through the resin layer that has been transformed at ...

Embodiment 2

[0068] Ion exchange method produces electroplating grade nickel sulfamate, comprises the following steps:

[0069] Step 1: Resin Transformation

[0070] Sodium hydroxide is configured into a solution with a mass concentration of 5%, and when the temperature drops below 40 degrees Celsius, the sodium hydroxide solution enters from the upper end of the ion exchange column at a speed of 4 m / hour and then recovers the effluent solution for the following For the first configuration of lye, the consumption of resin transformation sodium hydroxide solution is 2.5 times of resin volume;

[0071] Step Two: Wash

[0072] Use deionized water with a conductivity of less than 10μs / cm to enter from the upper end of the ion exchange column to wash the lye in the ion exchange column, and the washing water is recovered for the preparation of lye;

[0073] Step Three: Ion Exchange

[0074] Pass the nickel salt solution of any concentration through the transformed resin layer at a flow rate o...

Embodiment 3

[0086] Ion exchange method produces electroplating grade nickel sulfamate, comprises the following steps:

[0087] Step 1: Resin Transformation

[0088] Sodium hydroxide is configured into a solution with a mass concentration of 5%, and when the temperature drops below 40 degrees Celsius, the sodium hydroxide solution enters from the upper end of the ion exchange column at a speed of 5 m / hour and then recovers the effluent solution for the following For the second configuration of lye, the amount of resin transformation sodium hydroxide solution is 3 times of resin volume;

[0089] Step Two: Wash

[0090] Use deionized water with a conductivity of less than 10μs / cm to enter from the upper end of the ion exchange column to wash the lye in the ion exchange column, and the washing water is recovered for the preparation of lye;

[0091] Step Three: Ion Exchange

[0092] Pass the nickel salt solution of any concentration through the resin layer that has been transformed at a flo...

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PUM

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Abstract

The invention discloses production of nickel aminosulfonate or cobalt aminosulfonate through an ion exchange method; the production of nickel aminosulfonate or cobalt aminosulfonate through the ion exchange method relates to ion exchange resin, an ion exchange column, amino sulfonic acid, a pure alkali solution and deionized water. The production comprises the production steps of ion exchange resin transformation, adsorption, elution and the like. The implementation scheme having the advantages of simple process route, low cost and continuous production is provided for production of nickel aminosulfonate or cobalt aminosulfonate.

Description

technical field [0001] The invention relates to the production of electroplating-grade nickel sulfamate or electroplating-grade cobalt sulfamate by an ion exchange method, belonging to the field of electroplating chemistry. Background technique [0002] Nickel sulfamate and cobalt sulfamate are important electroplating main salt and catalyst raw materials. Widely used in electroplating industry and electroforming industry. Its existing production process includes: 1. Nickel (cobalt) salt is prepared into basic carbonate and then reacted with sulfamic acid to generate nickel (cobalt) sulfamate. The process includes complex unit operations such as synthesis, filtration, and washing. It is cumbersome and the process is complicated. 2. Metal and sulfamic acid generate nickel (cobalt) sulfamate under the action of catalyst. The catalyst used in its production is an oxidant, which cannot be completely removed, and can passivate the anode if the oxidant is used in excess for ele...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B21/096B01J47/02B01J47/14
CPCC01B21/096B01J47/02B01J47/14
Inventor 杜兴胜汤森进曾昭崐蒋良华于金刚龙长江陈小娟叶为辉蒲玲
Owner 江西核工业兴中科技有限公司
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