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Production process and production device for electroplating grade potassium pyrophosphate

A technology of potassium pyrophosphate and production equipment, which is applied in the production system and process field of high-quality electroplating grade potassium pyrophosphate, and can solve problems such as low content of potassium pyrophosphate products, poor Hull cell test effect, and excessive foggy area. , achieving excellent test results, excellent Hull cell test results, and avoiding secondary pollution

Active Publication Date: 2016-09-28
湖北省兴发磷化工研究院有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, domestic electroplating grade potassium pyrophosphate basically adopts one-step or two-step production process, and the production site has a lot of dust, and the bulk density of the product after atomization is small, about 0.3g / mL~0.5g / mL, and the dust recovery rate Low, and most of them use clean energy such as natural gas or hydrogen as fuel, which greatly increases the production cost. The content of potassium pyrophosphate product obtained by this production process is relatively low, the content is less than 99%, and the complexation index is relatively small, approximately 2.6mL In the range of ~2.9mL, the effect of the Hull cell test is poor, such as poor brightness of the coating, excessive foggy area, more spots and perforations, etc. The impurities in the product are relatively high, especially metal elements such as sodium calcium magnesium aluminum iron Impurities

Method used

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  • Production process and production device for electroplating grade potassium pyrophosphate
  • Production process and production device for electroplating grade potassium pyrophosphate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] First add 6 tons of 48% potassium hydroxide to the neutralization reactor, add 2.9 tons of 85% phosphoric acid under stirring to react, adjust the pH value of the neutralization solution to 8.7, and pass through the fine filtration equipment. After fine filtration, the slurry temperature Keep it at 80°C, put the storage tank slurry into the evaporation concentration device for concentration, and concentrate to 66wt%; then put the concentrated solution into the continuous crystallization device for continuous crystallization operation, the continuous crystallization feed temperature is controlled at 68°C, and the mass concentration is controlled At 70%, the temperature in the crystallization area is controlled at 35°C. After centrifugation, the filtrate returns to the evaporation and concentration device, and the dipotassium hydrogen phosphate crystal enters the vacuum drying equipment for vacuum drying treatment. The vacuum degree is -0.09MPa, the temperature is 130°C, an...

Embodiment 2

[0017] First add 6 tons of 48% potassium hydroxide to the neutralization reaction kettle, add 2.9 tons of 85% phosphoric acid under stirring to react, adjust the pH value of the neutralization solution to 8.9, and pass the slurry temperature after fine filtration by fine filtration equipment Keep the temperature at 85°C, put the slurry in the storage tank into the evaporation concentration device for concentration, and concentrate it to 67wt%; At 68%, the temperature in the crystallization area is controlled at 32°C. After centrifugation, the filtrate is returned to the evaporation and concentration device, and the dipotassium hydrogen phosphate crystals enter the vacuum drying equipment for vacuum drying. The vacuum degree is -0.10MPa, the temperature is 110°C, and the vacuum After drying, the moisture content of the material is controlled at 3%; the dried material is transported into a dynamic polymerization furnace for polymerization, the polymerization temperature is contro...

Embodiment 3

[0019] First add 6 tons of 48% potassium hydroxide to the neutralization reaction kettle, add 2.9 tons of 85% phosphoric acid under stirring to react, adjust the pH value of the neutralization solution to 9.1, and pass the slurry temperature after fine filtration by fine filtration equipment Keep the temperature at 90°C, put the storage tank slurry into the evaporation concentration device for concentration, and concentrate to 68wt%; then put the concentrated solution into the continuous crystallization device for continuous crystallization operation, the continuous crystallization feed temperature is controlled at 68°C, and the mass concentration is controlled At 71%, the temperature in the crystallization area is controlled at 36°C. After centrifugation, the filtrate is returned to the evaporation and concentration device, and the dipotassium hydrogen phosphate crystal enters the vacuum drying equipment for vacuum drying. The vacuum degree is -0.10MPa, the temperature is 100°C...

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Abstract

The invention discloses a production process for electroplating grade potassium pyrophosphate. The production process comprises the following steps of taking 85 percent phosphoric acid and 48 percent potassium hydroxide as raw materials; performing a neutralization reaction in a neutralization reaction kettle, and controlling the pH value of slurry to be 8.5 to 9.5; filtering the slurry by a fine filter, then feeding the slurry into a slurry storage tank, and keeping the temperature of the slurry in the storage tank to be 70 to 90DEG C; feeding the slurry in the storage tank into an evaporation and concentration device for concentrating; then feeding a concentrated solution into a continuous crystallization device for performing continuous crystallization operation; after centrifugal treatment, returning filtrate to the evaporation and concentration device and enabling a potassium dihydrogen thophosphate crystal to enter vacuum drying equipment for performing vacuum drying treatment; conveying a dried material into an indirect heating dynamic polymerization furnace and polymerizing to form potassium pyrophosphate; cooling, breaking, screening and packaging to obtain a finished product. Compared with electroplating grade potassium pyrophosphate on the market, the electroplating grade potassium pyrophosphate obtained by the invention has the advantages of higher dissolution speed, higher purity, more excellent complexing power and better Hull cell test results.

Description

technical field [0001] The invention belongs to the technical field of electroplating grade potassium pyrophosphate production, and in particular relates to a high-quality electroplating grade potassium pyrophosphate production system and process. Background technique [0002] Potassium pyrophosphate is mainly used in cyanide-free electroplating, replacing sodium cyanide as a complexing agent for electroplating. It is also used as a pretreatment and pyrophosphate plating solution for electroplating. It can also be used as an additive to configure laundry detergent components, metal surface detergents and bottle cleaner components, and various cleaning agents. It can also be used as a clay dispersant in the ceramic industry, a dispersant and buffer for pigments and dyes. In the bleaching and dyeing industry, it is used to remove a small amount of ferric ions in water to improve the quality of bleaching and dyeing. It is used as emulsifier, tissue modifier, chelating agent,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/42
CPCC01B25/425C01P2006/80
Inventor 屈云郑国伟范佳利陈海山孙勋佳龚敏
Owner 湖北省兴发磷化工研究院有限公司
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