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Method for producing chromium oxide green with low soluble chromium and zero hexavalent chromium

A technology of chromium oxide green and zero hexavalent chromium, which is applied in the field of metallurgy and chemical industry, can solve the problems of unreachable, unreachable, and reduced product hexavalent chromium, and achieve the effect of broad market prospect and high profit value

Inactive Publication Date: 2021-01-08
GANSU JINSHI CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, it is found in the actual production process that the above-mentioned method can generally treat hexavalent chromium to below 10ppm, and there are still difficulties in further processing to reduce hexavalent chromium, but the biggest problem is that the chromium sulfate generated after the reduction of hexavalent chromium by sulfur in thiourea is Soluble trivalent chromium salt, soluble chromium is still greater than 100ppm, which cannot meet the standard requirements of chromium oxide green products with low soluble chromium
[0004] CN108793252A (public date: 2018.11.13) discloses a method for reducing hexavalent chromium in chromium oxide green, and records a method for reducing hexavalent chromium in the product through thermal decomposition using reducing agents such as ammonium salt, ammonia water, alcohol and aldehyde , which has basically the same principle as CN103253709A, through thermal treatment to achieve the purpose of reducing hexavalent chromium in the product, but can not achieve the effect of completely reducing the soluble chromium in the product to below 20ppm

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Present embodiment provides a kind of chromium oxide green production method of low soluble chromium, zero hexavalent chromium, comprises the steps:

[0022] S1. Put 20 tons of chromic anhydride into a rotary kiln and thermally decompose it at a temperature of 1100° C. to produce about 7.4 tons of chromium oxide green. At this time, the chromium oxide green contains 253 ppm of hexavalent chromium and 386 ppm of soluble chromium;

[0023] S2. Directly mix urea at the end of the rotary kiln at a material temperature of 350°C, and perform thermal treatment for 62 minutes under stirring conditions. Mix 3kg of urea per ton of chromium oxide green, and use 22.2Kg of urea in total for 7.4 tons of chromium oxide green. Sampling and detection after the reaction shows that the chromium oxide green product now contains 48ppm of hexavalent chromium and 102ppm of soluble chromium;

[0024] S3, put 2 tons of chromium oxide green products obtained through heat treatment in step S2 in...

Embodiment 2

[0027] Present embodiment provides a kind of chromium oxide green production method of low soluble chromium, zero hexavalent chromium, comprises the steps:

[0028] S1. Put 20 tons of chromic anhydride into a rotary kiln and thermally decompose it at a temperature of 1100°C to produce about 7.4 tons of chromium oxide green. At this time, the chromium oxide green contains 208ppm of hexavalent chromium and 345ppm of soluble chromium;

[0029] S2. Directly at the end of the rotary kiln, mix urea into the chromium oxide green at a material temperature of 460°C, mix 4.5kg of urea per ton of chromium oxide green, and heat-treat for 85 minutes under stirring conditions; take samples for testing after the reaction, at this time Chromium oxide green products contain 38ppm of hexavalent chromium and 79ppm of soluble chromium;

[0030] S3, put 2 tons of chromium oxide green products obtained through heat treatment in step S2 into 5 m 3 Add 5kg of formaldehyde in the water washing pulpin...

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Abstract

The invention discloses a method for producing chromium oxide green with low soluble chromium and zero hexavalent chromium, which comprises the following steps of S1, producing chromium oxide green byadopting a chromic anhydride thermal decomposition method: directly putting chromic anhydride into a rotary kiln, and performing high-temperature thermal decomposition at the temperature of 1100 DEGC to produce chromium oxide green, S2, conducting thermal treatment: directly mixing urea into the chromium oxide green produced in the step S1 at the material temperature of 350-460 DEG C at the tailof a rotary kiln for reaction, S3, putting the chromium oxide green product treated by the thermal method in the step S2 into a washing slurrying tank, and adding an organic reducing agent and the chromium oxide green product into the washing slurrying tank for mixing reaction, and after the reaction is finished, adding caustic soda until the pH value of the material is 7-7.5, and S4, sequentially filtering, drying and crushing the material finally obtained in the step S3, and producing to obtain the final chromium oxide green product. The hexavalent chromium content of the product produced by the method can be reduced to below 1ppm, the soluble chromium content is reduced to below 20ppm, and the international and domestic low soluble chromium and zero hexavalent chromium chromium chromium oxide green product standards are met.

Description

technical field [0001] The invention relates to the technical field of metallurgy and chemical industry, in particular to a production method of chromium oxide green which is green and environment-friendly and can realize low soluble chromium and zero hexavalent chromium. Background technique [0002] With the increasing awareness of environmental protection in the current society, chromium-based products need to develop green environmental protection products with zero hexavalent chromium and low soluble chromium. The chromium oxide green produced by the traditional chromic anhydride thermal decomposition method puts chromic anhydride into the rotary kiln and thermally decomposes it at a temperature of 1050-1350°C to form chromium trioxide. However, because chromic anhydride itself is a hexavalent chromium salt product, some Complete hexavalent chromium is not decomposed, so the hexavalent chromium produced is generally between 200-1000ppm, and the soluble chromium is highe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G37/02
CPCC01G37/02
Inventor 张忠元陈荣孔红霞朱紫谢希智
Owner GANSU JINSHI CHEM