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Comprehensive utilization technology of iron ore sintering dust

A technology of iron ore and soot, which is applied in the field of comprehensive utilization of iron ore sintering soot, can solve the problems of lead loss and low extraction rate, and achieve the effects of short processing time, simple process flow and easy operation

Active Publication Date: 2016-06-08
攀枝花火凤凰再生资源回收利用有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above method adopts water leaching to extract raw materials, and the leaching rates of potassium, copper and silver only reach 80-85%, 50-70% and 30-50% respectively, and the extraction rate is low, and part of the lead enters in the form of lead chloride. The leaching solution causes the loss of lead in the leaching slag. At the same time, because the leaching solution contains a large amount of sodium chloride after the purification treatment, due to the enrichment of sodium chloride, only about 70% of high-quality potassium chloride products can be obtained. The remaining products are mixtures of potassium and sodium, and the content of potassium chloride can only reach 60-70%.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] A. Add 1000ml of water, 150g of vanadium industrial mixed salt slag, and 1g of diethanolamine to the beaker. After dissolving and mixing, add 500g of sintering soot at room temperature and 500rpm under stirring conditions at a liquid-solid mass ratio of 2.0:1.0. , and leached for 0.5h, so that the soluble chloride salts such as potassium chloride in the soot ash raw material were dissolved into the liquid phase, and the leaching slag and leaching liquid were obtained through separation; the leaching slag was divided into 2 times with 100 grams of water (50 grams / time) After washing and drying, it weighs 254 grams. Analysis shows that it contains 18.26% of Pb, 1.57% of K, 0.16% of Cu, and 48g / t of Ag. The leaching rates of potassium, copper, and silver are 96.61%, 92.87%, and 91.47%, respectively.

[0036] B. Mix the leaching solution and the washing solution of step A, and add Na 2 11 grams of industrial sodium sulfide with an S content of 60%, reacted for 1.0h, and obt...

Embodiment 2

[0041] A. Add 750ml of water, 150g of vanadium industrial mixed salt slag, 2g of diethanolamine to the beaker, dissolve and mix them, and add 500g of sintering soot at room temperature and 300rpm under stirring conditions at a liquid-solid mass ratio of 1.5:1.0 And leaching for 1.0h, so that the soluble chloride salts such as potassium chloride in the soot ash raw material dissolve into the liquid phase, and the leaching residue and the leaching liquid are obtained through separation; the leaching residue is washed twice (50 grams / time) with 100 grams of water , weighs 264 grams after drying, and analysis shows that it contains Pb17.61%, K1.79%, Cu0.18%, Ag50g / t, and the leaching rates of potassium, copper, and silver are 95.98%, 91.66%, and 90.77%, respectively.

[0042] B. Mix the leaching solution and washing solution of step A, and add Na 2 12 grams of industrial sodium sulfide with an S content of 60%, reacted for 0.5 hours, and obtained copper-silver enriched slag and fi...

Embodiment 3

[0047] A. Add 800ml of water, 160g of vanadium industrial mixed salt slag, and 2g of diethanolamine to the beaker. After dissolving and mixing, according to the liquid-solid mass ratio of 1.6:1.0, add 500g of sintering soot at room temperature and stirring at 300rpm And leaching for 0.75h, so that the soluble chloride salts such as potassium chloride in the soot ash raw material dissolve into the liquid phase, and the leaching residue and the leaching liquid are obtained through separation; the leaching residue is washed twice (50 grams / time) with 100 grams of water , weighs 258 grams after drying, and the analysis shows that it contains Pb17.94%, K1.62%, Cu0.15%, Ag54g / t, and the leaching rates of potassium, copper, and silver are 96.45%, 93.21%, and 90.26%, respectively.

[0048] B. Mix the leaching solution and the washing solution of step A, and add Na 2 11.5 grams of industrial sodium sulfide with an S content of 60%, reacted for 0.75 hours, and obtained copper-silver enr...

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PUM

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Abstract

The invention discloses a comprehensive utilization process of iron ore sintering dust ash. The process comprises the following steps: a, adding vanadium industry mixed salt slag and diethanol amine into water, adding the iron ore sintering dust ash to leach after dissolution and separating to obtain lead slag and a leachate; b, adding sodium sulfide according to the content of copper and silver in the leachate obtained in the step a to react and filtering to obtain copper and silver enriched slag and a filtrate; c, adding sodium perchlorate according to the content of potassium ions in the filtrate obtained in the step b to react and filtering to obtain a potassium perchlorate precipitate and a filtrate; d, washing and drying the potassium perchlorate precipitate to obtain a potassium perchlorate product; e, adding activated carbon and polysilicate aluminum ferrite in the filtrate obtained in the step c to react and filtering to obtain a colorless transparent filtrate; f, evaporating, concentrating and crystallizing the colorless transparent filtrate and carrying out solid and liquid separation to obtain an industrial sodium chloride product. The comprehensive utilization process has the benefits that potassium, copper and silver in the sintering dust can be effectively extracted, the technological process is simple, the operation is safe, and the social and economic benefits are better.

Description

technical field [0001] The invention belongs to the research field of industrial waste utilization in the metallurgical industry, and in particular relates to a comprehensive utilization process of iron ore sintering soot. Background technique [0002] Iron ore powder sintering soot is the industrial waste collected by the dust collection system during the sintering process of iron ore raw materials in iron and steel enterprises. Its main components are: K 2 O20~35%, Na 2 O5~8%, Cl25~35%, Pb8~15%, Cu0.8~1.5%, Fe10~15%, CaO5~8%, Al 2 o 3 0.1~1.0%, MgO0.5~1.2%, SiO 2 3-5%, Ag200-400g / t. [0003] At present, the treatment process of iron ore powder sintering soot is mainly to extract metal elements such as lead and zinc in the slag by volatilization after mixing with blast furnace gas mud, and a large amount of valuable potassium chloride contained in the slag has not been properly recovered. Recycling and utilization; or adding to the blast furnace as a raw material for b...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/02C22B13/00C22B11/00C22B15/00C01B11/18C01D3/04
CPCY02P10/20
Inventor 易德华苏毅郑仁和
Owner 攀枝花火凤凰再生资源回收利用有限责任公司
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