CN103255294A - Comprehensive reuse process of ferrochrome smelting slag - Google Patents
Comprehensive reuse process of ferrochrome smelting slag Download PDFInfo
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- CN103255294A CN103255294A CN2013101747440A CN201310174744A CN103255294A CN 103255294 A CN103255294 A CN 103255294A CN 2013101747440 A CN2013101747440 A CN 2013101747440A CN 201310174744 A CN201310174744 A CN 201310174744A CN 103255294 A CN103255294 A CN 103255294A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
The invention discloses a comprehensive reuse process of ferrochrome smelting slag, belonging to the field of comprehensive utilization of metallurgy slag. A chemical method is adopted, an acid-alkali process is additionally adopted, and substances in the slag can be directly extracted to directly produce serial chemical products with high additional value. The treatment process is free of secondary pollution and wastewater, waste gas and waste residue discharge, is clean, environment-friendly and energy-saving. A great deal of slag can be treated, the cost is low, the comprehensive utilization rate is high, recycled products are good in quality, high in value and large in market demand. By utilizing the process, the circulation economic development is greatly prompted.
Description
Technical field
The present invention relates to the comprehensive recycling technology of a kind of ferrochrome smelting slag, belong to the technical field of extracting substance direct production Chemicals from the industry metallurgy waste residue, be particularly suitable for the slag ashes processing that ferrochrome smelting enterprise produces.
Background technology
Original ferrochrome smelting treatment of slag falls as offal treatment basically, has only the enterprise of only a few to be used for cement brick processed.So both occupied ground and land resources also were the significant wastage to resource, were unfavorable for the requirement of green environment development.Existing technology is just carried out processing and utilizing to containing high-titanium blast furnace slag, but has many deficiencies, and utilising efficiency is not high, and practical application is difficult to promote.
Disclosed Chinese invention patent " with the method for the treatment of blast furnace slag with diluted chlorhydric acid ", the patent No.: CN94108086.2, publication number: CN1099424, open day: 1995.03.01, there is following problem in this invention:
1. do not utilize and extract iron protoxide in the slag, thin iron powder.
2. slag contains Fe in the solution behind dissolving with hydrochloric acid
2+, there is not extraction and application, influence other metal ion extraction in the solution.
3. contain Mg in the solution
2+, AI
3+Ion adds hydrochloric acid uncrystallizable separation purification magnesium chloride and aluminum chloride.
Therefore, adopt existing technology to be difficult to the ferrochrome smelting slag is carried out comprehensive recycling.Because it is increasingly extensive that ferrochrome is used, domestic ferrochrome smelting industry is flourish, and the annual slag that produces up to ten million tons can't be handled, and takies a large amount of land resourcess, and environment is caused detrimentally affect.Owing to be rich in multiple metal in the slag, country " 12 " planning explicitly calls for, the ferrous metallurgy waste reside comprehensive utilization, as an important behave of recycling economy development.
Summary of the invention
The objective of the invention is to comprehensive recycling ferrochrome smelting slag, protection environment and resource turn waste into wealth, and promote recycling economy development, create good business economic benefit and social benefit, benefit the nation and the people.
The objective of the invention is to reach by following measure:
The comprehensive recycling technical process of a kind of ferrochrome smelting slag is characterized in that: in the comprehensive recycling process of ferrochrome smelting slag, add alkali and the material in the slag all can be extracted through adding acid, directly make series chemical product, step is as follows:
1. with slag (its composition: FeCr, FeO, Cr
2O
3, AI
2O
3, MgO, SiO
2, CaO) wear into 200 order fine powders, the acid that adds capacity was fully stirred 2-3 hour, and collected hydrogen and obtain hydrogen product, question response adds water fully and makes soluble substance become ion, the metal ion in the mixing solutions is: Cr
3+, Fe
2+, AI
3+, Mg
2+, Ca
2+, throw out is: Cr
2O
3, SiO
2
2. discharge solution filters throw out, wash, and obtains Cr
2O
3, SiO
2, add hydrofluoric acid again, make SiO
2SiF is made in dissolving
4Product, insolubles filtration, washing, drying make Cr
2O
3Product;
3. mixing solutions (Cr
3+, Fe
2+, AI
3+, Mg
2+, Ca
2+) the middle alkali that adds, make Cr
3+, Fe
2+, AI
3+All be precipitated as Cr (OH)
3, Fe (OH)
3, AI (OH)
3, discharge solution (Mg
2+, Ca
2+), throw out to be filtered, washs, drying makes Cr (OH)
3, Fe (OH)
3, AI (OH)
3Mix product;
4. (Mg in the mixing solutions
2+, Ca
2+) adding Na
2SO
4Or MgSO
4, make Ca
2+All be precipitated as CaSO
4, discharge solution, throw out to be filtered, washs, drying makes products C aSO
4
5. add alkali in the mixing solutions, make Mg
2+All be precipitated as Mg (OH)
2, discharge solution, throw out to be filtered, washs, drying makes product Mg (OH)
2, the solution circulated recycling of discharge;
6. will make Cr (OH)
3, Fe (OH)
3, AI (OH)
3Mixture further separate purification, add alkali and make AI (OH)
3Dissolving fully, filtration, washing obtain Cr (OH)
3, Fe (OH)
3Mixture adds acid and makes the AI (OH) that has dissolved in the filtrate
3Become AI (OH) again
3Precipitation is separated out fully, and filtration, washing, drying make product A I (OH)
3
7. with Cr (OH)
3, Fe (OH)
3Add alkali in the mixture and make Cr (OH)
3Dissolving fully, filtration, washing, drying make product F e (OH)
3, add acid in the filtrate and make the Cr (OH) that has dissolved
3Become Cr (OH) again
3Precipitation is separated out fully, and filtration, washing, drying make products C r (OH)
3, with this products C r (OH)
3Make Cr through high-temperature roasting
2O
3The chrome green product;
8. with Cr (OH)
3, Fe (OH)
3Add acid in the mixture and make Cr (OH)
3Dissolving fully, filtration, washing, drying make product F e (OH)
3, the filtrate evaporation drying is made the chromic salt product.
Embodiment
For improving this invention technology, become scientific and technological productive forces.In on 02 15th, 2012 to the slag of ferrochrome smelting enterprise Hunan Province to red iron alloy company limited, divide according to this technical process and to handle for 3 times, average, the result shows:
1. all substances are extracted and produce series chemical product in the slag, and the product that comprehensive utilization ratio 98.5% (wherein 1.5% is ashes) is produced by 1 ton of slag extracting substance of every processing calculates finished product: Cr (OH)
3230kg, Fe (OH)
3310kg, Cr
2O
3190kg, Mg (OH)
2205kg, CaSO
490kg, AI (OH)
3140kg, SiF
4160kg, H
29.8kg, chromic salt 250kg.
2. whole slag treatment flow process non-secondary pollution does not have " three wastes " discharging, environmental protection, energy-conservation, cleaning.
Practice shows that this invention technology has better practicability, meets the requirement of recycling economy development, and good benefits in environment, economic benefit and social benefit are arranged.
Claims (1)
1. comprehensive recycling technical process of ferrochrome smelting slag is characterized in that: in the comprehensive recycling process of ferrochrome smelting slag, add alkali and the material in the slag all can be extracted through adding acid, directly make series chemical product, step is as follows:
(1). with slag (its composition: FeCr, FeO, Cr
2O
3, AI
2O
3, MgO, SiO
2, CaO) wear into 200 order fine powders, the acid that adds capacity was fully stirred 2-3 hour, and collected hydrogen and obtain hydrogen product, question response adds water fully and makes soluble substance become ion, the metal ion in the mixing solutions is: Cr
3+, Fe
2+, AI
3+, Mg
2+, Ca
2+, throw out is: Cr
2O
3, SiO
2
(2). discharge solution, throw out is filtered, washs, obtain Cr
2O
3, SiO
2, add hydrofluoric acid again, make SiO
2SiF is made in dissolving
4Product, insolubles filtration, washing, drying make Cr
2O
3Product;
(3). mixing solutions (Cr
3+, Fe
2+, AI
3+, Mg
2+, Ca
2+) the middle alkali that adds, make Cr
3+, Fe
2+, AI
3+All be precipitated as Cr (OH)
3, Fe (OH)
3, AI (OH)
3, discharge solution (Mg
2+, Ca
2+), throw out to be filtered, washs, drying makes Cr (OH)
3, Fe (OH)
3, AI (OH)
3Mix product;
(4). (Mg in the mixing solutions
2+, Ca
2+) adding Na
2SO
4Or MgSO
4, make Ca
2+All be precipitated as CaSO
4, discharge solution, throw out to be filtered, washs, drying makes products C aSO
4
(5). add alkali in the mixing solutions, make Mg
2+All be precipitated as Mg (OH)
2, discharge solution, throw out to be filtered, washs, drying makes product Mg (OH)
2, the solution circulated recycling of discharge;
(6). will make Cr (OH)
3, Fe (OH)
3, AI (OH)
3Mixture further separate purification, add alkali and make AI (OH)
3Dissolving fully, filtration, washing obtain Cr (OH)
3, Fe (OH)
3Mixture adds acid and makes the AI (OH) that has dissolved in the filtrate
3Become AI (OH) again
3Precipitation is separated out fully, and filtration, washing, drying make product A I (OH)
3
(7). with Cr (OH)
3, Fe (OH)
3Add alkali in the mixture and make Cr (OH)
3Dissolving fully, filtration, washing, drying make product F e (OH)
3, add acid in the filtrate and make the Cr (OH) that has dissolved
3Become Cr (OH) again
3Precipitation is separated out fully, and filtration, washing, drying make products C r (OH)
3, with this products C r (OH)
3Make Cr through high-temperature roasting
2O
3The chrome green product;
(8). with Cr (OH)
3, Fe (OH)
3Add acid in the mixture and make Cr (OH)
3Dissolving fully, filtration, washing, drying make product F e (OH)
3, the filtrate evaporation drying is made the chromic salt product.
Priority Applications (1)
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CN2013101747440A CN103255294A (en) | 2012-05-02 | 2013-04-28 | Comprehensive reuse process of ferrochrome smelting slag |
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CN201210141510.1 | 2012-05-02 | ||
CN2012101415101A CN102676831A (en) | 2012-05-02 | 2012-05-02 | Process for recycling ferrochromium smelting slag comprehensively |
CN2013101747440A CN103255294A (en) | 2012-05-02 | 2013-04-28 | Comprehensive reuse process of ferrochrome smelting slag |
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CN2012101415101A Pending CN102676831A (en) | 2012-05-02 | 2012-05-02 | Process for recycling ferrochromium smelting slag comprehensively |
CN2013101747440A Pending CN103255294A (en) | 2012-05-02 | 2013-04-28 | Comprehensive reuse process of ferrochrome smelting slag |
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Families Citing this family (3)
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CN103506372B (en) * | 2013-09-18 | 2015-05-20 | 薛彦辉 | Coal-fired furnace slag processing method |
CN106145033A (en) * | 2015-04-08 | 2016-11-23 | 唐翔 | Cr VI technique is removed in chemical chromium slag and metallurgical slag comprehensive utilization |
CN110028039A (en) * | 2019-03-01 | 2019-07-19 | 光钰科技股份有限公司 | Method for treating industrial waste acid |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN85105628A (en) * | 1985-07-06 | 1987-01-14 | 莫玉裔 | The nontoxic processing extraction Ca. and Mg of chromium slag reduction method |
CN1038771A (en) * | 1989-07-05 | 1990-01-17 | 广州市东山区珠峰新技术开发研究所 | The eliminating poison of chromium cinder comprehensive use |
CN1063232A (en) * | 1991-11-21 | 1992-08-05 | 邓绍齐 | Countercurrent circulation sectional leaching separation method for comprehensive utilization of chromium slag |
ZA915484B (en) * | 1990-01-24 | 1993-03-31 | Mintek And Samancor Ltd | The production of chromium hydroxide/basic chromium sulphate and conversion thereof to chromium metal or chromic acid |
CN101380510A (en) * | 2008-10-30 | 2009-03-11 | 杨恩清 | Chromic slag wet method detoxifcation and resource comprehensive utilization new technique |
-
2012
- 2012-05-02 CN CN2012101415101A patent/CN102676831A/en active Pending
-
2013
- 2013-04-28 CN CN2013101747440A patent/CN103255294A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN85105628A (en) * | 1985-07-06 | 1987-01-14 | 莫玉裔 | The nontoxic processing extraction Ca. and Mg of chromium slag reduction method |
CN1038771A (en) * | 1989-07-05 | 1990-01-17 | 广州市东山区珠峰新技术开发研究所 | The eliminating poison of chromium cinder comprehensive use |
ZA915484B (en) * | 1990-01-24 | 1993-03-31 | Mintek And Samancor Ltd | The production of chromium hydroxide/basic chromium sulphate and conversion thereof to chromium metal or chromic acid |
CN1063232A (en) * | 1991-11-21 | 1992-08-05 | 邓绍齐 | Countercurrent circulation sectional leaching separation method for comprehensive utilization of chromium slag |
CN101380510A (en) * | 2008-10-30 | 2009-03-11 | 杨恩清 | Chromic slag wet method detoxifcation and resource comprehensive utilization new technique |
Non-Patent Citations (3)
Title |
---|
包新华等: "《无机化学试验》", 30 September 2010, 上海大学出版社, article "《无机化学试验》", pages: 228-230 * |
汤淳东: "关于Al、Cr及Al(OH)3 、Cr(OH)3两性的分析", 《南通职大教学研究》, 15 December 1994 (1994-12-15) * |
裘家奎: "《无机定性分析》", 30 June 1937, 中外图书公司, article "《无机定性分析》", pages: 130-132 * |
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Application publication date: 20130821 |