CN101250632A - Method for smelting low carbon manganese-silicon using artificialness Mn3O4 in sublimation electric furnace - Google Patents
Method for smelting low carbon manganese-silicon using artificialness Mn3O4 in sublimation electric furnace Download PDFInfo
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- CN101250632A CN101250632A CNA2008100735178A CN200810073517A CN101250632A CN 101250632 A CN101250632 A CN 101250632A CN A2008100735178 A CNA2008100735178 A CN A2008100735178A CN 200810073517 A CN200810073517 A CN 200810073517A CN 101250632 A CN101250632 A CN 101250632A
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Abstract
The invention relates to a method for producing low-carbon manganese-silicon alloy through utilizing silicoferrite or crystal silicon as reducing agent and deacidizing Mn3O4 in a refining electric furnace. The method comprises the following steps: firstly, preparing Mn3O4, mixing manganese oxide ore and liquid phase reducing agent such as molasses (waste honey water), leaching out with spirit of sulphur, adding alkali to precipitate, cleaning, and preparing Mn3O4, secondly, breaking silicon iron into grain size which is less than or equal to 20mm, breaking quicklime pile which contains CaO>=85% into grain size which is 8-50mm, pelletizing Mn3O4 which is prepared through the step one, and drying, thirdly, melting slag and refining, smelting furnace burden of low-carbon manganese-silicon alloy, preparing according to the proposition requirement for producing low-carbon manganese-silicon alloy which contains Mn, mixing material, feeding material, refining, tapping, sedating, removing slag, and casting. Since the method utilizes artificial Mn3O4 and silicon iron, the carbon containing content of manganese-silicon alloy which is smelted is only 0.27-0.3, and the requirement of low-carbon manganese iron whose carbon containing amount is less than 0.4% can be satisfied. And the method has low production cost and stable product quality.
Description
One, technical field
The present invention relates to smelting low carbon manganese-silicon technical field, particularly use artificial Mn
3O
4The method of smelting low carbon manganese-silicon in electric refining furnaces.
Two, background technology
Traditional manganese-silicon production technology will be used rich manganese slag and the rich manganese ore of low-phosphorous low iron, the smelting process technology maturation, but present domestic manganese resource has been difficult to satisfy the rich manganese slag of high manganese.Adopt manganese salt method to produce Mn
3O
4It is present research direction.Synthesize Mn
3O
4, at first to process manganese oxide ore, ripe treatment process has two kinds at present, and first reduction roasting method is MnO
2Be reduced into MnO, use then the method for sulfuric acid leaching.This method energy consumption height, environmental pollution is big; Another kind method is wet method, and wherein using more is so-called " two ore deposit methods ", and is namely mutually mixed manganese ore and troilite, uses then sulfuric acid leaching, utilizes FeS in the troilite to reduce MnO
2Generate MnSO
3Vitriolization again.This method Separation of Solid and Liquid is difficulty, has also brought in addition the objectionable impurities such as S, As a large amount of in the troilite into, increases to purify difficulty.
Smelting the production manganese-silicon with electro carbothermic process in mineral hot furnace, is that utilization raising Si content reduces the C content in the alloy.Owing to use mineral hot furnace, produce the power consumption height, it is big to produce exhausted air quantity, and water consumption is big, and product phosphorus content height is difficult to satisfy the production phosphorus content less than the requirement of 1.0% medium-low carbon ferromanganese low-carbon high strength steel to manganese-silicon.
Refining furnace be smelt medium-low carbon ferromanganese or in the special-purpose type of furnace of humble carbon ferrochrome, in electric refining furnaces with manganese-silicon or silicochromium adopt traditional electro silicothermic process produce medium-low carbon ferromanganese or in humble carbon ferrochrome technology very ripe.In recent ten years because the development that " Bo Lunfa " and heat are converted refining techniques, utilize the special fusing of refining furnace to contain the manganese molten slag or contain the chromium slag, then slag and manganese-silicon or silicochromium are carried out that ladle-to-ladle heat is converted or shaking ladle heat convert produce medium-low carbon ferromanganese or in the production technology of humble carbon ferrochrome also ripe, but owing to use raw-material limitation, be difficult to produce low-carbon ferromanganese and chromic carbide iron.
Three, summary of the invention
The object of the present invention is to provide a kind of artificial Mn that uses
3O
4The method of smelting low carbon manganese-silicon in electric refining furnaces, it has overcome traditional reduction roasting method and has prepared Mn
3O
4The energy consumption height, environmental pollution is big; The wet method Separation of Solid and Liquid is difficulty, brings objectionable impurities into, increases the shortcoming that purifies difficulty.Smelt carbon manganese-silicon carbon content only be 0.27～0.3, can satisfy the requirement of carbon content less than 0.4% low carbon ferromanganese.
The present invention achieves the above object by the following technical programs: use artificial Mn
3O
4The method of smelting low carbon manganese-silicon may further comprise the steps in electric refining furnaces,
(1) preparation Mn
3O
4
Press manganese oxide ore: the liquid-phase reduction agent: sulfuric acid=1: 0.1-0.2: 0.5-0.6 (weight ratio), manganese oxide ore and liquid-phase reduction agent are mixed, use sulfuric acid leaching, the alkaline chemical precipitation deironing is cleaned, and is prepared into Mn
3O
4
(2) raw material is prepared
Ferrosilicon processing is broken into granularity≤20mm, and it is 8-50mm that the quick lime that will contain CaO 〉=85% is broken into granularity, with Mn
3O
4Make ball and dry.
(3) fusing and refining
Earlier with Mn
3O
4The lime of pelletizing and lime total amount 1/3rd mixes, join in the refining furnace in batches and melt, the molten clear rear about Mn40-45% of slag manganese content, basicity 0.8-1.0, when treating that furnace charge melts clear and 1500 ℃ of left and right sides of slag temperature, add by stages and in groups ferrosilicon and remaining lime to the molten bath and stir, furnace charge all adds, and the control basicity of slag is at 1.0-1.2, refining 10-15 minute, Si in the stove and MnO reaction reaches balance, top of the slag calmness in the stove, can tap a blast furnace, calm, skim, pour into a mould.
Wherein, the charge composition that the smelting low carbon manganese-silicon contains contains the Mn requirement by production low Carbon Manganese silicon alloy to be prepared, and as will smelt the low Carbon Manganese silicon alloy that contains Mn 〉=80% time, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 3.0-3.5: 1.5-1.9 (weight ratio); When smelting the low Carbon Manganese silicon alloy that contains Mn 〉=72%, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.7-3.1: 1.3-1.7 (weight ratio); Smelt when containing Mn 〉=65% low Carbon Manganese silicon alloy, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.4-2.8: 1.1-1.5 (weight ratio).
Described liquid-phase reduction agent is molasses, starch.
Described ferrosilicon is wherein a kind of of 75% ferrosilicon, 65% ferrosilicon, silicon metal.
Outstanding substantive distinguishing features of the present invention and marked improvement are, owing to adopt artificial Mn
3O
4And ferrosilicon, impurity is few, and the phosphorus content of ferrosilicon is low, and producing the manganese-silicon phosphorus content of coming only is 0.27～0.3, can satisfy phosphorus content less than the requirement of 0.4% low-carbon ferromanganese.Production cost is low, constant product quality.
Four, description of drawings
Fig. 1 is the artificial Mn that uses of the present invention
3O
4The process chart of the method for smelting low carbon manganese-silicon in electric refining furnaces.
Contrast Fig. 1 of the present inventionly uses artificial Mn3O
4The technological process of the method for smelting low carbon manganese-silicon is in electric refining furnaces, earlier with artificial Mn3O
4Make pelletizing, mix with lime, add in the refining furnace and melt, When furnace charge fusing fully and slag temperature during 1500 ℃ of left and right sides, add to the molten bath dribs and drabs again ferrosilicon and Remaining lime also stirs, and when furnace charge all adds, treats that Si and the MnO reaction in the stove reaches balance, Can tap a blast furnace, calm, skim, cast, finishing, check, warehouse-in.
Five, embodiment
By the following examples technical scheme of the present invention is described in further detail.
Concrete technical scheme of the present invention is made of following method steps:
1, preparation Mn
3O
4Press manganese oxide ore: the liquid-phase reduction agent: sulfuric acid=1: 0.1-0.2: 0.5-0.6 (weight ratio), manganese oxide ore and liquid-phase reduction agent such as molasses are mixed, use sulfuric acid leaching, the alkaline chemical precipitation deironing is cleaned, and is prepared into Mn
3O
4Its chemical ingredients is: Mn 〉=69%, Fe≤0.05%, P≤0.05%, S≤0.03%, Sn≤0.001%, Pb≤0.001%.
2, raw material is prepared.Ferrosilicon is broken into granularity≤20mm, and it is 8-50mm that the quick lime that will contain CaO 〉=85% is broken into granularity, will manually synthesize Mn
3O
4Make ball and dry;
3, change slag and refining: charge composition contains the Mn requirement and prepares by producing different low Carbon Manganese silicon alloys, and as will smelt the low Carbon Manganese silicon alloy that contains Mn 〉=80% time, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 3.0-3.5: 1.5-1.9 (weight ratio); When smelting the low Carbon Manganese silicon alloy that contains Mn 〉=72%, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.7-3.1: 1.3-1.7 (weight ratio); Smelt when containing Mn 〉=65% low Carbon Manganese silicon alloy, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.4-2.8: 1.1-1.5 (weight ratio).
Spice, reinforced, refining requirement: earlier with Mn
3O
4The lime of pelletizing and lime total amount 1/3rd mixes and joins in the refining furnace in batches and melts, the molten clear rear about Mn40-45% of slag manganese content, basicity 0.8-1.0, when molten clear and slag temperature is 1500 ℃ of left and right sides when furnace charge, add dribs and drabs ferrosilicon and remaining lime to the molten bath and stir, when furnace charge all adds, basicity of slag is pressed 1.0-1.2 control, refining 10-15 minute, treat that Si and MnO reaction in the stove reach balance, top of the slag calmness in the stove, can tap a blast furnace, calm, skim, pour into a mould.
The present invention is because used artificial Mn
3O
4And ferrosilicon, impurity is few, and the phosphorus content of ferrosilicon is low, and producing the manganese-silicon phosphorus content of coming only is 0.27～0.3, can satisfy phosphorus content less than the requirement of 0.4% low-carbon ferromanganese.Production cost is low, constant product quality.Used ferrosilicon can be 75% ferrosilicon, 65% ferrosilicon or silicon metal.
Claims (4)
1. use artificial Mn
3O
4The method of smelting low carbon manganese-silicon in electric refining furnaces is characterized in that this method contains following steps:
(1) preparation Mn
3O
4
Press manganese oxide ore: the liquid-phase reduction agent: sulfuric acid=1: 0.1-0.2: 0.5-0.6 (weight ratio), manganese oxide ore and liquid-phase reduction agent are mixed, use sulfuric acid leaching, the alkaline chemical precipitation deironing is cleaned, and is prepared into Mn
3O
4,
(2) raw material is prepared
Ferrosilicon processing is broken into granularity≤20mm, and it is 8-50mm that the quick lime that will contain CaO 〉=85% is broken into granularity, with Mn
3O
4Make ball and dry,
(3) fusing and refining
Earlier with Mn
3O
4The lime of pelletizing and lime total amount 1/3rd mixes, join in the refining furnace in batches and melt, treat that the molten clear and slag temperature of furnace charge is in the time of 1500 ℃, add by stages and in groups ferrosilicon and remaining lime to the molten bath and stir, furnace charge all adds, and the control basicity of slag is at 1.0-1.2, refining 10-15 minute, Si in the stove and MnO reaction reaches balance, top of the slag calmness in the stove, can tap a blast furnace, calm, skim, pour into a mould.
2. method according to claim 1, the charge composition that it is characterized in that the smelting low carbon manganese-silicon contains the Mn requirement by production low Carbon Manganese silicon alloy to be prepared, and as will smelt the low Carbon Manganese silicon alloy that contains Mn 〉=80% time, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 3.0-3.5: 1.5-1.9 (weight ratio); When smelting the low Carbon Manganese silicon alloy that contains Mn 〉=72%, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.7-3.1: 1.3-1.7 (weight ratio); Smelt when containing Mn 〉=65% low Carbon Manganese silicon alloy, its proportioning is pressed ferrosilicon: Mn
3O
4Pelletizing: lime=1: 2.4-2.8: 1.1-1.5 (weight ratio).
3. method according to claim 1 is characterized in that described ferrosilicon is wherein a kind of of 75% ferrosilicon, 65% ferrosilicon, silicon metal.
4. method according to claim 1 is characterized in that described liquid-phase reduction agent is molasses, starch.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2008100735178A CN100572575C (en) | 2008-04-01 | 2008-04-01 | Use artificial Mn 3O 4The method of smelting low carbon manganese-silicon in electric refining furnaces |
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|---|---|---|---|
| CNB2008100735178A CN100572575C (en) | 2008-04-01 | 2008-04-01 | Use artificial Mn 3O 4The method of smelting low carbon manganese-silicon in electric refining furnaces |
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| CN101250632A true CN101250632A (en) | 2008-08-27 |
| CN100572575C CN100572575C (en) | 2009-12-23 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102031322A (en) * | 2010-10-25 | 2011-04-27 | 中钢集团吉林铁合金股份有限公司 | Method for producing medium and low micro-carbon ferro chrome alloy by shaking ladle dilution and Perrin process |
| CN105969978A (en) * | 2016-07-22 | 2016-09-28 | 江苏省冶金设计院有限公司 | System and method for preparing ferrochrome |
| CN106702141A (en) * | 2016-12-30 | 2017-05-24 | 山东盛荣新材料有限公司 | Method for preparing hematite-manganese-aluminum composite through red mud |
| CN107541609A (en) * | 2016-06-23 | 2018-01-05 | 陕西友力实业有限公司 | A kind of manganese alloy smelting process |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2461759A1 (en) * | 1979-07-17 | 1981-02-06 | Sofrem | HIGH SILICON SILICON AND MANGANESE REDUCING ALLOY, AND APPLICATIONS |
-
2008
- 2008-04-01 CN CNB2008100735178A patent/CN100572575C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102031322A (en) * | 2010-10-25 | 2011-04-27 | 中钢集团吉林铁合金股份有限公司 | Method for producing medium and low micro-carbon ferro chrome alloy by shaking ladle dilution and Perrin process |
| CN107541609A (en) * | 2016-06-23 | 2018-01-05 | 陕西友力实业有限公司 | A kind of manganese alloy smelting process |
| CN105969978A (en) * | 2016-07-22 | 2016-09-28 | 江苏省冶金设计院有限公司 | System and method for preparing ferrochrome |
| CN105969978B (en) * | 2016-07-22 | 2018-08-21 | 江苏省冶金设计院有限公司 | The system and method for preparing ferrochrome |
| CN106702141A (en) * | 2016-12-30 | 2017-05-24 | 山东盛荣新材料有限公司 | Method for preparing hematite-manganese-aluminum composite through red mud |
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| CN100572575C (en) | 2009-12-23 |
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Granted publication date: 20091223 Termination date: 20140401 |