CN202063976U - Equipment for producing high manganese-silicon by low-grade ferromanganese ore - Google Patents
Equipment for producing high manganese-silicon by low-grade ferromanganese ore Download PDFInfo
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- CN202063976U CN202063976U CN201120007638XU CN201120007638U CN202063976U CN 202063976 U CN202063976 U CN 202063976U CN 201120007638X U CN201120007638X U CN 201120007638XU CN 201120007638 U CN201120007638 U CN 201120007638U CN 202063976 U CN202063976 U CN 202063976U
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Abstract
The utility model relates to equipment and a process for producing high manganese-silicon by low-grade ferromanganese ore. The high-content manganese-silicon (with 50-85% manganese content) can be produced by low-grade manganese ore (wherein the content of TMn is 10-25%), and barren resources are efficiently used. The equipment comprises a smelting furnace (9), an oxidation furnace (13), an electric arc furnace (21) and a high-temperature conveying system, wherein the high-temperature conveying system is connected with the smelting furnace (9) through a pot-string distributing device (6), the bottom of the smelting furnace (9) is connected with the upper part of the oxidation furnace (13) through an iron overflowing opening (17) shaped like a Chinese character 'yi (second)', and the middle part of the smelting furnace (9) is connected with a slag runner (20) and the oxidation furnace (13) through slag outlets (19). In the equipment, 1300-1350 DEG high-temperature waste gases produced in the smelting furnace are used for sintering equipment so as to sinter the low-manganese pellets to 1200-1250 DEG, high-temperature heat in the waste gases is sufficiently used, coal gases in the electric arc furnace and the oxidation furnace are recovered to generate electricity or to heat fuel in the furnaces, and slag in the electric arc furnace and the oxidation furnace are sufficiently used to produce cement; and the equipment has the advantages of high utilization efficiency of energy sources, energy saving and low comprehensive cost, reduces emission and has better economic and social benefits.
Description
Technical field
The utility model relates to the production unit and the processing method of manganese alloy, relates in particular to a kind of equipment and processing method of utilizing low-grade ferrous manganese ore to produce high manganese-silicon, belongs to technical field of ferrous metallurgy.
Background technology
China's iron and steel output holds a safe lead the world with more than 700,000,000 tons production capacity at present, increase the iron alloy demand is also huge, but the consequent energy, resource, blowdown presssure is huge.Along with the pay attention to day by day of international community to environmental protection, the shortage of resources such as manganese ore, people constantly seek a kind of method of utilizing of low-grade manganese, for example certain ore deposit is based on rhodochrosite (MnCO3), spathic iron ore (FeCO3), being difficult to magnetic separation separates, TMn content 12～20%, TFe content 12～18%, the raising of TFe and TMn grade has only 2～3% behind the high intensity magnetic separation.The magnetic roasting is under the best processing condition that assay optimization goes out: 750 ℃ of neutral roastings of maturing temperature, roasting time 1 hour, TFe content brings up to 15.42% by 13.01% in the roasted ore, TMn content brings up to 17.76% by 14.99%, roasted ore TFe content behind fine grinding and high intensity magnetic separation brings up to 29.02% by 13.01%, and TMn content brings up to 29.68% by 14.99%, TFe content 10.57% in the mine tailing, TMn content 13.51% is to the Mn serious waste of resources.
Patent CN200810068700.9 discloses and has a kind ofly produced high silicomanganese technology with electric refining furnaces, adopts the low mid-carbon fe-mn of industrial ferrosilicon and coke reduction to produce manganese in the waste residue.Patent CN01129197.4 discloses a kind of method of producing manganese-silicon with the low carbon ferromanganese smelted furnace cinder, does manganese in the reductive agent reduced blast furnace with ferrosilicon powder.Patent CN200810073518.2 discloses a kind of method of producing low carbon ferromanganese, with artificial Mn
3O
4For raw material, with the ferrosilicon is reductive agent, produces silicomanganese at electric refining furnaces.Above patent is the manganese of raw material reduction of low grade with the ferrosilicon all, is the waste of resource, is cut into higher.Patent CN02114376.5 discloses a kind of production technology of high silicon manganese-silicon alloy, an electric furnace is produced liquid silicon manganese alloy, another electric furnace is produced liquid ferrosilicon, carrying out the outer heat of stove then converts, so being traditional technology, can't solve low-grade ferromanganese mineral intergrowth, and the close mining and metallurgy of ferromanganese content is produced the demand of high manganese-silicon.
Summary of the invention
At the deficiencies in the prior art, the utility model provides a kind of equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon.
The utility model provides a kind of equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon, comprises smelting furnace (9), oxidized still (13), electric arc furnace (21) and high temperature conveying system; The high temperature conveying system links to each other with smelting furnace (9) through a string jar distributor (6), the bottom of smelting furnace (9) links to each other by the top of excessive iron mouth (17) of " second " shape and oxidized still (13), and the middle part of smelting furnace (9) links to each other with electric arc furnace (21) with slag chute (20) by slag notch (19);
Preferably, the high temperature conveying system comprises: feed bin (3), skip car (4), track (5) and string jar distributor (6); A string jar distributor (6) links to each other with the top of smelting furnace, and feed bin (3) links to each other with pellet sintering equipment (1) by blow tank (2); Feed bin (3) is connected through track (5) with a string jar distributor (6); Skip car (4) runs on the track (5).
Preferably, smelting furnace (9) top is provided with gas exit (7), melting oxygen rifle (8), melting coaloust-oxygen gun (18), smelting furnace top links to each other with the string jar distributor (6) of high temperature conveying system, and the smelting furnace middle part is provided with slag notch (19), and the bottom is provided with the excessive iron mouth (17) of " second " shape;
Preferably, oxidized still (13) top is provided with oxygen rifle (10), oxidized still gas port (11) and oxidized still flux string jar (12), and links to each other with smelting furnace (9) by the excessive iron mouth (17) of " second " shape; The oxidized still middle part is provided with oxidized still slag notch (14), and the oxidized still bottom sides is provided with iron notch (15), and the bottom is provided with gas permeable brick (16);
Preferably, the top of electric arc furnace (21) is provided with electrode (22) and electric arc furnace flux string jar (23), and the middle part of electric arc furnace (21) is provided with coaloust-oxygen gun (24) and carbon rifle (25), and the bottom of electric arc furnace (21) is provided with electric arc slag outlet (26) and alloy outlet (27).
Preferably, described equipment also comprises pellet sintering equipment (1), and pellet sintering equipment (1) links to each other with the feed bin (3) of high temperature conveying system one end by blow tank (2).
Preferably, described pellet sintering equipment (1) is belt type roasting machine, the grate kiln that directly goes out high temperature (1200 ℃～1250 ℃) pelletizing, or other pellet sintering equipment.
Preferably, the top that melting oxygen rifle (8) inserts slag is blown into oxygen in slag, makes carbon more than needed and CO burning in the slag of top emit a large amount of heats, and fusing contains manganese material and flux.According to the size and the smelting needs of stove, melting oxygen rifle can be 2 to 8, is arranged in suitable position around the furnace wall, and those skilled in the art can select the quantity and the position of melting oxygen rifle according to actual needs.
Preferably, melting coaloust-oxygen gun (18) inserts the slag bottom and spray into oxygen and carbonaceous material in smelting furnace, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials, or oxygen channel and carbonaceous material pipeline are arranged side by side.According to the size and the smelting needs of stove, the melting coaloust-oxygen gun can be 2 to 12, is arranged in suitable position around the furnace wall, and those skilled in the art can select the quantity and the position of melting coaloust-oxygen gun according to actual needs.
Preferably, smelting furnace (9) is the cylindrical stove that molten bath district diameter is little, slag district diameter is big, and oxidized still (13) and electric arc furnace (21) are cylindrical stoves.
Preferably, oxidized still (13) bottom is provided with BOTTOM OXYGEN gas permeable brick (16), and molten steel is carried out continuously weak oxygen blast, makes the stable C that takes off of molten steel, shortens the strong oxygen blow duration of oxidized still oxygen rifle (10), prevents that big boiling, splash etc. from appearring in molten steel, improves liquid steel temperature.Oxidized still BOTTOM OXYGEN gas permeable brick is established 1～5 according to the size of oxidized still, and those skilled in the art can select the quantity and the position of BOTTOM OXYGEN gas permeable brick according to actual needs.Oxidized still (13) top is provided with oxygen rifle (10) blowing molten steel, makes the temperature of C content in the steel and molten steel reach the requirement of RH or LF refining furnace fast; Oxidized still flux string jar (12) adds sludging flux for oxidized still.
Preferably, coaloust-oxygen gun (24) inserts electric arc furnace (21) slag top, sprays into coal dust and oxygen making foamed slag to the slag surface, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials, or oxygen channel and carbonaceous material pipeline are arranged side by side.According to the size and the smelting needs of stove, coaloust-oxygen gun can be 1 to 3, is arranged in suitable position around the furnace wall, and those skilled in the art can select the quantity and the position of coaloust-oxygen gun according to actual needs.
Preferably, carbon rifle (25), insert electric arc furnace (21) slag middle part, in melting slag, spray into coke powder or blue powdered carbon, size and smelting needs according to stove, the carbon rifle can be 1 to 3, is arranged in suitable position around the furnace wall, and those skilled in the art can select the quantity and the position of carbon rifle according to actual needs.
Advantage of the present utility model is embodied in:
(1) utilizes low-grade ferromanganese mineral intergrowth, cut Mn, Fe content close (TMn content 12～20%, TFe content 12～18%) is produced high-load manganese-silicon, makes manganese content reach 50～85%, and barren resource is efficiently utilized.
(2) 1300～1350 ℃ of high-temp waste gas of smelting furnace are used for agglomerating plant low manganese ore pellet sintering to 1200～1250 ℃, heat of high temperature in the waste gas is fully used, the coal gas of electric arc furnace and oxidized still is recovered and is used to generate electricity or the fuel of process furnace, the slag of electric arc furnace and oxidized still is made into cement and is fully used, efficiency of energy utilization height, energy-saving and emission-reduction, comprehensive cost are low, have favorable economic benefit and social benefit.
Description of drawings
Fig. 1 is a block diagram of the present utility model.Wherein: 1: agglomerating plant, 2: blow tank, 3: feed bin, 4: skip car, 5: track, 6: string jar distributor, 7: gas exit, 8: melting oxygen rifle, 9: smelting furnace, 10: oxygen rifle, 11: oxidized still gas port, 12: oxidized still flux string jar, 13: oxidized still, 14: oxidized still slag notch, 15: iron notch, 16: gas permeable brick, 17: " second " shape iron mouth that overflows, 18: the melting coaloust-oxygen gun, 19: slag notch, 20: slag chute, 21: electric arc furnace, 22: electrode, 23: electric arc furnace flux string jar, 24: coaloust-oxygen gun, 25: the carbon rifle, 26: the outlet of electric arc slag, 27: the alloy outlet.
Embodiment:
Following examples are to further specify of the present utility model, but the utility model is not limited thereto.
Embodiment 1:
The utility model also provides a kind of equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon, comprises pellet sintering equipment 1, smelting furnace 9, oxidized still 13, electric arc furnace 21 and high temperature conveying system; The feed bin 3 of high temperature conveying system one end links to each other with pellet sintering equipment 1 by blow tank 2, the string jar distributor 6 of the other end links to each other with smelting furnace (9), smelting furnace 9 links to each other by the excessive iron mouth 17 of " second " shape with oxidized still 13, and smelting furnace 9 links to each other with electric arc furnace 21 with slag chute 20 by slag notch 19;
Smelting furnace 9 tops are provided with gas exit 7, melting oxygen rifle 8, melting coaloust-oxygen gun 18, and smelting furnace top links to each other with the string jar distributor 6 of high temperature conveying system, and the smelting furnace middle part is provided with slag notch 19, and the bottom links to each other with the excessive iron mouth 17 of " second " shape;
Oxidized still 13 tops are provided with oxygen rifle 10, oxidized still gas port 11 and oxidized still flux string jar 12, and link to each other with the excessive iron mouth 17 of " second " shape; The oxidized still middle part is provided with oxidized still slag notch 14, and the oxidized still bottom sides is provided with iron notch 15, and the bottom is provided with gas permeable brick 16;
The high temperature conveying system comprises: feed bin 3, skip car 4, track 5, string jar distributor 6; A string jar distributor 6 links to each other with the top of smelting furnace, and feed bin 3 links to each other with pellet sintering equipment 1 by blow tank 2; Feed bin 3 is connected through track 5 with a string jar distributor 6; Skip car 4 runs on the track 5.
The top that melting oxygen rifle 8 inserts slag is blown into oxygen in slag, make carbon more than needed and CO burning in the slag of top emit a large amount of heats, fusion manganese material and flux.Melting oxygen rifle is 3, is arranged in 120 degree positions around the furnace wall.
Melting coaloust-oxygen gun 18 inserts the slag bottom and spray into oxygen and carbonaceous material in smelting furnace, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials.The melting coaloust-oxygen gun is 4, is arranged in the position of 90 degree symmetrical distributions on every side, furnace wall.
Smelting furnace 9 is cylindrical stoves that molten bath district diameter is little, slag district diameter is big, and oxidized still (13) is cylindrical stove.
Oxidized still 13 bottoms are provided with BOTTOM OXYGEN gas permeable brick 16, and molten steel is carried out continuously weak oxygen blast, make the stable C that takes off of molten steel, shorten oxidized still oxygen rifle the last 10 oxygen blow duration, prevent that big boiling, splash etc. from appearring in molten steel, improves liquid steel temperature.Oxidized still BOTTOM OXYGEN gas permeable brick is established 3, and 1/3 radius, 120 degree are put layout in the bottom.Oxidized still 13 tops are provided with oxygen rifle 10 blowing molten steel, make the temperature of C content in the steel and molten steel reach the requirement of RH or LF refining furnace fast; Oxidized still flux string jar 12 adds sludging flux for oxidized still.
Coaloust-oxygen gun 24 inserts electric arc furnace 21 slag tops, sprays into coal dust and oxygen making foamed slag to the slag surface, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials, or oxygen channel and carbonaceous material pipeline are arranged side by side.Coaloust-oxygen gun is 2, is arranged symmetrically on the furnace wall.
A kind of processing method of utilizing low-grade ferrous manganese ore to produce high manganese-silicon comprises the steps:
1) low-grade manganese is made pelletizing, be sintered to 1200～1250 ℃ in agglomerating plant, the high temperature oxidation pelletizing adds smelting furnace by the high temperature conveying system;
2) be pre-formed thick 700-800mm iron bath and thick 600-700mm slag in the smelting furnace, in smelting furnace, add flux slag making desulfurization, dephosphorization, basicity of slag is controlled in 0.5～1.2 scope, melting oxygen rifle is blown into oxygen in the slag of top, make CO and carbon burning more than needed in the slag of top emit a large amount of heats, fusion manganese material and flux make smelting temperature reach 1400-1450 ℃; The melting coaloust-oxygen gun sprays into carbonaceous material and oxygen in the slag of bottom, and keeps having in the slag of middle and lower part the 20-40wt% carbon of having more than needed, and iron wherein is reduced into molten iron, and the oxide compound of manganese is by enrichment in the slag;
3) molten iron continuously flows into oxidized still by the excessive iron mouth of " second " shape, adds flux slag making desulfurization, dephosphorization in oxidized still, and basicity of slag is controlled in 3.0～3.5 scopes, obtains qualified molten iron; Can also further adjust C content and temperature in the molten steel by oxidized still BOTTOM OXYGEN gas permeable brick and top blow oxygen lance oxygen blast,, directly supply LF or RH refining furnace to obtain the qualified molten steel of 1550 ℃～1700 ℃ of C content 0.01～0.50%, temperature;
4) high-temperature slag in the smelting furnace (1400 ℃～1450 ℃) flows into electric arc furnace, and the heat of high temperature in the slag is fully used; In electric arc furnace, add flux slag making desulfurization, dephosphorization by electric arc furnace flux string jar; Utilize electrode arc rapid heating slag to reach 1550～1800 ℃; Coaloust-oxygen gun is to electric arc furnace slag surface coal injection and oxygen making foamed slag, and foamy slag makes the electric arc heat fully be absorbed by slag around covering electrode, reduces the infringement of electric arc to the electric arc furnace furnace wall refractory simultaneously; The carbon rifle sprays into blue charcoal or the coke powder of granularity 3～10mm on slag and the MnSi alloy liquid interface in electric arc furnace, make Mn oxide and Si oxide in 1550～1800 ℃ slag, be reduced into the MnSi alloy, the manganese-silicon of manganese content 50～85%, Si content 10～40%, other element and foreign matter content 5～10%;
5) high-temp waste gas of smelting furnace (1300～1350 ℃) is used for agglomerating plant low manganese ore pellet sintering to 1200～1250 ℃, and the heat of high temperature in the waste gas is fully used.The coal gas of electric arc furnace and oxidized still is recovered and is used to generate electricity or the fuel of process furnace.The slag of electric arc furnace and oxidized still is made into cement and is fully used.
Low-grade manganese is especially based on rhodochrosite (MnCO3), spathic iron ore (FeCO3), TMn content 14%, TFe content 13%, SiO
2Content 20%, all the other are moisture and unavoidable impurities.Described Mn and Fe are that the form with oxide compound exists in low-grade manganese, and TMn is meant the content of full manganese, and TFe is meant the content of full iron.
Basicity of slag is a dual alkalinity, and computing method refers to Ca/SiO
2Ratio.Carbonaceous material is a coal dust.
The melting coaloust-oxygen gun by the downward oblique cutting of melting furnace wall to apart from 300～200mm place, scum interface, in slag, implement to be rich in the winding-up of carbon material, burning carbonaceous materials provides institute's heat requirement to the smelting furnace fusion reduction reaction, control carbon-to-oxygen ratio, minimizing slag increase C in a large number in molten iron, provide reductive agent, heat and sufficient physical-chemical reaction dynamic conditions for containing manganese material fast restore.Preferably, be rich in the winding-up of carbon material, by rich carbon 20～40wt% control carbon-to-oxygen ratio.N is adopted in the carbonaceous material winding-up
2Be carrier.
The surface of coaloust-oxygen gun slag in electric arc furnace is according to coal dust 5% coal injection more than needed and oxygen making foamed slag.N is adopted in the carbonaceous material winding-up
2Be carrier.
The carbon rifle sprays into blue charcoal or the coke powder of granularity 3～10mm on slag and the MnSi alloy liquid interface in electric arc furnace, spray into blue powdered carbon 115Kg according to the content ton slag of Mn and Si oxide compound.N is adopted in blue carbon or the winding-up of coke powder material
2Be carrier.
Flux is one or more in unslaked lime, rhombspar, the fluorite etc., and smelting furnace flux is that unslaked lime and rhombspar add in 3: 1 ratio molten iron 120 kgs per ton; Oxidized still flux is that unslaked lime, rhombspar, fluorite are in 30 kilograms of addings of 3: 2: 1 ratio molten steel per ton; Electric arc furnace flux unslaked lime, rhombspar, fluorite are in 30 kilograms of addings of 3: 2: 1 ratio molten steel per ton.
MnSi alloy: Mn:56.48%, Si:40.55%, other is 2.97% years old.
Embodiment 2:
The top that melting oxygen rifle 8 inserts slag is blown into oxygen in slag, make carbon more than needed and CO burning in the slag of top emit a large amount of heats, fusion manganese material and flux.Melting oxygen rifle is 8, is arranged symmetrically in around the furnace wall.Melting coaloust-oxygen gun 18 can be 12.Be arranged in the position of 30 degree symmetrical distributions on every side, furnace wall.
Oxidized still BOTTOM OXYGEN gas permeable brick 16 is established 1, and 1/3 radius is arranged in the bottom.Coaloust-oxygen gun 24 inserts electric arc furnace 21; Coaloust-oxygen gun 24 is 1, is arranged on the furnace wall.Carbon rifle 25 inserts electric arc furnace 21 slags middle part, sprays into coke powder or blue powdered carbon in melting slag, and the carbon rifle is 2, is arranged symmetrically in around the furnace wall.
Other is with embodiment 1.
Embodiment 3:
The top that melting oxygen rifle 8 inserts slag is blown into oxygen in slag, make carbon more than needed and CO burning in the slag of top emit a large amount of heats, fusion manganese material and flux.Melting oxygen rifle can be 5, is arranged symmetrically in around the furnace wall.Melting coaloust-oxygen gun 18 is 8.Be symmetrically distributed in around the furnace wall.
Oxidized still BOTTOM OXYGEN gas permeable brick 16 is established 5 according to the size of oxidized still, the 1/3 radius symmetric arrangement in the bottom.
Coaloust-oxygen gun 24 inserts electric arc furnace 21; Coaloust-oxygen gun is 3, is 120 degree and is arranged symmetrically on the furnace wall.Carbon rifle 25 inserts electric arc furnace 21 slags middle part, sprays into coke powder or blue powdered carbon in melting slag, and the carbon rifle is 1, is arranged in the furnace wall location about.
Other is with embodiment 1.
Claims (10)
1. an equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon comprises smelting furnace (9), oxidized still (13), electric arc furnace (21) and high temperature conveying system; The high temperature conveying system links to each other with smelting furnace (9) through a string jar distributor (6), the bottom of smelting furnace (9) links to each other by the top of excessive iron mouth (17) of " second " shape and oxidized still (13), and the middle part of smelting furnace (9) links to each other with electric arc furnace (21) with slag chute (20) by slag notch (19).
2. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 is characterized in that,
Smelting furnace (9) top is provided with gas exit (7), melting oxygen rifle (8), melting coaloust-oxygen gun (18), smelting furnace top links to each other with the string jar distributor (6) of high temperature conveying system, the smelting furnace middle part is provided with slag notch (19), and the bottom is provided with the excessive iron mouth (17) of " second " shape.
3. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 or 2, it is characterized in that, oxidized still (13) top is provided with oxygen rifle (10), oxidized still gas port (11) and oxidized still flux string jar (12), and links to each other with smelting furnace (9) by the excessive iron mouth (17) of " second " shape; The oxidized still middle part is provided with oxidized still slag notch (14), and the oxidized still bottom sides is provided with iron notch (15), and the bottom is provided with gas permeable brick (16).
4. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 or 2, it is characterized in that, the top of electric arc furnace (21) is provided with electrode (22) and electric arc furnace flux string jar (23), the middle part of electric arc furnace (21) is provided with coaloust-oxygen gun (24) and carbon rifle (25), and the bottom of electric arc furnace (21) is provided with electric arc slag outlet (26) and alloy outlet (27).
5. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 or 2 is characterized in that, the high temperature conveying system comprises: feed bin (3), skip car (4), track (5) and string jar distributor (6); A string jar distributor (6) links to each other with the top of smelting furnace, and feed bin (3) links to each other with pellet sintering equipment (1) by blow tank (2); Feed bin (3) is connected through track (5) with a string jar distributor (6); Skip car (4) runs on the track (5);
Described pellet sintering equipment (1) is belt type roasting machine or the grate kiln that directly goes out 1200 ℃～1250 ℃ high temperature pelletizing.
6. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1, it is characterized in that, described equipment also comprises pellet sintering equipment (1), and pellet sintering equipment (1) links to each other with the feed bin (3) of high temperature conveying system one end by blow tank (2).
7. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 is characterized in that, melting oxygen rifle (8) is 2 to 8;
Melting coaloust-oxygen gun (18) inserts the slag bottom, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials, or oxygen channel and carbonaceous material pipeline are arranged side by side; The melting coaloust-oxygen gun can be 2 to 12.
8. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 or 2 is characterized in that, smelting furnace (9) is the cylindrical stove that molten bath district diameter is little, slag district diameter is big, and oxidized still (13) and electric arc furnace (21) are cylindrical stoves.
9. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1 is characterized in that, oxidized still (13) bottom is provided with BOTTOM OXYGEN gas permeable brick (16), and oxidized still BOTTOM OXYGEN gas permeable brick is established 1～5; Oxidized still (13) top is provided with oxygen rifle (10).
10. the equipment that utilizes low-grade ferrous manganese ore to produce high manganese-silicon as claimed in claim 1, it is characterized in that, coaloust-oxygen gun (24) inserts electric arc furnace (21) slag top, and its heart portion pipeline is that oxygen, external pipe are carbonaceous materials, or oxygen channel and carbonaceous material pipeline are arranged side by side; Coaloust-oxygen gun is 1 to 3;
Carbon rifle (25) inserts electric arc furnace (21) slag middle part, and the carbon rifle is 1 to 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120007638XU CN202063976U (en) | 2011-01-12 | 2011-01-12 | Equipment for producing high manganese-silicon by low-grade ferromanganese ore |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120007638XU CN202063976U (en) | 2011-01-12 | 2011-01-12 | Equipment for producing high manganese-silicon by low-grade ferromanganese ore |
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|---|---|---|---|
| CN201120007638XU Expired - Fee Related CN202063976U (en) | 2011-01-12 | 2011-01-12 | Equipment for producing high manganese-silicon by low-grade ferromanganese ore |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102041400A (en) * | 2011-01-12 | 2011-05-04 | 董亚飞 | Process and equipment for producing high-content manganese silicon alloy from low-grade ferromanganese ore |
| CN102679740A (en) * | 2012-06-04 | 2012-09-19 | 云南建水锰矿有限责任公司 | Distributing equipment, combined distributing equipment and distributing method thereof |
| CN113604661A (en) * | 2021-07-02 | 2021-11-05 | 宁夏天元锰业集团有限公司 | Process method for producing manganese-silicon alloy by using full manganese carbonate ore |
-
2011
- 2011-01-12 CN CN201120007638XU patent/CN202063976U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102041400A (en) * | 2011-01-12 | 2011-05-04 | 董亚飞 | Process and equipment for producing high-content manganese silicon alloy from low-grade ferromanganese ore |
| CN102041400B (en) * | 2011-01-12 | 2012-11-07 | 董亚飞 | Process and equipment for producing high-content manganese silicon alloy from low-grade ferromanganese ore |
| CN102679740A (en) * | 2012-06-04 | 2012-09-19 | 云南建水锰矿有限责任公司 | Distributing equipment, combined distributing equipment and distributing method thereof |
| CN102679740B (en) * | 2012-06-04 | 2014-10-15 | 云南建水锰矿有限责任公司 | Distributing equipment, combined distributing equipment and distributing method thereof |
| CN113604661A (en) * | 2021-07-02 | 2021-11-05 | 宁夏天元锰业集团有限公司 | Process method for producing manganese-silicon alloy by using full manganese carbonate ore |
| CN113604661B (en) * | 2021-07-02 | 2023-03-07 | 宁夏天元锰业集团有限公司 | Process method for producing manganese-silicon alloy by using full manganese carbonate ore |
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