CN1212410C - Method for realizing zero exhaust for fully steelmaking of steel dust and mud - Google Patents
Method for realizing zero exhaust for fully steelmaking of steel dust and mud Download PDFInfo
- Publication number
- CN1212410C CN1212410C CN 02117732 CN02117732A CN1212410C CN 1212410 C CN1212410 C CN 1212410C CN 02117732 CN02117732 CN 02117732 CN 02117732 A CN02117732 A CN 02117732A CN 1212410 C CN1212410 C CN 1212410C
- Authority
- CN
- China
- Prior art keywords
- iron
- steel
- furnace
- dust
- steelmaking
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The present invention relates to a method for realizing the zero discharge of steel dust mud by fully using the steel dust mud for steelmaking, which comprises the preparation of a material whose carbon content is 0.5 to 2 times as much as the theoretic amount of reduced iron oxide, and basicity is 0.5 to 1.5 from steel dust mud, the obtainment of basic sponge iron by mixing, molding, drying, roasting and reducing the material, smelting and separation, steel making and other technological processes; steel dust mud can be used for smelting after being directly proportioned without separation, so the present invention not only simplifies treatment facilities of the dust mud but also realizes the zero discharge of the dust mud by fully utilizing the dust mud, has the advantages of very low cost, and high unification of environmental benefit and economic benefit.
Description
Technical Field
The invention relates to a method for treating iron and steeldust and mud, in particular to a method for realizing zero emission of the iron and steel dust and mud in steel making.
Background
The iron and steel smelting needs the working procedures of sintering, blast furnace iron making, converter or electric furnace steel making, lime roasting, coking, steel rolling and the like, a large amount of dust and mud are inevitably generated, particularly, the dust and gas mud of a blast furnace and the sludge of a converter have extremely fine granularity, an effective treatment method is not available, and an iron and steel plant can only be stockpiled, occupies large area of land, wastes the resources and is even more serious the bad effect of causing environmental pollution. The main components of the blast furnace dust and the gas mud are 30-40% of iron and 30-40% of carbon, a small amount of calcium oxide, magnesium oxide and other impurities, the main components of the converter sludge are 50-60% of iron and calcium oxide and magnesium oxide which are main impurities, and the iron, calcium and magnesium contained in the dust and mud are all beneficial components for steel smelting, so that the dust and gas mud has great development and utilization values.
In the prior art, a method for treating dust and mud is to mix a certain amount of iron ore powder with the dust and mud to improve the iron content, then to prepare sintered ore or pellet ore, and to send the sintered ore or pellet ore and ore balls sintered by the iron ore powder back to a blast furnace for ironmaking again.
In other method for treating dust and mud, such as in industrially developed countries of Europe, America, Japan, etc., certain lime is added into the converter sludge, and the mixture is cold-pressed to form pellets, and then the pellets are sent back to a converter or an electric furnace to be used as a steelmaking slagging agent or a cooling agent. Although the method solves the problem of dust and mud discharge, the iron oxide can not be reduced in the process of steelmaking again and is discharged again, so that the steelmaking cost is increased, and the problem of environmental protection cannot be effectively solved.
The present adhesive can not solve the worldwide problem of high-temp. decomposition, so that the cold-set pellet pulverization is serious, and the smooth operation of blast furnace is affected, so far, the cold-set pellet blast furnace iron-smelting is only stopped in experimental stage all over the world, and there is no precedent for application in industrial production.
The method for treating dust and mud is characterized by that the converter mud is decondensed, fine-ground, magnetically separated and reselected to obtain a very small quantity of components with high iron content, and can be used for making reduced iron powder, iron oxide red and industrial cleaning agent, etc. because the social demand of these products is less than 1% of that of dust and mud produced by smelting iron and steel, and only the converter mud can be used, said method can play a certain role, but is far from the fundamental treatment of dust and mud pollution.
Disclosure of Invention
The invention aims to utilize all the iron and steel dust and mud, smelt into steel to realize zero emission, thoroughly solve the pollution problem of the iron and steel dust and mud, and obtain great economic benefit, thereby achieving high unification of environmental protection benefit and economic benefit. Therefore, the method for realizing zero emission of all steel making by the steel dust and mud is provided.
The invention is realized by the following method: the method comprises the technical processes of proportioning, mixing, molding, drying, roasting, reducing, melting and steelmaking;
a. preparing materials: materials such as smoke dust, sludge, steel rolling iron scale, coke powder, lime powder and the like discharged by blast furnaces, converters, electric furnaces and the like in iron and steel plants are supplemented with iron ore powder, CaO and MgO according to the carbon content of 0.5-2 times of the oxidation theoretical amount of reduced iron and the alkalinity of 0.5-1.5;
b. mixing materials: after proportioning according to the proportion, uniformly mixing by using mixing equipment such as a stirrer, an edge runner mill, a moistening mill and the like;
c. molding: after the materials are mixed uniformly, the powder is made into balls, blocks and other shapes with the granularity of 6-35 mm by using forming equipment such as a disc pelletizer, an extruder and the like;
d. and (3) drying: drying at 300 deg.C to water content below 5%;
e. roasting and reducing: placing the dried balls and blocks into a kiln such as a rotary hearth furnace, a trolley type continuous furnace and the like, and heating for 10-240 minutes at 900-1400 ℃ in an open flame manner to obtain pre-reduced alkaline sponge iron with the metallization rate of more than 60%;
f. melting and separating: directly adding the pre-reduced sponge iron out of the roasting furnace into a melting shaft furnace in a hot state, melting the pre-reduced sponge iron by using coke and hot air with the temperature of more than 500 ℃ as heat sources, separating slag from iron, wherein the slag is used for manufacturing cement, and byproduct gas of the melting furnace is used for roasting the reducing furnace as supplementary energy;
g. steel making: the molten ironafter slag iron separation is used for oxygen blowing steel making by a converter, and the byproduct high-temperature coal gas is directly used for roasting a reduction furnace after simple dust removal and is used as a supplementary energy source.
The object of the invention can also be achieved by the following technical measures:
when the materials are mixed, only one kind of dust mud can be mixed with the iron ore powder and the coke powder.
When the materials are mixed, only iron ore powder, lime powder and coke powder can be used for mixing.
During the material mixing, coal powder can also be used as a carbon source material.
The adhesive can be added during the material preparation to enhance the strength of the balls and blocks.
When the alkalinity of the prepared materials is too high, acid materials such as bentonite and the like can also be added.
The melting separation can also use electric furnaces such as a submerged arc furnace, an electric arc furnace, an induction furnace and the like to melt thermal state pre-reduced sponge iron and separate slag iron, the melting separation shaft furnace can also use coal and oxygen as heat sources, can also use coke and oxygen-enriched air as heat sources, the roasted and reduced pre-reduced sponge iron can also be cooled to below 300 ℃ under the condition of avoiding contact with oxygen as much as possible, and can also be hot-pressed into iron blocks for blast furnace iron making, electric furnace steel making or converter cooling agents, the melted iron after melting separation can also be cast into iron blocks for steel making or casting, and can also be directly cast,
compared with the prior art, the invention has the following advantages:
1. the blast furnace dust and the gas mud contain 30-40% of Fe and 30-40% of C, in order to utilize the iron content, the prior art needs to perform many operations such as magnetic separation, gravity separation and the like, iron is selected as a roasting material, carbon and the rest materials thereof are discharged as tailings, the invention does not need any separation and is directly used, the iron content is utilized, the carbon in the iron content also becomes a reducing agent for reducing iron oxide, calcium and magnesium become fluxes, the dust and the gas mud can be completely utilized, dust mud treatment facilities are simplified, and the investment is reduced.
2. The converter sludge contains 50-60% of Fe, 15-20% of CaO and MgO, and the same as the treatment of blast furnace gas sludge, the prior art needs ore dressing, and the invention does not need sorting and is fully utilized.
3. The alkaline pre-reduced sponge iron formed by the ingredients fully utilizes the calcium and magnesium impurities in the dust and mud, reduces the separation cost, becomes a slagging flux, does not need to add limestone and dolomite during melting separation, reduces the consumption of coke, and reduces the CO of a melting furnace2The atmosphere is favorable for reduction, and the calorific value of the byproduct gas is high.
4. The invention can fully utilize blast furnace dust removal ash, gas mud, converter, electric furnace sludge, lime powder, iron scale and coke powder generated in the steel smelting process with necessary iron ore powder and powder ore, and produce steel products, realizes zero emission, fundamentally solves the pollution problem of steel dust and mud, and has revolutionary and profound influence on environmental protection.
5. The dust and mud of iron and steel belong to the waste discharge, almost without cost, the invention turns it into the steel product, its cost is lower than any existing smelting technology, the billet cost is only several hundred yuan, medium-sized steel mill discharges the dust and mud and can produce several ten thousand tons of billets annually, the profit is several thousand yuan, while solving the pollution, can create enormous economic benefits.
Description of the drawings:
FIG. 1 is a process flow diagram of the present invention.
Detailed Description
The method of the invention is described in detail below with reference to the accompanying drawings and examples:
the process flow of the invention is as follows: batching → mixing → shaping → drying → roasting reduction → melting → steel making → billet.
1. Preparing materials:
the materials such as smoke dust, sludge, steel rolling iron scale, coke powder, lime powder and the like discharged by blast furnaces, converters, electric furnaces and the like of iron and steel plants and iron ore powder can be used as raw materials. The blast furnace ash and the gas mud contain 30-40% of iron, 30-40% of carbon and partial calcium oxide and magnesium oxide, the converter sludge contains 50-60% of iron and partial calcium oxide and magnesium oxide, the coke powder is mainly a carbon-containing substance, and the lime powder is powder of roasted lime and mainly contains calcium oxide. The prepared carbon-containing material and the oxide of the iron have the following reaction when being roasted and heated:
the carbon content of the ingredients is required to be 0.5-2 times of the theoretical amount of the reduced iron oxidation, the ingredients are insufficiently reduced when the carbon content is too low, the carbon content is easily reoxidized at high temperature, the reaction is fast when the carbon content is higher, the carbon content is thoroughly reduced, the high-temperature oxidation can be prevented, and the strength is poorer after the carbon content is too high.
Adding alkaline materials such as CaO, MgO, and the like, mainly during melting with SiO2、Al2O3When the acidic materials form low-melting-point slag to realize slag-iron separation and alkalinity (CaO/SiO)2) The materials are mixed according to the proportion of 0.5-1.5, the furnace lining is easy to erode when the alkalinity is too low, the desulfurization effect is avoided, and the fluidity is not good when the alkalinity is too high, so that the desulfurization is not facilitated. When the electric furnace is used for melting, the alkalinity of the ingredients can be properly increased and the ingredients are mixed according to the proportion of 1-3.5.
The added CaO not only has the functions of flux and desulfurization, but also has the function of binder by reacting with water to form slaked lime during molding, and other binders can be added or not added so as to reduce the cost. Meanwhile, the slaked lime also has a catalytic effect on the reduction reaction of the ferric oxide.
2. Mixing material
After the raw materials are proportioned, the raw materials are uniformly mixed by various devices with mixing functions, such as a stirrer, anedge runner mill, a moistening mill and the like.
3. Shaping of
After the materials are mixed uniformly, the powder is made into balls, blocks and other shapes with the granularity of 6-35 mm by using forming equipment such as a disc pelletizer, a double-roller extruder and the like, the granularity is too small, the air permeability and heat transfer are poor during roasting reduction, the reduction reaction is not facilitated to be carried out, the heat transfer is slow when the granularity is too large, and the reduction time is too long.
4. Drying
The formed balls and blocks are dried at the temperature of below 100-300 ℃ by using the waste heat of a roasting reduction furnace until the moisture content is less than 5%, when the drying temperature is too high, the green balls are easy to crack due to high moisture content, when the temperature is too low, the drying time is long, the equipment is large, and the investment is high. When the pellets dried until the moisture content is less than 5 percent are put into a roasting furnace for reduction, the pellets are basically not cracked and can keep intact shapes.
5. Reduction by roasting
And (3) putting the dried pellets into a rotary hearth furnace, a trolley type continuous furnace and other kilns, heating for 10-240 minutes at the high temperature of 900-1400 ℃ in an open flame manner to obtain pre-reduced alkaline sponge iron with the metallization rate of more than 60%, wherein the heating fuel is the byproduct gas of a melting furnace and the byproduct gas of oxygen converter steelmaking. When the roasting temperature is lower, the corresponding time is prolonged, when the temperature is higher, the time is shortened, when the temperature is too low, the reduction reaction is too slow, and when the temperature is too high, the pellets are easy to bond, and the discharging is difficult. The pellets are directly heated in an oxidizing atmosphere under open flame, mainly by the reduction reaction of carbon-containing materials in the pellets and iron oxide, and because the carbon content is higher, the pellets can avoid or reduce reoxidation after high-temperature reduction, and the metallization rate of the pre-reduced sponge iron is improved.
The converter gas can be used for roasting the reduction furnace as a heat source only by simply removing dust, the high-temperature physical sensible heat of the converter gas is utilized, the fuel is saved, the cooling and dust removal investment of the converter gas is greatly reduced, the CO content of the high-temperature converter gas is high, and excellent protective atmosphere is provided for preventing pellets from being reoxidized after reduction, so that multiple purposes are achieved.
The invention only needs to provide necessary external heating source when the roasting furnace is opened, after the normal production, namely the melting furnace and the converter, is switched into, the external heating source is not needed, the carbon-containing material and the coal gas are matched in the pellets as supplementary heat sources, the roasting reduction can be sufficiently maintained, and the high-temperature waste gas of the roasting furnace can also be used for generating power.
6. Melting and separating
Pre-reduced basic sponge iron heat after roastingDirectly adding into a melting shaft furnace in a state, using coke and hot air with the temperature of more than 500 ℃ as energy sources, melting the pre-reduced sponge iron, further reducing, separating slag and iron, using slag to manufacture cement, and using molten iron to make steel or cast into iron blocks or castings. Directly adding into the melting furnace in a thermal state to avoidreoxidation in the cooling process, and using hot air with the temperature of more than 500 ℃ to ensure that CO in the melting furnace is melted2Reducing the iron sponge into CO, creating a good reducing atmosphere to finish the final reduction of the iron sponge, and providing good fuel for a roasting and reducing furnace, wherein the CO content and the heat value of the byproduct gas are high. The hot air is prepared by heat exchange of byproduct gas by a heat exchanger or a hot blast stove. Oxygen-enriched air or pure oxygen can be blown into the melting furnace, coke is used little or not used at all, and the consumption of the coke is reduced.
7. Making steel
The molten iron after slag iron separation is used for oxygen blowing steel making by a converter, and the byproduct gas is directly used for roasting a reduction furnace after simple dust removal, is used as a supplementary energy source, and is cast into a billet after being refined by the known technology.
Example 1:
85 tons of gas mud, 100 tons of imported fine ore and 7.6 tons of lime powder are used for smelting iron in a Tang steel blast furnace, ingredients are added, the carbon content is 1.98 times of the oxidation physical theoretical quantity of reduced iron, the alkalinity is 1.47, the materials are mixed uniformly, pellets of 6-20 mm are prepared by a disk pelletizer, the pellets are dried for 30 minutes at 270 ℃, the moisture content is less than 5 percent, the pellets are placed into a trolley type continuous furnace and are roasted for 11 minutes at 1370 ℃ to obtain pre-reduced alkaline sponge iron with the metallization rate of 85 percent, the pre-reduced alkaline sponge iron is directly added into a melting shaft furnace in a hot state, the hot air temperature is 500 ℃, after melting, slag and iron are separated, the slag is prepared into water slag which is used for preparing cement, and molten iron is used for converter.
Example 2:
50 tons of converter sludge, 50 tons of iron scale powder and 60 tons of gas mud which are discharged in compliance with steel are mixed, the carbon content is 0.51 time of the oxidation theoretical amount of reduced iron, the alkalinity is 1, a material is mixed for 10 minutes by an edge runner mill, a 35mm flat ball is made by a double-roll extruder, the mixture is put into a furnace and dried for 1 hour at 300 ℃, the moisture is less than 5 percent, the mixture is roasted for 240 minutes at 900 ℃, pre-reduced alkaline sponge iron with the metallization rate of 63 percent is obtained, and 96 tons of steel billets are obtained by melting and steelmaking like the embodiment 1.
Example 3:
70 tons of gas mud, 100 tons of iron ore powder and 5 tons of coke powder are used, the carbon content is 1.3 times of the oxidation physical theoretical quantity of reduced iron, the alkalinity is 0.53, the materials are mixed uniformly, pellets of 6-16 mm are prepared by a disk pelletizer, the pellets are dried for 1.5 hours at 100 ℃, the moisture content is 2 percent, the pellets are placed into a roasting reduction furnace and roasted for 40 minutes at 1250 ℃, pre-reduced alkaline sponge iron with the metallization rate of 98 percent is obtained, and the rest conditions are the same as those in the example 1, so that 109 tons of steel billets are obtained.
Example 4:
the method comprises the following steps of mixing 25 tons of coke powder, 100 tons of converter sludge and 11 tons of bentonite, wherein the carbon content is 0.8 time of the oxidation theoretical amount of reduced iron, the alkalinity is 1.2, the mixture is uniform, pelletizing by a disk pelletizer to form pellets of 10-20 mm, drying for 1 hour at 210 ℃, putting the pellets into a roasting reduction furnace, roasting for 210 minutes at 1050 ℃ to obtain pre-reduced alkaline sponge iron with the metallization rate of 61%, and obtaining 57 tons of steel billets under the same conditions as in example 1.
Claims (9)
1. A method for realizing zero emission of steel dust and mud in all steelmaking comprises the technical processes of proportioning, mixing, molding, drying, roasting reduction, melting and separating and steelmaking, and is characterized in that:
a. preparing materials: smoke dust, sludge, steel rolling iron scale, coke powder and lime powder materials discharged by blast furnaces, converters and electric furnaces of iron and steel plants are supplemented with iron ore powder, CaO and MgO, and the carbon content is 0.5-2 times of the oxidation physical theoretical quantity of reduced iron and the alkalinity is 0.5-1.5;
b. mixing materials: after proportioning according to the proportion, uniformly mixing by using a stirrer, an edge runner mill and a moistening mill mixing device;
c. molding: after the materials are mixed uniformly, the powder is made into balls and blocks with the granularity of 6-35 mm by a disc pelletizer and an extruder forming device;
d. and (3) drying: drying at 300 deg.C to water content below 5%;
e. roasting and reducing: placing the dried balls and blocks into a rotary hearth furnace and a trolley type continuous furnace kiln, and heating for 10-240 minutes at 900-1400 ℃ in an open flame manner to obtain pre-reduced alkaline sponge iron with the metallization rate of more than 60%;
f. melting and separating: directly adding the pre-reduced sponge iron out of the roasting furnace into a melting shaft furnace in a hot state, melting the pre-reduced sponge iron by using coke and hot air with the temperature of more than 500 ℃ as heat sources, separating slag from iron, wherein the slag is used for manufacturing cement, and byproduct gas of the melting furnace is used for roasting the reducing furnace as supplementary energy;
g. steel making: the molten iron after slag iron separation is used for oxygen blowing steel making by a converter, and the byproduct high-temperature coal gas is directly used for roasting a reduction furnace after simple dust removal and is used as a supplementary energy source.
2. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: when the material is prepared, a dust mud is mixed with iron ore powder and coke powder.
3. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: the coal powder is used as carbon source ingredient.
4. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: when in proportioning, the binder is added to enhance the strength of the balls and blocks.
5. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: when the alkalinity of the prepared material is too high, the bentonite acid material is added.
6. The method for realizing zero emission of all steel makingby using the steel dust and sludge according to claim 1, which is characterized in that: smelting the hot pre-reduced sponge iron in a submerged arc furnace, an electric arc furnace or an induction furnace, and separating slag and iron.
7. The method for realizing zero emission of all steel making from the steel dust and sludge according to claim 1, which is characterized in that: the melting shaft furnace uses coal and oxygen as heat sources, and uses coke and oxygen-enriched air as heat sources.
8. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: the pre-reduced sponge iron after roasting reduction is cooled to below 300 ℃ under the condition of avoiding contact with oxygen as much as possible, and is hot-pressed into iron blocks which are used as coolants for blast furnace iron making, electric furnace steel making or converters.
9. The method for realizing zero emission of all steelmaking from the iron and steel dust and sludge as claimed in claim 1, which is characterized in that: and casting the molten iron after melting into iron blocks for steelmaking or casting, and directly casting.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02117732 CN1212410C (en) | 2002-05-15 | 2002-05-15 | Method for realizing zero exhaust for fully steelmaking of steel dust and mud |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02117732 CN1212410C (en) | 2002-05-15 | 2002-05-15 | Method for realizing zero exhaust for fully steelmaking of steel dust and mud |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1458289A CN1458289A (en) | 2003-11-26 |
CN1212410C true CN1212410C (en) | 2005-07-27 |
Family
ID=29426646
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 02117732 Expired - Fee Related CN1212410C (en) | 2002-05-15 | 2002-05-15 | Method for realizing zero exhaust for fully steelmaking of steel dust and mud |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1212410C (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1312297C (en) * | 2004-12-10 | 2007-04-25 | 李增元 | Nickel-containing sponge iron, and its preparing method and method for producing nickel alloy billet |
CN100436610C (en) * | 2007-04-06 | 2008-11-26 | 中国科学院过程工程研究所 | Method of eliminating NOx in metallurgy sintering process |
CN102031361B (en) * | 2009-09-30 | 2013-03-13 | 鞍钢股份有限公司 | Comprehensive treatment and utilization method of iron and steel dust and mud |
CN101700955B (en) * | 2009-11-24 | 2011-08-03 | 马鞍山钢铁股份有限公司 | Dehydration and drying method and device of metallurgical slurry with no pollution |
CN102296138B (en) * | 2011-08-15 | 2013-07-31 | 陕西延长石油中陕金属矿业有限公旬 | Method for preparing ferrovanadium intermetallic compound and titanium slags by linear moving bed prereduction and shaft furnace melting process |
CN102776361A (en) * | 2012-06-12 | 2012-11-14 | 山西太钢不锈钢股份有限公司 | Method for producing sinter through utilizing stainless steel dedusting ash and stainless steel mill scale |
CN102816925A (en) * | 2012-08-24 | 2012-12-12 | 首钢总公司 | Method and system for recycling iron-containing sludge |
CN103526029B (en) * | 2013-09-27 | 2017-03-29 | 泰州永兴合金材料科技有限公司 | A kind of method that acid-washing stainless steel sludge prepares nichrome |
CN103468855B (en) * | 2013-09-30 | 2015-04-22 | 攀钢集团攀枝花钢钒有限公司 | Rotating furnace coolant, preparing method thereof and use method thereof |
CN103667572B (en) * | 2013-12-09 | 2015-12-02 | 东北大学 | The gas-based shaft kiln directly reduced smelting process of a kind of high-chromic vanadium-titanium ferroferrite |
CN104694758A (en) * | 2015-03-13 | 2015-06-10 | 宝钢发展有限公司 | Technique for comprehensively utilizing iron-containing dust mud |
CN106480309A (en) * | 2015-08-31 | 2017-03-08 | 鞍钢股份有限公司 | Dust and mud pellet for alkali metal removal treatment and preparation method thereof |
CN106544456A (en) * | 2015-09-17 | 2017-03-29 | 鞍钢股份有限公司 | Method for producing cold-pressed block for converter by using iron in blast furnace granulated slag |
CN107760808A (en) * | 2017-10-29 | 2018-03-06 | 长沙拓扑陆川新材料科技有限公司 | A kind of method that the pig iron is produced with scrap iron |
CN108672714A (en) * | 2018-04-24 | 2018-10-19 | 上海大学 | The method that alloy powder is directly prepared by cold rolling sludge |
CN110331295A (en) * | 2019-08-09 | 2019-10-15 | 通化建新科技有限公司 | It is a kind of metallurgy solid waste, dangerous waste handle hot-assembling method |
CN113736941B (en) * | 2021-08-19 | 2022-11-29 | 重庆赛迪热工环保工程技术有限公司 | Iron-containing dust and mud recycling method |
CN114774680A (en) * | 2022-04-24 | 2022-07-22 | 酒泉钢铁(集团)有限责任公司 | Mixed treatment method of Bayer process red mud and converter OG mud |
CN115679037B (en) * | 2023-01-05 | 2023-03-28 | 北京科技大学 | Self-circulation absorption and utilization method and system for steelmaking dust of electric arc furnace |
-
2002
- 2002-05-15 CN CN 02117732 patent/CN1212410C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1458289A (en) | 2003-11-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1212410C (en) | Method for realizing zero exhaust for fully steelmaking of steel dust and mud | |
CN101984080B (en) | Process and device for separating iron and aluminum silica slag from red mud and removing alkali metal | |
CN103468961B (en) | A kind of airtight cupola furnace process Steel Plant are containing zinc, lead powder dirt processing method | |
KR101158883B1 (en) | Self-reducing, cold-bonded pellets | |
CN101270410A (en) | Cold bonded pellet and method of producing the same | |
CN106755656A (en) | A kind of method that slag metallurgy one-step method is reclaimed | |
CN111485063B (en) | High-efficiency utilization process of aluminum ash in electrolytic aluminum plant | |
CN103451346B (en) | Copper smelting slag reduction method | |
CN102534199A (en) | Comprehensive utilization process of zinc-containing iron dust | |
CN111910072A (en) | Preparation and use methods of pre-reduced fluxed pellets with steel slag as partial raw material | |
WO2023130784A1 (en) | Additive for reducing roasting temperature of fluxed magnetite pellets and use method | |
CN113088607A (en) | Method for smelting and recovering iron, vanadium and sodium from red mud | |
CN107488784B (en) | A kind of blast furnace ironmaking superfluxed pellets and its production method | |
CN103952540B (en) | Ion dust mud contaning and high silicon iron concentrate is utilized to produce the technique of prereduced burden | |
CN101255484A (en) | Composite cooling agent for steel-smelting and production technique thereof | |
CN1037917C (en) | Technique for smelting ferrochrome using powdered Cr ore reductive sintered blocks | |
JPH10147806A (en) | Production of high quality reduced iron from ironmaking dust | |
CN201933128U (en) | Equipment for removing red-mud separated iron, aluminum-silicon slag and alkali metal | |
CN115710634A (en) | Method for treating sintering dust removal ash and waste coating of continuous casting tundish | |
RU2352648C2 (en) | Charge for manufacturing of bricks for metallurgical production | |
CN108642231B (en) | Converter slag modifier and method for preparing low-alkalinity slag system by using same | |
KR101017628B1 (en) | Reduced iron from mill scale and manufacturing method thereof | |
CN1804051A (en) | Dedusting magnesium iron ball and its application in electric furnace slag-making | |
CN111434783A (en) | Slag former for electric furnace steelmaking and manufacturing method thereof | |
CN113337673B (en) | Preparation method of converter steelmaking efficient dephosphorization agent |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |