CN106045301B - A method of producing mineral wool using converter molten state early period slag - Google Patents

A method of producing mineral wool using converter molten state early period slag Download PDF

Info

Publication number
CN106045301B
CN106045301B CN201610369708.3A CN201610369708A CN106045301B CN 106045301 B CN106045301 B CN 106045301B CN 201610369708 A CN201610369708 A CN 201610369708A CN 106045301 B CN106045301 B CN 106045301B
Authority
CN
China
Prior art keywords
slag
mineral wool
molten state
early period
converter
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.)
Active
Application number
CN201610369708.3A
Other languages
Chinese (zh)
Other versions
CN106045301A (en
Inventor
范鼎东
沈乾坤
邓爱军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Metallurgical Development In Science And Technology Co Ltd In East China Maanshan City
Anhui University of Technology AHUT
Original Assignee
Metallurgical Development In Science And Technology Co Ltd In East China Maanshan City
Anhui University of Technology AHUT
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Metallurgical Development In Science And Technology Co Ltd In East China Maanshan City, Anhui University of Technology AHUT filed Critical Metallurgical Development In Science And Technology Co Ltd In East China Maanshan City
Priority to CN201610369708.3A priority Critical patent/CN106045301B/en
Publication of CN106045301A publication Critical patent/CN106045301A/en
Application granted granted Critical
Publication of CN106045301B publication Critical patent/CN106045301B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C13/00Fibre or filament compositions
    • C03C13/06Mineral fibres, e.g. slag wool, mineral wool, rock wool

Abstract

The invention discloses a kind of methods producing mineral wool using converter molten state early period slag, belong to Slag Wool Production field.Converter molten state early period slag is poured into smelting furnace by the present invention, and reducing agent and modification agent are added in toppling process, restore quenched;After standing 0.5~1.5 hour after agitated mixing, slag of the temperature between 1380 DEG C~1430 DEG C is sent to cotton equipment processed and is processed into mineral wool.The present invention has given full play to the double dominant of molten state slag itself " slag " and " heat ", using ferrosilicon, aluminum shot as reducing agent, silicon, aluminium and reacting for ferriferous oxide are silicon thermal response, thermit reaction, can meet the heat supply for entirely restoring quenched process with a large amount of heat generation.Recrement is directly prepared into the mineral wool of high added value after recycling valuable element, comprehensively recyling for molten state slag is realized, not only solves the emission problem of slag, the production cost of mineral wool can also be reduced, there is preferable economy and environmental benefit.

Description

A method of producing mineral wool using converter molten state early period slag
Technical field
The present invention relates to Slag Wool Production fields, and converter molten state early period slag is utilized more specifically to a kind of The method for producing mineral wool.
Background technology
The sustainable development of steel industry need to break through the utilization of resources constraint bottleneck, slag as carry can resource, no matter its Using energy source, the utilization of resources, or it is not only urgent but also necessary as new inorganic non-metallic materials utilization.What converter smelting was toppled over Molten state slag has abundant high temperature thermal resource, metals resources and CaO, MgO, SiO2、Al2O3Equal useful components.Experiment It measuring, heat content when 1600 DEG C of slag is 2000KJ/kg, the releasable 1600-1800MJ/ tons of slag of 1 ton of liquid slag of water quenching cooling, It is equivalent to the heat of 55-61kg standard coals.
Currently, hot steel slag, other than small part returns to metallurgical process recycling, mainly still first passing through cooling medium will Slag is transformed into cold conditions from hot, is then used again.Cooling treatment is used to molten state slag, then carries out magnetic separation recovery gold The industrial flow of category, convenient for mechanization, technological process is simple, cost is relatively low.But be also easy to produce waste water, dust and pollute environment, and And the waste of slag high temperature resource and ferriferous oxide and tailings resource is also resulted in, belong to the lower treatment process of added value.
Mineral wool is to utilize slag or clinker, through soaring stove heat melting after being mixed with coke and adjusting material, using high speed from Staple shape inorfil made of the techniques such as heart method or blowing process, then using processes systems such as machine-shaping, solidification and cuttings At mineral wool product.Mineral wool production main fuel be coke, production one ton of mineral wool product take around consumption coke 250kg with On.Furnace cupola produces the high energy consumption of mineral wool and pollution is big due to the limitation of technique itself and equipment.It is produced using molten state slag On the one hand mineral wool takes full advantage of the sensible heat resource of molten state slag, on the other hand also steel slag resource " turns waste into wealth ", realizes The zero-emission of slag.In addition, also reduce the production cost of mineral wool, the further genralrlization application of mineral wool product has huge Economic benefit, social benefit and environmental benefit.
Through retrieval, also has more disclosure about the scheme for producing mineral wool using molten state clinker.Such as Chinese patent application Numbers 201410239791.3, the applying date is on May 30th, 2014, and invention and created name is:It is a kind of to utilize high temperature blast furnace slag and height The method of warm power plant's slag production mineral wool, this application by smelting iron and steel blast furnace high-temperature liquid state blast furnace slag and come from power plant High-temperature liquid state power plant slag be placed in smelting furnace, in a furnace heating, it is quenched after, reach ingredient needed for mineral wool product and high speed from Melt temperature needed for scheming>1400 DEG C, then high-temperature fusant enters back into high speed centrifugation and mineral wool fiber is made at cotton machine.This application Case is by directly utilizing high-temperature liquid state blast furnace slag and high-temperature liquid state power plant slag so that high-temperature liquid state blast furnace slag and power plant in steel plant The sensible heat of slag is utilized, and saves the energy expenditure of mineral wool production technology, also fully utilizes slag resource in steel plant.
Chinese Patent Application No. 201510250252.4, the applying date are on May 15th, 2015, and invention and created name is:One The melting method of kind liquid blast furnace production mineral wool;This application adds acid additives progress in liquid blast furnace slag ladle Quenched, the slag ladle for filling liquid blast furnace just heats under the electrodes, stirring of inert gas is blown in slag ladle bottom, then by liquid Blast furnace slag is poured into electric furnace, there is the liquid blast furnace of quenched good twice slag ladle, continuous heating heat preservation in electric furnace;Finally open Stove is slagged tap, and clinker is continuously sent to glass wool making machine and is processed into mineral wool.This application is relative to traditional furnace cupola and the high energy of kiln Consumption, the sensible heat of liquid blast furnace are utilized effectively, and blast furnace ironmaking is made effectively to be combined with the production technology of mineral wool.
Above-mentioned application case be can yet be regarded as a kind of good scheme that mineral wool is produced using molten state slag, but above-mentioned application case More focus has been placed on the higher blast furnace slag of recycling degree, and has been the sensible heat resource profit in molten state blast furnace slag It uses, is not particularly suited for containing (Fe at presentnO) it is up to 15%~30% slag difficult to deal with.Since the component of blast furnace slag limits System so that above-mentioned application case carries out slag quenched process, it is necessary to additional addition electric heater unit carries out heat supplement, and And there is no the specific method for proposing to recycle for metals resources in slag component in above-mentioned application case, the resource of slag can not be solved Change problem realizes the high value added utilization of slag.
Invention content
1. technical problems to be solved by the inivention
The present invention recycles existing insufficient for current molten state slag, provides and a kind of is melted early period using converter The method that state slag produces mineral wool;The present invention adds silicon, al reducing agent in converter molten state early period slag, to solve in slag The recycling of metals resources, and solve the benefit of heat using the chemical heat generated in the sensible heat and reduction reaction of molten state slag It gives;Contain SiO on a small quantity by addition2、Al2O3Substance is finely adjusted slag component, and mineral wool directly is made in slag, realizes The high value added utilization of tailings.While slag is turned waste into wealth, also reduces the production cost of mineral wool, improves iron and steel enterprise Comprehensive benefit, but also can reduce environmental pollution, the benign cycle of the ecosystem is maintained, realizes society, economy and environment Win-win.
2. technical solution
In order to achieve the above objectives, technical solution provided by the invention is:
A kind of method producing mineral wool using converter molten state early period slag of the present invention, step are:By converter early period Molten state slag is poured into smelting furnace, and reducing agent and modification agent are added in toppling process, restore quenched;It is agitated mixed After standing 0.5~1.5 hour after even, slag of the temperature between 1380 DEG C~1430 DEG C is sent to cotton equipment processed and is processed into mine Cotton, remaining solid-state bloom return in converter.
Further, the raw material for producing mineral wool includes the converter molten state early period steel that mass percent is 70%~90% Slag, 5%~10% reducing agent and 5%~20% modification agent.
Further, the converter molten state early period slag include following mass percent component CaO 30~ 50%, SiO215~30%, FeO 10~30%, MgO 2~10%, Al2O31~5%.
Further, the converter molten state early period slag is the deslagging that the double slags of converter stay slag method, and temperature exists Between 1350 DEG C~1500 DEG C, basicity of slag is between 1.0~2.0.
Further, the reducing agent is made of the mixing of one or both of ferrosilicon, aluminum shot, the granularity of reducing agent For 5~50mm.
Further, the modification agent is to contain SiO2、Al2O3One or more mixing composition in substance, modification The granularity of agent is 5~20mm.
Further, described to contain SiO2、Al2O3Substance is cullet, clay, flyash or red mud.
Further, add reducing agent and modification agent restore it is quenched after in slag FeO content 5% hereinafter, Acidity coefficient (SiO2+Al2O3)/(CaO+MgO) it is 1.1~1.6.
Further, the smelting furnace number is that each converter is equipped with 2~5.
Further, the smelting furnace is improved slag ladle, and the shell of smelting furnace is steel plate, and inner wall is fire resistant heat preserving stove Lining.
3. advantageous effect
Using technical solution provided by the invention, compared with existing known technology, there is following remarkable result:
(1) of the invention " a method of producing mineral wool using converter molten state early period slag ", from resource utilization degree Lower slag is started with, and the efficient Utilizing question for molten state low alkalinity slag early period that converter smelting is toppled over is solved.In abundant profit While with metallurgical slag thermal resource, recycled metals resources, realized the high value added utilization of tailings, by slag change give up into Treasured reduces the production cost of mineral wool, improves iron and steel enterprise's comprehensive benefit, but also can reduce environmental pollution, and maintains ecosystem The win-win of society, economy and environment is realized in the benign cycle of system;
(2) of the invention " a method of producing mineral wool using converter molten state early period slag ", technological process is simple, through also The former quenched ingredient and temperature requirement that can be very good to meet mineral wool production, and by the cooperation of modification agent, acidity can be expanded The mineral wool glassy state of the quenched range of coefficient, preparation is good, and at fine rate height, acidity coefficient adjustable extent is wide, can meet various The market demand of change;
(3) of the invention " a method of producing mineral wool using converter molten state early period slag ", using in ferrosilicon, aluminum shot One or two are used as reducing agent, silicon, aluminium to be reacted for silicon thermal response, thermit reaction, the adjoint a large amount of heat of meeting with ferriferous oxide It generates, the heat supply for entirely restoring quenched process can be met;Simultaneously using the ferriferous oxide in silicon, aluminium reducing slag, temperature At 1350 DEG C or more, reduction rate can reach 98% or more;And the product that silicon, aluminium are reacted with ferriferous oxide is SiO2、Al2O3, While reducing modification agent addition, the product for restoring generation helps to improve the acidity of melt, but also slag composition Homogenization is more smooth;
(4) of the invention " a method of producing mineral wool using converter molten state early period slag ", stay slag using the double slags of converter One deslagging of method, temperature is between 1350 DEG C~1500 DEG C, and for basicity of slag between 1.0~2.0, the converter basicity of slag in the period is low And stable components, contribute to the production of mineral wool;
(5) present invention " a method of using converter molten state early period slag produce mineral wool ", 2 are equipped with for each converter~ 5 smelting furnaces can be very good the discontinuity for solving converter deslagging and mineral wool continuous production under the cooperation of 2~5 smelting furnaces Contradiction.
Description of the drawings
Fig. 1 is process flow diagram of the present invention using converter molten state early period slag production mineral wool.
Specific implementation mode
To further appreciate that present disclosure, the present invention is described in detail in conjunction with the accompanying drawings and embodiments.
A kind of method producing mineral wool using converter molten state early period slag of the present invention, raw material is mainly by following quality hundred The group than meter is divided to be grouped as:70%~90% converter molten state early period slag, 5%~10% reducing agent and 5%~20% Modification agent.The converter molten state early period slag is the deslagging that the double slags of converter stay slag method, i.e., by upper stove terminal slag Part or all is stayed in stove, then in blowing 3~5 minutes or so, the slag that the when of falling stove pours out for the first time.Slag temperature at this time Degree is between 1350 DEG C~1500 DEG C, and for basicity of slag between 1.0~2.0, the mass percent of key component is as follows:CaO is 30 ~50%, SiO2For 15~30%, FeO be 10~30%, MgO it is 2~10%, Al2O3It is 1~5%.Compared to converter finishing slag For, converter molten state early period slag temperature and ingredient are all more stable so that the reduction of ferriferous oxide and the hot tune of tailings Matter is more prone to carry out, and contributes to the production of mineral wool.
The step of carrying out mineral wool production using converter molten state early period slag is as follows:
During converter molten state early period slag is poured into smelting furnace, going back for above-mentioned mass percent is added into smelting furnace Former agent and modification agent restore quenched.For meet mineral wool production ingredient and temperature requirement, reduction it is quenched after slag in FeO Content 5% hereinafter, acidity coefficient (SiO2+Al2O3)/(CaO+MgO)=1.1~1.6, the symbology ingredient of oxide In various oxides mass percent.It is small that 0.5~1.5 is stood after stirring and evenly mixing the ingredient reached needed for mineral wool product When, keep the ingredient of slag uniform, realizes the separation of slag and metal, finally the slag by temperature between 1380 DEG C~1430 DEG C It send to cotton equipment processed and is processed into mineral wool, remaining solid-state bloom returns in converter.
The reducing agent of the present invention is made of the mixing of one or both of ferrosilicon, aluminum shot, and granularity is 5~50mm.Use silicon Iron or aluminum shot are as reducing agent, although the cost of reducing agent itself is higher, silicon, aluminium react for silicon heat instead with ferriferous oxide It answers, thermit reaction, can be generated with a large amount of heat;Silicon, aluminium reacted with ferriferous oxide release chemical reaction heat can meet it is whole The heat of a flow is fed, and can be calculated by the heat budget of whole flow process, and heat income is mainly silicon heat, aluminium The heat of heat and molten state slag;The expenditure heat of slag heating after modification agent is mainly added in heat expenditure, and slag pours into slag Slag heat dissipation etc. when tank in the heat absorption of slag ladle wall surface and reaction process, heat budget in whole process calculates as follows:
(1) during with ferrosilicon, aluminium fusion reduction reaction occurs for slag, the chemical reaction being related to is as follows:
2 (FeO)+Si=(SiO2)+2Fe
3 (FeO)+2Al=(Al2O3)+3Fe
The heat that ferrosilicon process, aluminothermic process generate can use formula:It calculates, Wherein ∑ M is the sum of the molal weight of original charging calculated by chemical reaction quantitative relation.
For n mol substances, under constant-pressure conditions, by temperature T1It is increased to T2Process institute calorific requirement can be calculated by following formula:
(2) reduction reaction heat is taken in:
Si reduction heat is taken in:
Aluminium reducing heat is taken in:
(3) reduction reaction heat is paid:
Data checks in:The specific heat of converter slag is 1.25kJ/kg. DEG C, and molten steel specific heat is 0.85kJ/kg. DEG C, modification agent Specific heat presses 0.7kJ/kg. DEG C.
So using silicon, aluminium as reducing agent, by adjusting the ratio of silicon, aluminium, the heat of generation can make slag heat up 100 DEG C~300 DEG C or so, the heat supply of whole flow process can be met completely.
Simultaneously using the ferriferous oxide in silicon, aluminium reducing slag, for temperature at 1350 DEG C or more, reduction rate can reach 98% More than.And the product that silicon, aluminium are reacted with ferriferous oxide is SiO2、Al2O3, while reducing modification agent addition, reduction generates Product help to improve the acidity of melt, but also the homogenization of slag composition is more smooth;The granularity of reducing agent is controlled In 5~50mm, then contribute to the addition of reducing agent and the progress of reduction reaction.
The modification agent of the present invention is to contain SiO2、Al2O3In substance one or more mixing composition, granularity be 5~ 20mm contains SiO2、Al2O3Cullet, clay, flyash or red mud specifically may be used in substance.The main mesh that modification agent is added Be to adjust the acidity coefficient of mineral wool, the basicity of converter molten state early period slag is between 1.0~2.0, in order to meet acid The requirement for spending coefficient needs that acidic oxide is added, and the present invention mainly utilizes SiO2、Al2O3To adjust.What the present invention used contains There is SiO2、Al2O3Substance such as cullet, clay, flyash or red mud have many advantages, such as that price is low, applicability is good, easy acquisition, and Steel plant can be cut down to a certain extent and contain SiO2、Al2O3Solid waste.The granularity control of modification agent 5~ 20mm, mainly inventor are summarized in production practice, when modification agent granularity is more than 20mm, are unfavorable for the thawing of modification agent, with And ingredient is uniform, to the hot quenched unfavorable of mineral wool, modification agent granularity is less than 5mm, and modification agent can be caused to be not easy to be added, together When will produce dust pollution.
Since 100 tons of converters about each hour goes out slag twice, slag tap every time about 6~8 tons, an annual output For the production line of 80,000 tons of mineral wool, 9 tons or so of materials per hour, so reach mineral wool production line per tank slag makes for 0.5 hour With, after 0.5 hour, the slag of next tank need to restore it is quenched finish, therefore the present invention is each converter be equipped with 2~5 smelting furnaces, one The mineral wool production line that annual output is 80,000 tons, to solve the contradiction of the discontinuity and mineral wool continuous production of converter deslagging.Smelting furnace Using improved slag ladle, shell is steel plate, and inner wall is that fire resistant heat preserving furnace lining also can while extending smelting furnace service life Enough reduce the production cost of mineral wool.
The present invention realizes the high value added utilization of tailings, and reducing agent is used as using one or both of ferrosilicon, aluminum shot, It is fed using reduction reaction heat to meet the heat of whole flow process, can recycle the metal in slag to greatest extent, low using price, The steel mill's solid-state castoff easily obtained improves iron and steel enterprise's comprehensive benefit as modification agent;And technological process is simple, through reduction The quenched ingredient and temperature requirement that can be very good to meet mineral wool production, and by the cooperation of modification agent, acidity system can be expanded The mineral wool glassy state of several quenched ranges, preparation is good, and at fine rate height, acidity coefficient adjustable extent is wide, can meet diversification The market demand.
Embodiment 1
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", raw material forms quality percentage Than for:80% converter molten state early period slag, 15% reducing agent, 5% modification agent.Converter molten state early period slag includes as follows The component of mass percent:CaO 37%, SiO229%, FeO 25%, MgO 4%, Al2O33%.Reducing agent is ferrosilicon, aluminium The mixture of grain, granularity are 10~30mm.Modification agent is cullet, and granularity is 5~20mm.
In conjunction with Fig. 1, the present embodiment production mineral wool the step of be:
(1) the double slags of converter that basicity of slag is 1.3 are stayed a deslagging of slag method, are poured into smelting furnace by temperature at 1400 DEG C or so In, each converter is equipped with 3 smelting furnaces, and slag adds the mixture of reducing agent ferrosilicon, aluminum shot, and modification during being placed in smelting furnace The reduction of agent cullet is quenched;
(2) it at transport to agitating device, stirs and evenly mixs, 0.5 hour is stood after reaching the ingredient needed for mineral wool product;
(3) by temperature at 1420 DEG C or so, the slag for meeting cotton ingredient processed send to cotton equipment processed and is processed into raw cotton;
(4) remaining solid-state bloom returns in converter, and mineral wool board, mineral wool felt, mineral wool pipe are obtained after raw cotton machine-shaping Or other mineral wool products.The testing result of raw cotton:Acidity coefficient is close to 1.6.
Embodiment 2
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", raw material forms quality percentage Than for:80% converter molten state early period slag, 10% reducing agent, 10% modification agent, converter molten state early period slag include such as The component of lower mass percent:CaO 45%, SiO225%, FeO 20%, MgO 5%, Al2O32.5%.Reducing agent is silicon Iron, granularity are 10~30mm.Modification agent is clay, and granularity is 5~20mm.
In conjunction with Fig. 1, the present embodiment production mineral wool the step of be:
(1) the double slags of converter that basicity of slag is 1.8 are stayed a deslagging of slag method, are poured into smelting furnace by temperature at 1420 DEG C or so In, each converter is equipped with 4 smelting furnaces, and smelting furnace is improved slag ladle, and shell is steel plate, and inner wall is fire resistant heat preserving furnace lining.Slag Reducing agent ferrosilicon is added during being placed in smelting furnace and the reduction of modification agent clay is quenched;
(2) it at transport to agitating device, stirs and evenly mixs, 1 hour is stood after reaching the ingredient needed for mineral wool product;
(3) by temperature at 1430 DEG C or so, the slag for meeting cotton ingredient processed send to cotton equipment processed and is processed into raw cotton;
(4) remaining solid-state bloom returns in converter, and mineral wool board, mineral wool felt, mineral wool pipe are obtained after raw cotton machine-shaping Or other mineral wool products.The testing result of raw cotton:Acidity coefficient is close to 1.7.
Embodiment 3
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", raw material forms quality percentage Than for:85% converter molten state early period slag, 9% reducing agent, 6% modification agent, converter molten state early period slag include as follows The component of mass percent:CaO 41%, SiO229%, FeO 18%, MgO 6%, Al2O33%.Reducing agent is aluminum shot, grain Degree is 10~30mm.Modification agent is flyash, and granularity is 5~20mm.
In conjunction with Fig. 1, the present embodiment production mineral wool the step of be:
(1) the double slags of converter that basicity of slag is 1.4 are stayed a deslagging of slag method, are poured into smelting furnace by temperature at 1450 DEG C or so In, each converter is equipped with 5 smelting furnaces, and slag adds reducing agent aluminum shot during being placed in smelting furnace and the reduction of modification agent flyash is adjusted Matter;
(2) it at transport to agitating device, stirs and evenly mixs, 1.5 hours is stood after reaching the ingredient needed for mineral wool product;
(3) by temperature at 1400 DEG C or so, the slag for meeting cotton ingredient processed send to cotton equipment processed and is processed into raw cotton;
(4) remaining solid-state bloom returns in converter, and mineral wool board, mineral wool felt, mineral wool pipe are obtained after raw cotton machine-shaping Or other mineral wool products.The testing result of raw cotton:Acidity coefficient is close to 1.4.
Embodiment 4
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", substantially with embodiment 1, no It is with place:Modification agent is the mixture of cullet and clay in the present embodiment.
Embodiment 5
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", substantially with embodiment 1, no It is with place:Modification agent is the mixture of cullet, clay and flyash in the present embodiment.
Embodiment 6
The present embodiment " a method of producing mineral wool using converter molten state early period slag ", substantially with embodiment 1, no It is with place:Modification agent is the mixture of cullet, clay and red mud in the present embodiment.
A kind of method producing mineral wool using converter molten state early period slag described in Examples 1 to 6, has given full play to molten The double dominant for melting state slag itself " slag " and " heat " is adding suitable reducing agent, modification agent, will be remaining after recycling valuable element Slag is directly prepared into high added value mineral wool, realizes comprehensively recyling for molten state slag, and the discharge for not only solving slag is asked Topic, can also reduce production cost, avoid the wasting of resources, have preferable economy and environmental benefit.
Schematically the present invention and embodiments thereof are described above, description is not limiting, institute in attached drawing What is shown is also one of embodiments of the present invention, and actual structure is not limited to this.So if the common skill of this field Art personnel are enlightened by it, without departing from the spirit of the invention, are not inventively designed and the technical solution Similar frame mode and embodiment, are within the scope of protection of the invention.

Claims (6)

1. a kind of method producing mineral wool using converter molten state early period slag, step are:By converter molten state early period slag It is poured into smelting furnace, and adds reducing agent and modification agent in toppling process, restore quenched;It is stood after agitated mixing After 0.5~1.5 hour, slag of the temperature between 1380 DEG C~1430 DEG C is sent to cotton equipment processed and is processed into mineral wool, it is remaining Solid-state bloom returns in converter;
The raw material of production mineral wool includes the converter molten state early period slag that mass percent is 70%~90%, 5%~10% Reducing agent and 5%~20% modification agent;
The converter molten state early period slag includes the component of following mass percent:CaO 30~50%, SiO215~ 30%, FeO 10~30%, MgO 2~10%, Al2O31~5%;
The reducing agent is made of the mixing of one or both of ferrosilicon, aluminum shot, and the granularity of reducing agent is 5~50mm.
2. a kind of method producing mineral wool using converter molten state early period slag according to claim 1, it is characterised in that: The converter molten state early period slag is the deslagging that the double slags of converter stay slag method, and temperature is between 1350 DEG C~1500 DEG C, slag Basicity is between 1.0~2.0.
3. a kind of method producing mineral wool using converter molten state early period slag according to claim 2, it is characterised in that: The modification agent is one kind in cullet, clay, flyash, red mud, or by cullet, clay, flyash, red mud The granularity of a variety of mixing compositions, modification agent is 5~20mm.
4. a kind of method producing mineral wool using converter molten state early period slag according to claim 2, it is characterised in that: Addition reducing agent and modification agent restore it is quenched after in slag FeO content 5% hereinafter, acidity coefficient (SiO2+Al2O3)/ (CaO+MgO) it is 1.1~1.6.
5. a kind of method producing mineral wool using converter molten state early period slag according to claim 4, it is characterised in that: The smelting furnace number is that each converter is equipped with 2~5.
6. a kind of method producing mineral wool using converter molten state early period slag according to claim 5, it is characterised in that: The smelting furnace is improved slag ladle, and the shell of smelting furnace is steel plate, and inner wall is fire resistant heat preserving furnace lining.
CN201610369708.3A 2016-05-25 2016-05-25 A method of producing mineral wool using converter molten state early period slag Active CN106045301B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610369708.3A CN106045301B (en) 2016-05-25 2016-05-25 A method of producing mineral wool using converter molten state early period slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610369708.3A CN106045301B (en) 2016-05-25 2016-05-25 A method of producing mineral wool using converter molten state early period slag

Publications (2)

Publication Number Publication Date
CN106045301A CN106045301A (en) 2016-10-26
CN106045301B true CN106045301B (en) 2018-10-12

Family

ID=57171993

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610369708.3A Active CN106045301B (en) 2016-05-25 2016-05-25 A method of producing mineral wool using converter molten state early period slag

Country Status (1)

Country Link
CN (1) CN106045301B (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106946484B (en) * 2017-03-23 2018-12-21 华北理工大学 A method of utilizing suspension flyash Treated By Modified Slag cotton
CN108117253A (en) * 2017-12-08 2018-06-05 宁夏吉元君泰新材料科技有限公司 A kind of hardening and tempering method of silicon manganese slag production mineral wool
CN108264224A (en) * 2017-12-30 2018-07-10 王虎 A kind of smelting process that slag is smelted into mineral wool material in convertor steelmaking process
CN108863039A (en) * 2018-05-29 2018-11-23 宁夏吉元冶金集团有限公司 A kind of method of ferronickel liquid hot slag production granulated wool
CN110055370B (en) * 2019-04-30 2021-06-04 马鞍山钢铁股份有限公司 High-temperature steel slag modifier and modification pretreatment process
CN110255914A (en) * 2019-06-12 2019-09-20 内蒙古普泽新材料科技有限公司 A kind of preparation process of solid waste silicon manganese slag production mineral wool
CN110240437B (en) * 2019-07-09 2021-10-22 鞍钢股份有限公司 Tempering agent for melting blast furnace slag and preparation method thereof
CN110218827A (en) * 2019-07-09 2019-09-10 鞍钢股份有限公司 A kind of molten blast furnace slag adjusting material and its preparation, application method
CN110669935A (en) * 2019-10-29 2020-01-10 北京大学 Process for multi-component separation and tailing quenching and tempering utilization of red mud
CN114105506A (en) * 2020-08-26 2022-03-01 宝山钢铁股份有限公司 Steel slag modifier and steel slag thermal modification treatment process
CN114105505A (en) * 2020-08-26 2022-03-01 宝山钢铁股份有限公司 Steel slag modifier and steel slag modification treatment process
CN112374764A (en) * 2020-11-26 2021-02-19 中冶华天南京工程技术有限公司 Method for preparing mineral wool by thermal state tempering of molten steel slag
CN112960917B (en) * 2021-01-28 2022-11-08 天津水泥工业设计研究院有限公司 Method for on-line adjusting slagging alkalinity of smelting reduction furnace by using construction waste
CN114058744B (en) * 2021-10-20 2023-03-17 首钢集团有限公司 Method for modifying slag
CN115747390A (en) * 2022-11-28 2023-03-07 凉山瑞京环保资源开发有限公司 Method for preparing mineral wool by quenching and tempering steel slag reducing slag

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1400181A (en) * 2002-09-02 2003-03-05 严煜 Method for hot-charging, smelting and producing mineral wool fibre by adopting blast furnace
CN101704631A (en) * 2009-11-13 2010-05-12 北京大学 Method for manufacturing slag fiber by using thermal-state blast furnace slag
CN101792255A (en) * 2010-02-08 2010-08-04 杨锦耀 Method for preparing inorganic fiber fused mass from blast furnace molten slag
CN102698634A (en) * 2012-05-25 2012-10-03 安徽工业大学 Device and method for homogenizing high-temperature melt
CN102796833A (en) * 2012-08-06 2012-11-28 上海宝冶钢渣综合开发实业有限公司 Modification technology of iron reduction and component reconstruction for molten slag
CN103803793A (en) * 2013-11-18 2014-05-21 河北联合大学 Method for preparing inorganic fibers by using direct blowing of blast furnace molten slag

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1400181A (en) * 2002-09-02 2003-03-05 严煜 Method for hot-charging, smelting and producing mineral wool fibre by adopting blast furnace
CN101704631A (en) * 2009-11-13 2010-05-12 北京大学 Method for manufacturing slag fiber by using thermal-state blast furnace slag
CN101792255A (en) * 2010-02-08 2010-08-04 杨锦耀 Method for preparing inorganic fiber fused mass from blast furnace molten slag
CN102698634A (en) * 2012-05-25 2012-10-03 安徽工业大学 Device and method for homogenizing high-temperature melt
CN102796833A (en) * 2012-08-06 2012-11-28 上海宝冶钢渣综合开发实业有限公司 Modification technology of iron reduction and component reconstruction for molten slag
CN103803793A (en) * 2013-11-18 2014-05-21 河北联合大学 Method for preparing inorganic fibers by using direct blowing of blast furnace molten slag

Also Published As

Publication number Publication date
CN106045301A (en) 2016-10-26

Similar Documents

Publication Publication Date Title
CN106045301B (en) A method of producing mineral wool using converter molten state early period slag
CN106191344B (en) A kind of method for mixing the production of slag melting and reducing and modifier treatment
CN106348626B (en) A method of recycling converter molten state slag is to produce concrete admixture
CN103553337A (en) Sintering process method and device for producing microcrystalline glass by using blast furnace slag
CN104909540A (en) Melting method for production of mineral wool from liquid blast furnace slag
CN101559953A (en) Method for using high-temperature liquid silicon manganese alloy slag as raw material to produce cast stone
CN101684507B (en) Direct steel making technique by reducing iron ore with gas
CN101531454B (en) A mineral wool boiling melting method of directly using grainy waste slag and coal
CN102674856B (en) Method for preparing tundish fireproof spray paint by using steel slag tailings
CN104556702A (en) Method for preparing high-alkalinity glass ceramic from metallurgical slag
CN106086608A (en) A kind of method utilizing carbon manganese slag to produce low Carbon Manganese silicon alloy
CN104673965B (en) A kind of online method of modifying of liquid steel slag
CN103643056B (en) The smelting process of low carbon ferromanganese
CN102994688B (en) Pretreatment technology of terminal steel slag in converter
CN110453025A (en) A kind of method that high calcium v-bearing steel slag smelts the rich vanadium pig iron
CN103555874A (en) Thermal refining method of blast furnace hot slags
CN105217947A (en) A kind of method utilizing high temperature blast furnace slag and high temperature power plant slag slag wool production
Chen et al. Review of pellets and blast furnace slag research progress: The effects of MgO on metallurgical properties
CN103643094B (en) The smelting process of high carbon ferromanganese
CN101469378B (en) Method for preparing alsifer from high-alumina fly ash and magnetic beads
CN102251115B (en) Method for producing high-carbon manganese-iron alloy from high-alkalinity manganese ore
CN102146500A (en) Fluxing agent for smelting steel as well as preparation and use methods thereof
CN108504799B (en) The method of finishing slag FeO content is reduced in a kind of modification of melt vessel slag
CN106467935A (en) A kind of copper ashes and the Application way of carbide slag
CN100564546C (en) A kind of earlier stage slag-smelting method for pre-smelting electric furnace

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant