CN202530095U - Centrifugal molten slag dry granulation and waste heat recovery power generation system - Google Patents
Centrifugal molten slag dry granulation and waste heat recovery power generation system Download PDFInfo
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- CN202530095U CN202530095U CN2012200415665U CN201220041566U CN202530095U CN 202530095 U CN202530095 U CN 202530095U CN 2012200415665 U CN2012200415665 U CN 2012200415665U CN 201220041566 U CN201220041566 U CN 201220041566U CN 202530095 U CN202530095 U CN 202530095U
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/022—Methods of cooling or quenching molten slag
- C21B2400/026—Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/034—Stirring or agitating by pressurised fluids or by moving apparatus
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/052—Apparatus features including rotating parts
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/052—Apparatus features including rotating parts
- C21B2400/054—Disc-shaped or conical parts for cooling, dispersing or atomising of molten slag rotating along vertical axis
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/08—Treatment of slags originating from iron or steel processes with energy recovery
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
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Abstract
The utility model provides a centrifugal molten slag dry granulation and waste heat recovery power generation system and belongs to the technical field of ferrous metallurgy slag treatment and waste energy recovery. The system comprises a slag receiving device, a slag centrifugation quenching granulation device, a slag annealing device, a waste heat recovery power generation device and a waste gas purification device. Molten slag is subjected to quenching granulation by using the unique centrifugation granulation device, is quenched to be in a glassy state, and is further annealed by using a water cooling type vibration grate; and waste heat recovered by quenching and annealing flows through a double channel type waste heat boiler to produce steam so as to push a steam turbine generator unit to do work to generate power. By the system, the centrifugation granulation device can safely and stably run at high temperature for a long time, the quenching and dry granulation of the molten slag can be smoothly realized, and the high-temperature waste heat resources of the slag can be fully and efficiently recycled on the basis of not influencing subsequent utilization value.
Description
Technical field
The utility model belongs to ferrous metallurgy slag treatment and complementary energy recovery technology field, particularly relates to a kind of centrifugal molten slag dry type granulation and waste heat recovery generating system.
Background technology
Show that according to data the energy consumption of China Steel industry accounts for the 10-15% of national total energy consumption, in Iron and Steel Production, can produce a large amount of slags, one ton of pig iron of every production is wanted by-product 0.3-0.6 ton blast furnace slag, and one ton of steel of every production are wanted 0.13 ton of slag of by-product.The initial temperature of above-mentioned molten slag is rich in a large amount of sensible heat resources up to 1400-1600 ℃, if be not used or direct shrend, then the serious waste energy and pollution of ecological environment.
In China, the main application of blast furnace slag is to make the adulterant of cement, so water quenching is topmost mode.Water quenching is a kind of traditional blast furnace slag quench treatment process, is about to molten slag and places cold slag bath, and slag is met sharply cooling and granular of water, grabs out with crane through the slag bath post precipitation to place on the yard.Water quenching mainly contains Yin Bafa, figure daraf(reciprocal of farad), end filter method, Lhasa method etc.The major defect of water quenching has: the new water of (1) mass consumption, waste water resource; (2) do not reclaim the slag sensible heat, the serious waste residual heat resources; (3) atmospheric pollution (SO
2, H
2Gaseous sulphides such as S); (4) the system maintenance work amount is big; (5) during grinding, grain slag must be dried, and still wants consumes energy.
There is above shortcoming in blast furnace water quenching treatment technology based on traditional; Abroad (like Japan, Britain etc.) are from the eighties of last century development and use dry process blast furnace slag that just begins one's study the eighties; This method not only can be practiced thrift new water significantly; The sensible heat of blast furnace slag can also be reclaimed, in addition, the same effect of traditional water treatment blast furnace slag can be reached behind the blast furnace slag granulation.Can be divided into physics recovery of heat method and chemical heat absorption method according to the melting slag waste heat recovery technology, wherein the former is according to the difference of slag pre-treating process, is divided into drum process, wind quench method, continuous casting type waste heat boiler method, revolving cup method and mechanical mixing method again; The chemical heat absorption method is utilized melting slag heat, with slag heat through the endothermic chemical reaction recovery that is used, like methane vapor reforming reacted H
2And CO, and coal gasification reaction.
Domestic in China; The scholar concentrates research revolving cup or plate-spinning centrifugal granulation method to handle molten slag mostly; According to documents such as its paper of having delivered, patents; All stay in theoretical investigation or small-sized simulated experiment stage, the method and technology of effective industrialized slag chilling granulation and waste heat recovery also do not occur.At present, the centrifugal granulation method is better in molten slag granulation effect, but very undesirable aspect chilling effect and afterheat of slags recovery thermo-efficiency.And under long-time hot conditions, the transmission and the lubrication problem of centrifugal granulation device are not well solved.
At present, the waste heat of molten slag is unique high-temperature residual heat resource that is not used effectively in the iron and steel enterprise.Efficiently, reclaim the metallurgy melting afterheat of slags high-qualityly and will become the important means that iron and steel enterprise reduces comprehensive energy consumption.
Summary of the invention
Deficiency to existing centrifugal dry type chilling granulation technique; According to the requirement of molten slag chilling dry type granulation and the characteristic of slag; The utility model provides a kind of centrifugal molten slag dry type granulation and waste heat recovery generating system, to reach the purpose of effective chilling granulation molten slag and recovery high-temperature residual heat resource.
For realizing the foregoing invention purpose, the technical scheme that the utility model adopts is following:
A kind of centrifugal molten slag dry type granulation and waste heat recovery generating system comprise connecing slag device, the centrifugal chilling granulating device of slag, slag annealing device, exhaust heat recovery power generation device and exhaust gas purification and treatment device:
The said slag device that connects is by connecing slag ladle and slag ladle is formed;
The centrifugal chilling granulating device of said slag is made up of heat pipe axle, revolving cup, phonomoter and a gas blower etc., and wherein, heat pipe axle one end is connected with revolving cup and places in the centrifugal granulation stove, and the heat pipe axle the other end links to each other with water-cooling jacket and places outside the centrifugal granulation stove; Phonomoter links to each other with transmission mechanism, and transmission mechanism is connected with said heat pipe axle and places outside the centrifugal granulation stove; Said heat pipe axle is connected through the noncontact of magnetic ring group with high-temperature bearing on the centrifugal granulation stove; Bottom in the said centrifugal granulation stove is provided with air distribution plate, and a said gas blower is connected with the air distribution plate inlet;
Said slag annealing device mainly comprises cooler, uses water-cooled vibration comb bed in the cooler; The slag inlet of said cooler links to each other with said centrifugal granulation stove through the slag diversion trench, and the cooling air intake of cooler links to each other with the secondary gas blower; The afterbody of said cooler is provided with broken slag device;
Said exhaust heat recovery power generation device mainly comprises waste heat boiler, turbine, generator, condenser, cooling tower and thermal deaerator; Said waste heat boiler comprises membrane wall, drum, two stage superheater, primary superheater, secondary evaporimeter, one-level vaporizer, economizer and forced circulation pump; The high-temperature residual heat suction opening of said centrifugal granulation stove is connected with the high temperature inlet of waste heat boiler through the high temperature airduct; The middle temperature waste heat suction opening of said cooler is connected with the middle temperature inlet of waste heat boiler through middle temperature airduct; The temperature inlet is positioned at the primary superheater below in the said waste heat boiler; Set gradually said two stage superheater, primary superheater, secondary evaporimeter, one-level vaporizer and economizer in the said waste heat boiler from top to bottom; Said two stage superheater is connected with the main inlet throttle-stop valve of turbine through the female pipe of main steam, and said turbine links to each other with generator; The exhaust steam outlet of said turbine links to each other with condenser, and the hot well of condenser links to each other with the inlet of condensate pump; The pond, bottom of said cooling tower links to each other with the recirculated cooling water pump, and the recirculated cooling water pump links to each other with the cooling water inlet of said condenser, and the cooling water outlet of said condenser links to each other with the top of cooling tower; Said condensed water pump outlet is connected with the inlet of thermal deaerator; The pipe of boiler feedwater simultaneously also is connected with the inlet of said thermal deaerator; The outlet of thermal deaerator links to each other with the inlet of waste heat boiler service pump, and waste heat boiler feedwater pump outlet links to each other with the inlet of said economizer;
Said exhaust gas purification and treatment device comprises electrostatic precipitator, induced draft fan and chimney; The lingering remnants of past customs mouth of the smoke outlet of said waste heat boiler and cooler links to each other with the inlet of electrostatic precipitator; The outlet of electrostatic precipitator links to each other with the inlet of induced draft fan, and the outlet of induced draft fan links to each other with chimney.
Be provided with water-cooling jacket at heat pipe axle cold junction, can play the effect of protection heat pipe axle, produced simultaneously hot water can heat or freeze.Be connected through the magnetic ring group is contactless between heat pipe axle and the high-temperature bearing, realize the high-temperature bearing operation steady in a long-term under the hot conditions.In addition, the centrifugal granulation stove can adopt high temperature, gravity type boat davit, stainless steel-sodium heat pipe axle, to realize long lifetime, the safe operation of granulating device under hot conditions.The appearance that connects slag ladle and slag ladle is all laid heat-insulating protective layer; Heat-insulating protective layer is laid in the outside of centrifugal granulation stove, and the high-temperature wearable layer is laid in its inboard.
The utility model utilizes the method for above-mentioned power generation system: after the molten slag that blast furnace ironmaking produces separates through scum; Collect and be transported to slag ladle by the described slag ladle that connects; Through the slag chute on the slag ladle slag is caused on the revolving cup in the centrifugal granulation stove again; The cf-that produces through the revolving cup high speed rotating is with the molten slag granulation and throw away, and the cooling air cooling with gas blower feeds is chilled to glassy particles; Slag granules behind the chilling is dropped on the water-cooled vibration comb bed by the slag diversion trench utilizes the secondary gas blower slowly to cool off; Fully the cooled slag granules of heat exchange drops down onto feed bin after the cooler afterbody is further handled through crushing system, through chain conveyor the slag of handling well is delivered to stockyard at last; High-temp waste gas is delivered to waste heat boiler high temperature inlet from centrifugal granulation stove high-temperature residual heat suction opening through the high temperature airduct; In warm waste gas warm waste heat suction opening from cooler cover in the waste heat boiler temperature inlet through middle temperature airduct; Waste heat boiler produces sub-high pressure time high-temperature steam, and steam is used for promoting the turbo-generator generating; After the waste gas that the lingering remnants of past customs of cooler and waste heat boiler are discharged mixes, handle the back through the chimney discharge through electrostatic precipitator.
The advantage of the utility model is following:
1. utilize heat pipe axle and non-contact type magnetic ring, solved the mechanical transmission problem of centrifugal granulation equipment under hot conditions, guarantee long lifetime, the safe and stable operation of granulating device.
2. the centrifugal granulation stove is the slag quenching apparatus, and cooler is the slag annealing device, and the slag quenching process separates with annealing process and carries out, the available energy that causes with the direct mixing of the residual heat resources of avoiding different energy levels (fire with) loss.
3. waste heat boiler adopts ∏ type structure, high temperature and two smoke inlets of middle temperature, presses the cascade utilization of energy level to realize residual heat resources, improves waste heat recovery efficient.
Description of drawings
Fig. 1 is the utility model centrifugal molten slag dry type granulation and waste heat recovery generating system structure iron.
Fig. 2 is the contactless structure iron that is connected between heat pipe axle and the bearing among Fig. 1.
Except that the literal of having indicated, 1-connects slag ladle among the above-mentioned figure, 2-slag ladle, 3-slag chute, gas blower of 4-, 5-phonomoter, 6-water-cooling jacket; The 7-transmission mechanism, 8-high-temperature bearing, 9-heat pipe axle, 10-revolving cup, 11-air distribution plate, 12-high-temperature residual heat suction opening, 13-centrifugal granulation stove; 14-slag diversion trench, warm waste heat suction opening among the 15-, 16-cooler, 17-windbreak, 18-water-cooled vibration comb bed, 19-broken slag device, 20-secondary gas blower; 21-lingering remnants of past customs mouth, 22-chain conveyor, 23-stockyard, 24-high temperature inlet, 25-membrane wall, 26-drum, 27-two stage superheater; The 28-primary superheater, 29-secondary evaporimeter, 30-one-level vaporizer, 31-economizer, 32-forced circulation pump, temperature inlet among the 33-, 34-waste heat boiler; The 35-turbine, 36-generator, 37-condenser, 38-waste heat boiler service pump, 39-condensate pump, 40-recirculated cooling water pump; The 41-cooling tower, 42-thermal deaerator, 43-electrostatic precipitator, 44-induced draft fan, 45-chimney, 46-magnetic ring group.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is explained further details.
As depicted in figs. 1 and 2; Centrifugal molten slag chilling dry type granulation of the utility model and waste heat recovery generating system comprise and connect slag device, the centrifugal chilling granulating device of slag, slag annealing device, exhaust heat recovery power generation device and exhaust gas purification and treatment device; Wherein, connecing the slag device forms with slag ladle 2 by connecing slag ladle 1; The centrifugal chilling granulating device of slag mainly is made up of heat pipe axle 9, revolving cup 10, phonomoter 5 and a gas blower 4 etc.; Heat pipe axle 9 one ends are connected with revolving cup 10 and place in the centrifugal granulation stove 13; The other end of heat pipe axle 9 links to each other with water-cooling jacket 6, and phonomoter 5 links to each other with transmission mechanism 7, and transmission mechanism 7 is connected with heat pipe axle 9 and is positioned at the below of water-cooling jacket 6; Transmission mechanism 7 and water-cooling jacket 6 all place the outside of centrifugal granulation stove 13; Heat pipe axle 9 is connected through 46 noncontacts of magnetic ring group with high-temperature bearing 8 on the centrifugal granulation stove 13, and the bottoms in the centrifugal granulation stove 13 are provided with 11, gas blowers 4 of air distribution plate and air distribution plate and enter the mouth and 11 be connected; The slag annealing device mainly comprises cooler 16, uses water-cooled vibration comb bed 18 in the cooler 16; The slag inlet of cooler 16 links to each other with the outlet of slag diversion trench 14, and the cooling air intake of cooler 16 links to each other with secondary gas blower 20; The afterbody of cooler 16 is provided with broken slag device 19.
The exhaust heat recovery power generation device mainly comprises waste heat boiler 34, turbine 35, generator 36, condenser 37, cooling tower 41, thermal deaerator 42; Waste heat boiler 34 comprises membrane wall 25, drum 26, two stage superheater 27, primary superheater 28, secondary evaporimeter 29, one-level vaporizer 30, economizer 31 and forced circulation pump 32; The high-temperature residual heat suction opening 12 of centrifugal granulation stove 13 is connected with the high temperature inlet 24 of waste heat boiler 34 through the high temperature airduct; The middle temperature waste heat suction opening 15 of cooler 16 is connected with the middle temperature inlet 33 of waste heat boiler 34 through middle temperature airduct; The middle temperature inlet 33 of waste heat boiler 34 is positioned at primary superheater 28 belows; Set gradually two stage superheater 27, primary superheater 28, secondary evaporimeter 29, one-level vaporizer 30 and economizer 31 in the waste heat boiler 34 from top to bottom; Two stage superheater 27 is connected with the main inlet throttle-stop valve of turbine 35 through the female pipe of main steam, and turbine 35 links to each other with generator 36; The exhaust steam outlet of turbine 35 links to each other with condenser 37, and the hot well of condenser 37 links to each other with the inlet of condensate pump 39; The pond, bottom of cooling tower 41 links to each other with recirculated cooling water pump 40, and recirculated cooling water pump 40 links to each other with the cooling water inlet of condenser 37, and the cooling water outlet of condenser 37 links to each other with the top of cooling tower 41; The outlet of condensate pump 39 is connected with the inlet of thermal deaerator 42; The pipe of boiler feedwater simultaneously also is connected with the inlet of thermal deaerator 42; The outlet of thermal deaerator 42 links to each other with the inlet of waste heat boiler service pump 38, and the outlet of waste heat boiler service pump 38 links to each other with the inlet of economizer 31.
The centrifugal molten slag chilling dry type granulation and the waste heat recovery generating system of the utility model: utilize unique centrifugal granulation device molten slag chilling and dry type granulation, slowly cool off through water-cooled vibration comb bed again; High-temp waste gas is delivered to waste heat boiler high temperature inlet from centrifugal granulation stove high-temperature residual heat suction opening through the high temperature airduct; In warm waste gas warm waste heat suction opening from cooler cover in the waste heat boiler temperature inlet through middle temperature airduct; Waste heat boiler produces sub-high pressure time high-temperature steam, and steam is used for promoting the turbo-generator generating.
The concrete grammar embodiment that realizes the utility model is following:
1,1400-1600 ℃ molten slag is sent into storage in the slag ladle 2 through connecing slag ladle 1.
2, the molten slag in the slag ladle gets into centrifugal granulation stoves 13 through slag chute 3, under the effect of centrifugal granulation device, is crushed to the small-particle below the 5mm, and the freezing air that utilizes gas blower 4 to blast simultaneously is chilled to its temperature about 900 ℃.
3, the water-cooling jacket on heat pipe axle top produces about 80 ℃ hot water, gets into pipe network so that follow-up central heating or refrigeration.
4, the slag granules behind fragmentation and chilling drops down onto on the water-cooled vibration comb bed 18 in the cooler 16; The freezing air heat exchange that blasts with the secondary gas blower 20 of cooler; Slag after abundant cooling heat transferring and break process is once more sent into stockyard 23, and the slag granules temperature is reduced to below 150 ℃.
5, high-temp waste gas (about 850 ℃) is delivered to waste heat boiler high temperature inlet 24 from centrifugal granulation stove high-temperature residual heat suction opening 12 through the high temperature airduct; In warm waste gas (about 650 ℃) warm waste heat suction opening 15 from cooler cover in the waste heat boiler temperature inlet 33 through middle temperature airduct; Waste heat boiler 34 produces (485 ℃ of time high temperature sub-high pressures; 5.3MPa) steam, pushing turbine 35 realizes that with generator 36 thermal power transfer is an electric energy.Through computational analysis, realizing that the clinker glass body burden is not less than on 90% the basis, a ton slag waste heat recovery net electric generation is about 80kWh/t.
Slag, system's waste heat recovery efficient is about 52%.
The embodiment that the above is merely the utility model does not constitute the qualification to the utility model protection domain.Any modification of being done within any spirit and principle at the utility model, be equal to replacement and improvement etc., all should be included within the claim protection domain of the utility model.
Claims (5)
1. centrifugal molten slag dry type granulation and waste heat recovery generating system; Comprise connecing slag device, the centrifugal chilling granulating device of slag, slag annealing device, exhaust heat recovery power generation device and exhaust gas purification and treatment device, it is characterized in that: the said slag device that connects is by connecing slag ladle (1) and slag ladle (2) is formed;
The centrifugal chilling granulating device of said slag is made up of heat pipe axle (9), revolving cup (10), phonomoter (5) and a gas blower (4) etc.; Wherein, Heat pipe axle one end is connected with revolving cup and places in the centrifugal granulation stove (13), and the heat pipe axle the other end links to each other with water-cooling jacket (6) and places outside the centrifugal granulation stove; Phonomoter links to each other with transmission mechanism (7), and transmission mechanism is connected with said heat pipe axle and places outside the centrifugal granulation stove; Said heat pipe axle is connected through magnetic ring group (46) noncontact with high-temperature bearing (8) on the centrifugal granulation stove; Bottom in the said centrifugal granulation stove is provided with air distribution plate (11), and a said gas blower is connected with the air distribution plate inlet;
Said slag annealing device mainly comprises cooler (16), uses water-cooled vibration comb bed (18) in the cooler; The slag inlet of said cooler links to each other with said centrifugal granulation stove through slag diversion trench (14), and the cooling air intake of cooler links to each other with secondary gas blower (20); The afterbody of said cooler is provided with broken slag device (19);
Said exhaust heat recovery power generation device mainly comprises waste heat boiler (34), turbine (35), generator (36), condenser (38), cooling tower (41) and thermal deaerator (42); Said waste heat boiler comprises membrane wall (25), drum (26), two stage superheater (27), primary superheater (28), secondary evaporimeter (29), one-level vaporizer (30), economizer (31) and forced circulation pump (32); The high-temperature residual heat suction opening (12) of said centrifugal granulation stove is connected with the high temperature inlet (24) of waste heat boiler through the high temperature airduct; The middle temperature waste heat suction opening (15) of said cooler is connected with the middle temperature inlet (33) of waste heat boiler through middle temperature airduct; The temperature inlet is positioned at the primary superheater below in the said waste heat boiler; Set gradually said two stage superheater, primary superheater, secondary evaporimeter, one-level vaporizer and economizer in the said waste heat boiler from top to bottom; Said two stage superheater is connected with the main inlet throttle-stop valve of turbine through the female pipe of main steam, and said turbine links to each other with generator; The exhaust steam outlet of said turbine links to each other with condenser, and the hot well of condenser links to each other with the inlet of condensate pump; The pond, bottom of said cooling tower links to each other with recirculated cooling water pump (40), and the recirculated cooling water pump links to each other with the cooling water inlet of said condenser, and the cooling water outlet of said condenser links to each other with the top of cooling tower; The outlet of said condensate pump (39) is connected with the inlet of thermal deaerator; The pipe of boiler feedwater simultaneously also is connected with the inlet of said thermal deaerator; The outlet of thermal deaerator links to each other with the inlet of waste heat boiler service pump, and waste heat boiler feedwater pump outlet links to each other with the inlet of said economizer;
Said exhaust gas purification and treatment device comprises electrostatic precipitator (43), induced draft fan (44) and chimney (45); The lingering remnants of past customs mouth (21) of the smoke outlet of said waste heat boiler and cooler links to each other with the inlet of electrostatic precipitator; The outlet of electrostatic precipitator links to each other with the inlet of induced draft fan, and the outlet of induced draft fan links to each other with chimney.
2. a kind of centrifugal molten slag dry type granulation according to claim 1 and waste heat recovery generating system is characterized in that the said appearance that connects slag ladle and slag ladle is all laid heat-insulating protective layer.
3. a kind of centrifugal molten slag dry type granulation according to claim 1 and waste heat recovery generating system is characterized in that heat-insulating protective layer is laid in the outside of said centrifugal granulation stove, and the high-temperature wearable layer is laid in its inboard.
4. a kind of centrifugal molten slag dry type granulation according to claim 1 and waste heat recovery generating system is characterized in that, said heat pipe axle is stainless steel-sodium heat pipe axle.
5. a kind of centrifugal molten slag dry type granulation according to claim 1 and waste heat recovery generating system is characterized in that said waste heat boiler is a ∏ type frame mode.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200415665U CN202530095U (en) | 2012-02-09 | 2012-02-09 | Centrifugal molten slag dry granulation and waste heat recovery power generation system |
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| CN2012200415665U CN202530095U (en) | 2012-02-09 | 2012-02-09 | Centrifugal molten slag dry granulation and waste heat recovery power generation system |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102559957A (en) * | 2012-02-09 | 2012-07-11 | 南京凯盛开能环保能源有限公司 | Centrifugal type fusion slag quenching and dry type granulating, and waste heat recovery power generation system and method |
| CN103215393A (en) * | 2013-04-27 | 2013-07-24 | 河北钢铁股份有限公司邯郸分公司 | Metallurgical liquid-state slag treatment process and equipment |
| CN103866057A (en) * | 2014-03-31 | 2014-06-18 | 江苏融达新材料股份有限公司 | Recovery device of high use value metallurgy waste residues |
| CN105018658A (en) * | 2015-08-20 | 2015-11-04 | 北京立化科技有限公司 | Integrated device for metallurgy slag granulation and multi-stage heat energy recovery |
| CN109595947A (en) * | 2019-01-17 | 2019-04-09 | 苏州良造能源科技有限公司 | A kind of industrial slags cement sensible heat recovery system and its recovery method |
| CN115141901A (en) * | 2022-06-02 | 2022-10-04 | 中节能工业节能有限公司 | Slag recovery system |
| CN115597075A (en) * | 2022-10-31 | 2023-01-13 | 中国矿业大学（Cn） | Ultralow-concentration gas heat-storage combustion system and method based on magnetic field induction |
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2012
- 2012-02-09 CN CN2012200415665U patent/CN202530095U/en not_active Withdrawn - After Issue
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102559957A (en) * | 2012-02-09 | 2012-07-11 | 南京凯盛开能环保能源有限公司 | Centrifugal type fusion slag quenching and dry type granulating, and waste heat recovery power generation system and method |
| CN102559957B (en) * | 2012-02-09 | 2013-04-24 | 南京凯盛开能环保能源有限公司 | Centrifugal type fusion slag quenching and dry type granulating, and waste heat recovery power generation system and method |
| CN103215393A (en) * | 2013-04-27 | 2013-07-24 | 河北钢铁股份有限公司邯郸分公司 | Metallurgical liquid-state slag treatment process and equipment |
| CN103215393B (en) * | 2013-04-27 | 2014-07-30 | 河北钢铁股份有限公司邯郸分公司 | Metallurgical liquid-state slag treatment process and equipment |
| CN103866057A (en) * | 2014-03-31 | 2014-06-18 | 江苏融达新材料股份有限公司 | Recovery device of high use value metallurgy waste residues |
| CN103866057B (en) * | 2014-03-31 | 2015-09-23 | 江苏融达新材料股份有限公司 | A kind of retrieving arrangement of high utility value metallurgical slag |
| CN105018658A (en) * | 2015-08-20 | 2015-11-04 | 北京立化科技有限公司 | Integrated device for metallurgy slag granulation and multi-stage heat energy recovery |
| CN109595947A (en) * | 2019-01-17 | 2019-04-09 | 苏州良造能源科技有限公司 | A kind of industrial slags cement sensible heat recovery system and its recovery method |
| CN109595947B (en) * | 2019-01-17 | 2023-10-03 | 苏州良造能源科技有限公司 | Industrial slag sensible heat recovery system and recovery method thereof |
| CN115141901A (en) * | 2022-06-02 | 2022-10-04 | 中节能工业节能有限公司 | Slag recovery system |
| CN115141901B (en) * | 2022-06-02 | 2024-02-20 | 中节能工业节能有限公司 | Slag recovery system |
| CN115597075A (en) * | 2022-10-31 | 2023-01-13 | 中国矿业大学（Cn） | Ultralow-concentration gas heat-storage combustion system and method based on magnetic field induction |
| CN115597075B (en) * | 2022-10-31 | 2023-06-30 | 中国矿业大学 | Ultralow-concentration gas heat-storage combustion system and method based on magnetic field induction |
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