CN108855941A - A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system - Google Patents
A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system Download PDFInfo
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- CN108855941A CN108855941A CN201810833674.8A CN201810833674A CN108855941A CN 108855941 A CN108855941 A CN 108855941A CN 201810833674 A CN201810833674 A CN 201810833674A CN 108855941 A CN108855941 A CN 108855941A
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- waste heat
- gas
- flue gas
- outlet
- heat flue
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- 239000002918 waste heat Substances 0.000 title claims abstract description 171
- 239000003546 flue gas Substances 0.000 title claims abstract description 138
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 136
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 101
- 239000010959 steel Substances 0.000 title claims abstract description 101
- 239000002893 slag Substances 0.000 title claims abstract description 61
- 239000000843 powder Substances 0.000 title claims abstract description 53
- 239000003595 mist Substances 0.000 title claims description 42
- 239000007789 gas Substances 0.000 claims abstract description 149
- 238000002485 combustion reaction Methods 0.000 claims abstract description 34
- 230000003068 static effect Effects 0.000 claims abstract description 23
- 230000001105 regulatory effect Effects 0.000 claims description 54
- 238000009826 distribution Methods 0.000 claims description 34
- 238000009825 accumulation Methods 0.000 claims description 23
- 239000000428 dust Substances 0.000 claims description 19
- 239000000779 smoke Substances 0.000 claims description 17
- 230000008676 import Effects 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 238000005338 heat storage Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 238000005096 rolling process Methods 0.000 claims description 7
- 238000012544 monitoring process Methods 0.000 claims description 6
- 239000003034 coal gas Substances 0.000 claims description 5
- 239000003517 fume Substances 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 2
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 239000000446 fuel Substances 0.000 abstract description 7
- 238000004064 recycling Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000005245 sintering Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229910001341 Crude steel Inorganic materials 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B9/00—Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
- B07B9/02—Combinations of similar or different apparatus for separating solids from solids using gas currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/06—Feeding or discharging arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H3/00—Air heaters
- F24H3/006—Air heaters using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0052—Details for air heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/18—Arrangement or mounting of grates or heating means
- F24H9/1854—Arrangement or mounting of grates or heating means for air heaters
- F24H9/1877—Arrangement or mounting of combustion heating means, e.g. grates or burners
- F24H9/1881—Arrangement or mounting of combustion heating means, e.g. grates or burners using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
- F27D2017/006—Systems for reclaiming waste heat using a boiler
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The invention discloses a kind of steel slag micro mists using steel plant's waste heat flue gas to select powder system, including waste heat flue gas gas source, residual heat flue mechanism, waste heat flue gas booster body, gas source, compensation combustion type hot-blast stove, static powder separating machine, feeding mechanism, coarse fodder stocking mechanism, cyclone cylinder, dedusting mechanism, fines stocking mechanism and exhaust gear；Waste heat flue gas in waste heat flue gas gas source enters compensation combustion type hot-blast stove using waste heat flue gas booster body and is heated according to residual heat flue mechanism is entered；Compensation combustion type hot-blast stove enters static powder separating machine, coarse fodder in static powder separating machine stores coarse fodder stocking mechanism again, fines is stored in fines stocking mechanism after cyclone cylinder Conveyance, the outlet air of cyclone cylinder is filtered through dedusting mechanism and is discharged, it is heated using the waste heat flue gas of steel plant's waste heat as the hot wind in hot-blast stove, not only the recycling of the waste heat flue gas of steel plant's waste heat had been realized, but also has greatly reduced the fuel cost in hot-blast stove.
Description
The present invention relates to steel slag micro mist manufacturing technology field more particularly to a kind of steels using steel plant's waste heat flue gas
Slag micro mist selects powder system.
Background technique
Currently, steel slag and slag are steel industry discharge amount maximum metallurgical slags, according to relevant iron-making and steel-making technique, steel slag
Quantum of output be crude steel yield 12-15%, slag is the 25%-35% of crude steel yield.Have after the slag water quenching that blast furnace process generates
There is very big activity, after being fabricated to micro mist, as the admixture of cement mixture and mixed mud, comprehensive utilization ratio is up to 90% or more.
The steel slag generated is made steel since there are the calcium oxide of free state and magnesia, causes stability bad, utilization rate is less than 20%.Mesh
One, the preceding steel slag application with good prospect is that steel slag tailings production that is heat is stewing and being crushed after selecting iron becomes specific surface area
The slag micro powder of 400m2/kg.Become double-doped powder after above-mentioned slag micro powder and slag micropowder are mixed according to a certain percentage, as
The substitute of clinker.Current this application method graduallys mature.
As patent 201621266637.6 produces using slag micro powder and slag micropowder mention in the equipment of double-doped powder one
Sample needs to use hot-blast stove in the production process of slag micropowder or slag micro powder, the purpose is to material dried with
Meet subsequent technique requirement.Hot-blast stove used at present is all to enter heating furnace burning, furnace outlet temperature using normal temperature air
Degree is usually at 300-400 DEG C according to process requirement.It is usually used in hot-blast stove for heating the fuel of normal temperature air at present
The surplus gas of steel mill.General steel mill's blast furnace gas more than needed is calculated according to the electricity price of power generation, the valence of blast furnace gas for generating electricity
Lattice are about 0.2 yuan/Nm3, and calculating to the blast furnace gas consumption of micro mist per ton is about 70-100Nm3/ tons, then fuel per ton at
This is 14-20 yuan/ton, and the fuel cost in hot-blast stove accounts between the 30-40% of totle drilling cost.
There are many waste heat flue gases in another aspect steel plant, for example at least there are several types of waste heats：1）The row of blast funnace hot blast stove
Smoke temperature degree is between 120-160 DEG C；2）The cold third section exhaust of the ring of sintering process is also at 150-230 DEG C or more；3）Steel rolling heating
Furnace exhaust gas temperature is also at 150 DEG C or more；4）For gas fired-boiler exhaust gas temperature also at 140 degrees Celsius or more.Existing technology
In, the waste heat direct emission generated in these steel plant's distinct devices, technique causes the very big wasting of resources.
Summary of the invention
The object of the present invention is to provide a kind of steel slag micro mists using steel plant's waste heat flue gas to select powder system, can be abundant
It is heated using the waste heat flue gas of steel plant's waste heat as the hot wind in hot-blast stove, realizes the waste heat flue gas of steel plant's waste heat
It recycles, and greatly reduces the fuel cost in hot-blast stove.
The technical solution adopted by the present invention is：
A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system, including waste heat flue gas gas source, residual heat flue mechanism,
Waste heat flue gas booster body, gas source, compensation combustion type hot-blast stove, static powder separating machine, feeding mechanism, coarse fodder stocking mechanism, whirlwind
Cylinder, dedusting mechanism, fines stocking mechanism and exhaust gear；
The waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism of the waste heat flue gas gas source, residual heat flue machine
The waste heat exhanst gas outlet of structure connects the waste heat gas inlet of waste heat flue gas booster body by waste heat smoke regulating valve, and described is remaining
The waste heat exhanst gas outlet of hot fume booster body connects the combustion-supporting gas inlet of compensation combustion type hot-blast stove by combustion-supporting smoke regulating valve,
And the waste heat exhanst gas outlet of waste heat flue gas booster body connects the air distribution flue gas of compensation combustion type hot-blast stove by air distribution smoke regulating valve
Import；The gas exit of gas source connects the gas inlet of compensation combustion type hot-blast stove by gas regulator；
The air outlet of the air inlet connection compensation combustion type hot-blast stove of the static powder separating machine, the feed inlet of the static powder separating machine
Feeding mechanism, the coarse fodder outlet connection coarse fodder stocking mechanism of static powder separating machine are connected, the fine material outlet of static powder separating machine connects rotation
The feed inlet of air duct, the hot wind inlet of cyclone cylinder connect the air outlet of compensation combustion type hot-blast stove by cyclone cylinder hot wind regulating valve, rotation
The discharge port of air duct connects fines stocking mechanism；Dedusting mechanism air inlet connection cyclone cylinder air outlet, dedusting mechanism it is remaining
Material outlet connection fines stocking mechanism, the exhaust outlet of dedusting mechanism connect exhaust gear by exhaust regulating valve, dedusting mechanism
Waste heat flue gas reuse outlet connects the waste heat flue gas reuse import of compensation combustion type hot-blast stove by waste heat flue gas reuse regulating valve.
The dedusting mechanism includes bag-type dust machine and dedusting fan, and the air inlet of the bag-type dust machine connects rotation
The clout outlet connection fines stocking mechanism of the air outlet bag-type dust machine of air duct, the gas vent of bag-type dust machine connect dedusting
The exhaust outlet of the gas feed of blower, dedusting fan connects exhaust gear, the waste heat flue gas of dedusting fan by exhaust regulating valve
Reuse outlet connects the waste heat flue gas reuse import of compensation combustion type hot-blast stove by waste heat flue gas reuse regulating valve.
It further includes temperature monitoring mechanism that the steel slag micro mist using steel plant's waste heat flue gas, which selects powder system, described
Temperature monitoring mechanism includes temperature sensor, analog-to-digital conversion module, microprocessor and display module；The temperature sensor is set
It is placed in the gas vent of bag-type dust machine；The temperature signal output end of the temperature sensor connects the defeated of analog-to-digital conversion module
Enter end, the input terminal of the output end connection microprocessor of analog-to-digital conversion module, the output end of microprocessor connects display module
Input terminal.
The waste heat flue gas gas source includes that the first pressure charging system and the first regulating valve, the second pressure charging system and second are adjusted
Valve, third pressure charging system and third regulating valve, the 4th pressure charging system and the 4th regulating valve；The waste heat of first pressure charging system
Gas inlet by the first regulating valve connect blast funnace hot blast stove exhanst gas outlet, the first pressure charging system waste heat exhanst gas outlet connection more than
First waste heat gas inlet of heating flue mechanism；The waste heat gas inlet of second pressure charging system is connected by the second regulating valve
Sintering circular-cooler third section exhanst gas outlet is connect, the waste heat exhanst gas outlet of the second pressure charging system connects more than the second of residual heat flue mechanism
Hot fume import；The waste heat gas inlet of the third pressure charging system connects heater for rolling steel flue gas by third regulating valve and goes out
Mouthful, the third waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism of third pressure charging system；Described the 4th increases
The waste heat gas inlet of pressure system connects the exhanst gas outlet of gas fired-boiler smoke evacuation system, the 4th pressure charging system by the 4th regulating valve
Waste heat exhanst gas outlet connection residual heat flue mechanism the 4th waste heat gas inlet.
The hot-blast stove includes heat accumulation room, multiple heat storages, multiple burners, multiple burners fixed setting
In on heat accumulation chamber enclosure, and multiple burners are successively arranged from top to bottom；Each burner include combustion-supporting flue gas into
Mouth and gas inlet, and the waste heat exhanst gas outlet of the combustion-supporting gas inlet connection waste heat flue gas booster body of burner, burner
Gas inlet connection gas source gas exit, the hot-blast outlet of burner is connected to heat accumulation room；Multiple accumulation of heats
Between body is top-down to be fixedly installed on heat accumulation chamber interior, and each heat storage respectively corresponds between a pair of of adjacent burners
Every；Air distribution flue gas extension tube attached is further fixedly arranged on the heat accumulation room, the entrance of the air distribution flue gas extension tube attached is air distribution
The outlet of gas inlet, air distribution flue gas extension tube attached is connected to heat accumulation room.
The air distribution flue gas extension tube attached is obliquely installed, and the oblique burner side of air distribution gas inlet of air distribution flue gas extension tube attached
To the center line of air distribution flue gas extension tube attached and the angle of heat accumulation room center line are less than or equal to 45o。
The number of the air distribution flue gas extension tube attached is multiple.
It is of the invention to provide a kind of steel slag micro mist using steel plant's waste heat flue gas and select powder system, it can make full use of
Waste heat flue gas in steel plant everywhere is converged in residual heat flue mechanism, enters back into hot wind by the waste heat flue gas of steel plant's waste heat
It is heated to be high-temperature hot-air in furnace, realizes the recycling of the waste heat flue gas of steel plant's waste heat, and waste heat flue-gas temperature itself is remote
Higher than normal temperature air, therefore greatly reduce the fuel cost in hot-blast stove.
Further, by the way that burner is successively arranged from top to bottom, the leveled heating of hot wind in hot-blast stove is realized, is made
It obtains gas-fired in hot-blast stove to stablize, hot-wind heated is uniform, and heating speed is fast, the heat for avoiding burner combustion coal gas from obtaining
Loss, has saved resource.
Detailed description of the invention
Fig. 1 is structural scheme of mechanism of the invention；
Fig. 2 is waste heat flue gas air source structure schematic diagram of the invention；
Fig. 3 is compensation combustion type hot-blast stove structural schematic diagram of the invention.
Specific embodiment
As shown in Figure 1, a kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system, the waste heat including steel plant
Flue gas gas source 22, the residual heat flue mechanism 1 for converging steel plant's many places waste heat flue gas, waste heat flue gas booster body 3, coal gas gas
Source 2, compensation combustion type hot-blast stove 4, static powder separating machine 5, feeding mechanism 6, coarse fodder stocking mechanism 8, cyclone cylinder 7, dedusting mechanism, fines storage
Deposit mechanism 11 and exhaust gear 12；
The dedusting mechanism includes bag-type dust machine 9 and dedusting fan 10, and the gas vent of bag-type dust machine 9 connects dedusting wind
The gas feed of machine 10, bag-type dust machine 9 and dedusting fan 10 form two-stage dedusting mechanism, the particle being further reduced in exhaust gas
Object prevents Particulate Pollution environment.
The waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism 1 of the waste heat flue gas gas source 22, it is remaining
The waste heat exhanst gas outlet of heating flue mechanism 1 passes through the waste heat flue gas of waste heat smoke regulating valve V1 connection waste heat flue gas booster body 3
The waste heat exhanst gas outlet of import, the waste heat flue gas booster body 3 passes through combustion-supporting smoke regulating valve V3 connection compensation combustion type hot wind
The combustion-supporting gas inlet of furnace 4, and the waste heat exhanst gas outlet of waste heat flue gas booster body 3 is mended by air distribution smoke regulating valve V2 connection
The air distribution gas inlet of burning type hot-air furnace 4；The gas exit of gas source 2 passes through gas regulator V7 connection compensation combustion type hot-blast stove
4 gas inlet；
The static powder separating machine 5 air inlet connection compensation combustion type hot-blast stove 4 air outlet, the static powder separating machine 5 into
Material mouth connects feeding mechanism 6, the coarse fodder outlet connection coarse fodder stocking mechanism 8 of static powder separating machine 5, and the fines of static powder separating machine 5 goes out
The feed inlet of mouth connection cyclone cylinder 7, the hot wind inlet of cyclone cylinder 7 pass through cyclone cylinder hot wind regulating valve V4 connection compensation combustion type hot-blast stove
The discharge port of 4 air outlet, cyclone cylinder 7 connects fines stocking mechanism 11；The air inlet connection cyclone cylinder 7 of bag-type dust machine 9
Air outlet, the clout outlet connection fines stocking mechanism 11 of bag-type dust machine 9, the exhaust outlet of dedusting fan 10 are adjusted by exhaust
It is mended by the V5 connection of waste heat flue gas reuse regulating valve the waste heat flue gas reuse outlet of valve V6 connection exhaust gear 12, dedusting fan 10
The waste heat flue gas reuse import of burning type hot-air furnace 4.
As shown in Fig. 2, the waste heat flue gas in the waste heat flue gas gas source 22 mostlys come from steel plant in the present embodiment
It is discharged in this four equipment of middle blast funnace hot blast stove 13, sintering circular-cooler third section 15, heater for rolling steel 17 and gas fired-boiler 18
Waste heat flue gas.The waste heat flue gas gas source 22 includes the first pressure charging system 14 and the first regulating valve V8, the second pressure charging system 16
With the second regulating valve V9, third pressure charging system 17 and third regulating valve V10, the 4th pressure charging system 20 and the 4th regulating valve V11；Institute
The waste heat gas inlet for the first pressure charging system 14 stated is by 13 exhanst gas outlet of the first regulating valve V8 connection blast funnace hot blast stove, and first
First waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism 1 of pressure charging system 14；The second pressurization system
The waste heat gas inlet of system 16 passes through 15 exhanst gas outlet of the second regulating valve V9 connection sintering circular-cooler third section, the second pressure charging system
Second waste heat gas inlet of 16 waste heat exhanst gas outlet connection residual heat flue mechanism 1；The third pressure charging system 17 it is remaining
Hot fume import passes through 17 exhanst gas outlet of third regulating valve V10 connection heater for rolling steel, the waste heat flue gas of third pressure charging system 17
The third waste heat gas inlet of outlet connection residual heat flue mechanism 1；The waste heat gas inlet of 4th pressure charging system 20 is logical
Cross the exhanst gas outlet of 18 smoke evacuation system of the 4th regulating valve V11 connection gas fired-boiler, the waste heat exhanst gas outlet of the 4th pressure charging system 20
Connect the 4th waste heat gas inlet of residual heat flue mechanism 1.According to blast funnace hot blast stove 13, sintering circular-cooler third section in steel plant
15, the operating condition of heater for rolling steel 17 and gas fired-boiler 18 adjusts first regulating valve V8 corresponding with equipment, the second regulating valve
V9, third regulating valve V10 and the 4th regulating valve V11 are adjusted and select to the waste heat flue gas entered in residual heat flue mechanism 1
It selects.
The working principle of the invention and process are as follows：Distinct device in steel plant, the waste heat flue gas generated in technique are direct
Discharge causes the wasting of resources of thermal energy carried in flue gas, and steel plant produce the hot-blast stove of steel slag micro mist important equipment, again
It needs the air of room temperature being heated to 300-400 DEG C.
In steel plant blast funnace hot blast stove 13, sintering circular-cooler third section 15, heater for rolling steel 17 and gas fired-boiler 18 this four
The waste heat flue gas being discharged in a equipment respectively enters in residual heat flue mechanism 1, and mixing, and different temperatures are collected in residual heat flue
Waste heat flue gas exchange heat, open subsequent waste heat flue gas enter waste heat flue gas booster body 3 pressurization, waste heat flue gas booster body
3 guarantee waste heat flue gases can overcome the resistance in entire steel slag micro mist production system, successfully complete flue gas recirculation or discharge.
After the pressurization of waste heat flue gas booster body 3, waste heat flue gas a part in waste heat flue gas booster body 3 is as to be added
The hot-air of heat, is entered in hot-blast stove by the air distribution gas inlet of the self-complementary burning type hot-air furnace 4 of pipeline；Waste heat flue gas booster body
Waste heat flue gas another part in 3 enters hot wind by the combustion-supporting gas inlet of the self-complementary burning type hot-air furnace 4 of pipeline as combustion air
In furnace；Due to waste heat flue gas
Self-temperature is higher, therefore, the combustion-supporting smoke pre-heating the step in, saved the energy, simplified hot air furnace device, together
When also assure hot blast temperature and efficient burning.
Coal gas in gas source 2, which enters in hot-blast stove, to burn, and further heating enters the waste heat flue gas in hot-blast stove.Add
The hot wind of heat to suitable temperature enters in static powder separating machine 5.Feeding mechanism 6 specifically includes raw material stocking mechanism and raw material conveyance
Structure is the mixing iron and steel slag micro mist of roller press grinding system production in raw material stocking mechanism.Raw material transshipment acitivity is by mixing iron and steel
Into static powder separating machine 5, steel slag micro powder screen is selected as coarse fodder steel slag micro mist and fines by static powder separating machine 5 for the transport of slag micro mist
Steel slag micro mist, fines steel slag micro mist is directly from the outlet of the coarse fodder of static powder separating machine 5 enters in coarse fodder stocking mechanism 8 and stores
Come, in actual production, the coarse fodder stored in coarse fodder stocking mechanism 8 is added into roller press grinding system again wears into micro mist, real
Existing steel slag resource makes full use of.
Fines steel slag micro mist then enters cyclone cylinder 7, fines steel slag micro mist and heat from the fine material outlet of static powder separating machine 5
Wind separation, the discharge port of fines steel slag micro mist from cyclone cylinder 7 enter fines stocking mechanism 11 and store.
High-temperature hot-air in hot-blast stove enters cyclone cylinder 7, in the mistake that cyclone cylinder 7 separates fines steel slag micro mist with hot wind
Cheng Zhong adjusts the high-temperature hot-air being directly entered in cyclone cylinder 7 in self-heating wind furnace by adjusting cyclone cylinder hot wind regulating valve V4
Amount increases the aperture of cyclone cylinder hot wind regulating valve V4, is directly entered rotation in self-heating wind furnace if fines steel slag micro mist humidity is high
The amount of high-temperature hot-air in air duct 7 increases, and takes away more vapor, reduces fines steel slag micro mist humidity.Conversely, if fines
Steel slag micro mist humidity is low, then reduces the aperture of cyclone cylinder hot wind regulating valve V4, be directly entered in cyclone cylinder 7 in self-heating wind furnace
The amount of high-temperature hot-air is reduced, and is taken away vapor and is just reduced, and guarantees that fines steel slag micro mist humidity meets the requirements.
Fines steel slag micro mist is separated with hot wind in cyclone cylinder 7, it is still micro- with a small amount of fines steel slag in hot wind
Therefore dedusting mechanism is arranged in the air outlet of cyclone cylinder 7, the fines steel slag in the hot wind that further cyclone cylinder 7 is discharged in powder
Micro mist is filtered and is collected, and the fines steel slag micro mist of collection enters in fines stocking mechanism 11 from the clout outlet of dedusting mechanism to be stored up
It deposits, to guarantee that fines steel slag micro mist is not wasted, is also prevented from micro- containing fines steel slag in the hot wind being discharged by cyclone cylinder 7
Powder causes environmental pollution.
By the exhaust gas that dedusting mechanism is discharged, still contains heat, therefore, a part of exhaust gas is connected to the benefit of air-heater
The waste heat flue gas reuse import of burning type hot-air furnace 4 is back in hot-blast stove, and waste gas circulation is utilized, further saves energy, separately
It is a part of then be discharged from exhaust gear 12.The aperture of waste heat flue gas reuse regulating valve V5 and exhaust regulating valve V6 are adjusted respectively,
The ratio for neutralizing the exhaust gas entered in exhaust gear 12 into hot-blast stove can be adjusted according to the actual situation, guarantee the conjunction of waste heat flue gas
Manage reuse.
It is of the invention to provide a kind of steel slag micro mist using steel plant's waste heat flue gas and select powder system, it can make full use of
Waste heat flue gas in steel plant everywhere is converged in residual heat flue mechanism 1, enters back into hot wind by the waste heat flue gas of steel plant's waste heat
It is heated to be high-temperature hot-air in furnace, realizes the recycling of the waste heat flue gas of steel plant's waste heat, and waste heat flue-gas temperature itself is remote
Higher than normal temperature air, therefore greatly reduce the fuel cost in hot-blast stove.
The steel slag micro mist using steel plant's waste heat flue gas selects powder system, further includes temperature monitoring mechanism, described
Temperature monitoring mechanism include temperature sensor, analog-to-digital conversion module, microprocessor and display module；The temperature sensor
It is set to the gas vent of bag-type dust machine 9, acquires the temperature signal in 9 exit of bag-type dust machine；The temperature sensor
Temperature signal output end connection analog-to-digital conversion module input terminal, by temperature sensor acquire temperature signal be converted to number
Value, the input terminal of the output end connection microprocessor of analog-to-digital conversion module, the temperature signal that temperature sensor acquires is divided
Analysis combing, the input terminal of the output end connection display module of microprocessor, after microprocessor analysis is handled, in disappearance module
The gas temperature of 9 temperature point of real-time display bag-type dust machine.The microprocessor is single-chip microcontroller, and the display module is
Charactron.
According to the gas temperature of 9 temperature point of bag-type dust machine, air distribution smoke regulating valve V2 and gas regulator V7 is adjusted
Aperture, guarantee hot-blast stove discharge hot blast temperature meet the requirements.
As shown in figure 3, the steel slag micro mist using steel plant's waste heat flue gas selects powder system, the hot-blast stove packet
Heat accumulation room 24, multiple heat storages 25, multiple burners 23 are included, multiple burners 23 are fixedly installed on 24 shell of heat accumulation room
On, and multiple burners 23 are successively arranged from top to bottom, so that 4 stratified combustion of compensation combustion type hot-blast stove, by what need to be heated
Waste heat flue gas breaks the whole up into parts, avoid because flue gas volume it is excessive caused by conduct heat slow, the even problem of uneven heating, guarantee compensation combustion type heat
Wind furnace flameholding improves the heating efficiency of waste heat flue gas；In the present embodiment, the burner 23 is all set in heat accumulation room
Left side.
Each burner 23 includes combustion-supporting gas inlet 23-1 and gas inlet 23-2, and the combustion-supporting flue gas of burner 23
The waste heat exhanst gas outlet of import 23-1 connection waste heat flue gas booster body 3, the gas inlet 23-2 connection coal gas gas of burner 23
The hot-blast outlet of the gas exit in source 2, burner 23 is connected to heat accumulation room 24；Multiple heat storages 25 are top-down solid
Surely it is set to inside heat accumulation room 24, and each heat storage 25 respectively corresponds the interval between a pair of of adjacent burners 23, guarantees combustion
23 flameholding of burner；Air distribution flue gas extension tube attached 26 is further fixedly arranged on the heat accumulation room 24, outside the air distribution flue gas
The entrance of adapter tube 26 is air distribution gas inlet, and the outlet of air distribution flue gas extension tube attached 26 is connected to heat accumulation room 24.The pressurization of waste heat flue gas
The pressurized waste heat flue gas air self-distribution flue gas extension tube attached 26 of mechanism 3 enters in hot-blast stove by leveled heating.
The steel slag micro mist using steel plant's waste heat flue gas selects powder system, and the air distribution flue gas extension tube attached 26 tilts
Setting, and the air distribution flue gas extension tube attached 26 is tilted to the left, the outlet and 24 right part of heat accumulation room of air distribution flue gas extension tube attached 26
Connection, and the angle of the center line of the air distribution flue gas extension tube attached 26 and 24 center line of heat accumulation room is less than or equal to 45 degree, from
And guarantees the flue gas entered in compensation combustion type hot-blast stove 4 and, far from burner 23, avoid enter into the waste heat flue gas in compensation combustion type hot-blast stove 4
The burning of burner 23 is interfered, the stability that burner 23 burns is reduced.
The steel slag micro mist using steel plant's waste heat flue gas selects air distribution flue gas extension tube attached 26 described in powder system
Number be it is multiple, the waste heat flue gas air intake efficiency in compensation combustion type hot-blast stove 4 is improved, to guarantee the heat that burner 23 distributes
It is fully utilized.
Claims (7)
1. a kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system, it is characterised in that：Including waste heat flue gas gas source,
Residual heat flue mechanism, waste heat flue gas booster body, gas source, compensation combustion type hot-blast stove, static powder separating machine, feeding mechanism, coarse fodder
Stocking mechanism, cyclone cylinder, dedusting mechanism, fines stocking mechanism and exhaust gear；
The waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism of the waste heat flue gas gas source, residual heat flue machine
The waste heat exhanst gas outlet of structure connects the waste heat gas inlet of waste heat flue gas booster body by waste heat smoke regulating valve, and described is remaining
The waste heat exhanst gas outlet of hot fume booster body connects the combustion-supporting gas inlet of compensation combustion type hot-blast stove by combustion-supporting smoke regulating valve,
And the waste heat exhanst gas outlet of waste heat flue gas booster body connects the air distribution flue gas of compensation combustion type hot-blast stove by air distribution smoke regulating valve
Import；The gas exit of gas source connects the gas inlet of compensation combustion type hot-blast stove by gas regulator；
The air outlet of the air inlet connection compensation combustion type hot-blast stove of the static powder separating machine, the feed inlet of the static powder separating machine
Feeding mechanism, the coarse fodder outlet connection coarse fodder stocking mechanism of static powder separating machine are connected, the fine material outlet of static powder separating machine connects rotation
The feed inlet of air duct, the hot wind inlet of cyclone cylinder connect the air outlet of compensation combustion type hot-blast stove by cyclone cylinder hot wind regulating valve, rotation
The discharge port of air duct connects fines stocking mechanism；Dedusting mechanism air inlet connection cyclone cylinder air outlet, dedusting mechanism it is remaining
Material outlet connection fines stocking mechanism, the exhaust outlet of dedusting mechanism connect exhaust gear by exhaust regulating valve, dedusting mechanism
Waste heat flue gas reuse outlet connects the waste heat flue gas reuse import of compensation combustion type hot-blast stove by waste heat flue gas reuse regulating valve.
2. the steel slag micro mist according to claim 1 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Institute
The dedusting mechanism stated includes bag-type dust machine and dedusting fan, the outlet air of the air inlet connection cyclone cylinder of the bag-type dust machine
The clout outlet connection fines stocking mechanism of mouth bag-type dust machine, the gas of the gas vent connection dedusting fan of bag-type dust machine
The exhaust outlet of import, dedusting fan connects exhaust gear by exhaust regulating valve, and the waste heat flue gas reuse outlet of dedusting fan is logical
Excess enthalpy thermal flue gas back connects the waste heat flue gas reuse import of compensation combustion type hot-blast stove with regulating valve.
3. the steel slag micro mist according to claim 2 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Also
Including temperature monitoring mechanism, the temperature monitoring mechanism includes temperature sensor, analog-to-digital conversion module, microprocessor and display
Module；The temperature sensor is set to the gas vent of bag-type dust machine；The temperature signal of the temperature sensor is defeated
Outlet connects the input terminal of analog-to-digital conversion module, the input terminal of the output end connection microprocessor of analog-to-digital conversion module, micro process
The input terminal of the output end connection display module of device.
4. the steel slag micro mist according to claim 1 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Institute
The waste heat flue gas gas source stated includes that the first pressure charging system and the first regulating valve, the second pressure charging system and the second regulating valve, third increase
Pressure system and third regulating valve, the 4th pressure charging system and the 4th regulating valve；The waste heat gas inlet of first pressure charging system
Blast funnace hot blast stove exhanst gas outlet is connected by the first regulating valve, the waste heat exhanst gas outlet of the first pressure charging system connects residual heat flue machine
First waste heat gas inlet of structure；The waste heat gas inlet of second pressure charging system connects sintered ring by the second regulating valve
Cold third section exhanst gas outlet, the second pressure charging system waste heat exhanst gas outlet connection residual heat flue mechanism the second waste heat flue gas into
Mouthful；The waste heat gas inlet of the third pressure charging system connects heater for rolling steel exhanst gas outlet, third by third regulating valve
The third waste heat gas inlet of the waste heat exhanst gas outlet connection residual heat flue mechanism of pressure charging system；4th pressure charging system
Waste heat gas inlet connects the exhanst gas outlet of gas fired-boiler smoke evacuation system, the waste heat cigarette of the 4th pressure charging system by the 4th regulating valve
4th waste heat gas inlet of gas outlet connection residual heat flue mechanism.
5. the steel slag micro mist according to claim 1 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Institute
The hot-blast stove stated includes heat accumulation room, multiple heat storages, multiple burners, and multiple burners are fixedly installed on outside heat accumulation room
On shell, and multiple burners are successively arranged from top to bottom；Each burner include combustion-supporting gas inlet and coal gas into
Mouthful, and the waste heat exhanst gas outlet of the combustion-supporting gas inlet connection waste heat flue gas booster body of burner, the gas inlet of burner
The gas exit of gas source is connected, the hot-blast outlet of burner is connected to heat accumulation room；Multiple heat storages are from top to bottom
Be fixedly installed on heat accumulation chamber interior, and each heat storage respectively corresponds the interval between a pair of of adjacent burners；The storage
Air distribution flue gas extension tube attached is further fixedly arranged on hot cell, the entrance of the air distribution flue gas extension tube attached is air distribution gas inlet, is matched
The outlet of wind and smoke gas extension tube attached is connected to heat accumulation room.
6. the steel slag micro mist according to claim 5 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Institute
It states air distribution flue gas extension tube attached to be obliquely installed, and the oblique burner direction of air distribution gas inlet of air distribution flue gas extension tube attached, matches wind and smoke
The center line of gas extension tube attached and the angle of heat accumulation room center line are less than or equal to 45o。
7. the steel slag micro mist according to claim 6 using steel plant's waste heat flue gas selects powder system, it is characterised in that：Institute
The number for the air distribution flue gas extension tube attached stated is multiple.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109663447A (en) * | 2019-02-21 | 2019-04-23 | 唐山市神州机械有限公司 | A kind of dry separation system and dry dressing method of the underground based on circulating current |
| CN117366546A (en) * | 2023-12-07 | 2024-01-09 | 四川铭能科技开发有限公司 | Gas turbine tail gas afterburning system based on hot-blast furnace |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0240245A (en) * | 1988-08-01 | 1990-02-09 | Ishikawajima Harima Heavy Ind Co Ltd | Method and device for preventing dew condensation of waste gas from precrushing mill |
| US20030097840A1 (en) * | 2001-11-23 | 2003-05-29 | Hsu Justin Chin-Chung | Koh flue gas recirculation power plant with waste heat and byproduct recovery |
| CN101492756A (en) * | 2009-03-03 | 2009-07-29 | 袁长胜 | Full dry purification and residual heat utilization equipment and method for converter gas |
| CN101551199A (en) * | 2009-04-13 | 2009-10-07 | 杭州锅炉集团股份有限公司 | Recovery method of steel slag residual heat and system thereof |
| CN101716547A (en) * | 2008-10-10 | 2010-06-02 | 卢忠远 | Method for preparing ultra-fine powder by waste heat of plant |
| KR20110012918A (en) * | 2009-07-31 | 2011-02-09 | 한국염색기술연구소 | Device for producing fuel of dyeing wastewater sludge in coal-fired power utility boiler plant and method thereof |
| CN102851420A (en) * | 2012-09-12 | 2013-01-02 | 首钢总公司 | Steelmaking residual heat step recycling method |
| CN103041904A (en) * | 2012-12-25 | 2013-04-17 | 鞍山钢铁集团公司 | Steel slag powder producing method employing roller press |
| CN103776045A (en) * | 2014-01-16 | 2014-05-07 | 西安交通大学 | Method and system for recycling residual heat of ash and slag of liquid slag-tapping boiler |
| CN103939932A (en) * | 2014-04-28 | 2014-07-23 | 中冶华天工程技术有限公司 | Blast furnace gas boiler flue gas waste heat deep recycling system |
| CN104003635A (en) * | 2013-02-21 | 2014-08-27 | 高县天顺建材有限责任公司 | Waste heat grinding process and device |
| CN104402279A (en) * | 2014-10-24 | 2015-03-11 | 中节能六合天融环保科技有限公司 | Preparation technology of tailing ultrafine powder used in cement mixture and concrete admixture |
| CN105312142A (en) * | 2015-11-26 | 2016-02-10 | 鞍山钢铁集团公司矿渣开发公司 | Method for final powder grinding of metallurgical steel slag and production line thereof |
| CN106766966A (en) * | 2017-02-08 | 2017-05-31 | 中冶华天工程技术有限公司 | A kind of heater for rolling steel waste heat recycling system |
| CN206817993U (en) * | 2017-03-13 | 2017-12-29 | 北京汉能清源科技有限公司 | The energy saving transmission device of cement furnace waste heat boiler steam drive cement mill |
| CN208613051U (en) * | 2018-07-26 | 2019-03-19 | 郑州沃特节能科技股份有限公司 | A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system |
-
2018
- 2018-07-26 CN CN201810833674.8A patent/CN108855941B/en active Active
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0240245A (en) * | 1988-08-01 | 1990-02-09 | Ishikawajima Harima Heavy Ind Co Ltd | Method and device for preventing dew condensation of waste gas from precrushing mill |
| US20030097840A1 (en) * | 2001-11-23 | 2003-05-29 | Hsu Justin Chin-Chung | Koh flue gas recirculation power plant with waste heat and byproduct recovery |
| CN101716547A (en) * | 2008-10-10 | 2010-06-02 | 卢忠远 | Method for preparing ultra-fine powder by waste heat of plant |
| CN101492756A (en) * | 2009-03-03 | 2009-07-29 | 袁长胜 | Full dry purification and residual heat utilization equipment and method for converter gas |
| CN101551199A (en) * | 2009-04-13 | 2009-10-07 | 杭州锅炉集团股份有限公司 | Recovery method of steel slag residual heat and system thereof |
| KR20110012918A (en) * | 2009-07-31 | 2011-02-09 | 한국염색기술연구소 | Device for producing fuel of dyeing wastewater sludge in coal-fired power utility boiler plant and method thereof |
| CN102851420A (en) * | 2012-09-12 | 2013-01-02 | 首钢总公司 | Steelmaking residual heat step recycling method |
| CN103041904A (en) * | 2012-12-25 | 2013-04-17 | 鞍山钢铁集团公司 | Steel slag powder producing method employing roller press |
| CN104003635A (en) * | 2013-02-21 | 2014-08-27 | 高县天顺建材有限责任公司 | Waste heat grinding process and device |
| CN103776045A (en) * | 2014-01-16 | 2014-05-07 | 西安交通大学 | Method and system for recycling residual heat of ash and slag of liquid slag-tapping boiler |
| CN103939932A (en) * | 2014-04-28 | 2014-07-23 | 中冶华天工程技术有限公司 | Blast furnace gas boiler flue gas waste heat deep recycling system |
| CN104402279A (en) * | 2014-10-24 | 2015-03-11 | 中节能六合天融环保科技有限公司 | Preparation technology of tailing ultrafine powder used in cement mixture and concrete admixture |
| CN105312142A (en) * | 2015-11-26 | 2016-02-10 | 鞍山钢铁集团公司矿渣开发公司 | Method for final powder grinding of metallurgical steel slag and production line thereof |
| CN106766966A (en) * | 2017-02-08 | 2017-05-31 | 中冶华天工程技术有限公司 | A kind of heater for rolling steel waste heat recycling system |
| CN206817993U (en) * | 2017-03-13 | 2017-12-29 | 北京汉能清源科技有限公司 | The energy saving transmission device of cement furnace waste heat boiler steam drive cement mill |
| CN208613051U (en) * | 2018-07-26 | 2019-03-19 | 郑州沃特节能科技股份有限公司 | A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109663447A (en) * | 2019-02-21 | 2019-04-23 | 唐山市神州机械有限公司 | A kind of dry separation system and dry dressing method of the underground based on circulating current |
| CN109663447B (en) * | 2019-02-21 | 2024-03-08 | 唐山神州机械集团有限公司 | Underground dry separation system and method based on circulating air flow |
| CN117366546A (en) * | 2023-12-07 | 2024-01-09 | 四川铭能科技开发有限公司 | Gas turbine tail gas afterburning system based on hot-blast furnace |
| CN117366546B (en) * | 2023-12-07 | 2024-03-19 | 四川铭能科技开发有限公司 | Gas turbine tail gas afterburning system based on hot-blast furnace |
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