CN209322919U - Environment-friendly white-removing treatment and waste heat utilization system for blast furnace slag - Google Patents
Environment-friendly white-removing treatment and waste heat utilization system for blast furnace slag Download PDFInfo
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- CN209322919U CN209322919U CN201822213767.9U CN201822213767U CN209322919U CN 209322919 U CN209322919 U CN 209322919U CN 201822213767 U CN201822213767 U CN 201822213767U CN 209322919 U CN209322919 U CN 209322919U
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- 239000002893 slag Substances 0.000 title claims abstract description 68
- 239000002918 waste heat Substances 0.000 title claims abstract description 14
- 238000001914 filtration Methods 0.000 claims abstract description 139
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 114
- 238000005469 granulation Methods 0.000 claims abstract description 53
- 230000003179 granulation Effects 0.000 claims abstract description 53
- 238000001816 cooling Methods 0.000 claims abstract description 32
- 230000007613 environmental effect Effects 0.000 claims abstract description 19
- 239000007921 spray Substances 0.000 claims description 44
- 239000003818 cinder Substances 0.000 claims description 28
- 238000012545 processing Methods 0.000 claims description 21
- 238000012360 testing method Methods 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 9
- 238000005057 refrigeration Methods 0.000 claims description 7
- 238000010926 purge Methods 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 20
- 238000011010 flushing procedure Methods 0.000 abstract description 11
- 230000008569 process Effects 0.000 abstract description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 7
- 229910052717 sulfur Inorganic materials 0.000 abstract description 7
- 239000011593 sulfur Substances 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 5
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 description 17
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 10
- 230000009471 action Effects 0.000 description 9
- 238000005457 optimization Methods 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 239000000446 fuel Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000010791 quenching Methods 0.000 description 5
- 230000000171 quenching effect Effects 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 238000004064 recycling Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000003915 air pollution Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 241001062472 Stokellia anisodon Species 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a blast furnace slag environmental protection disappears and whitely handles and waste heat utilization system, including granulation tower (4), chimney (1), filtering ponds (9), first waste heat refrigerator (16), second waste heat refrigerator (32), cooling tower (43) and tank (44), granulation tower (4) are connected with chimney (1) through granulation tower steam conduit (2), and the lower part of granulation tower (4) is passed through slag-water mixture pipeline (6) and is connected with filtering ponds (9), and the lower part of chimney (1) is passed through condensate water shower water piping (5) and is connected with filtering ponds (9). The environment-friendly white-eliminating treatment and waste heat utilization system for the blast furnace slag can fully recover steam heat energy in the granulation process, can also recover heat energy of slag flushing water in the filter tank and steam, simultaneously reduces the workload of the cooling tower, can also reduce the emission of sulfur-containing steam in the slag treatment process, realizes white-eliminating treatment, and really realizes energy conservation, emission reduction and effective cyclic utilization of energy.
Description
Technical field
The utility model relates to metallurgy industries to smelt iron field, and particularly a kind of blast furnace cinder environmental protection disappears white processing and waste heat
Utilize system.
Background technique
It can be generated when blast furnace process high-temperature liquid state slag (1350 DEG C -1500 DEG C), domestic annual 700000000 tons of molten iron of production produces
Raw 2.5 hundred million tons of high-temperature liquid state slag.The correlative study of many years has been carried out both at home and abroad, it is desirable to blast furnace cinder heat is made full use of,
Realize heat recovery.
Chinese patent CN106282445B, 2017 publication date January 4 disclose a kind of " recycling blast furnace slag waste heat
Device and recovery method ", this method are mixed with high-temperature liquid state slag using metal ball, obtain 500 DEG C~800 DEG C blast furnace slag and
The solid mixt of metal ball, mixture complete the recycling of broken apart and waste heat by rotating metallic cage, and this method obtains molten
Slag fragment is difficult to realize to be recycled, and the solid mixt of 500 DEG C~800 DEG C of blast furnace slag and metal ball is in rotating metallic cage
Complete broken apart, very serious to the abrasion meeting of metal cage under the condition of high temperature, the operation to equipment life and whole system
Rate can be generated and be seriously affected.
Precipitating filtration method (often claiming bottom filter method) grain slag technique is generallyd use both at home and abroad to handle slag.State of Blast Furnace is advanced
Row hydraulic discharged slag after being smashed slag with water quenching, becomes loose slag-water slurry (often claiming grain slag), grain slag enters through sluice
Filtering ponds, liquid water are filtered through the filtering layer in filtering ponds, are left solid wet slag particle in filtering bottom of pond portion, are then passed through bridge
Formula grab bucket crane grabs slag particle, entrucking is transported outward.Slag particle (partial size 0.2mm~3mm) purposes obtained after water quenching is wide
It is general, it can be used as cement materials, thermal insulating filling etc., clinker made to be fully used.
(about 70 DEG C~90 DEG C) of blast furnace slag quenching water are used as a kind of temperature waste heat sources, have the characteristics that temperature is stable, flow is big,
For the UTILIZATION OF VESIDUAL HEAT IN of washing slag water, Chinese patent CN207585372U discloses " blast furnace punching July 6 2018 publication date
Washing slag water is led to circulatory pool by elevator pump, drainage tube by pulp water afterheat utilizing system ", the system, and circulatory pool connects heating pump,
The water outlet of heating pump connects sintered mix water pipeline by water supplying pipe, and it is dense that circulatory pool also connects dynamics factory by first pipe
Brine discharge tube line, can also be by heat exchanger after, after the waste heat of superfluous water is made full use of inject circulatory pool follow
Ring uses.Washing slag water is led to circulatory pool from pond and other measures is taken to carry out UTILIZATION OF VESIDUAL HEAT IN again by the system, can be lost so big
Calorimetric amount is unfavorable for the thermal energy recycling of washing slag water.
Patent CN207121610U, March 20 2018 publication date disclose " blast furnace slag flushing vapor waste heat recycling
Utilize system ", which will be delivered to steam accumulation of heat through steam reheater after the collection of flushing cinder water vapour using extractor fan
Device, lithium bromide refrigerating water dispenser group, are finally condensed into condensed water for steam and generate chilled water.The system is needed in original grain slag system
Additional mating large number of equipment on the basis of system, such as extractor fan, steam reheater, steam accumulator, gas-liquid heat exchanger
Deng system flow complexity, equipment investment height；Not only there are a large amount of washing slag waters (about into washing slag water circulating water pool in the system
70 DEG C~90 DEG C), there are also the slag particle obtained after slag water quenching, other part steam (about 60 DEG C~100 DEG C) cannot be by draught hood
Trapping can enter circulating water pool along pipeline, and the washing slag water of circulating water pool and the heat of steam are not recycled adequately.
Patent CN101265039B 2008 publication dates September 17th, discloses a kind of " environment-friendly type bottom filter process State of Blast Furnace
Slag treatment equipment and processing method ", this method can reduce flushing cinder water, reduce water consume, improve the rate of filtration, reduce filtering ponds
Occupied area, the technology have been applied for many years and have achieved good result.The water quenching of high-temperature liquid state slag is by recirculated water (about 40
DEG C) complete, it needs to use after cooling down washing slag water (about 70 DEG C~90 DEG C), in the method, washing slag water is through filtering
Cooling tower is directly got to by upper tower pump after pipe to be cooled down, and not only wastes the thermal energy of washing slag water, and increase cooling tower
Workload.
By being analyzed above it is found that although the recoverable side of blast furnace grain slag system filtering ponds heat has been provided in the prior art
Method, but there have various defects to have in different degrees of and different aspect to be to be solved, it is necessary to study new blast furnace grain slag system mistake
Filter tank heat energy recovering method realizes that the Efficient Cycle of the energy utilizes and reduces air pollution.
In the treatment process of blast furnace cinder, a large amount of high-temperature steams of existing granulation also have filtering ponds temperature stabilization, stream
Big washing slag water is measured, there are also steam existing for filtering ponds surface long term when flushing cinder, recycles the thermal energy of these washing slag waters and steam simultaneously
The putting idle discharge of sulfur-bearing steam is reduced to be of great significance for energy-saving and emission-reduction.
Utility model content
In order to recycle the thermal energy in blast furnace granulated slag, the utility model provides a kind of blast furnace cinder environmental protection and disappears white processing and remaining
Heat utilization system, which disappears white processing and afterheat utilizing system can sufficiently recycle the steam heat of granulation
Can, the thermal energy of filtering ponds washing slag water and steam can be also recycled, while reducing the workload of cooling tower, can also reduced at slag
The white processing that disappears is realized in the discharge of science and engineering skill sulfur-bearing steam, really realizes that the Efficient Cycle of energy-saving and emission-reduction and the energy utilizes.
The utility model solves that technical application used by its technical problem is novel to be: a kind of blast furnace cinder environmental protection disappears white place
Reason and afterheat utilizing system, including granulation tower, chimney, filtering ponds, the first engine exhaust-powered refrigerator, the second engine exhaust-powered refrigerator, cooling tower
And tank, granulation tower by be granulated tower jet chimney connect with chimney, be granulated tower lower part pass through slag-water slurry pipeline and
The lower part of filtering ponds connection, chimney is connect by condensed water shower water pipeline with filtering ponds, and the top of filtering ponds passes through filtering ponds
Jet chimney is connect with chimney, and the first engine exhaust-powered refrigerator is arranged on filtering ponds jet chimney, filtering ponds, the second utilizing waste heat for refrigeration
Machine, cooling tower and tank are sequentially connected in series.
Granulator and heat exchanger are provided in granulation tower, granulator is located at the lower section of the high-temperature slag entrance of granulation tower, changes
Hot device is located at the top of granulator, is granulated the high-temperature slag entrance of tower between heat exchanger and granulator.
It is granulated tower jet chimney and is equipped with the first air-introduced machine, granulation tower jet chimney and the junction for being granulated tower are located at heat exchange
The top of device.
Spray equipment, demister and back purge system, filtering ponds jet chimney and cigarette are successively arranged in chimney from bottom to top
The junction of chimney is located at the lower section of spray equipment, and the junction for being granulated tower jet chimney and chimney also is located under spray equipment
Side, spray equipment contain along the circumferential uniform alternately arranged long spray gun of chimney and short spray gun, long spray gun and short spray gun uniformly
It is disposed with multiple high-pressure nozzles.
The filtering ponds contain the first filtering point pond being disposed adjacent side by side and the second filtering point pond, the top of the filtering ponds
Portion is equipped with removable vapour hood, and removable vapour hood can seal the first filtering point pond or the second filtering point pond.
The top in the first filtering point pond and the second filtering point pond is equipped with steam outlet, the steam outlet and filtering ponds
Jet chimney connection, filtering ponds jet chimney are equipped with the second air-introduced machine.
The high-temperature steam of first filtering point pond or the second filtering point pond discharge, which is able to enter in the first engine exhaust-powered refrigerator, to do work,
The high-temperature steam is able to enter in chimney after acting, and the first engine exhaust-powered refrigerator is connected with the first heat exchange pipeline, first heat exchange
The first heat transferring medium in pipeline can be freezed in the first engine exhaust-powered refrigerator and enter air-conditioner set after cooling.
Second engine exhaust-powered refrigerator is set in pump house, and between filtering ponds and tank, cooling tower is located at pump house
The top of tank.
The high temperature filtration water energy flowed out in filtering ponds is enough to do work in the second engine exhaust-powered refrigerator, the connection of the second engine exhaust-powered refrigerator
Have the second heat exchange pipeline, this second heat exchange pipeline in second heat transferring medium can be freezed in the second engine exhaust-powered refrigerator and
Enter air-conditioner set after cooling.
Tank is connect by waterline with granulation tower and chimney, and the outlet at bottom of filtering ponds was externally connected with drainage inspection
Analytical unit is surveyed, this is crossed drainage and tests and analyzes water quality, temperature and flow that unit was able to detect drainage.
The beneficial effects of the utility model are:
1, the utility model can sufficiently in the steam and filtering ponds of melt back Slag treatment process washing slag water thermal energy, realize energy
The Efficient Cycle in source utilizes.
2, the utility model proposes the steam treatment measures sprayed afterwards that first exchanges heat, it is possible to reduce slag treatment process sulfur-bearing
The white processing that disappears is realized in the discharge of steam, reduces air pollution.
3, high temperature filtration water temperature after heat exchanger is handled reduces, and can reduce the workload of cooling tower, realizes efficient
It is cooling.
4, the utility model uses the engine exhaust-powered refrigerator of motorless heat exchanger and low energy consumption, effect low with operating cost
The high advantage of benefit.
5, the utility model tests and analyzes the water quality for crossing drainage, while detecting the temperature of drainage, flow, and handle
All testing results are timely fed back to blast furnace central control system, to optimization blast furnace raw material and fuel quality and proportion, optimization blast furnace operating, promote
It plays an important role into smooth operation of furnace.
Detailed description of the invention
The accompanying drawings constituting a part of this application is used to provide a further understanding of the present invention, this is practical
Novel illustrative embodiments and their description are not constituteed improper limits to the present invention for explaining the utility model.
Fig. 1 be blast furnace cinder environmental protection described in the utility model disappear it is white processing and afterheat utilizing system top view.
Fig. 2 is the structural schematic diagram for being granulated tower.
Fig. 3 is the structural schematic diagram of chimney, filtering ponds, pump house, cooling tower and tank.
Fig. 4 is the top view of spray equipment.
1, chimney；2, it is granulated tower jet chimney；3, the first air-introduced machine；4, it is granulated tower；5, condensed water shower water pipeline；6, slag
Aqueous mixtures pipeline；71, the first valve；72, the second valve；81, the first filtering ponds pipeline；82, the second filtering ponds pipeline；9, mistake
Filter tank；91, the first filtering divides pond；92, the second filtering divides pond；10, heat exchanger；11, granulator；12, back purge system；13, it removes
Foam device；14, spray equipment；15, filtering ponds jet chimney；16, the first engine exhaust-powered refrigerator；17, the first electric butterfly valve；18, first
Hand-operated butterfly valve；19, vapour hood is moved；20, the second Hand-operated butterfly valve；21, the second electric butterfly valve；22, the first check valve；23,
Three Hand-operated butterfly valves；24, third electric butterfly valve；25, thermometer；26, flowmeter；27, the 4th Hand-operated butterfly valve；28, heat-exchanger pump；29,
Second one-way valve；30, the 4th electric butterfly valve；31, the 5th Hand-operated butterfly valve；32, the second engine exhaust-powered refrigerator；33, upper tower pump；34,
Six Hand-operated butterfly valves；35, the 7th Hand-operated butterfly valve；36, slag flushing pump；37, third check valve；38, the 5th electric butterfly valve；39, the 8th hand
Dynamic butterfly valve；40, long spray gun；41, short spray gun；42, high-pressure nozzle；43, cooling tower；44, tank；45, the second air-introduced machine；46,
Air-conditioner set；47, pump house.
Specific embodiment
It should be noted that in the absence of conflict, the features in the embodiments and the embodiments of the present application can phase
Mutually combination.The utility model will be described in detail below with reference to the accompanying drawings and embodiments.
A kind of blast furnace cinder environmental protection disappears white processing and afterheat utilizing system, including granulation tower 4, chimney 1, filtering ponds 9, first
Engine exhaust-powered refrigerator 16, the second engine exhaust-powered refrigerator 32, cooling tower 43 and tank 44, granulation tower 4 by granulation tower jet chimney 2 with
Chimney 1 connects, and the lower part of granulation tower 4 is connect by slag-water slurry pipeline 6 with filtering ponds 9, and the lower part of chimney 1 passes through condensed water
Shower water pipeline 5 is connect with filtering ponds 9, and the top of filtering ponds 9 is connect by filtering ponds jet chimney 15 with chimney 1, and more than first
Refrigerating machine 16 is arranged on filtering ponds jet chimney 15, filtering ponds 9, the second engine exhaust-powered refrigerator 32, cooling tower 43 and tank
44 are sequentially connected in series,.
In the present embodiment, it as shown in Figure 1, granulation tower 4, chimney 1 and filtering ponds 9 are triangularly arranged, is granulated in tower 4 and sets
It is equipped with granulator 11 and heat exchanger 10, granulator 11 is located at the lower section of the high-temperature slag entrance of granulation tower 4, and heat exchanger 10 is located at grain
Change the top of device 11, is granulated the high-temperature slag entrance of tower 4 between heat exchanger 10 and granulator 11.Granulator is located at granulation tower
Below the entrance of high-temperature slag, vapor heat exchanger is located at the top of granulator close to granulation top of tower.
In the present embodiment, granulation tower jet chimney 2 is equipped with the first air-introduced machine 3, granulation tower jet chimney 2 and granulation tower
4 junction is located at the upper end of granulation tower 4, and granulation tower jet chimney 2 is located at the upper of heat exchanger 10 with the junction for being granulated tower 4
Side.Non-condensing steam introduces chimney by air-introduced machine from the jet chimney of granulation top of tower side in granulation tower.
In the present embodiment, spray equipment 14, demister 13 and back purge system are successively arranged in chimney 1 from bottom to top
12, the junction of filtering ponds jet chimney 15 and chimney 1 is located at the lower section of spray equipment 14, is granulated tower jet chimney 2 and chimney 1
Junction also be located at the lower section of spray equipment 14, one or more layers can be set in spray equipment 14, and spray equipment 14 contains edge
Circumferential uniformly alternately arranged long spray gun 40 and the short spray gun 41 of chimney 1 have been evenly arranged on long spray gun 40 and short spray gun 41 more
A high-pressure nozzle 42, as shown in Figure 4.
In the present embodiment, the filtering ponds 9 contain the first filtering point pond 91 being disposed adjacent side by side and the second filtering point
Pond 92, the top of the filtering ponds 9 are equipped with removable vapour hood 19, and removable vapour hood 19 can seal the first filtering point pond 91
Or second filtering divide pond 92.Removable vapour hood is set at the top of filtering ponds, and when flushing cinder, removable vapour hood realized filtering ponds
Sealing, avoids sulfur-bearing steam from putting idle discharge；Flushing cinder removes vapour hood after stopping to grab slag particle in slag operation cleaning filtering ponds.
In the present embodiment, the top in the first filtering point pond 91 and the second filtering point pond 92 is equipped with steam outlet, should
Steam outlet is connect with filtering ponds jet chimney 15, and filtering ponds jet chimney 15 is equipped with the second air-introduced machine 45.Second air inducing
Machine 45 sequentially enters filtering ponds steam pipe after the steam in the first filtering point pond 91 and the second filtering 92 surface of point pond capable of being detached
Road 15 and the first engine exhaust-powered refrigerator 16.Condensed water shower water pipeline 5 can pass through the first filtering ponds pipeline 81 and the second mistake respectively
Filter tank pipeline 82 is correspondingly connected with the first filtering point pond 91 and the second filtering point pond 92, and slag-water slurry pipeline 6 can lead to respectively
The first filtering ponds pipeline 81 and the second filtering ponds pipeline 82 is crossed to be correspondingly connected with the first filtering point pond 91 and the second filtering point pond 92,
As shown in Figure 1.
In the present embodiment, the high-temperature steam that the first filtering point pond 91 or the second filtering point pond 92 are discharged is able to enter first
It does work in engine exhaust-powered refrigerator 16, which can be entered in chimney 1 after acting by filtering ponds jet chimney 15, and first
Engine exhaust-powered refrigerator 16 is connected with the first heat exchange pipeline, the first heat transferring medium (normal-temperature water or other Jie in the first heat exchange pipeline
Matter) it can be freezed in the first engine exhaust-powered refrigerator 16 and enter air-conditioner set 46 after cooling, which can
It is recycled between the first engine exhaust-powered refrigerator 16 and air-conditioner set 46.
In the present embodiment, the second engine exhaust-powered refrigerator 32 is set in pump house 47, and pump house 47 is located at filtering ponds 9 and storage
Between pond 44, cooling tower 43 is located at the top of tank 44, and more series connection or simultaneously can be set into the second engine exhaust-powered refrigerator 32
The mode of connection.First engine exhaust-powered refrigerator 16 and the second engine exhaust-powered refrigerator 32 all can be suction-type lithium bromide engine exhaust-powered refrigerators.
In the present embodiment, the high temperature filtration water energy flowed out in filtering ponds 9 is enough to do work in the second engine exhaust-powered refrigerator 32, the
Two engine exhaust-powered refrigerators 32 are connected with the second heat exchange pipeline, this second heat exchange pipeline in the second heat transferring medium (normal-temperature water or other
Medium) it can be freezed in the second engine exhaust-powered refrigerator 32 and enter air-conditioner set 46, the second heat transferring medium energy after cooling
It is enough to be recycled between the second engine exhaust-powered refrigerator 32 and air-conditioner set 46, as shown in Figure 3.
In the present embodiment, tank 44 is connect by waterline with granulation tower 4 and chimney 1, and the bottom of filtering ponds 9 goes out
Mouth was externally connected with drainage and tests and analyzes unit, this cross drainage test and analyze unit be able to detect the water quality of drainage, temperature and
Flow.
High temperature filtration water temperature under the action of the second engine exhaust-powered refrigerator 32, which reduces, becomes filter at low temperature water, filter at low temperature water
Enter tank after further cooling down into cooling tower, it is spare as low temperature washing slag water, conveying water, shower water, realized drainage
Recycle.
At filtering ponds outlet at bottom, the water quality for crossing drainage is tested and analyzed, while detecting the temperature of drainage, stream
Amount, and all testing results are timely fed back to blast furnace central control system, optimization blast furnace raw material and fuel quality and proportion, optimization blast furnace behaviour
Make, promote smooth operation of furnace.
Be described below the blast furnace cinder environmental protection disappear it is white processing and afterheat utilizing system the course of work.
Granulator 11 is set below the entrance of the high-temperature slag (1350 DEG C~1500 DEG C) of granulation tower 4, high-temperature slag exists
Granulation is completed under the action of a large amount of high speed granulation water, slag-water slurry falls into the bottom of granulation tower 4.It is defeated to be granulated the introducing of 4 bottom of tower
Water (about 40 DEG C~45 DEG C) are sent, under the action of conveying water, slag-water slurry enters filtering ponds.
Vapor heat exchanger 10 is set at the top of granulation tower 4 in the top of granulator 11, grain is arranged in granulation 4 top-side of tower
Change tower jet chimney 2 and the first air-introduced machine 3.Under the action of the first air-introduced machine 3, the steam generated during slag granulating is (about
80 DEG C~100 DEG C) it is being granulated 4 moved upward inside of tower, when steam passes through heat exchanger 10, it is introduced into the normal-temperature water of heat exchanger 10
(about 25 DEG C~35 DEG C) absorb a large amount of thermal energy and become hot water (about 60 DEG C~80 DEG C), and a large amount of steam are condensed into water in heat transfer process
It is dropped into granulation 4 bottom of tower.Non-condensing steam enters chimney 1 from the granulation tower jet chimney 2 of granulation 4 top-side of tower.
One layer of (or multilayer) spray equipment 14, foam removal are sequentially arranged above what granulation tower jet chimney 2 exported in chimney 1
Device 13, back purge system 12.
Spray equipment 14 is by the multiple long spray guns 40 and short spray gun 41 that uniform crossover is arranged on 1 inside sustained height of chimney
It forms, is evenly arranged multiple high-pressure nozzles 42 on long spray gun and short spray gun.According to process requirements, can be arranged on different height
The long spray gun 40 and short spray gun 41 and its subsidiary high-pressure nozzle 42 of many levels.Shower water (about 40 DEG C~45 DEG C) is from high pressure spray
Spray pattern is formed inside chimney after first 42 ejection, the shower water of atomization is uniformly covered with chimney inner space.
After non-condensing steam enters chimney 1, become condensed water, condensed water and shower water under the action of atomizing spray water
1 bottom of chimney is fallen into together enters filtering ponds (the first filtering point pond 91 or the second filtering point pond along condensed water shower water pipeline 5
92).Demister 13 is arranged above spray equipment 14, eliminates non-condensing steam and small water droplet；Back purge system 12 is periodically right
Demister 13 is backwashed, and is blocked after avoiding demister 13 from being used for a long time.
The slag-water slurry pipeline 6 drawn from granulation tower 4 intersects remittance with the condensed water shower water pipeline 5 drawn from chimney 1
It closes, draws two filtering ponds pipelines (the first filtering ponds pipeline 81 and the second filtering ponds pipeline 82) from point and respectively enter first
Filtering point pond 91 or the second filtering divide pond 92.Into the first filtering ponds pipeline 81 and the second filtering ponds pipeline 82 of two filtering ponds
On be separately installed with the first valve 71 and the second valve 72, when needing using first filtering point pond 91, close the second filtering ponds
The second valve 72 on pipeline 82.
Removable vapour hood 19 is set at the top of filtering ponds, the steam of filtering pool surface is sealed；Flushing cinder can after stopping
Moving steam cover 19 is removed to grab slag.Filtering ponds are drawn in position aperture of the filtering ponds side wall at chimney 1 close to top
The steam on surface.Second air-introduced machine 45 is set outside filtering ponds side-wall hole.It is close in the negative pressure and vapour hood of the second air-introduced machine 45
Under the action of envelope, the steam on 9 surface of filtering ponds is pulled out filtering ponds into the first engine exhaust-powered refrigerator 16.
Normal-temperature water (about 25 DEG C~35 DEG C) becomes low-temperature cold water (about 5 DEG C~15 after the first engine exhaust-powered refrigerator 16 refrigeration
DEG C), most of steam condenses into water droplet under the action of the first engine exhaust-powered refrigerator 16, and filtering ponds are entered together with slag-water slurry
9, fraction steam is not condensed into chimney 1, is become water droplet under the action of spray equipment 14 in chimney 1, is fallen into chimney bottom
Portion enters filtering ponds 9.
Second engine exhaust-powered refrigerator 32 is set in pump house 47, and high temperature filtration water (about 70 DEG C~90 DEG C) is from filtering bottom of pond portion
By the second engine exhaust-powered refrigerator 32 after outflow, complete to treat refrigerant (normal-temperature water or other media) in heat exchanging process
Refrigeration.
Normal-temperature water (about 25 DEG C~35 DEG C) is after the second engine exhaust-powered refrigerator 32 (suction-type lithium bromide engine exhaust-powered refrigerator) refrigeration
As low-temperature cold water (about 5 DEG C~15 DEG C), enter air-conditioner set 46 by check valve, electric butterfly valve and Hand-operated butterfly valve.High temperature mistake
Drainage enters the second utilizing waste heat for refrigeration after heat-exchanger pump 28, second one-way valve 29, the 4th electric butterfly valve 30 and the 5th Hand-operated butterfly valve 31
Machine 32, temperature, which reduces, under the action of the second engine exhaust-powered refrigerator 32 becomes filter at low temperature water (about 50 DEG C~60 DEG C), filter at low temperature
Water enters cooling tower 43 through upper tower pump 33 and the 6th Hand-operated butterfly valve 34, complete it is cooling after become cooling water (about 40 DEG C~45 DEG C) into
Enter tank 44 to store for future use.When needing flushing cinder, cooling water is drawn from water storage bottom of pond portion, promotes power through slag flushing pump 36, then
Granulator 11 is guided into through third check valve 37, the 5th electric butterfly valve 38 and the 8th Hand-operated butterfly valve 39 as cryogenic pelletization water, is realized
Cross recycling for drainage.
The cooling water of tank is also used as the spray water circulation use of the conveying water of granulation tower bottom, chimney.
The variation of blast furnace raw material and fuel quality and proportion will lead to the composition transfer of blast furnace cinder, and then change the water of drainage
Matter.At filtering ponds outlet at bottom, the water quality for crossing drainage flowed out after filter layer filtering is tested and analyzed, while temperature being installed
Degree meter 25 and flowmeter 26 detected temperature, the flow of drainage, and all testing results are timely fed back to control in blast furnace and are
System to optimization blast furnace raw material and fuel quality and proportion, optimization blast furnace operating, promotes smooth operation of furnace to play an important role.
The low-temperature cold water (about 5 DEG C~15 DEG C) obtained through suction-type lithium bromide engine exhaust-powered refrigerator can be used as air conditioning water
It is sent to air-conditioner set, production technology is can also be used as with chilled water and is sent to the corresponding system of blast furnace (such as furnace body cooling system).The
One engine exhaust-powered refrigerator 16 and the second engine exhaust-powered refrigerator 32 tool can change heat exchanger into, (about 60 DEG C of the hot water after heat exchanger heats
~70 DEG C) it is widely used, it may be used as bathing pool shower, the heat supply in winter of life water system after introducing user's pipe network, can also use
Make the material humidification preheating etc. of industrial water system.
The thermal energy of washing slag water and steam is effectively recycled in steam and filtering ponds during slag granulating, is reduced
Putting to idle discharge for sulfur-bearing steam realizes that steam disappears white, is of great significance for energy-saving and emission-reduction.
The utility model have the advantage that make full use of steam in granulation tower, washing slag water and steam is remaining in filtering ponds
Heat realizes that the Efficient Cycle of the energy utilizes；The white processing that disappears is realized in the discharge for reducing filtering ponds sulfur-bearing steam, reduces air pollution；
Crossing drainage temperature after engine exhaust-powered refrigerator is handled reduces, and can reduce the workload of cooling tower, realizes efficiently cooling；Using low
The suction-type lithium bromide engine exhaust-powered refrigerator of energy consumption, the electrical equipment in refrigeration cycle is mainly solution pump (circulating pump), power
Only 5kW~10kW has the advantages that operating cost is low, high efficiency.
The utility model tests and analyzes the water quality for crossing drainage, while detecting the temperature of drainage, flow, and institute
There is testing result to be timely fed back to blast furnace central control system, to optimization blast furnace raw material and fuel quality and proportion, optimization blast furnace operating, promotes
Smooth operation of furnace plays an important role.
The above, only specific embodiment of the utility model cannot limit the range that utility model is implemented, institute with it
With the displacement of its equivalent assemblies, or according to equivalent variations made by the utility model patent protection scope and modification, should all still fall within
The scope that this patent is covered.In addition, between technical characteristic and technical characteristic in the utility model, technical characteristic and technical application
Between novel, technical application it is novel it is novel with technical application between use can be freely combined.
Claims (10)
- White processing and afterheat utilizing system 1. a kind of blast furnace cinder environmental protection disappears, which is characterized in that the blast furnace cinder environmental protection disappears white Processing and afterheat utilizing system include granulation tower (4), chimney (1), filtering ponds (9), the first engine exhaust-powered refrigerator (16), the second waste heat Refrigeration machine (32), cooling tower (43) and tank (44), granulation tower (4) are connected by granulation tower jet chimney (2) and chimney (1) It connects, the lower part of granulation tower (4) is connect by slag-water slurry pipeline (6) with filtering ponds (9), and the lower part of chimney (1) passes through condensation Water spray waterpipe (5) is connect with filtering ponds (9), and the top of filtering ponds (9) passes through filtering ponds jet chimney (15) and chimney (1) Connection, the first engine exhaust-powered refrigerator (16) are arranged on filtering ponds jet chimney (15), filtering ponds (9), the second engine exhaust-powered refrigerator (32), cooling tower (43) and tank (44) are sequentially connected in series.
- White processing and afterheat utilizing system 2. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that granulation tower (4) granulator (11) and heat exchanger (10) are provided in, granulator (11) is located under the high-temperature slag entrance of granulation tower (4) Side, heat exchanger (10) are located at the top of granulator (11), and the high-temperature slag entrance of granulation tower (4) is located at heat exchanger (10) and granulation Between device (11).
- White processing and afterheat utilizing system 3. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that granulation tower Jet chimney (2) is equipped with the first air-introduced machine (3), and granulation tower jet chimney (2) and the junction for being granulated tower (4) are located at heat exchanger (10) top.
- White processing and afterheat utilizing system 4. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that chimney (1) it is successively arranged spray equipment (14), demister (13) and back purge system (12), filtering ponds jet chimney from bottom to top in (15) it is located at the lower section of spray equipment (14) with the junction of chimney (1), is granulated the connection of tower jet chimney (2) and chimney (1) Place also is located at the lower section of spray equipment (14), and spray equipment (14) contains the circumferential uniformly alternately arranged long spray along chimney (1) Multiple high-pressure nozzles (42) have been evenly arranged on rifle (40) and short spray gun (41), long spray gun (40) and short spray gun (41).
- White processing and afterheat utilizing system 5. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that the mistake Contain the first filtering point pond (91) and the second filtering point pond (92) being disposed adjacent side by side, the top of the filtering ponds (9) in filter tank (9) Portion is equipped with removable vapour hood (19), and removable vapour hood (19) can seal the first filtering point pond (91) or the second filtering point pond (92)。
- White processing and afterheat utilizing system 6. blast furnace cinder environmental protection according to claim 5 disappears, which is characterized in that the first mistake The top of filter point pond (91) and the second filtering point pond (92) is equipped with steam outlet, the steam outlet and filtering ponds steam pipe Road (15) connection, filtering ponds jet chimney (15) are equipped with the second air-introduced machine (45).
- White processing and afterheat utilizing system 7. blast furnace cinder environmental protection according to claim 6 disappears, which is characterized in that the first mistake The high-temperature steam of filter point pond (91) or the second filtering point pond (92) discharge is able to enter acting in the first engine exhaust-powered refrigerator (16), should High-temperature steam is able to enter in chimney (1) after acting, and the first engine exhaust-powered refrigerator (16) is connected with the first heat exchange pipeline, this first The first heat transferring medium in heat exchange pipeline can be freezed in the first engine exhaust-powered refrigerator (16) and enter air conditioner after cooling Group (46).
- White processing and afterheat utilizing system 8. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that more than second Refrigerating machine (32) is set in pump house (47), and pump house (47) is located between filtering ponds (9) and tank (44), cooling tower (43) it is located at the top of tank (44).
- White processing and afterheat utilizing system 9. blast furnace cinder environmental protection according to claim 8 disappears, which is characterized in that filtering ponds (9) the high temperature filtration water energy flowed out in enough acting, the second engine exhaust-powered refrigerator (32) in the second engine exhaust-powered refrigerator (32) are connected with Second heat exchange pipeline, second second heat transferring medium to exchange heat in pipeline can be freezed simultaneously in the second engine exhaust-powered refrigerator (32) Enter air-conditioner set (46) after cooling.
- White processing and afterheat utilizing system 10. blast furnace cinder environmental protection according to claim 1 disappears, which is characterized in that water storage Pond (44) is connect by waterline with granulation tower (4) and chimney (1), and the outlet at bottom of filtering ponds (9) was externally connected with drainage Unit is tested and analyzed, this is crossed drainage and tests and analyzes water quality, temperature and flow that unit was able to detect drainage.
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| CN109402311A (en) * | 2018-12-27 | 2019-03-01 | 中冶京诚工程技术有限公司 | Environment-friendly white-removing treatment and waste heat utilization system for blast furnace slag |
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| CN109402311A (en) * | 2018-12-27 | 2019-03-01 | 中冶京诚工程技术有限公司 | Environment-friendly white-removing treatment and waste heat utilization system for blast furnace slag |
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