CN209602579U - A kind of blast furnace stops wind flue gas processing device again - Google Patents
A kind of blast furnace stops wind flue gas processing device again Download PDFInfo
- Publication number
- CN209602579U CN209602579U CN201822209583.5U CN201822209583U CN209602579U CN 209602579 U CN209602579 U CN 209602579U CN 201822209583 U CN201822209583 U CN 201822209583U CN 209602579 U CN209602579 U CN 209602579U
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- Prior art keywords
- gas
- blast furnace
- flue gas
- pipeline
- furnace roof
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 239000003546 flue gas Substances 0.000 title claims abstract description 87
- 239000007789 gas Substances 0.000 claims abstract description 65
- 239000000428 dust Substances 0.000 claims abstract description 41
- 239000007788 liquid Substances 0.000 claims abstract description 31
- 238000003795 desorption Methods 0.000 claims abstract description 25
- 239000003034 coal gas Substances 0.000 claims abstract description 8
- 239000002245 particle Substances 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000001816 cooling Methods 0.000 claims description 12
- 229910000831 Steel Inorganic materials 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 7
- 239000010959 steel Substances 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 3
- 239000011152 fibreglass Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- 238000009792 diffusion process Methods 0.000 claims 6
- 239000003245 coal Substances 0.000 claims 1
- 230000000505 pernicious Effects 0.000 abstract description 14
- 206010018987 Haemorrhage Diseases 0.000 abstract description 8
- 230000000740 bleeding Effects 0.000 abstract description 8
- 231100000319 bleeding Toxicity 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 8
- 230000036571 hydration Effects 0.000 abstract description 5
- 238000006703 hydration reaction Methods 0.000 abstract description 5
- 230000002588 toxic Effects 0.000 abstract description 5
- 231100000331 toxic Toxicity 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 9
- 235000019504 cigarettes Nutrition 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 6
- 235000015450 Tilia cordata Nutrition 0.000 description 6
- 235000011941 Tilia x europaea Nutrition 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 239000004571 lime Substances 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 239000000779 smoke Substances 0.000 description 5
- 206010019133 Hangover Diseases 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 210000003800 Pharynx Anatomy 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 238000005299 abrasion Methods 0.000 description 2
- 230000003247 decreasing Effects 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- -1 meanwhile Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229910000617 Mangalloy Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000004642 transportation engineering Methods 0.000 description 1
Abstract
The utility model discloses a kind of blast furnaces to stop wind flue gas processing device again, including blast furnace roof, the first blast furnace roof desorption tube and the second blast furnace roof desorption tube, blast furnace roof is respectively communicated with blast furnace roof No.1 bleeding valve and No. two bleeding valves by furnace roof spherical tank (or coal gas tedge).The utility model passes through cyclone dust collectors, gas cooler, gas-liquid separator, graphited ethylene-steam condenser, flue gas heater, the setting of circulating heat pump and chimney, CO can largely be contained to generating during direct emission, CO2 and dust it is toxic, combustible mixed gas is sufficiently handled, solve the problems, such as that current flue gas processing device cannot sufficiently be handled pernicious gas, avoid air environmental pollution, dust-laden particle in high-temperature flue gas that can be in line to blast furnace recycles, and pernicious gas is subjected to hydration process, so that the flue gas of discharge reaches national emission standard, it is worthy to be popularized.
Description
Technical field
The utility model relates to pernicious gas processing technology field, specially a kind of blast furnace is stopped wind again and is filled with fume treatment
It sets.
Background technique
Damping down and multiple wind are the method for operating blast furnace that blast furnace temporarily ceases production and then resumes production, and blast furnace stops production
It is just off with the basic operation resumed production and blast furnace of blowing in furnace is blown and restored in furnace, in process of production because of inspection
Repair, processing accident or other reasons need interrupt production when, out-of-blast smelting is just called damping down, according to the length of damping down time
Short, damping down 4h or more just claims long term blowing-down.Damping down 4h hereinafter, then claim short term damping-down, long term blowing-down can be divided into again plan damping down with
Unplanned (accident) damping down, plan damping down can also be divided into the full furnace charge damping down of plan and plan drop part charge level damping down.
Blast furnace is stopped, under multiple wind state, a large amount of coal gas of high temperature will be discharged from blast furnace roof desorption tube, in these coal gas of high temperature
Containing a large amount of dust, the white flue gas given off will seriously pollute environment, due to desorption tube top saturation wet flue gas stream with
Cold air contact outside desorption tube, the decline of wet flue gas temperature, moisture are in hypersaturated state, form droplet, therewith, droplet meeting
Accumulation forms big drop, starts secondary condensation and forms water mist, until humid air temperature is substantially close to big temperature at bleeder top
Degree, secondary condensation reaches the water mist hangover for utmostly forming desorption tube top, belongs to hypersaturated state, therefore generates a large amount of
Plumage mist contains toxic, the combustible mixing pernicious gas of a small amount of CO, CO2 and dust in these plumage mists, with the row of flue gas
It puts, drifts in atmosphere, atmosphere is polluted, form acid rain, destroy atmospheric strument, building etc..
The flue gas of blast furnace roof release at present generated during direct emission largely containing CO, CO2 and dust it is toxic, can
Combustion things mixed gas, causes air environmental pollution, as country keeps under strict control to environmental protection, takes newly-increased environmentally friendly tax, formulates and avoid the peak hour
Limited production strictly monitors discharge state, and most enterprises take the late into the night to stop, multiple wind measure, do not have to evade the monitoring of country
Have fundamentally to give and solve.
Utility model content
The purpose of this utility model is to provide a kind of blast furnaces to stop wind flue gas processing device again, and having can be to blast furnace flue gas
In pernicious gas the advantages of sufficiently being handled, pernicious gas cannot sufficiently be located by solving current flue gas processing device
The problem of reason.
To achieve the above object, the utility model provides the following technical solutions: a kind of blast furnace is stopped wind again and is filled with fume treatment
It sets, including blast furnace roof is referred to as blast furnace roof No.1 bleeding valve and No. two bleeding valves, the blast furnace roof passes through
Furnace roof spherical tank (or coal gas tedge) is respectively communicated with referred to as blast furnace roof No.1 bleeding valve and No. two bleeding valves, institute
It states No.1 bleeding valve and No. two bleeding valves passes through release cross over pipe connection, referred to as release general pipeline, the release
The tube wall surface of general pipeline is equipped with release main valve, and the release general pipeline is communicated with cyclone dust removal far from one end of release cross over pipe
Device, the cyclone dust collectors are communicated with blast furnace bucket by pipeline, the pipeline peace between the cyclone dust collectors and blast furnace bucket
Equipped with particulate matter unloading valve；
The exhaust pipe of the cyclone dust collectors is communicated with gas cooler, the exhaust pipe of the gas cooler by pipeline
It is communicated with gas-liquid separator by pipeline, the outlet of the gas-liquid separator is communicated with graphited ethylene-steam by pipeline and condenses
Device, the graphited ethylene-steam condenser gas outlet are communicated with flue gas heater, the flue gas heater and cigarette by pipeline
Circulating heat pump is communicated with by pipeline between Gas Cooler, the flue gas heater gas outlet is communicated with smoke evacuation cigarette by pipeline
Chimney.
Preferably, the inner wall of the cyclone dust collectors is equipped with wear-resistant liner, and the gas cooler uses the water of shell and tube
Direct cooling mode, cooling capacity are 600 cubes/min~3500 cube/min.
Preferably, the separation method of the gas-liquid separator is ultra-filtration and separation, and the different gas-liquid mixture of particle passes through micro-
Hole filter is sieved, and for liquid because gravity downstream to separator bottom and is discharged, gas enters graphited ethylene-steam condensation
Device.
Preferably, the condensation of a large amount of DN20 is housed in the graphited ethylene-steam condenser association system all parts
Steel pipe, and condense steel duct and be coated with graphite ene coatings, manage it is outer spray water evaporation, inner tube smoke by shower water evaporation endothermic into
One step is cooling, and the heat power source of the circulating heat pump is the heat of untreated flue gas at gas cooler, and the circulating heat pump is logical
Water is crossed to be media for heat exchange and transfer heat to flue gas heater.
Preferably, the height of the chimney is not less than the first blast furnace roof desorption tube and the second blast furnace roof desorption tube
Height, and chimney is steel construction and glass reinforced plastic mixed structure form.
Compared with prior art, the beneficial effects of the utility model are as follows:
, the utility model by cyclone dust collectors, gas cooler, gas-liquid separator, graphited ethylene-steam condenser,
The setting of flue gas heater, circulating heat pump and chimney, can to generated during direct emission largely containing CO, CO2 and
Toxic, the combustible mixed gas of dust are sufficiently handled, solve current flue gas processing device cannot to pernicious gas into
The problem of row is sufficiently handled, avoids air environmental pollution, and not wind flue gas processing device can be in line to blast furnace again for the blast furnace
High-temperature flue gas in dust-laden particle recycled, and pernicious gas is subjected to hydration process, so that the flue gas of discharge reaches state
Family's discharge standard, is worthy to be popularized.
, the utility model by setting cyclone dust collectors and cyclone dust collectors inner wall be equipped with wear-resistant liner, be to keep away
Exempt from containing a large amount of particulate matter flue dust by pipeline to ground, so that the abrasion of pipeline is caused, by the way that chimney is arranged
Height be not less than the first blast furnace roof desorption tube and the second blast furnace roof desorption tube height, can guarantee certain negative pressure
Amount, by the setting of particulate matter unloading valve, its effect is particulate matter after collecting to cyclone dust collectors and dust to high furnace charge
It is discharged in tank, to avoid the pollution to environment and the waste of the energy, by the setting of gas cooler, its cooling can
Further flue gas is dusted and pernicious gas is subjected to hydration process, passes through the setting of gas-liquid separator, its effect
It is that the flue gas after dedusting is pipelined to ground, due to the conveying of long range, former high-temperature flue gas is cooled down, cigarette
It is temperature-fall period when being conveyed in pipeline containing the saturated flue gas for detaching moisture in gas, a part of condensable gas group branch shape
It is flowed at droplet with gas, meanwhile, flue gas water increases after gas cooler, after gas-liquid separator, gas
The effect of liquid/gas separator is exactly the gas for handling this two parts and containing a small amount of lime set, realizes lime set recycling and by a part of gas phase
Purification, by the setting of graphited ethylene-steam condenser, its main function is while further decreasing flue-gas temperature, to subtract
Water droplet quantity entrained by few flue gas, can substantially slough 80%~90% flue gas, pass through the setting of flue gas heater, flue gas warp
After crossing heating, unsaturated higher temperatures flue gas is formed, is not easy to form plume and hangover at throat after chimney discharge.
Detailed description of the invention
Fig. 1 be the utility model Europe gallop furnace roof diffuse technical module figure；
Fig. 2 be the utility model Europe gallop furnace roof diffuse process flow chart；
Fig. 3 is the structural front view of the utility model cyclone dust collectors；
Fig. 4 is the structure top view of the utility model cyclone dust collectors.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Please refer to Fig. 1-3, a kind of blast furnace stops wind flue gas processing device again, including blast furnace roof, the first blast furnace roof are put
Separate tube and the second blast furnace roof desorption tube, blast furnace roof have been respectively communicated with the first blast furnace roof desorption tube and by furnace roof spherical tank
Two blast furnace roof desorption tubes, the first blast furnace roof desorption tube and the second blast furnace roof desorption tube pass through release cross over pipe and are communicated with
General pipeline is diffused, the tube wall surface for diffusing general pipeline is equipped with release main valve, and release general pipeline is communicated with far from one end of release cross over pipe
Cyclone dust collectors, the inner walls of cyclone dust collectors are equipped with wear-resistant liner, and the shape of cyclone dust collectors is circle, diameter from 0.9 meter to
2.5 meters are differed, and cyclone dust collectors are made of different modules, are divided into: shell, exhaust inner tube, it is resistance to that inner walls are equipped with microlite
Grind layer, the length for being vented inner tube is 0.9 meter~1.5 meters, have and be made with a thickness of 12mm manganese steel plate, microlite with a thickness of 16mm,
It is pasted using dedicated special clay, the dust-contained airflow inside cyclone dust collectors rotates, by means of centrifugal force by grit
Wall is separated and be trapped in from air-flow, then so that grit is fallen into ash bucket by gravity, passes through setting cyclone dust collectors and rotation
The inner wall of wind deduster is equipped with wear-resistant liner, be in order to avoid containing a large amount of particulate matter flue dust by pipeline to ground,
To cause the abrasion of pipeline, cyclone dust collectors are communicated with blast furnace bucket by pipeline, between cyclone dust collectors and blast furnace bucket
Pipe installing have particulate matter unloading valve, by the setting of particulate matter unloading valve, its effect be to cyclone dust collectors collect after
Particulate matter and dust discharged into blast furnace bucket, to avoid the pollution to environment and the waste of the energy, cyclone dust removal
The exhaust pipe of device is communicated with gas cooler by pipeline, and gas cooler uses the water direct cooling mode of shell and tube, flue gas
The liquid conduct flowed in cooler tube is tube side, its conduct of the liquid flowed outside pipe is shell side, and the wall surface of tube bank is to pass
Hot face, achieve the effect that it is cooling, cooling capacity be 600 cubes/min~3500 cube/min, pass through setting for gas cooler
It sets, its cooling can further be dusted flue gas and pernicious gas is carried out hydration process, the exhaust of gas cooler
Pipe is communicated with gas-liquid separator by pipeline, and the outlet of gas-liquid separator is communicated with graphited ethylene-steam condenser by pipeline,
The separation method of gas-liquid separator is ultra-filtration and separation, and the different gas-liquid mixture of particle is sieved by millipore filter, liquid
For body because gravity downstream to separator bottom and is discharged, gas enters graphited ethylene-steam condenser, passes through setting for gas-liquid separator
It sets, its effect is that the flue gas after dedusting is pipelined to ground, due to the conveying of long range, former high-temperature flue gas
Cooled down, is temperature-fall period when being conveyed in pipeline containing the saturated flue gas for detaching moisture in flue gas, a part of condensated gas
Body component will form droplet and flow with gas, meanwhile, flue gas water increases after gas cooler, passes through gas-liquid point
After device, the effect of gas-liquid separator is exactly the gas for handling this two parts and containing a small amount of lime set, and realization lime set recycles and will
A part of gas phase purifying, graphited ethylene-steam condenser gas outlet are communicated with flue gas heater by pipeline, pass through graphite second
The setting of alkene-steam condenser, its main function are to reduce water entrained by flue gas while further decreasing flue-gas temperature
Quantity is dripped, 80%~90% flue gas can be substantially sloughed, by the setting of flue gas heater, flue gas is formed not after heating
It is saturated higher temperatures flue gas, is not easy to form plume and hangover, flue gas heater and flue gas at throat after chimney discharge
Circulating heat pump is communicated with by pipeline between cooler, is equipped in graphited ethylene-steam condenser association system all parts
The condensation steel pipe of a large amount of DN20, and condense steel duct and be coated with graphite ene coatings, outer spray water evaporation is managed, inner tube smoke is by spray
Water drenching evaporation endothermic further cools down, and the heat power source of circulating heat pump is the heat of untreated flue gas at gas cooler, circulation
Heat pump is media for heat exchange by water and transfers heat to flue gas heater, and flue gas heater gas outlet is communicated with row by pipeline
Cigarette chimney, the height of chimney is not less than the height of the first blast furnace roof desorption tube and the second blast furnace roof desorption tube, and arranges
Cigarette chimney is steel construction and glass reinforced plastic mixed structure form, and the height by the way that chimney is arranged is put not less than the first blast furnace roof
The height of separate tube and the second blast furnace roof desorption tube can guarantee certain negative pressure amount, cooling by cyclone dust collectors, flue gas
The setting of device, gas-liquid separator, graphited ethylene-steam condenser, flue gas heater, circulating heat pump and chimney, can to
Toxic, combustible mixed gas largely containing CO, CO2 and dust are generated during direct emission sufficiently to be handled, and are solved
The problem of current flue gas processing device cannot sufficiently be handled pernicious gas, avoids air environmental pollution, the height
Furnace stop again wind with flue gas processing device can be in line to blast furnace high-temperature flue gas in dust-laden particle recycle, and by pernicious gas
Hydration process is carried out, so that the flue gas of discharge reaches national emission standard, is worthy to be popularized.
In use, flue gas and particulate matter that blast furnace roof generates pass through the first blast furnace roof desorption tube, the second blast furnace respectively
Furnace roof desorption tube, release cross over pipe and release general pipeline enter the inside of cyclone dust collectors, the ash-laden gas inside cyclone dust collectors
Stream rotates, and grit is separated to from air-flow by means of centrifugal force and is trapped in wall, then make grit by gravity
Ash bucket is fallen into, by opening particulate matter unloading valve, so that the particulate matter and dust after cyclone dust collectors collection enter blast furnace bucket
Internal discharge, remaining flue gas enters the inside of gas cooler, and gas cooler makes cigarette by the heat transfer effect of liquid
The decline of temperature degree, while flue gas is dusted and pernicious gas is subjected to aquation, enter the inside of gas-liquid separator later,
By long-distance transportation through pipeline to ground, former high-temperature flue gas is cooled down flue gas after dedusting, and gas-liquid separator is to containing a small amount of
The gas of lime set realizes lime set recycling or gas phase purifying, and flue gas enters the pipeline inside graphited ethylene-steam condenser later,
Water evaporation is sprayed outside pipeline, flue gas is further cooled down by the amount of heat that spray water evaporation absorbs in pipeline, can reduce smoke temperature
To 35 DEG C -38 DEG C, the liquid water in flue gas is largely removed at this time, cold in flue gas remaining as the saturation wet flue gas after preliminary cooling
But heat source of the untreated flue gas as circulating heat pump at device, circulating heat pump are media for heat exchange by water and transfer heat to
Flue gas heater, while constant pressure supply water is needed to pay attention to, the heat medium water that flue gas heater is transmitted by circulating heat pump is to graphited ethylene-
The incoming flue gas of steam condenser is heated, and flue gas forms unsaturated higher temperatures cigarette after the heating by flue gas heater
Gas is not easy to form plume and hangover at throat from the flue gas after chimney discharge, 85 DEG C of smoke temperature of chimney outlet,
Humidity is 3%-6%.
In summary: the blast furnace stop again wind flue gas processing device, by blast furnace roof, the first blast furnace roof desorption tube,
Second blast furnace roof desorption tube, release cross over pipe, release general pipeline, release main valve, cyclone dust collectors, blast furnace bucket, particulate matter unload
Grey valve, gas cooler, gas-liquid separator, graphited ethylene-steam condenser, flue gas heater, circulating heat pump and chimney
Be used cooperatively, solve the problems, such as that current flue gas processing device cannot sufficiently be handled pernicious gas.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (4)
1. a kind of blast furnace stops wind flue gas processing device, including coal gas diffusion at top of blast furnace pipe and diffusion valve again, it is characterised in that:
The blast furnace roof passes through coal gas diffusion pipe and diffusion valve by furnace roof spherical tank or coal gas tedge for original, to coal in State of Blast Furnace
Gas carries out direct emission, and is changed to and is retaining rough gas desorption tube and while diffusion valve, increases and coal gas diffusion pipe and puts
The parallel release cross over pipe of valve is dissipated, is referred to as this release communicating pipe to diffuse general pipeline, the tube wall surface of the release general pipeline is equipped with
Main valve is diffused, the release general pipeline is communicated with cyclone dust collectors far from one end of release cross over pipe, and the cyclone dust collectors pass through
Pipeline is communicated with blast furnace bucket, and the Pipe installing between the cyclone dust collectors and blast furnace bucket has particulate matter unloading valve；
The exhaust pipe of the cyclone dust collectors is communicated with gas cooler by pipeline, and the exhaust pipe of the gas cooler passes through
Pipeline is communicated with gas-liquid separator, and the outlet of the gas-liquid separator is communicated with graphited ethylene-steam condenser, institute by pipeline
It states graphited ethylene-steam condenser gas outlet and flue gas heater is communicated with by pipeline, the flue gas heater and flue gas are cold
But circulating heat pump is communicated with by pipeline between device, the flue gas heater gas outlet is communicated with chimney by pipeline.
2. a kind of blast furnace according to claim 1 stops wind flue gas processing device again, it is characterised in that: the cyclone dust removal
The inner wall of device is equipped with wear-resistant liner, and the gas cooler uses the water direct cooling mode of shell and tube, cooling capacity 600
Cube/min~3500 cube/min.
3. a kind of blast furnace according to claim 1 stops wind flue gas processing device again, it is characterised in that: the gas-liquid separation
The separation method of device is ultra-filtration and separation, and the different gas-liquid mixture of particle is sieved by millipore filter, and liquid is because of gravity
It downstream to separator bottom and is discharged, gas enters graphited ethylene-steam condenser.
4. a kind of blast furnace according to claim 1 stops wind flue gas processing device again, it is characterised in that: the chimney
Height be not less than the first blast furnace roof desorption tube and the second blast furnace roof desorption tube height, and chimney be steel construction with
Glass reinforced plastic mixed structure form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822209583.5U CN209602579U (en) | 2018-12-27 | 2018-12-27 | A kind of blast furnace stops wind flue gas processing device again |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822209583.5U CN209602579U (en) | 2018-12-27 | 2018-12-27 | A kind of blast furnace stops wind flue gas processing device again |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209602579U true CN209602579U (en) | 2019-11-08 |
Family
ID=68397213
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822209583.5U Expired - Fee Related CN209602579U (en) | 2018-12-27 | 2018-12-27 | A kind of blast furnace stops wind flue gas processing device again |
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| Country | Link |
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| CN (1) | CN209602579U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111850200A (en) * | 2020-07-29 | 2020-10-30 | 中冶华天南京工程技术有限公司 | Environment-friendly blowing-down method for blast furnace |
-
2018
- 2018-12-27 CN CN201822209583.5U patent/CN209602579U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111850200A (en) * | 2020-07-29 | 2020-10-30 | 中冶华天南京工程技术有限公司 | Environment-friendly blowing-down method for blast furnace |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191108 Termination date: 20211227 |