CN203128596U - Efficient blast furnace slag-washing water waste heat recycling system adopting bottom-filtration process - Google Patents
Efficient blast furnace slag-washing water waste heat recycling system adopting bottom-filtration process Download PDFInfo
- Publication number
- CN203128596U CN203128596U CN2013200346072U CN201320034607U CN203128596U CN 203128596 U CN203128596 U CN 203128596U CN 2013200346072 U CN2013200346072 U CN 2013200346072U CN 201320034607 U CN201320034607 U CN 201320034607U CN 203128596 U CN203128596 U CN 203128596U
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- blast furnace
- exhaust heat
- recovery system
- slag
- filter method
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/022—Methods of cooling or quenching molten slag
- C21B2400/024—Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/066—Receptacle features where the slag is treated
- C21B2400/074—Tower structures for cooling, being confined but not sealed
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/08—Treatment of slags originating from iron or steel processes with energy recovery
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The utility model relates to an efficient blast furnace slag-washing water waste heat recycling system adopting a bottom-filtration process. The efficient blast furnace slag-washing water waste heat recycling system adopting the bottom-filtration process comprises a graining box, a slag-washing ditch, a bottom-filtration tank, a hot water tank and circulating pumps, which are connected in sequence; the efficient blast furnace slag-washing water waste heat recycling system further comprises a cooling tower, an absorption type refrigerating unit and a heating device, which are connected in parallel; the input ends of the cooling tower, the absorption type refrigerating unit and the heating device connected in parallel are connected with the circulating pumps; and the output ends of the cooling tower, the absorption type refrigerating unit and the heating device connected in parallel are connected with the graining box. The efficient blast furnace slag-washing water waste heat recycling system adopting the bottom-filtration process can be used for solving the seasonal problem of blast furnace slag-washing water waste heat recycling adopting the bottom-filtration process, improving the slag-washing water waste heat recovery rate, realizing the sufficient recovery of the slag-washing water waste heat and achieving the purpose of saving energy and reducing emission.
Description
Technical field
The utility model relates to the waste heat recovery field of metallurgy industry, more particularly, relates to filter method using exhaust heat of slag flushing water recovery system at the bottom of a kind of blast furnace efficiently.
Background technology
Steel industry is the energy consumption rich and influential family, and can produce a large amount of waste heats in consumes energy, takes full advantage of the new opportunity that this part waste heat will become the steel industry development.Along with the progress of science and technology, the middle high-temperature residual heat of Steel Plant has progressively obtained effective recycling, and the utilization ratio of low temperature exhaust heat is very low, and to 2011, Steel Plant's low temperature exhaust heat utilization ratio only had an appointment 1%.
In blast furnace smelting process, every production 1t molten iron produces the blast furnace slag of about 0.3t, the heat that blast furnace slag is taken away accounts for 16% of blast furnace total energy consumption, these heats substantially all enter flushing cinder water, and along with the circulation of flushing cinder water is discharged into the atmosphere, water resource waste and thermal pollution have also been caused in the time of energy dissipation.
At present a lot of Steel Plant adopt a kind of end filter method flushing cinder technology; this technology is directly delivered to the granulated blast-furnace case with the high-temperature liquid state slag; the high velocity flow shrend cooling that in the granulation case, is ejected; form the particulate state grain slag; the slag-water slurry temperature generally can reach about 90 ℃; the flushing cinder water of high temperature enters filter tank, the end by sluice, is delivered to cooling tower cooling back cycling and reutilization after filtering, and this part heat all is dissipated in the process of circulation.At present, though the idea of many this part waste heats of recovery is also arranged, such as with flushing cinder water and outside cold water heat exchange, problem such as cold water obtains being used for heating etc. behind the heat, and it is low all to be difficult to solve efficient, and System production time is lacked, and rate of return on investment is low can't be applied.
In the most of area of China, the summer weather sweltering heat, humidity is very big, and blast furnace blowing engine is increased dehumidifying device has unusual effect to aspects such as blast furnace stable yields, Jie Jiao and reduction gas blower energy consumptions, and the blast furnace dehumidifying air blast also becomes the energy-saving and emission-reduction project of country's 12 iron and steel enterprise's keypoint recommendations.At present, dehumidifying Blast Technology on BF substantially all adopts electric power or steam driven, the running cost height, and rate of return on investment is low, so cause this technology to be difficult to popularize.In addition, China's most of area cold in winter, the sweltering heat in summer, plant area of steel mill and near residential quarter need be expended lot of energy and be used for winter heating and summer cooling gas.
The utility model content
The technical problems to be solved in the utility model is, filter method using exhaust heat of slag flushing water recovery system at the bottom of a kind of blast furnace efficiently is provided.
The technical scheme that its technical problem that solves the utility model adopts is: filter method using exhaust heat of slag flushing water recovery system at the bottom of constructing a kind of blast furnace efficiently, comprise the granulation case, sluice, filter tank, the end, hot tub and the recycle pump that connect successively, also comprise the cooling tower, absorption refrigeration unit, the heating plant that are connected in parallel; Input terminus after described cooling tower, absorption refrigeration unit, the heating plant parallel connection is connected with described recycle pump, and output terminal is connected with described granulation case.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, bottom, filter tank, the described end is provided with funneling flushing cinder water collection bucket, and described flushing cinder water collection bucket causes the bottom of described hot tub by pipeline.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, be provided with filtration unit between filter tank, the described end and the hot tub.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, described system also comprises the cold user, and described cold user is connected with described absorption refrigeration unit, and described cold user is air blow for removing moisture device or interchanger.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, the branch road at described cooling tower, absorption refrigeration unit and heating plant place is provided with trip valve.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, the input terminus of described absorption refrigeration unit and heating plant parallel branch is provided with chemicals dosing plant.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, the branch road at described absorption refrigeration unit and heating plant place is provided with sampling unit.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, described absorption refrigeration unit is lithiumbromide-water refrigerating machine group.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, described sluice and the outside, filter tank, the end are provided with insulation cover plate and insulation shell.
In filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently described in the utility model, described system also comprises condensate make-up piping, and described condensate make-up piping directly is connected with described granulation case.
Implement to filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently of the present utility model; have following beneficial effect: flushing cinder water obtains after filtering through water particle case, sluice and filter tank, end stage trapping is stored in hot water high purity in the hot tub; reduce bad phenomenon such as Corrosion of Pipeline and fouling, hot water is sustainable to be recycled.Hot water in the hot tub by recycle pump with delivery to cooling tower, absorption refrigeration unit or heating plant, realized refrigeration in summer, dehumidification and winter heating.Also be provided with cooling tower in the system, improved the stability of system, when absorption refrigeration unit and heating plant do not need work or maintenance, also do not influence the works better that blast furnace slag is handled.The utility model is filtered the seasonal problem that method using exhaust heat of slag flushing water recovery system reclaims at the bottom of having solved blast furnace, has improved the using exhaust heat of slag flushing water rate of recovery, has realized the abundant recovery of using exhaust heat of slag flushing water, reaches the purpose of energy-saving and emission-reduction.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples, in the accompanying drawing:
Fig. 1 is the utility model structural representation of filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently.
Embodiment
Understand for technical characterictic of the present utility model, purpose and effect being had more clearly, now contrast accompanying drawing and describe embodiment of the present utility model in detail.
As shown in Figure 1, the utility model efficiently at the bottom of the blast furnace filter method using exhaust heat of slag flushing water recovery system comprise granulation case 1, sluice 2, filter tank, the end 3, hot tub 4, recycle pump 5, cooling tower 6, absorption refrigeration unit 8 and heating plant 9.Wherein, granulation case 1, sluice 2, filter tank, the end 3, hot tub 4 and recycle pump 5 are connected successively, and cooling tower 6, absorption refrigeration unit 8 and heating plant 9 are connected in parallel.Input terminus after cooling tower 6, absorption refrigeration unit 8, heating plant 9 parallel connections is connected with recycle pump 5, and output terminal is connected with granulation case 1.Absorption refrigeration unit 8 can be tried one's best and be arranged near hot tub 4, also can reduce the cost of system with the thermosteresis that reduces system.
Flushing cinder water contacts with the blast furnace slag of high-temperature fusion in granulation case 1, produces a large amount of steam and high temperature flushing cinder water.Slag-water slurry is delivered to sluice 2 from granulation case 1, and flushing cinder water enters filter tank, the end 3, and residual most of solid impurity particle is deposited on 3 bottoms, filter tank, the end in the flushing cinder water, and the hot water high purity in the hot tub 4 can be avoided corrosive pipeline or fouling.
Further, system of the present utility model also comprises cold user 10, and cold user 10 can be devices such as air blow for removing moisture device or interchanger.Cold user 10 is connected with absorption refrigeration unit 8, and absorption refrigeration unit 8 can be cold user 10 cold is provided.The air blow for removing moisture device can be the blast furnace blowing engine dehumidification, can be the room cooling by interchanger.
Further, the master loop at recycle pump 5 places is provided with trip valve 12, the branch road at cooling tower 6 places is provided with trip valve 14, the branch road at absorption refrigeration unit 8 places is provided with trip valve 15, the branch road at heating plant 9 places is provided with trip valve 16, and the input terminus of absorption refrigeration unit 8 and heating plant 9 parallel branches is provided with trip valve 13.
In summer, trip valve 12, trip valve 13 and trip valve 15 are opened, trip valve 14 and trip valve 16 are all closed, the hot water that comes out from recycle pump 5 is sent into the producer of absorption refrigeration unit 8 by pipeline 17, pipeline 18 and pipeline 19, realizes heat exchange by vaporizer and the condenser of absorption refrigeration unit 8.Absorption refrigeration unit 8 in the present embodiment is lithiumbromide-water refrigerating machine group.8 work are freezed thereby hot water drives the absorptionmachine group, and the cold of generation is delivered to the air blow for removing moisture device or provides cold by interchanger to the user by the refrigerant medium.Directly return granulation case 1 from the water at low temperature that producer flows out by pipeline 21, pipeline 23 and pipeline 25, the using exhaust heat of slag flushing water that forms a sealing drives refrigeration system.
In the winter time, close trip valve 14 and trip valve 15, open trip valve 12, trip valve 13 and trip valve 16, hot water is sent into heating plant 9 by pipeline 17 and pipeline 18, and hot water and the external world carry out heat exchange, provide heat to the user.Then directly return granulation case 1 through piping 22, pipeline 23 and pipeline 25 from the water at low temperature that heating plant 9 flows out, form the warm recycle system of flushing cinder hydromining of another sealing.
In some month in spring, autumn; when perhaps unit cooler 8 and heating system need be overhauled; unit cooler 8 and heating plant 9 may not need operation; trip valve 13, trip valve 15 and trip valve 16 are all closed; trip valve 12 and trip valve 14 are opened; hot water all entered cooling tower 6 by pipeline 24 and cooled off this moment, returned granulation case 1 then, guaranteed the works better of blast furnace slag treatment system.
Further, between filter tank, the end 3 and hot tub 4 filtration unit can be set, the pulp water that liquidates filters, and improves the cleanliness factor of hot water.3 bottoms, filter tank, the end are provided with funneling flushing cinder water collection bucket 27, flushing cinder water collection bucket 27 causes the bottom of hot tub 4 by pipeline, flushing cinder water is accumulated in the hot tub 4 by filtration unit and by funneling flushing cinder water collection bucket 27 and pipeline, the calorific loss when having avoided hot water directly to trickle down to hot tub 4 by filter tank, the end 3.
Further, the input terminus of absorption refrigeration unit 8 and heating plant 9 parallel branches is provided with chemicals dosing plant 7, can regulate the pH value, hardness, calcium, magnesium ion concentration of hot water etc., improves water quality, thereby reduces bad phenomenon such as Corrosion of Pipeline and fouling.
Further, the branch road at absorption refrigeration unit 8 and heating plant 9 places is provided with sampling unit 11, and water quality is detected in the sampling back, can control the dose that adds of chemicals dosing plant 7 according to detected result.
Further, recycle pump 5 has two at least, and two or more recycle pump 5 parallel connections guarantee the normal conveying of hydraulic pressure and hot water.
Further, in order to reduce the thermosteresis of system, improve the flushing cinder water application efficiency, the transport pipe of hot tub 4, filter tank, the end 3, sluice 2 and total system all needs to be incubated and moistureproof the processing.Sluice 2 in the present embodiment and 3 outsides, filter tank, the end are provided with insulation cover plate and insulation shell 28, and hot tub 4 is enclosed construction, and access opening is set.
Further, system of the present utility model also comprises condensate make-up piping 29, and condensate make-up piping 29 directly is connected with granulation case 1, guarantees the sufficient supplies of flushing cinder water.
The utility model can switch to different flushing cinder water treatment modes according to the difference in season and the needs of production.The blast furnace slag quenching water of high temperature is directly used in and drives unit cooler 8 or be used for heating, thermo-efficiency height.In addition, be summer during refrigeration, and be winter during heating that the two mutually combines, solved the seasonal problem that filter method using exhaust heat of slag flushing water reclaims at the bottom of the blast furnace, improved the using exhaust heat of slag flushing water rate of recovery.The utility model can utilize by the high-temperature residual heat that flushing cinder water is contained more fully, reaches energy-conservation and purpose environmental protection.
By reference to the accompanying drawings embodiment of the present utility model is described above; but the utility model is not limited to above-mentioned embodiment; above-mentioned embodiment only is schematic; rather than it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; not breaking away under the scope situation that the utility model aim and claim protect, also can make a lot of forms, these all belong within the protection of the present utility model.
Claims (10)
1. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently for one kind, it is characterized in that, comprise the granulation case, sluice, filter tank, the end, hot tub and the recycle pump that connect successively, also comprise the cooling tower, absorption refrigeration unit, the heating plant that are connected in parallel; Input terminus after described cooling tower, absorption refrigeration unit, the heating plant parallel connection is connected with described recycle pump, and output terminal is connected with described granulation case.
2. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that bottom, filter tank, the described end is provided with funneling flushing cinder water collection bucket, and described flushing cinder water collection bucket causes the bottom of described hot tub by pipeline.
3. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that, is provided with filtration unit between filter tank, the described end and the hot tub.
4. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1, it is characterized in that, described system also comprises the cold user, and described cold user is connected with described absorption refrigeration unit, and described cold user is air blow for removing moisture device or interchanger.
5. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that the branch road at described cooling tower, absorption refrigeration unit and heating plant place is provided with trip valve.
6. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that the input terminus of described absorption refrigeration unit and heating plant parallel branch is provided with chemicals dosing plant.
7. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that the branch road at described absorption refrigeration unit and heating plant place is provided with sampling unit.
8. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that described absorption refrigeration unit is lithiumbromide-water refrigerating machine group.
9. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that described sluice and the outside, filter tank, the end are provided with insulation cover plate and insulation shell.
10. filter method using exhaust heat of slag flushing water recovery system at the bottom of the blast furnace efficiently according to claim 1 is characterized in that described system also comprises condensate make-up piping, and described condensate make-up piping directly is connected with described granulation case.
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CN2013200346072U CN203128596U (en) | 2013-01-23 | 2013-01-23 | Efficient blast furnace slag-washing water waste heat recycling system adopting bottom-filtration process |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108220511A (en) * | 2018-01-17 | 2018-06-29 | 安徽马钢工程技术集团有限公司 | Filter method Slag treatment method in a kind of In The Sub-mergedfurnace of The Ferroalloys bottom |
CN109457066A (en) * | 2018-12-27 | 2019-03-12 | 中冶京诚工程技术有限公司 | Blast furnace grain slag filtering tank waste heat refrigeration utilization equipment |
CN109487019A (en) * | 2018-12-27 | 2019-03-19 | 中冶京诚工程技术有限公司 | Blast furnace grain slag filtering pond waste heat refrigeration utilization system |
CN114752714A (en) * | 2022-05-18 | 2022-07-15 | 宝武集团鄂城钢铁有限公司 | Blast furnace slag treatment system |
-
2013
- 2013-01-23 CN CN2013200346072U patent/CN203128596U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108220511A (en) * | 2018-01-17 | 2018-06-29 | 安徽马钢工程技术集团有限公司 | Filter method Slag treatment method in a kind of In The Sub-mergedfurnace of The Ferroalloys bottom |
CN109457066A (en) * | 2018-12-27 | 2019-03-12 | 中冶京诚工程技术有限公司 | Blast furnace grain slag filtering tank waste heat refrigeration utilization equipment |
CN109487019A (en) * | 2018-12-27 | 2019-03-19 | 中冶京诚工程技术有限公司 | Blast furnace grain slag filtering pond waste heat refrigeration utilization system |
CN114752714A (en) * | 2022-05-18 | 2022-07-15 | 宝武集团鄂城钢铁有限公司 | Blast furnace slag treatment system |
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Granted publication date: 20130814 |