CN201148443Y - AOD revolving furnace flue gas waste heat recovery apparatus - Google Patents
AOD revolving furnace flue gas waste heat recovery apparatus Download PDFInfo
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- CN201148443Y CN201148443Y CNU2008200784057U CN200820078405U CN201148443Y CN 201148443 Y CN201148443 Y CN 201148443Y CN U2008200784057 U CNU2008200784057 U CN U2008200784057U CN 200820078405 U CN200820078405 U CN 200820078405U CN 201148443 Y CN201148443 Y CN 201148443Y
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- section flue
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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
- Y02P10/25—Process efficiency
Abstract
The utility model relates to a waste heat recovery device of smoke gas of an AOD converter, which comprises a high-temperature vaporization and cooling device of the smoke gas and a low-temperature waste heat recovery device of the smoke gas. The high-temperature vaporization and cooling device of the smoke gas comprises a furnace throat fixing-section flue, a middle first-section flue, a middle second-section flue, a middle third-section flue, a terminal flue and a steam drum, which are orderly communicated; the middle first-section flue, the middle second-section flue, the middle third-section flue, the terminal flue, the steam drum, an ascending pipe communicated with the upper side of the steam drum, and a corresponding descending pipe form a natural circulation system. The low-temperature waste heat recovery device of the smoke gas comprises a pre-heater, a heat exchanger, an economizer, a deaerator and a water supply pump; the pre-heater, the deaerator, an ascending pipe connected with deaerator, and a corresponding descending pipe form the natural circulation to heat the water in the deaerator so as to remove the oxygen, which saves the steam consumption; the water supply pump is used for pumping the deoxygenized water into the steam drum through the economizer, so as to fully reduce the temperature of the smoke and recollect the heat. In addition, because no circulating pump is added in the heat exchanger, the device saves the power.
Description
Technical field
The utility model relates to the cooling residual heat retrieving arrangement of a kind of ferrous metallurgy and field of energy-saving technology, particularly relates to a kind of AOD converter flue gas waste heat recovery apparatus.
Background technology
Traditional converter steelmaking pattern is little owing to the furnace gas amount, the flue-gas temperature height, and the fluctuation of cigarette temperature is big, and the dustiness height is so converter gas generally adopts water-cooled to handle.With the AOD converter is example, sees also shown in Figure 1ly, and the flue gas that the AOD converter smelting is produced is extracted out from its furnace roof, after the water-cooled flue cooling, drop to about 150 ℃ through machine power air cooling machine or spray cooler again, enter sack cleaner and purify, and be discharged into atmosphere by chimney through blower fan.
Because the cooling apparatus that traditional AOD converter gas is handled is the service water cooling, inlet water temperature is at 25～30 ℃, and the outlet water temperature is at 45～60 ℃.Though major part can be recycled after cooling tower was handled in round-robin water coolant water inlet, all there is about 3% consumption loss in each circulation, simultaneously the cycle consumption of service water a large amount of electric energy.In addition, most critical is that heat in the AOD converter gas is not but recycled fully.
With domestic existing AOD converter is example, adopts traditional water-cooling pattern, and per hour wind, volatilization consume the about 50t of recirculated water, the about 400kW of recirculated water power consumption, about 410 yuan/hour of working cost.
In addition, during the cooling of traditional service water, water hardness is higher, forms incrustation scale easily in cooling component, makes cooling component take place overheated and burns out.
This shows that above-mentioned existing AOD converter gas treatment technology is in energy consumption and technical major defect arranged, the existing AOD converter of incompatibility technology, and demand urgently further being improved.For reclaiming AOD converter gas heat, reduce the energy consumption per ton steel index, improve the efficiency of cycling economy of full factory, relevant manufacturer there's no one who doesn't or isn't seeks solution painstakingly, but do not see always that for a long time suitable design finished by development, and common product does not have appropriate structure to address the above problem, and this obviously is the problem that the anxious desire of relevant dealer solves.Therefore how to found a kind of converter waste-heat recovery device of novel texture, just become the primary goal of current industry.
Because the defective that above-mentioned existing AOD converter gas treatment technology exists, the design people is based on being engaged in this type of product design manufacturing abundant for many years practical experience and expertise, and the utilization of cooperation scientific principle, actively studied innovation, in the hope of founding a kind of novel AOD converter flue gas waste heat recovery apparatus, make it have more economic benefit.Through constantly research, design, and, create the utility model that has practical value finally through engineering application and after improving.
Summary of the invention
The purpose of this utility model is, overcomes the defective of existing AOD converter gas treatment unit, and a kind of AOD converter flue gas waste heat recovery apparatus of novel texture is provided, and technical problem to be solved is to make it fully reduce the converter gas temperature.The carbonated drink Recycle design that adopts pump circulation to combine with natural circulation simultaneously under the life-span of assurance device condition, reduces power consumption to greatest extent, thereby is suitable for practicality more.
The purpose of this utility model and to solve its technical problem be to adopt following technical scheme to realize.According to a kind of AOD converter flue gas waste heat recovery apparatus that the utility model proposes, it comprises: high-temperature flue gas apparatus for vapour-cooling portion, and it comprises: mouth fixed section flue is arranged at the converter mouth top; Middle I section flue is arranged at above-mentioned mouth fixed section flue top; Middle II section flue is arranged at above-mentioned middle I section flue top; Middle III section flue is arranged on above-mentioned middle II section flue top, and makes flue gas transfer horizontal direction to by vertical direction; The latter end flue connects above-mentioned middle III section flue, and makes flue gas transfer vertical direction to by horizontal direction; Drum, its upside are provided with the upcast that is connected with above-mentioned mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue, and the drum downside is provided with corresponding downtake; I section flue, middle II section flue, middle III section flue, latter end flue and above-mentioned drum and the upcast of upside connection thereof and corresponding downtake are formed natural cycle system jointly in above-mentioned; And high-pressure water heating recycle pump, be arranged at above-mentioned drum downside, and being communicated with the bottom of above-mentioned drum and above-mentioned mouth fixed section flue by downtake, described high-pressure circulation pump pumps into the water of separating in the above-mentioned drum in above-mentioned mouth fixed section flue, form the high pressure forced circulation system; And low-temperature flue gas waste-heat recovery device portion, be connected with above-mentioned high-temperature flue gas apparatus for vapour-cooling portion, described low-temperature flue gas waste-heat recovery device portion comprises: preheater, be connected in above-mentioned latter end flue below, flue gas enters preheater straight down by the latter end flue, and the upcast, the downtake that connect preheater are communicated with the formation natural circulation with above-mentioned drum; Interchanger is arranged at above-mentioned preheater below, and the upcast, the downtake that connect interchanger are communicated with the formation natural circulation with above-mentioned drum; Economizer is arranged at above-mentioned interchanger below, and the upcast that connects economizer is communicated with above-mentioned drum; Deoxygenator is communicated with above-mentioned preheater by the upcast that is arranged at its upside, and by the downtake that is arranged at its downside the water that carries out in the deoxygenator after deoxygenation is handled is exported in above-mentioned preheater and the above-mentioned economizer; And service pump, being arranged in above-mentioned deoxygenator downside downtake and the above-mentioned economizer water service pipe, the water that is used for carrying out in the above-mentioned deoxygenator after deoxygenation is handled pumps in above-mentioned drum through above-mentioned economizer.
The purpose of this utility model and solve its technical problem and also can adopt following technical measures further to realize.
Aforesaid AOD converter flue gas waste heat recovery apparatus, described mouth fixed section flue comprises oxygen muzzle and feed opening.
Aforesaid AOD converter flue gas waste heat recovery apparatus, the import of described mouth fixed section flue is provided with throttling set.
Aforesaid AOD converter flue gas waste heat recovery apparatus, described mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue are round shape.
Aforesaid AOD converter flue gas waste heat recovery apparatus, the inwall of described mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue is provided with membrane wall.
Aforesaid AOD converter flue gas waste heat recovery apparatus, described membrane wall is provided with interceptor between 140～170 °.
Aforesaid AOD converter flue gas waste heat recovery apparatus wherein is provided with the flue non-metal compensator between mouth fixed section flue and middle I section flue.
Aforesaid AOD converter flue gas waste heat recovery apparatus, described preheater, interchanger and economizer are assembled together, and are provided with casing, manhole, dust remover and ash bucket in described low-temperature flue gas waste-heat recovery device portion.
Aforesaid AOD converter flue gas waste heat recovery apparatus, described high-temperature flue gas apparatus for vapour-cooling portion is provided with a plurality of air inlet-outlet-housings.
By technique scheme, the utility model AOD converter flue gas waste heat recovery apparatus has following advantage at least:
The utility model AOD converter flue gas waste heat recovery apparatus has the converter gas of reduction temperature, the advantage of waste heat recovering energy conserving consumption reduction.It collects converter gas according to mouth fixed section, by high-temperature flue gas apparatus for vapour-cooling portion and low-temperature flue gas waste-heat recovery device portion, adopts radiation heat transfer and convective heat exchange to reduce flue-gas temperature, and the steam of generation can use for enterprise's productive life.At converter gas temperature height, the fluctuation of cigarette temperature is big, the unfavorable factor that dustiness is high, the compound recycle mode that water circulation system adopts pump circulation to combine with natural circulation, supporting throttling set and the interceptor of being provided with of membrane wall.
In addition, be provided with ash bucket in the interchanger bottom, in preheater, interchanger and economizer, be provided with dust remover, so not only avoided the booster phenomenon that takes place because of water wall tube local heating is inhomogeneous, reduce dust in flue gas simultaneously and on heat-transfer surface, accumulated the heat exchange efficiency reduction that causes, guaranteed the operational efficiency and the work-ing life of device.
In sum, the AOD converter flue gas waste heat recovery apparatus of the utility model special construction under the prerequisite that guarantees STEELMAKING PRODUCTION, has reduced energy consumption per ton steel, and recovered steam has improved full factory economic benefit, has plurality of advantages and practical value.And it is not seen in like product has similar structure design to publish or use and really genus innovation.No matter the more existing converter gas treatment technology of the present invention all has bigger improvement on product device, structure or function, have large improvement technically, and produced handy and practical effect, and have the extensive utility value of industry, really be a new and innovative, progressive, practical new design.
Above-mentioned explanation only is the general introduction of technical solutions of the utility model, for can clearer understanding technique means of the present utility model, and can be implemented according to the content of specification sheets, and for above-mentioned and other purposes, feature and advantage of the present utility model can be become apparent, below especially exemplified by preferred embodiment, and conjunction with figs., be described in detail as follows.
Description of drawings
Fig. 1 is the synoptic diagram of the AOD converter gas treatment unit of prior art.
Fig. 2 is the synoptic diagram of the utility model AOD converter flue gas waste heat recovery apparatus.
Fig. 3 A, 3B are respectively that the right side of high-temperature flue gas apparatus for vapour-cooling of the present utility model portion is looked, main TV structure synoptic diagram.
Fig. 4 A, 4B are respectively that the master of low-temperature flue gas waste-heat recovery device of the present utility model portion looks, right TV structure synoptic diagram.
Fig. 5 A is the structural representation that membrane wall is installed in the flue of the present utility model, and Fig. 5 B is the structure enlarged view at its II-II place of Fig. 5 A.
Fig. 6 is the structural representation of throttling set of the present utility model.
Fig. 7 is the structural representation of flue non-metal compensator of the present utility model.
Fig. 8 A is the structural representation of air inlet-outlet-housing of the present utility model, and Fig. 8 B, 8C, 8D are respectively A-A, the B-B of Fig. 8 A, the sectional view of C-C.
Fig. 9 A is the structural representation of feed opening of the present utility model, Fig. 9 B be Fig. 9 A A-A, sectional view, and Fig. 9 C is the B-B sectional view of Fig. 9 B.
10: high-temperature flue gas apparatus for vapour-cooling portion
11: mouth fixed section flue 111: the oxygen muzzle
112: feed opening 113: throttling set
12: middle I section flue 121: flue non-metal compensator
13: middle II section flue 14: middle III section flue
15: latter end flue 16: drum
17: high-pressure circulation pump 18: membrane wall
181: interceptor 19: the Inlet and outlet water header
20: low-temperature flue gas waste-heat recovery device portion
21: preheater 22: interchanger
221: casing 23: economize coal gas
24: deoxygenator 25: service pump
26: dust remover 27: manhole
28: ash bucket
UPD: upcast DND: downtake
Embodiment
For further setting forth the utility model is to reach technique means and the effect that predetermined goal of the invention is taked, below in conjunction with accompanying drawing and preferred embodiment, to according to its embodiment of AOD converter flue gas waste heat recovery apparatus, structure, feature and the effect thereof that the utility model proposes, describe in detail as after.
See also shown in Fig. 2, Fig. 3 A and Fig. 3 B, Fig. 2 is the synoptic diagram of the utility model AOD converter flue gas waste heat recovery apparatus, and Fig. 3 A, 3B are respectively that the right side of high-temperature flue gas apparatus for vapour-cooling of the present utility model portion is looked, main TV structure synoptic diagram.The utility model AOD converter flue gas waste heat recovery apparatus comprises: high-temperature flue gas apparatus for vapour-cooling portion 10 and low-temperature flue gas waste-heat recovery device portion 20.
High-temperature flue gas apparatus for vapour-cooling portion 10, as shown in Figure 2, it comprises mouth fixed section flue 11, concrete structure adopts the membrane wall flue, can be high temperature resistant and flue gas that hot strength is big, import is direction straight up, annular water distribution is set two ends up and down at flue, compile header and corresponding air inlet-outlet-housing 19 (shown in Fig. 8 A～8D), the water-inlet header ingress is provided with throttling set 113 (as shown in Figure 6), steam water interface is in the outlet header of mouth fixed section flue 11 upper ends compiles by upcast UPD importing drum 16, and in drum 16 with steam and water sepn, by corresponding downtake DND the water of separating in the drum 16 is imported high-pressure circulation pump 17, enter the water-inlet header of mouth fixed section flue 11 lower ends after the pressurization, finish whole pump circulation process.
In addition, drum 16 upsides also are provided with many vapour pipes (among the figure not formula), by these vapour pipes with isolated steam output in the drum 16.The flue gas middle I section flue 12 of upwards flowing through, middle II section flue 13, middle III section flue 14, latter end flue 15, and in middle III section flue 14 outlet turnings be horizontal flow to, turn to once more through latter end flue 15 and to be that direction flows out high-temperature flue gas apparatus for vapour-cooling portion 10 straight down, wherein each section all is provided with annular water distribution at the smoke entrance place, compile header and corresponding air inlet-outlet-housing 19, steam water interface is in each section flue outlet header compiles by upcast UPD importing drum 16, and in drum 16 with steam and water sepn, by corresponding downtake DND the water of separating in the drum 16 is imported each section flue water-inlet header, finish each section natural circulation process.
Between mouth fixed section flue 11 and middle I section flue 12, be provided with a flue non-metal compensator 121 (as shown in Figure 7), in order to absorb the thermal expansion of membrane wall flue; Mouth fixed section flue also is provided with aerobic muzzle, sublance mouth and feed opening (shown in Fig. 9 A～9C).
Described mouth fixed section flue 11, middle I section flue 12, middle II section flue 13, middle III section flue 14 and latter end flue 15 are all round shape, and its inwall is all film water cold wall structure, 140～170 ° of membrane wall 18, be preferably and be provided with interceptor 181 between 165 °, (shown in Fig. 5 A, 5B).
Low-temperature flue gas waste-heat recovery device portion 20, shown in Fig. 2, Fig. 4 A and Fig. 4 B, it comprises preheater 21, and flue gas enters preheater 21 straight down from latter end flue 15, and the steam water interface import and export is communicated with deoxygenator 24 by downtake DND, upcast UPD.Preheater 21 adopts the lower deaerated water of inlet temperature that high-temperature flue gas is carried out heat exchange.This part biggest advantage is to have reduced the cigarette temperature, reclaimed heat, has reduced the consumption of deoxygenator 24 self deoxygenation steam simultaneously.The flue gas interchanger 22 of flowing through straight down adopts natural circulation, and promptly the steam water interface import and export all is communicated with drum 16 by downtake DND, upcast UPD, utilizes the density difference generation pressure head of steam and water to circulate.Respective change has extremely strong self-regulation to the interior steam water interface mobile speed of pipeline along with absorbing the difference of heat under the different cigarette temperature in the converter smelting cycle different time sections in the natural circulation.Flue gas comes out to flow out low-temperature flue gas waste-heat recovery device portion 20 through economizer 23 from interchanger 22, and the steam water interface import is communicated with deoxygenator 24 by downtake DND, and outlet is communicated with drum 16 by upcast UPD.Preheater 21, interchanger 22 and economizer 23 are assembled together, and are provided with public casing 221, manhole 27, dust remover 26 and ash bucket 28 etc., form low-temperature flue gas waste-heat recovery device body.
In addition, low-temperature flue gas waste-heat recovery device portion 20 comprises deoxygenator 24 in addition, it is communicated with above-mentioned preheater 21 by the upcast UPD that is arranged at its upside, and the water after carrying out deoxygenation handle in downside being provided with deoxygenator 24 exports the downtake DND of above-mentioned preheater 21 and economizer 23 to, and service pump 25, be arranged among above-mentioned deoxygenator 24 downsides and the downtake DND that the steam water interface import of economizer 23 is connected, the water that carries out in the above-mentioned deoxygenator 24 after deoxygenation is handled is pumped in above-mentioned economizer 23.
The utility model AOD converter flue gas waste heat recovery apparatus; high temperature corrosion and dust stratification for fear of high-temperature flue gas; the radiation heating surface of special shape is set; adopt the vaporization type of cooling to reduce the cigarette temperature; but the macrobead of sedimentation simultaneously dust; fully absorb the heat of low-temperature flue gas at last by convection heating surface, select suitable funnel temperature to avoid low temperature corrosion.The utlity model has the advantage that reduces AOD converter gas temperature and recovered steam, compare with traditional AOD converter gas water-cooling pattern, have more the minimizing energy consumption per ton steel, the notable feature of increasing economic efficiency, it can adopt different device structures and carbonated drink Recycle design according to different operating environment and constructional feature.
The above, it only is preferred embodiment of the present invention, be not that the present invention is done any pro forma restriction, though the present invention discloses as above with preferred embodiment, yet be not in order to limit the present invention, any those skilled in the art are not in breaking away from the technical solution of the present invention scope, when the technology contents that can utilize above-mentioned announcement is made a little change or is modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solution of the present invention, according to technical spirit of the present invention to any simple modification that above embodiment did, equivalent variations and modification all still belong in the scope of technical solution of the present invention.
Claims (9)
1, a kind of AOD converter flue gas waste heat recovery apparatus is characterized in that it comprises:
High-temperature flue gas apparatus for vapour-cooling portion, it comprises:
Mouth fixed section flue is arranged at the converter mouth top;
Middle I section flue is arranged at above-mentioned mouth fixed section flue top;
Middle II section flue is arranged at above-mentioned middle I section flue top;
Middle III section flue is arranged on above-mentioned middle II section flue top, and makes flue gas transfer horizontal direction to by vertical direction;
The latter end flue connects above-mentioned middle III section flue, and makes flue gas transfer vertical direction to by horizontal direction;
Drum, its upside are provided with the upcast that is connected with above-mentioned mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue, and the drum downside is provided with corresponding downtake;
I section flue, middle II section flue, middle III section flue, latter end flue and above-mentioned drum and the upcast of upside connection thereof and corresponding downtake are formed natural cycle system jointly in above-mentioned; And
High-pressure circulation pump, be arranged at above-mentioned drum downside, and being communicated with the bottom of above-mentioned drum and above-mentioned mouth fixed section flue by downtake, described high-pressure water heating recycle pump pumps into the water of separating in the above-mentioned drum in above-mentioned mouth fixed section flue, form the high pressure forced circulation system; And
Low-temperature flue gas waste-heat recovery device portion is connected with above-mentioned high-temperature flue gas apparatus for vapour-cooling portion, and described low-temperature flue gas waste-heat recovery device portion comprises:
Preheater is connected in above-mentioned latter end flue below, and flue gas enters preheater straight down by the latter end flue, and the upcast, the downtake that connect preheater are communicated with the formation natural circulation with above-mentioned drum;
Interchanger is arranged at above-mentioned preheater below, and the upcast, the downtake that connect interchanger are communicated with the formation natural circulation with above-mentioned drum;
Economizer is arranged at above-mentioned interchanger below, and the upcast that connects economizer is communicated with above-mentioned drum;
Deoxygenator is communicated with above-mentioned preheater by the upcast that is arranged at its upside, and by the downtake that is arranged at its downside the water that carries out in the deoxygenator after deoxygenation is handled is exported in above-mentioned preheater and the above-mentioned economizer; And
Service pump is arranged in above-mentioned deoxygenator downside downtake and the above-mentioned economizer water service pipe, and the water that is used for carrying out in the above-mentioned deoxygenator after deoxygenation is handled pumps in above-mentioned drum through above-mentioned economizer.
2, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that described mouth fixed section flue comprises oxygen muzzle and feed opening.
3, AOD converter flue gas waste heat recovery apparatus according to claim 2 is characterized in that the import of described mouth fixed section flue is provided with throttling set.
4, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that described mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue are round shape.
5, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that the inwall of described mouth fixed section flue, middle I section flue, middle II section flue, middle III section flue and latter end flue is provided with membrane wall.
6, AOD converter flue gas waste heat recovery apparatus according to claim 5 is characterized in that described membrane wall is provided with interceptor between 140～170 °.
7, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that wherein being provided with the flue non-metal compensator between mouth fixed section flue and middle I section flue.
8, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that described preheater, interchanger and economizer are assembled together, and is provided with casing, manhole, dust remover and ash bucket in described low-temperature flue gas waste-heat recovery device portion.
9, AOD converter flue gas waste heat recovery apparatus according to claim 1 is characterized in that described high-temperature flue gas apparatus for vapour-cooling portion is provided with a plurality of air inlet-outlet-housings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200784057U CN201148443Y (en) | 2008-01-02 | 2008-01-02 | AOD revolving furnace flue gas waste heat recovery apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200784057U CN201148443Y (en) | 2008-01-02 | 2008-01-02 | AOD revolving furnace flue gas waste heat recovery apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201148443Y true CN201148443Y (en) | 2008-11-12 |
Family
ID=40116210
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200784057U Expired - Lifetime CN201148443Y (en) | 2008-01-02 | 2008-01-02 | AOD revolving furnace flue gas waste heat recovery apparatus |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101476015B (en) * | 2008-01-02 | 2010-09-01 | 中冶京诚工程技术有限公司 | AOD converter flue gas waste heat recovery apparatus |
| CN101619376B (en) * | 2009-07-31 | 2011-01-12 | 清华大学 | System for recovering converter gas sensible heat |
| CN102021265A (en) * | 2010-12-23 | 2011-04-20 | 北京京诚科林环保科技有限公司 | Movable smoke hood of converter smoke system |
| CN103063048A (en) * | 2013-01-29 | 2013-04-24 | 北京世纪源博科技股份有限公司 | Horizontal evaporative cooling flue for steelmaking electric furnace |
| CN104004879A (en) * | 2014-06-11 | 2014-08-27 | 中冶南方工程技术有限公司 | Equipment and method for recovering low-temperature-section waste heat of primary converter flue gas |
| CN104964264A (en) * | 2015-07-16 | 2015-10-07 | 烟台国冶冶金水冷设备有限公司 | Combined type automatic circulating system of heat recovery boiler |
| CN115323103A (en) * | 2022-08-11 | 2022-11-11 | 河北天越激光再制造科技有限公司 | Novel steelmaking converter vaporization cooling equipment and cooling process |
-
2008
- 2008-01-02 CN CNU2008200784057U patent/CN201148443Y/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101476015B (en) * | 2008-01-02 | 2010-09-01 | 中冶京诚工程技术有限公司 | AOD converter flue gas waste heat recovery apparatus |
| CN101619376B (en) * | 2009-07-31 | 2011-01-12 | 清华大学 | System for recovering converter gas sensible heat |
| CN102021265A (en) * | 2010-12-23 | 2011-04-20 | 北京京诚科林环保科技有限公司 | Movable smoke hood of converter smoke system |
| CN103063048A (en) * | 2013-01-29 | 2013-04-24 | 北京世纪源博科技股份有限公司 | Horizontal evaporative cooling flue for steelmaking electric furnace |
| CN104004879A (en) * | 2014-06-11 | 2014-08-27 | 中冶南方工程技术有限公司 | Equipment and method for recovering low-temperature-section waste heat of primary converter flue gas |
| CN104004879B (en) * | 2014-06-11 | 2016-08-10 | 中冶南方工程技术有限公司 | Flue gas low-temperature section waste heat recovery apparatus of converter and exhaust heat recovering method |
| CN104964264A (en) * | 2015-07-16 | 2015-10-07 | 烟台国冶冶金水冷设备有限公司 | Combined type automatic circulating system of heat recovery boiler |
| CN115323103A (en) * | 2022-08-11 | 2022-11-11 | 河北天越激光再制造科技有限公司 | Novel steelmaking converter vaporization cooling equipment and cooling process |
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Granted publication date: 20081112 Effective date of abandoning: 20080102 |