CN101173324A - Novel technique for comprehensive utilization of continuous strip annealing furnace flue gas exhaust heat and device thereof - Google Patents
Novel technique for comprehensive utilization of continuous strip annealing furnace flue gas exhaust heat and device thereof Download PDFInfo
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- CN101173324A CN101173324A CNA2006101249214A CN200610124921A CN101173324A CN 101173324 A CN101173324 A CN 101173324A CN A2006101249214 A CNA2006101249214 A CN A2006101249214A CN 200610124921 A CN200610124921 A CN 200610124921A CN 101173324 A CN101173324 A CN 101173324A
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Abstract
The invention relates to a new comprehensive utilization technology of flue gas residual heat for band steel continuous annealing oven, comprising a flue duct of an annealing oven, a plurality of driers, a plurality of rinsing solution box, in particular to the two-end heat exchangers, which is characterized in that the two-end heat exchangers are positioned on the smoke exhaust duct of the annealing oven, of which one end is used to heat air for drying, and the other end is used to heat various solutions of degreasing segment; the temperature of the annealing gas flue gas is controlled between 150-160 DEG C; in particular to the two-end heat exchangers connected into the flue pipeline, of which one end is an air flue gas heat exchanger; the air inlet is externally connected with a blower, and the air outlet is externally connected with a drying primary air duct, which are communicated with each drier by a secondary drier; the other end is a water flue gas heat exchanger; the water inlet externally connected with a water feeding pump, a soft water box and a return pipe, and the water outlet is externally connected with a hot water pipe; the heat exchange pipe is connected in parallel between the return pipe and the hot water pipe, which is communicated with each rinsing solution box. The invention has the advantages of full utilization of the annealing flue gas residual heat, lower investment cost, coal consumption saving, and is mainly used for the heat treatment of cold rolling thin steel strip in metallurgical industry.
Description
(1) technical field:
The present invention relates to the thermal treatment process technology of the cold rolling thin steel band of metallurgy industry.
(2) background technology:
Continuous strip annealing furnace is divided into two types basically, and is promptly horizontal and vertical.By the conveying of transfer equipment, unfolded band steel is finished heating, soaking (reduction or decarburization) and the whole heat treatment process of refrigerative in stove.For avoiding being with steel to produce high temperature oxidation in stove, and obtain the surface of light in stove, dual mode is mainly adopted in the stove heat supply: a kind of is to adopt the heat supply of total radiation pipe; Another kind is to adopt non-oxidation furnace and radiator tube bonded mode, and is especially in the majority in first kind of mode.Radiator tube can be divided into " I " type, " U " type, " W " type etc. according to its form.Combustion gas and combustion air heat radiator tube by the radiator tube internal combustion that is organized in of burner, and to the stove internal heating, discharge after with the combustion air preheating by the air heat exchanger of pyritous flue gas by being arranged on radiator tube outlet with heat radiation for radiator tube.Because the Heating temperature of radiator tube is higher, and its space is limited, the heat interchanging area of air heat exchanger is restricted, so the flue-gas temperature of discharging from radiator tube is still just very high, temperature is at 550-600 ℃.The smoke discharging mode of existing annealing furnace is that the flue gas with radiator tube mixes cold wind and its temperature will be reduced to below 250 ℃ discharges, or directly adopts high-temperature blower to discharge.
Also have several heat energy consumption points on the cold rolling thin steel band thermal treatment unit.The one, before going into furnace annealing, the band steel needs band steel cleaning by degreasing and dry, and technological process is alkali cleaning, electrolytic cleaning, water spray and warm air drying; The 2nd, need after the aftertreatment of band steel such as polishing, the passivation band steel is carried out warm air drying.For reaching good cleaning performance, need various scavenging solutions are heated to 60-80 ℃, present unit all adopts steam heating, and the exsiccant hot blast also adopts steam heating, uses steam-pipe to feed moisture eliminator and cleaning solution case.A common unit of producing 250000 tons per year need be equipped with the boiler dedicated of a 4t/h.
So for whole unit, the annealing furnace fume afterheat is also underused, and other power consumption points need to consume the new energy, cause the process energy consumption height of unit.Simultaneously, the cost of investment of boiler house is also higher.
(3) summary of the invention:
Purpose of the present invention is exactly to solve existing cold rolling thin steel band thermal treatment process energy consumption height, the unit investment is big, running cost is high problem, and a kind of continuous strip annealing furnace fume afterheat comprehensive utilization novel process and device thereof are provided.
The present invention is by the analysis-by-synthesis to each energy consumption point, carries out the heat calculation of unit, the fume afterheat comprehensive utilization technique of a kind of uniqueness that proposes in conjunction with the process characteristic of steel band thermal treatment unit.A kind of continuous strip annealing furnace fume afterheat comprehensive utilization of the present invention novel process, it is characterized in that: the two poles of the earth interchanger is set on the smoke discharging pipe of annealing furnace, one-level is used for the heat drying air, feed each moisture eliminator, another grade is used to heat the various solution of degreasing section, feed each cleaning solution case, the annealing furnace flue-gas temperature is controlled at 150-160 ℃.
The present invention is used for a kind of device of continuous strip annealing furnace fume afterheat comprehensive utilization novel process, include the smoke exhaust pipe of annealing furnace, some moisture eliminators, some cleaning solution casees, it is characterized in that: in the smoke exhaust pipe pipeline, insert the two poles of the earth interchanger, one-level is air-flue gas heat exchange device, the external gas blower of its blast inlet, and the external dry air main of its air outlet feeds each moisture eliminator through some branch wind pipes again; Another level is water-flue gas heat exchange device, the external service pump of its water-in, softened water tank and return water pipe, and the external hot-water line of its water outlet, the some heat transfer tubes of access in parallel between return water pipe and hot-water line, heat transfer tube places each cleaning solution case respectively.
Be furnished with by-pass valve in the outside of water-flue gas heat exchange device and mix cold blast valve in a kind of device in the continuous strip annealing furnace fume afterheat comprehensive utilization novel process of the present invention, to regulate, prevent the soft water overtemperature through water-exhaust gas volumn of flue gas heat exchange device and final funnel temperature.
UTILIZATION OF VESIDUAL HEAT IN principle of the present invention is as follows:
For making full use of the fume afterheat of annealing furnace, the two-stage interchanger is set on the smoke discharging pipe of annealing furnace, the first step is air-flue gas heat exchange device, the external gas blower of its blast inlet, cold wind is preheated to about 150 ℃ through interchanger, and drying air main, branch wind pipe are delivered to the warm air drying that each moisture eliminator on the unit is used for thermal treatment process.
The second stage is water-flue gas heat exchange device, consider each rinse bath solution compolision difference, can not mix, and for preventing the interchanger in-tube fouling, should adopt soft water as the heat conduction carrier, a softened water tank is set, adopt service pump that soft water is sent into the interchanger heating, high temperature soft water is sent into heat transfer tube in each cleaning solution case by hot-water line and is finished heating to cleaning solution, and low temperature soft water is back to softened water tank and recycles.The control of cleaning solution Heating temperature is undertaken by regulating the soft internal circulating load, simultaneously for preventing the soft water overtemperature, and can be by regulating by-pass valve and mixing cold blast valve to regulate through water-exhaust gas volumn of flue gas heat exchange device and final funnel temperature.
The present invention has carried out UTILIZATION OF VESIDUAL HEAT IN to the flue gas of continuous strip annealing furnace, need not be equipped with special-purpose boiler steam room and boiler plant, saved investment cost greatly, particularly save burnup running cost, article one, produce 250000 tons unit per year, can save 4000 tons of standard coals every year, save production cost about 3,200,000 yuan.
(4) description of drawings:
Accompanying drawing is apparatus of the present invention system architecture synoptic diagram.
Among the figure: 1-air-flue gas heat exchange device, 2-water-flue gas heat exchange device, 3-gas blower, the 4-by-pass valve, 5-induced-draft fan, 6-service pump, the 7-softened water tank, 8-cleaning solution case, 9-heat transfer tube, 10-mixes cold blast valve, 11-return water pipe, 12-hot-water line, the 13-variable valve, 14-smoke exhaust pipe, the dry air main of 15-, the 16-damper, 17-branch wind pipe, 18-moisture eliminator.
(5) embodiment:
Continuous strip annealing furnace fume afterheat comprehensive utilization novel process of the present invention is that the two poles of the earth interchanger is set on the smoke discharging pipe of annealing furnace, one-level is used for the heat drying air, feed each moisture eliminator, another grade is used to heat the various solution of tread flaking section, feed each cleaning solution case, the annealing furnace flue-gas temperature is controlled at 150-160 ℃.
The present invention is used for the device of continuous strip annealing furnace fume afterheat comprehensive utilization novel process referring to accompanying drawing, include the smoke exhaust pipe 14 of annealing furnace, three (or more) moisture eliminators 18, three (or more) cleaning solution casees 8, particularly be serially connected with two-stage interchanger 1 and 2 in the pipeline of smoke exhaust pipe 14, the tail end tipping of smoke exhaust pipe 14 has induced-draft fan 5; Wherein first step interchanger is air-flue gas heat exchange device 1, the external gas blower 3 of its blast inlet, and the external dry air main 15 of its air outlet feeds each moisture eliminator 18 respectively from three of air main 15 taps (or more) branch wind pipe 17 again.Wherein second stage interchanger is water-flue gas heat exchange device 2, the external successively service pump 6 of its water-in, softened water tank 7, return water pipe 11, the external hot-water line 12 of its water outlet; Three (or more) heat transfer tubes 9 of access in parallel between return water pipe 11 and hot-water line 12, heat transfer tube 9 places each cleaning solution case 8 respectively, and cleaning solution is heated.For preventing the soft water overtemperature, the present invention is furnished with the by-pass valve of adjusting 4 and mixes cold blast valve 10 in the outside of second stage water-flue gas heat exchange device 2.
For the Heating temperature of control cleaning solution is provided with variable valve 13 to regulate the soft internal circulating load at heat transfer tube 9 into and out of end.Be the temperature of control moisture eliminator 18, in each branch wind pipe 17, be provided with damper 16 with the control hot blast rate.
Claims (3)
1. a continuous strip annealing furnace fume afterheat fully utilizes novel process, it is characterized in that: the two poles of the earth interchanger is set on the smoke discharging pipe of annealing furnace, one-level is used for the heat drying air, feed each moisture eliminator, another grade is used to heat the various solution of degreasing section, feed each cleaning solution case, the annealing furnace flue-gas temperature is controlled at 150-160 ℃.
2. be used for a kind of device according to the described continuous strip annealing furnace fume afterheat comprehensive utilization of claim 1 novel process, include the smoke exhaust pipe of annealing furnace, some moisture eliminators, some cleaning solution casees, it is characterized in that: in the smoke exhaust pipe pipeline, insert the two poles of the earth interchanger, one-level is air-flue gas heat exchange device, the external gas blower of its blast inlet, and the external dry air main of its air outlet feeds each moisture eliminator through some branch wind pipes again; Another level is water-flue gas heat exchange device, the external service pump of its water-in, softened water tank and return water pipe, and the external hot-water line of its water outlet, the some heat transfer tubes of access in parallel between return water pipe and hot-water line, heat transfer tube places each cleaning solution case respectively.
3. according to a kind of device in the described continuous strip annealing furnace fume afterheat comprehensive utilization of claim 2 novel process, it is characterized in that: be furnished with by-pass valve in the outside of water-flue gas heat exchange device and mix cold blast valve.
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| CNB2006101249214A CN100500886C (en) | 2006-10-31 | 2006-10-31 | Novel technique for comprehensive utilization of continuous strip annealing furnace flue gas exhaust heat and device thereof |
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| CNB2006101249214A CN100500886C (en) | 2006-10-31 | 2006-10-31 | Novel technique for comprehensive utilization of continuous strip annealing furnace flue gas exhaust heat and device thereof |
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Cited By (18)
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| CN101871042A (en) * | 2010-06-25 | 2010-10-27 | 中冶南方(武汉)威仕工业炉有限公司 | Method and device for reusing flue gas waste heat of annealing furnace of continuous annealing unit |
| CN101899562A (en) * | 2010-07-14 | 2010-12-01 | 浙江佰耐钢带有限公司 | Waste heat utilization steel strip heat treatment system |
| CN101949649A (en) * | 2010-09-15 | 2011-01-19 | 新兴铸管股份有限公司 | Annealing furnace combustion air preheating device |
| CN102021299A (en) * | 2010-11-29 | 2011-04-20 | 佛山市高明基业冷轧钢板有限公司 | Device for utilizing residual heat of gas flue in hood-type annealing furnace |
| CN102078855A (en) * | 2009-11-27 | 2011-06-01 | 中国第一汽车集团公司 | Drying residual-heat utilization device of large-scale automobile coating production line |
| CN102563608A (en) * | 2010-12-31 | 2012-07-11 | 贵州中烟工业有限责任公司 | Secondary steam-recycling method for condensate collector |
| CN102559988A (en) * | 2012-03-01 | 2012-07-11 | 九源天能（北京）科技有限公司昆明分公司 | Tinder trapping and heat energy recovery device for flue gas of steelmaking converter |
| CN101906528B (en) * | 2009-06-08 | 2012-08-29 | 鞍钢股份有限公司 | Method for reducing folding mark defects of cold-rolled steel coil |
| CN102899477A (en) * | 2012-08-29 | 2013-01-30 | 江苏兴达钢帘线股份有限公司 | Steel wire heat-treatment processing line waste heat utilization conversion system |
| CN104344730A (en) * | 2013-08-02 | 2015-02-11 | 上海振世能源科技有限公司 | Smoke waste heat recycling system |
| CN106868262A (en) * | 2017-03-02 | 2017-06-20 | 北京福生智源科技有限公司 | It is provided with the cold-rolling continuous annealing production line high-temperature smoke discharging pipe of waste-heat recovery device |
| CN108026606A (en) * | 2016-08-19 | 2018-05-11 | 普锐特冶金技术日本有限公司 | Continuous annealing apparatus |
| CN110296601A (en) * | 2019-07-25 | 2019-10-01 | 启明星宇节能科技股份有限公司 | A kind of tunnel stove low nitrogen burning system and method for controlling combustion |
| CN110332815A (en) * | 2019-07-11 | 2019-10-15 | 黄石山力科技股份有限公司 | Adjustable flue gas waste heat utilization device and system |
| CN111457745A (en) * | 2020-03-30 | 2020-07-28 | 中冶南方工程技术有限公司 | Stainless steel production line and energy-saving method thereof |
| CN112370909A (en) * | 2020-09-30 | 2021-02-19 | 山东岱荣节能环保科技有限公司 | Dust removal device for flue gas waste heat utilization |
| CN114593612A (en) * | 2022-01-26 | 2022-06-07 | 何荣志 | A high-efficiency recovery system for low-temperature waste heat of a furnace |
| CN116287660A (en) * | 2023-02-02 | 2023-06-23 | 宜兴市惠华复合材料有限公司 | Cold-rolled metal strip annealing equipment capable of automatically conveying materials and using method |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101906528B (en) * | 2009-06-08 | 2012-08-29 | 鞍钢股份有限公司 | Method for reducing folding mark defects of cold-rolled steel coil |
| CN102078855A (en) * | 2009-11-27 | 2011-06-01 | 中国第一汽车集团公司 | Drying residual-heat utilization device of large-scale automobile coating production line |
| CN101871042A (en) * | 2010-06-25 | 2010-10-27 | 中冶南方(武汉)威仕工业炉有限公司 | Method and device for reusing flue gas waste heat of annealing furnace of continuous annealing unit |
| CN101899562A (en) * | 2010-07-14 | 2010-12-01 | 浙江佰耐钢带有限公司 | Waste heat utilization steel strip heat treatment system |
| CN101899562B (en) * | 2010-07-14 | 2012-05-23 | 浙江佰耐钢带有限公司 | Waste heat utilization steel strip heat treatment system |
| CN101949649A (en) * | 2010-09-15 | 2011-01-19 | 新兴铸管股份有限公司 | Annealing furnace combustion air preheating device |
| CN102021299B (en) * | 2010-11-29 | 2012-11-14 | 佛山市高明基业冷轧钢板有限公司 | Device for utilizing residual heat of gas flue in hood-type annealing furnace |
| CN102021299A (en) * | 2010-11-29 | 2011-04-20 | 佛山市高明基业冷轧钢板有限公司 | Device for utilizing residual heat of gas flue in hood-type annealing furnace |
| CN102563608A (en) * | 2010-12-31 | 2012-07-11 | 贵州中烟工业有限责任公司 | Secondary steam-recycling method for condensate collector |
| CN102563608B (en) * | 2010-12-31 | 2015-05-13 | 贵州中烟工业有限责任公司 | Secondary steam-recycling method for condensate collector |
| CN102559988A (en) * | 2012-03-01 | 2012-07-11 | 九源天能（北京）科技有限公司昆明分公司 | Tinder trapping and heat energy recovery device for flue gas of steelmaking converter |
| CN102559988B (en) * | 2012-03-01 | 2013-04-24 | 九源天能（北京）科技有限公司昆明分公司 | Tinder trapping and heat energy recovery device for flue gas of steelmaking converter |
| CN102899477A (en) * | 2012-08-29 | 2013-01-30 | 江苏兴达钢帘线股份有限公司 | Steel wire heat-treatment processing line waste heat utilization conversion system |
| CN104344730A (en) * | 2013-08-02 | 2015-02-11 | 上海振世能源科技有限公司 | Smoke waste heat recycling system |
| CN108026606A (en) * | 2016-08-19 | 2018-05-11 | 普锐特冶金技术日本有限公司 | Continuous annealing apparatus |
| CN106868262A (en) * | 2017-03-02 | 2017-06-20 | 北京福生智源科技有限公司 | It is provided with the cold-rolling continuous annealing production line high-temperature smoke discharging pipe of waste-heat recovery device |
| CN110332815A (en) * | 2019-07-11 | 2019-10-15 | 黄石山力科技股份有限公司 | Adjustable flue gas waste heat utilization device and system |
| CN110296601A (en) * | 2019-07-25 | 2019-10-01 | 启明星宇节能科技股份有限公司 | A kind of tunnel stove low nitrogen burning system and method for controlling combustion |
| CN110296601B (en) * | 2019-07-25 | 2024-05-03 | 启明星宇节能科技股份有限公司 | Low-nitrogen combustion system of tunnel kiln |
| CN111457745A (en) * | 2020-03-30 | 2020-07-28 | 中冶南方工程技术有限公司 | Stainless steel production line and energy-saving method thereof |
| CN112370909A (en) * | 2020-09-30 | 2021-02-19 | 山东岱荣节能环保科技有限公司 | Dust removal device for flue gas waste heat utilization |
| CN112370909B (en) * | 2020-09-30 | 2022-02-18 | 山东岱荣节能环保科技有限公司 | Dust removal device for flue gas waste heat utilization |
| CN114593612A (en) * | 2022-01-26 | 2022-06-07 | 何荣志 | A high-efficiency recovery system for low-temperature waste heat of a furnace |
| CN114593612B (en) * | 2022-01-26 | 2024-01-23 | 何荣志 | High-efficient recovery system of kiln low temperature waste heat |
| CN116287660A (en) * | 2023-02-02 | 2023-06-23 | 宜兴市惠华复合材料有限公司 | Cold-rolled metal strip annealing equipment capable of automatically conveying materials and using method |
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Address after: 435003 Guangzhou road Huangshi city Hubei province Tuanchengshan Development Zone No. 2 Patentee after: HUANGSHI SUNNY SCIENCE & TECHNOLOGY CO., LTD. Address before: 435003 Guangzhou road Huangshi city Hubei province Tuanchengshan Development Zone No. 2 Patentee before: Huangshi Sunny Science & Technology Development Co., Ltd. |