CN106907931A - Process and system that sintering deposit waste heat drags main exhauster are reclaimed with perpendicular cold kiln - Google Patents
Process and system that sintering deposit waste heat drags main exhauster are reclaimed with perpendicular cold kiln Download PDFInfo
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- 239000002918 waste heat Substances 0.000 title claims abstract description 62
- 238000005245 sintering Methods 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 42
- 238000001816 cooling Methods 0.000 claims abstract description 98
- 230000001360 synchronised effect Effects 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 9
- 239000002912 waste gas Substances 0.000 claims abstract description 9
- 239000000428 dust Substances 0.000 claims description 40
- 239000000463 material Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 238000009826 distribution Methods 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims description 23
- 230000005484 gravity Effects 0.000 claims description 19
- 229910000831 Steel Inorganic materials 0.000 claims description 7
- 239000011449 brick Substances 0.000 claims description 7
- 239000010959 steel Substances 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 4
- 238000004064 recycling Methods 0.000 claims description 4
- 238000009827 uniform distribution Methods 0.000 claims description 4
- 229910000914 Mn alloy Inorganic materials 0.000 claims description 3
- 230000003139 buffering effect Effects 0.000 claims description 3
- 238000006392 deoxygenation reaction Methods 0.000 claims description 3
- 230000009970 fire resistant effect Effects 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000003973 paint Substances 0.000 claims description 3
- 238000004321 preservation Methods 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 2
- 239000011819 refractory material Substances 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims 2
- 238000011084 recovery Methods 0.000 abstract description 23
- 238000010248 power generation Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 4
- 230000010354 integration Effects 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D15/00—Handling or treating discharged material; Supports or receiving chambers therefor
- F27D15/02—Cooling
- F27D15/0286—Cooling in a vertical, e.g. annular, shaft
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01D15/10—Adaptations for driving, or combinations with, electric generators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/02—Units comprising pumps and their driving means
- F04D25/08—Units comprising pumps and their driving means the working fluid being air, e.g. for ventilation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
- F27D17/15—Arrangements for using waste heat using boilers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27M—INDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
- F27M2003/00—Type of treatment of the charge
- F27M2003/04—Sintering
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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
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
本发明涉及一种用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法及系统,热烧结矿在竖冷窑内与冷空气换热,废气经除尘后送余热锅炉,生成的过热蒸汽送至汽轮机;汽轮机通过变速离合器和同步电机直接拖动烧结主抽风机运转。本发明采用新型结构的竖冷窑,可最大限度地提高烧结矿的余热回收率;通过同步电机实现汽轮机发电与电网电能的互补,保证烧结主抽风机正常运转;由竖冷窑、余热锅炉、汽轮机和烧结主抽风机构成完整的烧结厂能量利用工艺系统,汽轮机直接向主抽风机提供动力,减少向电网取电,并可避免常规技术中汽轮机发电并入电网、烧结主抽风机自电网取电时机械能转换为电能,电能再转换为机械能所造成的二次效率损失,对节能创效意义重大。The present invention relates to a process and system for recovering waste heat of sintered ore from a vertical cooling kiln to drive the main exhaust fan. The hot sintered ore exchanges heat with cold air in the vertical cooling kiln, and the waste gas is sent to the waste heat boiler after dedusting to generate superheated steam. Send it to the steam turbine; the steam turbine directly drives the sintering main exhaust fan to run through the variable speed clutch and synchronous motor. The invention adopts a vertical cooling kiln with a new structure, which can maximize the waste heat recovery rate of sintered ore; realize the complementarity of steam turbine power generation and grid electric energy through a synchronous motor, and ensure the normal operation of the sintering main exhaust fan; the vertical cooling kiln, waste heat boiler, The steam turbine and the sintering main exhaust fan constitute a complete energy utilization process system of the sintering plant. The steam turbine directly provides power to the main exhaust fan, reducing power consumption from the grid, and avoiding the integration of the steam turbine power generation into the grid and the sintering main exhaust fan from the grid in the conventional technology. The secondary efficiency loss caused by the conversion of mechanical energy into electrical energy and the conversion of electrical energy into mechanical energy is of great significance to energy saving and benefit creation.
Description
技术领域technical field
本发明涉及烧结矿余热回收及利用技术领域,尤其涉及一种用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法及系统。The invention relates to the technical field of sinter waste heat recovery and utilization, in particular to a process method and system for driving a main exhaust fan by recovering sinter waste heat from a vertical cooling kiln.
背景技术Background technique
主抽风机是烧结厂的最大耗能设备,其用电量约为全厂设备总用电量的30%;以265m2烧结机(95%作业率)为例,其配套的主抽风机功率为8000kW,全年约耗电56630MWh,按0.547元/kWh计算,每年需交电费3098万元。The main exhaust fan is the largest energy-consuming equipment in the sintering plant, and its power consumption is about 30% of the total power consumption of the equipment in the plant; taking a 265m 2 sintering machine (95% operating rate) as an example, the power of the supporting main exhaust fan It is 8000kW, and the annual power consumption is about 56630MWh. Calculated at 0.547 yuan/kWh, the annual electricity fee is 30.98 million yuan.
烧结矿温度约700~750℃,供应高炉的是冷矿,环冷机与带冷机因设备结构特点,只能回收约30%的废气热量;采用竖式冷却窑(竖冷窑)设备能够提高热量回收率,因此目前很多科研单位和企业采用竖冷窑回收烧结矿余热。如专利号为201310127744.5的《烧结矿炉式冷却装置》、专利号为93117175.X的《竖式烧结矿冷却机》、专利号为201310672967.X的《烧结矿用竖式冷却及余热回收炉》等等,且已有1套竖冷窑设备在天津天丰钢铁投产运行,余热回收率大大提高。The temperature of the sintered ore is about 700-750°C. The blast furnace is supplied with cold ore. Due to the structural characteristics of the equipment, the annular cooler and the belt cooler can only recover about 30% of the heat of the exhaust gas; the vertical cooling kiln (vertical cooling kiln) equipment can Improve the heat recovery rate, so many research institutes and enterprises currently use vertical cooling kilns to recover sinter waste heat. Such as "Sinter Furnace Cooling Device" with patent No. 201310127744.5, "Vertical Sinter Cooler" with patent No. 93117175.X, "Vertical Cooling and Waste Heat Recovery Furnace for Sinter" with patent No. 201310672967.X And so on, and a set of vertical cold kiln equipment has been put into operation in Tianjin Tianfeng Iron and Steel, and the recovery rate of waste heat has been greatly improved.
采用蒸汽锅炉回收高温废气是目前的常规做法,将蒸汽并入热力管网及利用蒸汽拖动汽轮机发电并入电网也是目前较为常用的能源转化方式。如专利号为201520756682.9的《烧结矿显热回收装置》、专利号为201610150596.2的《一种用于烧结矿冷却及显热高效回收利用系统》、专利号为201310127764.2的《一种带矿筛的烧结矿余热高效回收发电工艺及设备》均采用了竖冷窑+余热锅炉+汽轮机的方式。上述工艺路线的终点均为汽轮机发电并网,而烧结主抽风机需要自电网取电,在汽轮机发电时机械能转换为电能及烧结主抽风机取电时电能转换为机械能的两次能量转换过程中,必须存在能量损失,而且由于用电量巨大,该能量损失所造成的能源浪费及对应的资金浪费也是很惊人的。The use of steam boilers to recover high-temperature exhaust gas is a common practice at present. Incorporating steam into the heat pipe network and using steam to drive steam turbines to generate electricity and merge them into the power grid are also currently more commonly used energy conversion methods. For example, "Sinter Sensible Heat Recovery Device" with patent No. 201520756682.9, "A System for Sinter Cooling and Sensible Heat Efficient Recovery and Utilization" with patent No. 201610150596.2, and "A Sintering System with Sieve" with Patent No. 201310127764.2. The high-efficiency recovery of mine waste heat and power generation technology and equipment" all adopt the method of vertical cold kiln + waste heat boiler + steam turbine. The end point of the above process route is that the steam turbine generates power and is connected to the grid, while the sintering main exhaust fan needs to take power from the grid. During the two energy conversion processes, the mechanical energy is converted into electrical energy when the steam turbine generates power and the electrical energy is converted into mechanical energy when the sintering main exhaust fan takes power. , there must be energy loss, and due to the huge power consumption, the energy waste and corresponding capital waste caused by the energy loss are also amazing.
竖冷窑的密封性决定废气回收率,而其漏风点主要是上料及出料系统。国内目前采用的竖冷窑上料方式有:斜桥+伞状布料形式(专利号201511002240.6,《多角多面多层360度送风烧结矿冷却塔》);链板输送机+旋转布料形式(专利号201320185479.1,《一种烧结矿炉式冷却换热装置》;专利号201520756682.9,《烧结矿显热回收装置》);与烧结机出料端直连+钟式/伞状布料形式(专利号201310127744.5,《烧结矿炉式冷却装置》;专利号93117175.X,《竖式烧结矿冷却机》;专利号201310672967.X,《烧结矿用竖式冷却及余热回收炉》);其中斜桥上料为间断作业,单斗倾翻,但窑顶上部密封性不如链板连续作业、头部滚动卸料的效果好。与烧结机出料端直连的上料方式对前道工序的烧结机和竖窑的高度布置有很大的局限性。The airtightness of the vertical cooling kiln determines the waste gas recovery rate, and the air leakage point is mainly the feeding and discharging system. The feeding methods of vertical cold kiln currently used in China are: inclined bridge + umbrella-shaped material distribution form (patent number 201511002240.6, "multi-angle, multi-layer, 360-degree air supply sinter cooling tower"); chain plate conveyor + rotary material distribution form (patent number No. 201320185479.1, "A Sinter Furnace Cooling and Heat Exchange Device"; Patent No. 201520756682.9, "Sinter Sensible Heat Recovery Device"); directly connected to the discharge end of the sintering machine + bell/umbrella cloth form (Patent No. 201310127744.5 , "Sinter Furnace Cooling Device"; Patent No. 93117175.X, "Vertical Sinter Cooler"; Patent No. 201310672967.X, "Vertical Cooling and Waste Heat Recovery Furnace for Sinter"); Among them, the inclined bridge feeding For discontinuous operation, a single bucket is tilted, but the sealing of the upper part of the kiln roof is not as good as the continuous operation of the chain plate and the rolling discharge effect of the head. The feeding method directly connected to the discharge end of the sintering machine has great limitations on the height arrangement of the sintering machine and shaft kiln in the previous process.
目前竖冷窑常采用的卸料方式有:星型卸料机(专利号201220491407.5,《一种高效热量回收型烧结矿冷却系统》;专利号201610150596.2,《一种用于烧结矿冷却及显热高效回收利用系统》;专利号200910074513.6,《一种可高效回收烧结矿显热的立式烧结矿冷却机》);电振给料器(专利号93117175.X,《竖式烧结矿冷却机》);电振定量排料器+旋转排料阀(专利号201320185290.2,《烧结矿冷却炉的卸料装置》)、(专利号201520756682.9《烧结矿显热回收装置》)。由于入竖冷窑的烧结矿对粒度有要求,不能太小,星型/旋转卸料设备虽然密封性好,但有因物料挤压使颗粒料卡入设备间隙,影响正常运行的情况发生,比较而言电振给料器不存在碎料状况,但密封料柱要考虑合适的高度。At present, the unloading methods commonly used in vertical cooling kilns are: star unloading machine (Patent No. 201220491407.5, "A High-Efficiency Heat Recovery Type Sinter Cooling System"; Patent No. 201610150596.2, "A sinter cooling and sensible heat Efficient Recycling System"; Patent No. 200910074513.6, "A Vertical Sinter Cooler That Can Efficiently Recycle Sensible Heat of Sinter"); Electric Vibration Feeder (Patent No. 93117175.X, "Vertical Sinter Cooler" ); electric vibration quantitative discharger + rotary discharge valve (Patent No. 201320185290.2, "Unloading Device for Sinter Cooling Furnace"), (Patent No. 201520756682.9 "Sinter Sensible Heat Recovery Device"). Since the sintered ore entering the vertical cold kiln has requirements on the particle size, it should not be too small. Although the star type/rotary unloading equipment has good sealing performance, due to material extrusion, the granular material may be stuck in the equipment gap, affecting normal operation. In comparison, there is no broken material in the electric vibration feeder, but the appropriate height of the sealing material column should be considered.
竖冷窑热量回收热率的高低与固气换热情况有关,布料及布风方式是关键。国内目前采用的竖冷窑布料方式有:旋转布料(专利号201520756682.9,《烧结矿显热回收装置》;专利号201310127797.7,《烧结矿冷却炉旋转给料装置》);立式螺旋给料机、钟式布料(专利号201320185480.4,《一种烧结矿冷却炉悬挂式布料器》;专利号93117175.X,《竖式烧结矿冷却机》;专利号201511002240.6,《多角多面多层360度送风烧结矿冷却塔》;专利号201320814396.4,《烧结矿用竖式冷却及余热回收炉的加料装置》)等。采用的布风方式有:设多个风室周边送风(专利号201310128026.X,《一种烧结矿冷却炉》);中心送风(专利号201320814379.0,《烧结矿用竖式冷却及余热回收炉的送冷风装置》),中心(多层伞形)与周边(风环)相送风结合(专利号201520756682.9,《烧结矿显热回收装置》);百叶窗通风格(专利号201511002240.6,《多角多面多层360度送风烧结矿冷却塔》);多台风机圆周布置(专利号200910074513.6,《一种可高效回收烧结矿显热的立式烧结矿冷却机》)、(专利号93117175.X,《竖式烧结矿冷却机》)等。现有的布料设备使大颗料边缘分布,通过改变物料堆积角来改善分布情况,并不能做到物料在窑横截面上的均匀分布。送风方式采用周边与中心相结合的形式适合大尺寸截面的竖窑,能够保证冷风与物料均匀且充分地接触。The heat recovery rate of the vertical cooling kiln is related to the solid-gas heat exchange, and the way of distributing materials and air is the key. The vertical cooling kiln material distribution methods currently used in China include: rotary material distribution (Patent No. 201520756682.9, "Sinter Sensible Heat Recovery Device"; Patent No. 201310127797.7, "Sinter Cooling Furnace Rotary Feeding Device"); vertical screw feeder, Bell-type cloth (Patent No. 201320185480.4, "A Suspended Distributor for Sinter Cooling Furnace"; Patent No. 93117175.X, "Vertical Sinter Cooler"; Patent No. 201511002240.6, "Multi-angle, Multi-layer, 360-degree Air Supply Sintering Mine Cooling Tower"; Patent No. 201320814396.4, "Vertical Cooling and Waste Heat Recovery Furnace Feeding Device for Sintering Mine"), etc. The air distribution methods adopted include: setting up multiple air chambers for peripheral air supply (Patent No. 201310128026.X, "A Sinter Cooling Furnace"); central air supply (Patent No. 201320814379.0, "Sinter Vertical Cooling and Waste Heat Recovery Furnace cold air supply device"), the center (multi-layer umbrella) and the surrounding (air ring) are combined with air supply (patent No. 201520756682.9, "Sinter Sensible Heat Recovery Device"); louver ventilation style (patent No. 201511002240.6, Multi-faceted multi-layer 360-degree air supply sinter cooling tower"); multiple fans are arranged in a circle (Patent No. 200910074513.6, "A Vertical Sinter Cooler That Can Efficiently Recover Sensible Heat of Sinter"), (Patent No. 93117175.X , "Vertical Sinter Cooler"), etc. The existing material distributing equipment makes the edge distribution of large particles, and improves the distribution by changing the material accumulation angle, but cannot achieve uniform distribution of materials on the cross-section of the kiln. The air supply method adopts the combination of the periphery and the center, which is suitable for shaft kilns with large cross-sections, and can ensure that the cold air and materials are evenly and fully contacted.
综上所述,现有竖冷窑普遍存在密封性差、物料分布不均匀等问题,导致现场环境差,出料温度高,回收废气温度低,直接影响了出料输送设备的运行及热量回收率和热值,其后果是所创造的经济效益不佳,且设备维护费用高。To sum up, the existing vertical cold kilns generally have problems such as poor sealing and uneven distribution of materials, resulting in poor site environment, high discharge temperature, and low temperature of recycled exhaust gas, which directly affects the operation of the discharge conveying equipment and the heat recovery rate And calorific value, its consequence is that the economic benefits created are not good, and the equipment maintenance cost is high.
发明内容Contents of the invention
本发明提供了一种用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法及系统,采用新型竖冷窑冷却烧结矿,可最大限度地提高烧结矿的余热回收率,改善生产环境;竖冷窑产生的废气通过余热锅炉生成蒸汽送汽轮机,汽轮机产生的机械能直接拖动烧结主抽风机运行,并通过同步电机实现汽轮机发电与电网电能的互补,保证烧结主抽风机的正常运转;由竖冷窑、余热锅炉、汽轮机和烧结主抽风机构成的完整的烧结厂能量利用工艺系统,由汽轮机直接向主抽风机提供动力,减少向电网取电,并可避免常规技术中汽轮机发电并入电网、烧结主抽风机自电网取电时机械能转换为电能,电能再转换为机械能所造成的二次效率损失,对节能创效意义重大。The invention provides a process method and system for driving the main exhaust fan by recovering waste heat of sintered ore in a vertical cooling kiln. The use of a new type of vertical cooling kiln to cool the sintered ore can maximize the recovery rate of waste heat of the sintered ore and improve the production environment; The exhaust gas generated by the vertical cooling kiln is sent to the steam turbine through the waste heat boiler. The mechanical energy generated by the steam turbine directly drives the sintering main exhaust fan to run, and the synchronous motor realizes the complementarity between the power generation of the steam turbine and the electric energy of the grid to ensure the normal operation of the sintering main exhaust fan; The complete sintering plant energy utilization process system consisting of vertical cooling kiln, waste heat boiler, steam turbine and sintering main exhaust fan, the steam turbine directly provides power to the main exhaust fan, reducing power consumption from the grid, and avoiding the integration of steam turbine power generation in conventional technology The secondary efficiency loss caused by the conversion of mechanical energy into electrical energy when the power grid and sintering main exhaust fan draws power from the grid, and then conversion of electrical energy into mechanical energy, is of great significance to energy conservation and benefit creation.
为了达到上述目的,本发明采用以下技术方案实现:In order to achieve the above object, the present invention adopts the following technical solutions to realize:
用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法,包括如下步骤:The technical method of using the vertical cooling kiln to recover the sinter waste heat to drive the main exhaust fan includes the following steps:
1)烧结机生产的700℃以上的热烧结矿经单辊破碎机破碎后落入溜槽,由电振给料机一给至链斗输送机,然后提升送入竖冷窑;竖冷窑的上部设旋转布料器和分配器,分配器由沿竖冷窑圆周均布的多个下料溜槽组成;烧结矿从链斗输送机头部卸料,通过受料溜槽进入旋转布料器,旋转布料器沿分配器圆周布料,下料溜槽用于下料缓冲并将热烧结矿均布在竖冷窑横截面上;竖冷窑内的冷风由鼓风机提供,冷风在设于竖冷窑下部的中心风道出风口及环形风道出风口出风,保证冷风在竖冷窑内分布的均匀性;1) The hot sintered ore above 700°C produced by the sintering machine is crushed by the single roll crusher and falls into the chute, and is fed to the chain bucket conveyor by the electric vibrating feeder, and then lifted into the vertical cooling kiln; the vertical cooling kiln The upper part is equipped with a rotary distributor and a distributor. The distributor is composed of a plurality of discharge chutes uniformly distributed along the circumference of the vertical cooling kiln; the sintered ore is discharged from the head of the chain bucket conveyor, and enters the rotary distributor through the receiving chute, and the rotary distribution The distributor distributes material along the circumference of the distributor, and the discharge chute is used for buffering the discharge and evenly distributes the hot sinter on the cross section of the vertical cooling kiln; the cold air in the vertical cooling kiln is provided by a blower, and the cold air is in the center of the lower part of the vertical cooling kiln The air outlet of the air duct and the air outlet of the circular air duct ensure the uniform distribution of cold air in the vertical cooling kiln;
2)在竖冷窑中,烧结矿与冷空气进行逆流换热,冷却后温度<135℃的烧结矿由窑底均布的多个出料溜槽及电振给料机二卸至带式输送机上外运;窑内586℃以上的废气由窑顶排入重力除尘器进行一次除尘,除尘后的废气通过管道引入余热锅炉;2) In the vertical cooling kiln, the sintered ore and the cold air are subjected to countercurrent heat exchange, and the sintered ore with a temperature <135°C after cooling is discharged to the belt conveyor by multiple discharge chutes uniformly distributed at the bottom of the kiln and an electric vibrating feeder. The waste gas above 586℃ in the kiln is discharged from the kiln roof into the gravity dust collector for one-time dust removal, and the waste gas after dust removal is introduced into the waste heat boiler through the pipeline;
3)在余热锅炉内,废气与水进行热交换,生成的过热蒸汽送至汽轮机;换热后的低温废气进入布袋除尘器进行二次除尘,沉降后的粉尘连同重力除尘器和余热锅炉收集的粉尘一起由链板输送机集中外运;废气经除尘净化达标后,由引风机送往烟囱外排;3) In the waste heat boiler, the exhaust gas exchanges heat with water, and the superheated steam generated is sent to the steam turbine; the low-temperature exhaust gas after heat exchange enters the bag filter for secondary dust removal, and the settled dust is collected together with the gravity dust collector and the waste heat boiler. The dust is transported together by the chain conveyor; the exhaust gas is sent to the chimney by the induced draft fan after the dust removal and purification reach the standard;
4)汽轮机将过热蒸汽的热能转化为机械能,驱动变速离合器转动并带动同步电机运转,同步电机带动烧结主抽风机的叶片旋转实现烧结主抽风机的运转;当汽轮机能力富余时,同步电机剩余电能并入电网使用;当汽轮机能力不足时,同步电机自电网取电供烧结主抽风机使用,并保证烧结主抽风机正常运转;4) The steam turbine converts the thermal energy of the superheated steam into mechanical energy, drives the variable speed clutch to rotate and drives the synchronous motor to run, and the synchronous motor drives the blades of the sintering main exhaust fan to rotate to realize the operation of the sintering main exhaust fan; when the capacity of the steam turbine is sufficient, the remaining electric energy of the synchronous motor Connected to the grid for use; when the capacity of the steam turbine is insufficient, the synchronous motor takes power from the grid for the sintering main exhaust fan, and ensures the normal operation of the sintering main exhaust fan;
5)拖动汽轮机后的冷却蒸汽进入余热锅炉内实现循环利用;首先由冷凝器冷凝,凝结水由凝结水泵送至除盐水箱,经低压给水泵依次送入加热器、除氧器中加热、除氧后送至给水汽包,再经蒸发器和过热器后产生过热蒸汽送往汽轮机。5) The cooling steam after dragging the steam turbine enters the waste heat boiler to realize recycling; firstly, it is condensed by the condenser, and the condensed water is pumped from the condensed water to the desalinated water tank, and then sent to the heater and deaerator in sequence through the low-pressure feed water pump for heating, After deoxygenation, it is sent to the feed water steam drum, and then after passing through the evaporator and superheater, superheated steam is generated and sent to the steam turbine.
所述旋转布料器、鼓风机、电振给料机一、电振给料机二的驱动装置均为变频控制,保证竖冷窑内料面的稳定性及热烧结矿冷却的充分性及均匀性。The driving devices of the rotary distributor, blower, electric vibrating feeder 1, and electric vibrating feeder 2 are all controlled by frequency conversion to ensure the stability of the material surface in the vertical cooling kiln and the adequacy and uniformity of cooling of the hot sintered ore .
用于实现所述工艺方法的用竖冷窑回收烧结矿余热拖动主抽风机的工艺系统,包括按照工艺路线依次连接的竖冷窑、重力除尘器、余热锅炉、汽轮机、变速离合器、同步电机和烧结主抽风机;所述竖冷窑顶部的热烧结矿进料口上方设受料溜槽,烧结机后的单辊破碎机通过溜槽、电振给料机一和链斗输送机连接受料溜槽;受料溜槽的底部通过旋转布料器连接分配器,旋转布料器由布料器本体、旋转布料槽和驱动电机组成,旋转布料槽在布料器本体内倾斜设置,其顶部位于布料器本体顶部边沿并与驱动电机连接传动,底部位于分配器上方中部位置,在驱动电机带动下旋转布料槽绕竖冷窑中轴线转动;分配器由上部筒体和下部多个沿周向均布的下料溜槽组成,下料溜槽为向下扩大的锥形结构,其出料端设在竖冷窑的上部空间;竖冷窑的下部设中心风道出风口和环形风道出风口,环形风道出风口沿竖冷窑的外侧边缘设置多个,中心风道和环形风道分别通过风管连接鼓风机;竖冷窑底部设有多个沿圆周方向均布的出料溜槽,出料溜槽底部连接带式输送机;竖冷窑的顶部废气出口连接重力除尘器,重力除尘器后的高温废气管道连接余热锅炉中的蒸发器,低温废气管道通过布袋除尘器和引风机连接烟囱。A process system for driving the main exhaust fan by recovering sinter waste heat from a vertical cooling kiln for realizing the process method, including a vertical cooling kiln, a gravity dust collector, a waste heat boiler, a steam turbine, a variable speed clutch, and a synchronous motor sequentially connected according to the process route and the sintering main exhaust fan; a material receiving chute is set above the hot sinter feed inlet on the top of the vertical cooling kiln, and the single roll crusher after the sintering machine is connected to receive material through the chute, the electric vibration feeder and the chain bucket conveyor Chute; the bottom of the material receiving chute is connected to the distributor through a rotary distributor. The rotary distributor is composed of a distributor body, a rotary distributor chute and a driving motor. And it is connected with the driving motor for transmission. The bottom is located in the middle above the distributor. Driven by the driving motor, the rotating distributing chute rotates around the central axis of the vertical cooling kiln; The discharge chute is a tapered structure that expands downwards, and its discharge end is set in the upper space of the vertical cooling kiln; the lower part of the vertical cooling kiln is equipped with a central air duct outlet and an annular air duct outlet, and the annular air duct outlet is along the vertical The outer edge of the cold kiln is provided with several, the central air duct and the annular air duct are respectively connected to the blower through the air duct; the bottom of the vertical cold kiln is equipped with a plurality of discharge chutes uniformly distributed along the circumferential direction, and the bottom of the discharge chute is connected to the belt conveyor ; The top exhaust gas outlet of the vertical cold kiln is connected to the gravity dust collector, the high temperature exhaust gas pipeline behind the gravity dust collector is connected to the evaporator in the waste heat boiler, and the low temperature exhaust gas pipeline is connected to the chimney through the bag filter and induced draft fan.
所述重力除尘器、布袋除尘器和余热锅炉的粉尘出口分别连接链板输送机。The dust outlets of the gravity dust collector, the bag filter and the waste heat boiler are respectively connected to the chain conveyor.
所述余热锅炉中设有蒸发器、过热器、冷凝器、加热器和除氧器,所述蒸发器通过过热器连接汽轮机的过热蒸汽入口;汽轮机的冷却蒸汽出口连接冷凝器,冷凝器通过凝结水泵连接除盐水箱,除盐水箱通过给水泵连接加热器和除氧器,除氧器后的过热蒸汽管道通过给水汽包连接蒸发器。The waste heat boiler is equipped with an evaporator, a superheater, a condenser, a heater and a deaerator, and the evaporator is connected to the superheated steam inlet of the steam turbine through the superheater; the cooling steam outlet of the steam turbine is connected to the condenser, and the condenser passes through the condensation The water pump is connected to the desalinated water tank, and the desalted water tank is connected to the heater and deaerator through the feed water pump, and the superheated steam pipeline after the deaerator is connected to the evaporator through the feed water drum.
所述溜槽、受料溜槽、旋转布料槽、分配器、出料溜槽的本体由锅炉钢板或耐热不锈钢制成,根据需要设或不设内衬,内衬由高耐磨锰合金钢板或耐火材料制成。The body of the chute, receiving chute, rotating distribution chute, distributor, and discharging chute is made of boiler steel plate or heat-resistant stainless steel, with or without lining as required, and the inner lining is made of high wear-resistant manganese alloy steel plate or fire-resistant material.
所述竖冷窑自环形风道出风口以上的内壁设衬层,衬层由内层工作层和外层保温层组成,内层工作层由耐火砖砌筑,外层保温层耐火喷涂料形成,衬层由托砖环承托。The vertical cold kiln is provided with a lining layer on the inner wall above the air outlet of the circular air duct, the lining layer is composed of an inner working layer and an outer insulating layer, the inner working layer is made of refractory bricks, and the outer insulating layer is formed by refractory spray paint , the lining is supported by the supporting brick ring.
所述链斗输送机设密封保温罩。The chain bucket conveyor is provided with a sealed heat preservation cover.
所述驱动电机包括对称设置在布料器本体顶部边沿的2台电机,布料器本体顶部边沿设齿圈,齿圈在电机驱动下转动,并与设在旋转布料槽顶部的齿轮啮合传动,带动旋转布料槽沿布料器本体顶部边沿移动并实现旋转布料槽绕竖冷窑中心轴线的转动。The driving motor includes two motors symmetrically arranged on the top edge of the distributor body, and a ring gear is arranged on the top edge of the distributor body, and the ring gear rotates under the drive of the motor, and is engaged with the gear arranged on the top of the rotating distribution tank to drive the rotation. The distribution chute moves along the top edge of the distributor body and realizes the rotation of the rotating distribution chute around the central axis of the vertical cooling kiln.
所述下料溜槽和出料溜槽的数量均为6个。The number of the discharge chute and the discharge chute is 6.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1)采用新型竖冷窑冷却烧结矿,可实现物料颗粒在窑内的均匀分布,且窑内料面稳定性好,热矿冷却充分、均匀,最大限度地提高了烧结矿的余热回收率,且整体密封性好,可以改善生产环境;1) A new type of vertical cooling kiln is used to cool the sintered ore, which can realize the uniform distribution of material particles in the kiln, and the stability of the material surface in the kiln is good, the hot ore is cooled sufficiently and evenly, and the waste heat recovery rate of the sintered ore is maximized. And the overall sealing is good, which can improve the production environment;
2)竖冷窑产生的废气通过余热锅炉生成蒸汽送汽轮机,汽轮机产生的机械能直接拖动烧结主抽风机运行,通过同步电机实现汽轮机发电与电网电能的互补,保证烧结主抽风机的正常运转;其原理独特、结构新颖、构思巧妙、操作方式灵活;2) The waste gas generated by the vertical cooling kiln is sent to the steam turbine through the waste heat boiler, and the mechanical energy generated by the steam turbine directly drives the sintering main exhaust fan to run, and the synchronous motor is used to realize the complementarity between the power generation of the steam turbine and the electric energy of the grid to ensure the normal operation of the sintering main exhaust fan; Its principle is unique, the structure is novel, the concept is ingenious, and the operation mode is flexible;
3)由竖冷窑、余热锅炉、汽轮机和烧结主抽风机构成的完整的烧结厂能量利用工艺系统,由汽轮机直接向主抽风机提供动力,减少向电网取电,并可避免常规技术中汽轮机发电并入电网、烧结主抽风机自电网取电时机械能转换为电能,电能再转换为机械能所造成的二次效率损失,对节能创效意义重大。3) A complete sintering plant energy utilization process system consisting of a vertical cold kiln, waste heat boiler, steam turbine and sintering main exhaust fan. The steam turbine directly supplies power to the main exhaust fan, reducing power consumption from the grid and avoiding the need for steam turbines in conventional technologies. The secondary efficiency loss caused by the integration of power generation into the power grid and the sintering main exhaust fan taking power from the power grid is of great significance to energy saving and benefit creation.
附图说明Description of drawings
图1是本发明所述的用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法的流程图。Fig. 1 is the flow chart of the process of using the recovery of sinter waste heat from the vertical cooling kiln to drive the main exhaust fan according to the present invention.
图2是本发明所述竖冷窑的立面结构示意图。Fig. 2 is a schematic diagram of the facade structure of the vertical cooling kiln of the present invention.
图3是图2的局部放大图。FIG. 3 is a partially enlarged view of FIG. 2 .
图4是分配器的俯视图。Figure 4 is a top view of the dispenser.
图中:1.烧结机 2.单辊破碎机 3.溜槽 4.电振给料机一 5.链斗输送机 6.受料溜槽 7.旋转布料器 71.布料槽本体 72.旋转布料槽 73.驱动电机 8.分配器 81.筒体82.下料溜槽 9.竖冷窑 91.中心风道出风口 92.环形风道出风口 93.耐火砖 10.出料溜槽 11.电振给料机二 12.带式输送机 13.重力除尘器 14.余热锅炉 15.链板输送机 16.烟囱In the figure: 1. Sintering machine 2. Single roll crusher 3. Chute 4. Electric vibration feeder 5. Chain bucket conveyor 6. Receiving chute 7. Rotary distributor 71. Distributing trough body 72. Rotating distributing trough 73. Drive motor 8. Distributor 81. Cylinder body 82. Blanking chute 9. Vertical cooling kiln 91. Air outlet of central air duct 92. Air outlet of annular air duct 93. Refractory brick 10. Discharge chute 11. Electric vibration feed Material machine 2 12. Belt conveyor 13. Gravity dust collector 14. Waste heat boiler 15. Chain plate conveyor 16. Chimney
具体实施方式detailed description
下面结合附图对本发明的具体实施方式作进一步说明:The specific embodiment of the present invention will be further described below in conjunction with accompanying drawing:
如图1所示,本发明所述用竖冷窑回收烧结矿余热拖动主抽风机的工艺方法,包括如下步骤:As shown in Fig. 1, the technical method of dragging the main exhaust fan with vertical cooling kiln recovery sinter waste heat described in the present invention, comprises the following steps:
1)烧结机1生产的700℃以上的热烧结矿经单辊破碎机2破碎后落入溜槽3,由电振给料机一4给至链斗输送机5,然后提升送入竖冷窑9;竖冷窑9的上部设旋转布料器7和分配器8,分配器8由沿竖冷窑9圆周均布的多个下料溜槽82组成;烧结矿从链斗输送机5头部卸料,通过受料溜槽6进入旋转布料器7,旋转布料器7沿分配器8圆周布料,下料溜槽82用于下料缓冲并将热烧结矿均布在竖冷窑9横截面上;竖冷窑9内的冷风由鼓风机提供,冷风在设于竖冷窑9下部的中心风道出风口91及环形风道出风口92出风,保证冷风在竖冷窑9内分布的均匀性;1) The hot sintered ore above 700°C produced by sintering machine 1 is crushed by single roll crusher 2 and then falls into chute 3, fed to chain bucket conveyor 5 by electric vibrating feeder 1, and then lifted into vertical cooling kiln 9; The upper part of the vertical cooling kiln 9 is provided with a rotary distributor 7 and a distributor 8, and the distributor 8 is composed of a plurality of discharge chutes 82 uniformly distributed along the circumference of the vertical cooling kiln 9; the sintered ore is discharged from the head of the chain bucket conveyor 5 The material enters the rotary distributor 7 through the receiving chute 6, and the rotary distributor 7 distributes the material along the circumference of the distributor 8. The discharge chute 82 is used for buffering the discharge and uniformly distributes the hot sintered ore on the cross section of the vertical cold kiln 9; The cold air in the cold kiln 9 is provided by a blower, and the cold air is discharged from the central air duct air outlet 91 and the annular air duct air outlet 92 located at the bottom of the vertical cold kiln 9 to ensure the uniformity of distribution of the cold air in the vertical cold kiln 9;
2)在竖冷窑9中,烧结矿与冷空气进行逆流换热,冷却后温度<135℃的烧结矿由窑底均布的多个出料溜槽10及电振给料机二11卸至带式输送机12上外运;窑内586℃以上的废气由窑顶排入重力除尘器13进行一次除尘,除尘后的废气通过管道引入余热锅炉14;2) In the vertical cooling kiln 9, the sintered ore and the cold air are subjected to countercurrent heat exchange, and the sintered ore with a temperature <135°C after cooling is discharged to the The belt conveyor 12 is used for transportation; the waste gas above 586°C in the kiln is discharged from the kiln roof into the gravity dust collector 13 for one-time dust removal, and the waste gas after dust removal is introduced into the waste heat boiler 14 through the pipeline;
3)在余热锅炉14内,废气与水进行热交换,生成的过热蒸汽送至汽轮机;换热后的低温废气进入布袋除尘器进行二次除尘,沉降后的粉尘连同重力除尘器13和余热锅炉14收集的粉尘一起由链板输送机15集中外运;废气经除尘净化达标后,由引风机送往烟囱16外排;3) In the waste heat boiler 14, the exhaust gas exchanges heat with water, and the superheated steam generated is sent to the steam turbine; the low-temperature exhaust gas after heat exchange enters the bag filter for secondary dust removal, and the settled dust is combined with the gravity dust collector 13 and the waste heat boiler 14 The collected dust is transported together by the chain conveyor 15; the exhaust gas is sent to the chimney 16 by the induced draft fan after being dedusted and purified up to the standard;
4)汽轮机将过热蒸汽的热能转化为机械能,驱动变速离合器转动并带动同步电机运转,同步电机带动烧结主抽风机的叶片旋转实现烧结主抽风机的运转;当汽轮机能力富余时,同步电机剩余电能并入电网使用;当汽轮机能力不足时,同步电机自电网取电供烧结主抽风机使用,并保证烧结主抽风机正常运转;4) The steam turbine converts the thermal energy of the superheated steam into mechanical energy, drives the variable speed clutch to rotate and drives the synchronous motor to run, and the synchronous motor drives the blades of the sintering main exhaust fan to rotate to realize the operation of the sintering main exhaust fan; when the capacity of the steam turbine is sufficient, the remaining electric energy of the synchronous motor Connected to the grid for use; when the capacity of the steam turbine is insufficient, the synchronous motor takes power from the grid for the sintering main exhaust fan, and ensures the normal operation of the sintering main exhaust fan;
5)拖动汽轮机后的冷却蒸汽进入余热锅炉14内实现循环利用;首先由冷凝器冷凝,凝结水由凝结水泵送至除盐水箱,经低压给水泵依次送入加热器、除氧器中加热、除氧后送至给水汽包,再经蒸发器和过热器后产生过热蒸汽送往汽轮机。5) The cooling steam after driving the steam turbine enters the waste heat boiler 14 to realize recycling; firstly, it is condensed by the condenser, and the condensed water is pumped to the desalinated water tank by the condensed water pump, and then sent to the heater and the deaerator in turn for heating by the low-pressure feed water pump , After deoxygenation, it is sent to the steam feed drum, and then the superheated steam is generated after passing through the evaporator and superheater and sent to the steam turbine.
所述旋转布料器7、鼓风机、电振给料机一4、电振给料机二11的驱动装置均为变频控制,保证竖冷窑9内料面的稳定性及热烧结矿冷却的充分性及均匀性。The driving devices of the rotary distributor 7, blower, electric vibrating feeder 1 4, and electric vibrating feeder 2 11 are all controlled by frequency conversion to ensure the stability of the material surface in the vertical cold kiln 9 and the sufficient cooling of the hot sintered ore. sex and uniformity.
如图1、图2所示,用于实现所述工艺方法的用竖冷窑回收烧结矿余热拖动主抽风机的工艺系统,包括按照工艺路线依次连接的竖冷窑9、重力除尘器13、余热锅炉14、汽轮机、变速离合器、同步电机和烧结主抽风机;所述竖冷窑9顶部的热烧结矿进料口上方设受料溜槽6,烧结机1后的单辊破碎机2通过溜槽3、电振给料机一4和链斗输送机5连接受料溜槽6;如图3所示,受料溜槽6的底部通过旋转布料器7连接分配器8,旋转布料器7由布料器本体71、旋转布料槽72和驱动电机73组成,旋转布料槽72在布料器本体71内倾斜设置,其顶部位于布料器本体71顶部边沿并与驱动电机73连接传动,底部位于分配器8上方中部位置,在驱动电机73带动下旋转布料槽72绕竖冷窑9中轴线转动;分配器8由上部筒体81和下部多个沿周向均布的下料溜槽82组成(如图4所示),下料溜槽82为向下扩大的锥形结构,其出料端设在竖冷窑9的上部空间;竖冷窑9的下部设中心风道出风口91和环形风道出风口92,环形风道出风口92沿竖冷窑9的外侧边缘设置多个,中心风道和环形风道分别通过风管连接鼓风机;竖冷窑9底部设有多个沿圆周方向均布的出料溜槽10,出料溜槽10底部连接带式输送机12;竖冷窑9的顶部废气出口连接重力除尘器13,重力除尘器13后的高温废气管道连接余热锅炉14中的蒸发器,低温废气管道通过布袋除尘器和引风机连接烟囱16。As shown in Fig. 1 and Fig. 2, the process system for realizing the process method is to use the waste heat of sinter recovered by the vertical cold kiln to drive the main exhaust fan, including the vertical cold kiln 9 and the gravity dust collector 13 connected in sequence according to the process route , waste heat boiler 14, steam turbine, variable speed clutch, synchronous motor and sintering main exhaust fan; a material receiving chute 6 is arranged above the hot sinter feed inlet at the top of the vertical cold kiln 9, and the single roll crusher 2 behind the sintering machine 1 passes through The chute 3, the electric vibration feeder 4 and the chain bucket conveyor 5 are connected to the material receiving chute 6; as shown in Figure 3, the bottom of the material receiving chute 6 is connected to the distributor 8 through the rotating distributor 7, and the rotating distributor 7 is formed by the material Composed of a distributor body 71, a rotating distributing trough 72 and a drive motor 73, the rotating distributing trough 72 is installed obliquely in the distributor body 71, its top is located at the top edge of the distributor body 71 and is connected to the drive motor 73 for transmission, and the bottom is located above the distributor 8 In the middle position, driven by the driving motor 73, the rotating distributing chute 72 rotates around the central axis of the vertical cold kiln 9; the distributor 8 is composed of an upper cylinder 81 and a plurality of discharge chutes 82 evenly distributed along the circumferential direction in the lower part (as shown in Figure 4) , the blanking chute 82 is a tapered structure enlarged downwards, and its discharge end is located in the upper space of the vertical cooling kiln 9; the bottom of the vertical cooling kiln 9 is provided with a central air duct air outlet 91 and an annular air duct air outlet 92, and the annular air duct air outlet 92 A plurality of air duct air outlets 92 are arranged along the outer edge of the vertical cooling kiln 9, and the central air duct and the annular air duct are respectively connected to blowers through air ducts; the bottom of the vertical cooling kiln 9 is provided with a plurality of discharge chutes 10 uniformly distributed along the circumferential direction , the bottom of the discharge chute 10 is connected to the belt conveyor 12; the top exhaust gas outlet of the vertical cold kiln 9 is connected to the gravity dust collector 13, and the high-temperature exhaust gas pipeline behind the gravity dust collector 13 is connected to the evaporator in the waste heat boiler 14, and the low-temperature exhaust gas pipeline passes through the cloth bag The dust collector and the induced draft fan are connected to the chimney 16.
所述重力除尘器13、布袋除尘器和余热锅炉14的粉尘出口分别连接链板输送机15。The dust outlets of the gravity dust collector 13 , the bag filter and the waste heat boiler 14 are respectively connected to the chain conveyor 15 .
所述余热锅炉14中设有蒸发器、过热器、冷凝器、加热器和除氧器,所述蒸发器通过过热器连接汽轮机的过热蒸汽入口;汽轮机的冷却蒸汽出口连接冷凝器,冷凝器通过凝结水泵连接除盐水箱,除盐水箱通过给水泵连接加热器和除氧器,除氧器后的过热蒸汽管道通过给水汽包连接蒸发器。The waste heat boiler 14 is provided with an evaporator, a superheater, a condenser, a heater and a deaerator, and the evaporator is connected to the superheated steam inlet of the steam turbine through the superheater; the cooling steam outlet of the steam turbine is connected to the condenser, and the condenser passes through The condensate pump is connected to the desalinated water tank, the desalted water tank is connected to the heater and the deaerator through the feed water pump, and the superheated steam pipeline after the deaerator is connected to the evaporator through the feed water drum.
所述溜槽3、受料溜槽6、旋转布料槽72、分配器8、出料溜槽10的本体由锅炉钢板或耐热不锈钢制成,根据需要设或不设内衬,内衬由高耐磨锰合金钢板或耐火材料制成。The bodies of the chute 3, the receiving chute 6, the rotating distribution chute 72, the distributor 8, and the discharge chute 10 are made of boiler steel plate or heat-resistant stainless steel, with or without lining as required, and the lining is made of high wear-resistant Manganese alloy steel plate or refractory material.
所述竖冷窑9自环形风道出风口92以上的内壁设衬层,衬层由内层工作层和外层保温层组成,内层工作层由耐火砖砌筑,外层保温层耐火喷涂料形成,衬层由托砖环承托。The vertical cold kiln 9 is provided with a lining layer from the inner wall above the air outlet 92 of the annular air duct. The lining layer is composed of an inner working layer and an outer insulating layer. The inner working layer is made of refractory bricks, and the outer insulating layer is fire-resistant The paint is formed and the lining is supported by the brick ring.
所述链斗输送机5设密封保温罩。The chain bucket conveyor 5 is provided with a sealed heat preservation cover.
所述驱动电机73包括对称设置在布料器本体71顶部边沿的2台电机,布料器本体71顶部边沿设齿圈,齿圈在电机驱动下转动,并与设在旋转布料槽72顶部的齿轮啮合传动,带动旋转布料槽72沿布料器本体71顶部边沿移动并实现旋转布料槽72绕竖冷窑9中心轴线的转动。The drive motor 73 includes two motors symmetrically arranged on the top edge of the distributor body 71, the top edge of the distributor body 71 is provided with a ring gear, the ring gear rotates under the drive of the motor, and meshes with the gear on the top of the rotary distribution tank 72 Transmission drives the rotating distribution chute 72 to move along the top edge of the distributor body 71 and realizes the rotation of the rotating distribution chute 72 around the central axis of the vertical cold kiln 9 .
所述下料溜槽82和出料溜槽10的数量均为6个。The number of the discharge chute 82 and the discharge chute 10 is 6.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technical solution of the present invention Any equivalent replacement or change of the inventive concepts thereof shall fall within the protection scope of the present invention.
Claims (10)
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611246444.9A CN106907931A (en) | 2016-12-29 | 2016-12-29 | Process and system that sintering deposit waste heat drags main exhauster are reclaimed with perpendicular cold kiln |
| JP2019535806A JP6854899B2 (en) | 2016-12-29 | 2017-12-29 | Bulk material cooling |
| KR1020197018675A KR102389265B1 (en) | 2016-12-29 | 2017-12-29 | Cooling of bulk materials |
| PCT/CN2017/119855 WO2018121733A1 (en) | 2016-12-29 | 2017-12-29 | Cooling of bulk material |
| CN201780081582.2A CN110678711B (en) | 2016-12-29 | 2017-12-29 | Cooling of bulk material |
| UAA201907182A UA125441C2 (en) | 2016-12-29 | 2017-12-29 | Cooling of bulk material |
| PL17889512T PL3563108T3 (en) | 2016-12-29 | 2017-12-29 | Device, comprising a shaft cooler and an input device, and method for cooling hot sinter |
| RU2019119849A RU2762953C2 (en) | 2016-12-29 | 2017-12-29 | Cooling of bulk material |
| EP17889512.4A EP3563108B1 (en) | 2016-12-29 | 2017-12-29 | Device, comprising a shaft cooler and an input device, and method for cooling hot sinter |
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Effective date of registration: 20180305 Address after: 114000 Tiexi District, Anshan City, No. 1 Ring Road, No. Applicant after: ANSTEEL ENGINEERING TECHNOLOGY Corp.,Ltd. Applicant after: SIEMENS VAI METALS TECHNOLOGIES GmbH Address before: 114000 Tiexi District, Anshan City, No. 1 Ring Road, No. Applicant before: ANSTEEL ENGINEERING TECHNOLOGY Corp.,Ltd. |
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Application publication date: 20170630 |