CN112725556B - Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas - Google Patents
Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas Download PDFInfo
- Publication number
- CN112725556B CN112725556B CN202110066136.2A CN202110066136A CN112725556B CN 112725556 B CN112725556 B CN 112725556B CN 202110066136 A CN202110066136 A CN 202110066136A CN 112725556 B CN112725556 B CN 112725556B
- Authority
- CN
- China
- Prior art keywords
- pulverized coal
- flue gas
- molten iron
- blast furnace
- coal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003245 coal Substances 0.000 title claims abstract description 213
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 145
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 113
- 239000003546 flue gas Substances 0.000 title claims abstract description 111
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 70
- 238000010438 heat treatment Methods 0.000 title claims abstract description 64
- 238000000034 method Methods 0.000 title abstract description 20
- 238000002347 injection Methods 0.000 claims abstract description 40
- 239000007924 injection Substances 0.000 claims abstract description 40
- 239000007789 gas Substances 0.000 claims abstract description 36
- 239000000843 powder Substances 0.000 claims abstract description 33
- 238000002485 combustion reaction Methods 0.000 claims abstract description 15
- 239000002184 metal Substances 0.000 claims abstract description 15
- 229910052751 metal Inorganic materials 0.000 claims abstract description 15
- 239000000428 dust Substances 0.000 claims description 44
- 238000000926 separation method Methods 0.000 claims description 23
- 238000007789 sealing Methods 0.000 claims description 18
- 229910000831 Steel Inorganic materials 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 7
- 239000010959 steel Substances 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 5
- 238000010298 pulverizing process Methods 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 4
- 239000000779 smoke Substances 0.000 claims description 4
- 238000003723 Smelting Methods 0.000 abstract description 9
- 238000010079 rubber tapping Methods 0.000 abstract description 9
- 238000005266 casting Methods 0.000 abstract description 5
- 239000000446 fuel Substances 0.000 abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 230000008092 positive effect Effects 0.000 abstract description 2
- 230000000903 blocking effect Effects 0.000 description 19
- 239000004575 stone Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000003068 static effect Effects 0.000 description 5
- 239000000567 combustion gas Substances 0.000 description 2
- 239000012717 electrostatic precipitator Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B7/00—Blast furnaces
- C21B7/002—Evacuating and treating of exhaust gases
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
- C21B2100/40—Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
- C21B2100/44—Removing particles, e.g. by scrubbing, dedusting
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
- C21B2100/60—Process control or energy utilisation in the manufacture of iron or steel
- C21B2100/66—Heat exchange
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种利用高炉铁水除尘循环热烟气加热煤粉的方法和装置,属于冶金炼铁喷煤工艺及设备技术领域。The invention relates to a method and a device for heating pulverized coal by utilizing blast furnace molten iron dedusting and circulating hot flue gas, and belongs to the technical field of metallurgical ironmaking and coal injection technology and equipment.
背景技术Background technique
目前,在冶金炼铁领域,高炉喷吹用煤粉加热技术能有效提高煤粉燃烧效率,降低高炉燃料比,提高煤粉置换比,高炉喷吹用煤粉加热技术正在逐步推广使用,为高炉创造了可观的经济效益。但是,已有技术的喷煤煤粉加热技术采用的是高炉热风炉废烟气或燃烧炉热烟气进行煤粉加热,例如:中国发明专利CN201410070774.1的一种高炉喷煤系统煤粉预热工艺方法等等,上述已有技术存在问题是:热能利用效率低,煤粉加热后燃烧炉的热烟气(约在120℃以下),被排到大气中,这部分热能被白白的浪费掉。At present, in the field of metallurgical ironmaking, the pulverized coal heating technology for blast furnace injection can effectively improve the combustion efficiency of pulverized coal, reduce the fuel ratio of the blast furnace, and improve the pulverized coal replacement ratio. Created considerable economic benefits. However, the prior art pulverized coal heating technology uses blast furnace hot blast stove waste flue gas or combustion furnace hot flue gas to heat pulverized coal. Thermal process methods, etc., the above-mentioned existing technologies have problems: the utilization efficiency of thermal energy is low, and the hot flue gas (about 120°C below) of the combustion furnace after the pulverized coal is heated is discharged into the atmosphere, and this part of the thermal energy is wasted in vain. Lose.
发明内容SUMMARY OF THE INVENTION
本发明目的是提供一种利用高炉铁水除尘循环热烟气加热煤粉的方法和装置,充分利用高炉冶炼出铁过程中的铁水与除尘烟气换热后的热量进行喷煤煤粉的加热,排出的热烟气又返回铁水罐铁水沟除尘罩内,循环往复,最大限度的利用了高炉冶炼出铁过程中的铁水热量,能源利用效率高,经济效益显著,解决已有技术存在的上述问题。The purpose of the present invention is to provide a method and a device for heating pulverized coal by utilizing the hot flue gas of blast furnace molten iron dedusting and circulating, making full use of the heat exchanged between molten iron and dedusting flue gas in the blast furnace smelting and tapping process to heat pulverized coal by pulverized coal injection. The exhausted hot flue gas is returned to the dust removal hood of the molten iron tank and the hot metal ditch is circulated and reciprocated, and the heat of molten iron in the process of smelting and tapping of the blast furnace is utilized to the maximum extent, the energy utilization efficiency is high, and the economic benefit is significant. .
本发明的技术方案是:The technical scheme of the present invention is:
一种利用高炉铁水除尘循环热烟气加热煤粉的方法,利用高炉冶炼出铁过程中铁水罐及铁水沟除尘循环热烟气为主要热源,煤气燃烧炉或燃烧器产生的热烟气为辅助热源,对高炉喷吹煤粉进行加热。本发明充分利用高炉冶炼出铁过程中的铁水与除尘烟气换热后的热量,对喷吹煤粉进行加热,循环往复使用,最大限度的利用了高炉冶炼出铁过程中的铁水热量。A method for heating pulverized coal by utilizing hot flue gas of blast furnace molten iron dust removal and circulation, utilizing hot flue gas of hot metal tank and hot metal ditch dedusting circulation as main heat source, and hot flue gas generated by gas burner or burner as auxiliary The heat source is used to heat the blast furnace blown pulverized coal. The invention makes full use of the heat exchanged between molten iron and dedusting flue gas in the blast furnace smelting and tapping process, heats the blown pulverized coal, and uses it cyclically to make the most of the molten iron heat in the blast furnace smelting and tapping process.
铁水与除尘烟气换热后的热烟气对煤粉进行加热,加热后的煤粉进行高炉喷吹,热烟气对煤粉进行加热后温度降低,除尘后返回铁水罐及铁水沟上方进行换热,热烟气再对煤粉进行加热。The hot flue gas after the heat exchange between the molten iron and the dedusting flue gas heats the pulverized coal, and the heated pulverized coal is injected into the blast furnace. Heat exchange, and the hot flue gas heats the pulverized coal.
一种利用高炉铁水除尘循环热烟气加热煤粉的装置,铁水罐的上方设有铁水罐铁水沟除尘罩,铁水罐铁水沟除尘罩收集的烟气通过烟气管路一进入煤粉加热器,煤粉加热器内设有煤粉加热管,煤粉加热管的一端通过煤粉和气体分离装置连接高炉喷煤管线,另一端通过煤粉集粉喷吹器连接喷煤枪,喷煤枪向高炉内喷吹煤粉;煤粉加热器的烟气出口通过烟气管路二连接除尘器和循环引风机;所述铁水罐铁水沟除尘罩与铁水罐之间设有出口烟气分配器,循环引风机通过循环管路连接出口烟气分配器。The utility model relates to a device for heating pulverized coal by using hot flue gas from blast furnace molten iron dust removal and circulation. Above the molten iron tank is a dust removal cover for the molten iron tank. The pulverized coal heater is provided with a pulverized coal heating pipe. One end of the pulverized coal heating pipe is connected to the blast furnace coal injection pipeline through the pulverized coal and gas separation device, and the other end is connected to the coal injection gun through the coal powder collecting and powder injector. The pulverized coal is injected into the blast furnace; the flue gas outlet of the pulverized coal heater is connected to the dust collector and the circulating induced draft fan through the second flue gas pipeline; an outlet flue gas distributor is provided between the hot metal tank and the hot metal ditch dust removal cover and the molten iron tank , the circulating induced draft fan is connected to the outlet flue gas distributor through the circulating pipeline.
所述出口烟气分配器为环绕铁水罐上口外沿布置的环形管,环形管的底部密布出气孔,出气孔朝向铁水罐内;环形管与循环管路连接;出口烟气分配器水平环形布置,出口烟气分配器通过循环管路与循环引风机出口连通,排出的烟气在铁水罐外侧冷空气和铁水罐铁水沟除尘罩之间形成一层热烟幕,减少了冷空气进入铁水罐铁水沟除尘罩,提高了循环热烟气温度。The outlet flue gas distributor is an annular pipe arranged around the outer edge of the upper mouth of the molten iron tank, the bottom of the annular pipe is densely covered with air outlet holes, and the air outlet holes face the inside of the molten iron tank; the annular pipe is connected with the circulating pipeline; the outlet flue gas distributor is arranged in a horizontal ring shape , the outlet flue gas distributor is connected with the outlet of the circulating induced draft fan through the circulation pipeline, and the exhausted flue gas forms a layer of hot smoke screen between the cold air outside the molten iron tank and the dust removal cover of the molten iron ditch, which reduces the cold air entering the molten iron in the molten iron tank. The ditch dust cover increases the temperature of circulating hot flue gas.
所述烟气管路一连接燃烧炉或燃烧器。The flue gas pipeline is connected to the combustion furnace or the burner.
所述循环引风机通过阀门一连接烟筒;循环引风机通过阀门二连接循环管路。The circulating induced draft fan is connected to the chimney through the first valve; the circulating induced draft fan is connected to the circulating pipeline through the second valve.
所述高炉喷煤管线与煤粉加热管之间设有煤粉和气体分离装置,煤粉和气体分离装置为静态分离仓体,内部通过挡灰条或挡灰丝束分隔为左右两部分空间,右部分空间内通过挡灰过滤层分为上腔室和下腔室,上腔室通过挡灰条或挡灰丝束与左部分空间连通,下腔室的侧壁穿入与高炉喷煤管线连接的进煤管,下腔室的底部设有与煤粉加热管连接的煤粉出口;左部分空间顶部设有气体放散装置。A pulverized coal and gas separation device is arranged between the blast furnace coal injection pipeline and the pulverized coal heating pipe. The pulverized coal and gas separation device is a static separation bin body, and the interior is divided into left and right parts by ash blocking bars or ash blocking tows. , the right part of the space is divided into an upper chamber and a lower chamber through the ash blocking filter layer, the upper chamber is connected with the left part of the space through the ash blocking strip or the ash blocking tow, and the side wall of the lower chamber penetrates with the blast furnace coal injection The coal inlet pipe connected by the pipeline, the bottom of the lower chamber is provided with a coal powder outlet connected with the coal powder heating pipe; the top of the left part of the space is provided with a gas release device.
所述煤粉集粉喷吹器包括通过连通管路相互连通的集粉段和喷吹段两部分;集粉段为圆柱形,圆柱面周围均匀设置多个连接管路,内侧为空腔,用于存储煤粉;多根与煤粉加热管连通的连接管路均匀分布在集粉段圆柱面周围;喷吹段设有一个或多个出煤口与喷煤枪连通,喷吹段上部设有进气孔,喷吹段与煤粉和气体分离装置的排压管路连通,同时与喷吹加压管路连通,喷吹段下部设有流化装置,用于煤粉喷吹时流化煤粉。流化装置为本领域公知公用的市售设备。The pulverized coal collecting and pulverizing injector comprises two parts, a collecting section and a blowing section, which are communicated with each other through a communication pipeline; It is used to store pulverized coal; a plurality of connecting pipes connected to the pulverized coal heating pipe are evenly distributed around the cylindrical surface of the powder collecting section; There is an air inlet hole, the injection section is connected with the pressure discharge pipeline of the pulverized coal and gas separation device, and at the same time is connected with the injection pressure pipeline. Fluidized pulverized coal. The fluidizing device is a commercially available device well known in the art.
所述煤粉出口的底部设有上封板,上封板上设置多个上板孔,多根煤粉加热管分别与各自的上板孔连接。The bottom of the pulverized coal outlet is provided with an upper sealing plate, a plurality of upper plate holes are arranged on the upper sealing plate, and a plurality of pulverized coal heating pipes are respectively connected with the respective upper plate holes.
所述挡灰过滤层由网格带和石子构成,网格带为两层钢丝或其它材质构成的网格框架,内部装有石子,所起的作用是带有灰尘气体通过石子缝隙时,粉尘接触石子表面后,被阻拦,失去上升动力下落。The ash blocking filter layer is composed of mesh belts and stones. The mesh belt is a grid frame composed of two layers of steel wire or other materials. Stones are installed inside. After touching the surface of the stone, it was blocked and lost its upward power to fall.
所述挡灰条或挡灰丝束由丝状物构成,倒垂在静态分离仓体内,所起的作用是带有灰尘气体可以从挡灰条或挡灰丝束的缝隙通过,煤粉接触挡灰条或挡灰丝束表面后,被阻拦,失去动力下落。The ash blocking strip or the ash blocking tow is composed of filaments and hangs down in the static separation bin. After the surface of the ash-blocking strip or the ash-blocking tow is blocked, it loses power to fall.
所述左部分空间通过排压管路与旋风除尘器连接;所述挡灰过滤层的上方匹配声波清灰装置。The left part of the space is connected with the cyclone dust collector through a pressure discharge pipeline; the upper part of the dust blocking filter layer is matched with a sound wave dust cleaning device.
所述煤粉出口内设密封罐,所述下腔室底部为漏斗结构,漏斗中心通过下料管进入煤粉出口内的密封罐,对煤粉出口进行密封,保证煤粉和气体分离装置的封闭性。The pulverized coal outlet is provided with a sealing tank, the bottom of the lower chamber is a funnel structure, and the center of the funnel enters the sealing tank in the pulverized coal outlet through a feeding pipe to seal the pulverized coal outlet to ensure the separation of the pulverized coal and the gas. closedness.
所述进煤管端部设有缓冲罐,进入下腔室的煤粉通过缓冲罐降低冲击力。The end of the coal inlet pipe is provided with a buffer tank, and the pulverized coal entering the lower chamber can reduce the impact force through the buffer tank.
本发明涉及的声波清灰装置、气体放散装置、旋风除尘器和燃烧炉或燃烧器等等,为市售产品。The acoustic wave cleaning device, the gas dispersing device, the cyclone dust collector, the combustion furnace or the burner, etc. involved in the present invention are commercially available products.
所述煤粉加热管数量为多根,排列成管束布置,煤粉加热管为无缝钢管,设有翅片,增加换热面积。The number of the pulverized coal heating pipes is multiple, arranged in a tube bundle arrangement, and the pulverized coal heating pipes are seamless steel pipes with fins to increase the heat exchange area.
所述铁水罐铁水沟除尘罩为普通除尘罩,铁水罐铁水沟除尘罩设置在铁水罐和铁水沟上方;所述除尘器为常规除尘器,如旋风除尘器、多管除尘器、布袋除尘器、电除尘器和滤筒除尘器等。The dedusting hood for the molten iron ditch is a common dedusting hood, and the dedusting hood for the molten iron ditch is arranged above the molten iron tank and the molten iron ditch; , electrostatic precipitator and filter cartridge precipitator, etc.
所述燃烧炉或燃烧器为普通的燃烧炉和燃烧器,燃烧气体为可燃气体,燃烧炉或燃烧器热烟气出口与铁水罐铁水沟除尘罩和煤粉加热器之间的烟气管路一相连通。The combustion furnace or burner is an ordinary combustion furnace and burner, the combustion gas is a combustible gas, and the flue gas pipeline between the hot flue gas outlet of the combustion furnace or the burner and the dust removal cover of the molten iron tank and the hot metal ditch and the pulverized coal heater Connected.
所述循环引风机为普通引风机,循环引风机吸入口与煤粉加热器的烟气出口连通,循环引风机出口与出口烟气分配器和烟筒连通。The circulating induced draft fan is a common induced draft fan, the suction inlet of the circulating induced draft fan is communicated with the flue gas outlet of the pulverized coal heater, and the outlet of the circulating induced draft fan is communicated with the outlet flue gas distributor and the chimney.
所述烟气管路一、烟气管路二和循环管路设有保温层,减少热量损失。The first flue gas pipeline, the second flue gas pipeline and the circulation pipeline are provided with thermal insulation layers to reduce heat loss.
所述烟筒为常规设计排风烟筒。The chimney is a conventional design exhaust chimney.
所述煤粉加热器的外壳为钢制的中间外壳体,外面设有保温层,多根煤粉加热管布置在外壳内,外壳内有热烟气通过,与煤粉加热管换热,用于加热煤粉。The outer shell of the pulverized coal heater is a steel intermediate outer shell with a thermal insulation layer on the outside. A plurality of pulverized coal heating pipes are arranged in the outer shell, and hot flue gas passes through the outer shell to exchange heat with the pulverized coal heating pipes. for heating pulverized coal.
所述中间外壳体为长条筒状,水平布置,一端与烟气管路一连通,另一端与烟气管路二连通;中间外壳体顶部的侧壁设有上连筒,与煤粉出口连接,中间外壳体底部侧壁设有下连筒,与煤粉集粉喷吹器连接;多根煤粉加热管形成的管束通过上连筒进入中间外壳体内加热,然后通过下连筒与煤粉集粉喷吹器连接;所述下连筒的底部设有下封板,下封板上设有多个下板孔,多根煤粉加热管分别与各自的下板孔连接,多根煤粉加热管穿过下板孔与煤粉集粉喷吹器的连接管路连接。The intermediate outer shell is in the shape of a long cylinder, arranged horizontally, one end is connected with the flue gas pipeline, and the other end is connected with the second flue gas pipeline; the side wall of the top of the intermediate outer shell is provided with an upper connecting cylinder, which is connected with the pulverized coal outlet. The bottom side wall of the intermediate outer casing is provided with a lower connecting cylinder, which is connected with the pulverized coal collector and powder injector; the tube bundle formed by a plurality of pulverized coal heating pipes enters the intermediate casing through the upper connecting cylinder for heating, and then passes through the lower connecting cylinder and the coal powder. The powder collecting and powder blowing device is connected; the bottom of the lower connecting cylinder is provided with a lower sealing plate, the lower sealing plate is provided with a plurality of lower plate holes, and the plurality of pulverized coal heating pipes are respectively connected with the respective lower plate holes. The pulverized coal heating pipe is connected with the connecting pipeline of the pulverized coal collecting and pulverizing injector through the hole of the lower plate.
本发明的积极效果:充分利用了高炉冶炼出铁过程中的铁水与除尘烟气换热后热烟气的热量进行加热喷煤煤粉,排出的热烟气又返回铁水罐铁水沟除尘罩内,循环往复,重复利用,最大限度的回收了铁水的热量,提高了进入高炉煤粉的温度,提高了煤粉燃烬率,降低了高炉燃料比,提高了煤粉置换比,节能降耗,减少碳排放。增强了出铁场除尘的除尘效果,改善了高炉出铁场周围环境,尤其适合高炉出铁场除尘能力不足高炉进行改造,不仅改善了出铁场周围环境,而且通过提高炉煤粉温度创造可观的经济效益。相对已有的其它煤粉加热技术,不仅能更多的创效,而且降低了煤粉加热装置总体造价。The positive effect of the invention is that the heat of the hot flue gas after the heat exchange between the molten iron and the dust-removing flue gas in the blast furnace smelting and tapping process is fully utilized to heat the pulverized coal, and the discharged hot flue gas is returned to the dust-removing cover of the molten iron tank. , reciprocating, reusing, maximizing the recovery of the heat of molten iron, increasing the temperature of pulverized coal entering the blast furnace, increasing the burning rate of pulverized coal, reducing the fuel ratio of the blast furnace, improving the pulverized coal replacement ratio, saving energy and reducing consumption, Reduce carbon emissions. It enhances the dust removal effect of the casting yard, improves the surrounding environment of the blast furnace casting yard, and is especially suitable for the reconstruction of blast furnaces with insufficient dust removal capacity in the blast furnace casting yard. It not only improves the surrounding environment of the casting yard, but also creates a considerable economic benefits. Compared with other existing pulverized coal heating technologies, it can not only create more benefits, but also reduce the overall cost of the pulverized coal heating device.
附图说明Description of drawings
图1为本发明实施例整体示意图;1 is an overall schematic diagram of an embodiment of the present invention;
图2为本发明实施例煤粉加热器的结构示意图;2 is a schematic structural diagram of a pulverized coal heater according to an embodiment of the present invention;
图3为本发明实施例煤粉和气体分离装置的结构示意图;3 is a schematic structural diagram of a pulverized coal and gas separation device according to an embodiment of the present invention;
图4为本发明实施例煤粉和气体分离装置的A-A剖视示意图;Fig. 4 is the A-A sectional schematic diagram of the pulverized coal and gas separation device according to the embodiment of the present invention;
图5为本发明实施例煤粉集粉喷吹器的结构示意图;FIG. 5 is a schematic structural diagram of a pulverized coal collector and powder injector according to an embodiment of the present invention;
图6为本发明实施例铁水罐及除尘罩的结构示意图;6 is a schematic structural diagram of a molten iron tank and a dust hood according to an embodiment of the present invention;
图7为本发明实施例出口烟气分配器的B向结构示意图;FIG. 7 is a schematic view of the B-direction structure of the outlet flue gas distributor according to the embodiment of the present invention;
图中:铁水罐铁水沟除尘罩1、除尘器2、燃烧炉或燃烧器3、循环引风机4、出口烟气分配器5、烟气管路一6、烟筒7、煤粉加热器8、煤粉和气体分离装置9、排压管路10、煤粉集粉喷吹器11、煤粉加热管12、喷煤枪13、高炉14、中间外壳体15、喷吹加压管路16、进煤管17、静态分离仓体18、气体放散装置19、声波清灰装置20、旋风除尘器21、挡灰过滤层22、挡灰条或挡灰丝束23、煤粉出口24、网格带25、石子26、集粉段27、喷吹段28、出煤口29、进气孔30、流化装置31、铁水罐32、出气孔33、烟气管路二34、阀门一35、阀门二36、缓冲罐37、密封罐38、循环管路39、上连筒40、下连筒41、连接管路42、连通管路43。In the figure: 1,
具体实施方式Detailed ways
下面结合附图和实施例对本发明做进一步的说明:Below in conjunction with accompanying drawing and embodiment, the present invention will be further described:
一种利用高炉铁水除尘循环热烟气加热煤粉的方法,利用高炉冶炼出铁过程中铁水罐及铁水沟除尘循环热烟气为主要热源,煤气燃烧炉或燃烧器产生的热烟气为辅助热源,对高炉喷吹煤粉进行加热。本发明充分利用高炉冶炼出铁过程中的铁水与除尘烟气换热后的热量,对喷吹煤粉进行加热,循环往复使用,最大限度的利用了高炉冶炼出铁过程中的铁水热量。A method for heating pulverized coal by utilizing hot flue gas of blast furnace molten iron dust removal and circulation, utilizing hot flue gas of hot metal tank and hot metal ditch dedusting circulation as main heat source, and hot flue gas generated by gas burner or burner as auxiliary The heat source is used to heat the blast furnace blown pulverized coal. The invention makes full use of the heat exchanged between molten iron and dedusting flue gas in the blast furnace smelting and tapping process, heats the blown pulverized coal, and uses it cyclically to make the most of the molten iron heat in the blast furnace smelting and tapping process.
铁水与除尘烟气换热后的热烟气对煤粉进行加热,加热后的煤粉进行高炉喷吹,热烟气对煤粉进行加热后温度降低,除尘后返回铁水罐及铁水沟上方进行换热,热烟气再对煤粉进行加热。The hot flue gas after the heat exchange between the molten iron and the dedusting flue gas heats the pulverized coal, and the heated pulverized coal is injected into the blast furnace. Heat exchange, and the hot flue gas heats the pulverized coal.
一种利用高炉铁水除尘循环热烟气加热煤粉的装置,铁水罐32的上方设有铁水罐铁水沟除尘罩1,铁水罐铁水沟除尘罩1收集的烟气通过烟气管路一6进入煤粉加热器8,煤粉加热器8内设有煤粉加热管12,煤粉加热管12的一端通过煤粉和气体分离装置9连接高炉喷煤管线,另一端通过煤粉集粉喷吹器11连接喷煤枪13,喷煤枪13向高炉14内喷吹煤粉;煤粉加热器8的烟气出口通过烟气管路二34连接除尘器2和循环引风机4;所述铁水罐铁水沟除尘罩1与铁水罐32之间设有出口烟气分配器5,循环引风机4通过循环管路39连接出口烟气分配器5。A device for heating pulverized coal by using hot flue gas from blast furnace molten iron dust removal and circulation. Above the
所述出口烟气分配器5为环绕铁水罐上口外沿布置的环形管,环形管的底部密布出气孔33,出气孔33朝向铁水罐内;环形管与循环管路39连接;出口烟气分配器5水平环形布置,出口烟气分配器5通过循环管路39与循环引风机4出口连通,排出的烟气在铁水罐32外侧冷空气和铁水罐铁水沟除尘罩1之间形成一层热烟幕,减少了冷空气进入铁水罐铁水沟除尘罩1,提高了循环热烟气温度。The outlet flue gas distributor 5 is an annular pipe arranged around the outer edge of the upper mouth of the molten iron tank, the bottom of the annular pipe is densely covered with air outlet holes 33, and the air outlet holes 33 face the inside of the molten iron tank; the annular pipe is connected with the
所述烟气管路一6连接燃烧炉或燃烧器3。The flue gas pipeline one 6 is connected to the combustion furnace or the
所述循环引风机4通过阀门一35连接烟筒7;循环引风机4通过阀门二36连接循环管路39。The circulating induced
所述高炉喷煤管线与煤粉加热管12之间设有煤粉和气体分离装置9,煤粉和气体分离装置9为静态分离仓体18,内部通过挡灰条或挡灰丝束23分隔为左右两部分空间,右部分空间内通过挡灰过滤层22分为上腔室和下腔室,上腔室通过挡灰条或挡灰丝束23与左部分空间连通,下腔室的侧壁穿入与高炉喷煤管线连接的进煤管17,下腔室的底部设有与煤粉加热管12连接的煤粉出口24;左部分空间顶部设有气体放散装置19。A pulverized coal and
所述煤粉集粉喷吹器11包括通过连通管路43相互连通的集粉段27和喷吹段28两部分;集粉段为圆柱形,圆柱面周围均匀设置多个连接管路42,内侧为空腔,用于存储煤粉;多根与煤粉加热管12连通的连接管路42均匀分布在集粉段圆柱面周围;喷吹段28设有一个或多个出煤口29与喷煤枪13连通,喷吹段28上部设有进气孔30,喷吹段28与煤粉和气体分离装置9的排压管路10连通,同时与喷吹加压管路16连通,喷吹段28下部设有流化装置31,用于煤粉喷吹时流化煤粉。流化装置为本领域公知公用的市售设备。The pulverized coal collecting and
所述煤粉出口24的底部设有上封板,上封板上设置多个上板孔,多根煤粉加热管12分别与各自的上板孔连接。The bottom of the pulverized
所述挡灰过滤层22由网格带25和石子26构成,网格带25为两层钢丝或其它材质构成的网格框架,内部装有石子26,所起的作用是带有灰尘气体通过石子26缝隙时,粉尘接触石子26表面后,被阻拦,失去上升动力下落。The ash blocking
所述挡灰条或挡灰丝束23由丝状物构成,倒垂在静态分离仓体18内,所起的作用是带有灰尘气体可以从挡灰条或挡灰丝束的缝隙通过,煤粉接触挡灰条或挡灰丝束表面后,被阻拦,失去动力下落。The ash-blocking strips or ash-blocking
所述左部分空间通过排压管路10与旋风除尘器21连接;所述挡灰过滤层22的上方匹配声波清灰装置20。The left part of the space is connected with the
所述煤粉出口24内设密封罐38,所述下腔室底部为漏斗结构,漏斗中心通过下料管进入煤粉出口24内的密封罐38,对煤粉出口24进行密封,保证煤粉和气体分离装置9的封闭性。The pulverized
所述进煤管17端部设有缓冲罐37,进入下腔室的煤粉通过缓冲罐37降低冲击力。A
本发明涉及的声波清灰装置20、气体放散装置19、旋风除尘器21和燃烧炉或燃烧器3等等,为市售产品。The acoustic
所述煤粉加热管12数量为多根,排列成管束布置,煤粉加热管12为无缝钢管,设有翅片,增加换热面积。The number of the pulverized
所述铁水罐铁水沟除尘罩1为普通除尘罩,铁水罐铁水沟除尘罩1设置在铁水罐32和铁水沟上方;所述除尘器2为常规除尘器,如旋风除尘器、多管除尘器、布袋除尘器、电除尘器和滤筒除尘器等。The hot metal ditch
所述燃烧炉或燃烧器3为普通的燃烧炉和燃烧器,燃烧气体为可燃气体,燃烧炉或燃烧器热烟气出口与铁水罐铁水沟除尘罩1和煤粉加热器8之间的烟气管路一6相连通。The burner or
所述循环引风机4为普通引风机,循环引风机4吸入口与煤粉加热器8的烟气出口连通,循环引风机4出口与出口烟气分配器5和烟筒7连通。The circulating induced
所述烟气管路一6、烟气管路二34和循环管路39设有保温层,减少热量损失。The first
所述烟筒7为常规设计排风烟筒。The
所述煤粉加热器8的外壳为钢制的中间外壳体15,外面设有保温层,多根煤粉加热管12布置在外壳内,外壳内有热烟气通过,与煤粉加热管12换热,用于加热煤粉。The outer shell of the pulverized
所述中间外壳体15为长条筒状,水平布置,一端与烟气管路一6连通,另一端与烟气管路二34连通;中间外壳体15顶部的侧壁设有上连筒40,与煤粉出口24连接,中间外壳体15底部侧壁设有下连筒41,与煤粉集粉喷吹器11连接;多根煤粉加热管12形成的管束通过上连筒40进入中间外壳体15内加热,然后通过下连筒41与煤粉集粉喷吹器11连接;所述下连筒41的底部设有下封板,下封板上设有多个下板孔,多根煤粉加热管12分别与各自的下板孔连接,多根煤粉加热管12穿过下板孔与煤粉集粉喷吹器11的连接管路42连接。The intermediate
本实施例的具体工艺流程:The specific technological process of the present embodiment:
循环引风机4入口依次通过除尘器2、烟气管路二34、煤粉加热器8和烟气管路一6与铁水罐铁水沟除尘罩1出口连通,循环引风机4的出口通过循环管路39与出口烟气分配器5连接;The inlet of the circulating induced
系统工作时,循环引风机4出口出来的气体通过出口烟气分配器5的出气孔33内从上向下喷向铁水罐32,然后,在循环引风机4抽力的作用下上升,与铁水罐铁水沟的流动铁水换热,热烟气被吸入烟气管路一6,同时,燃烧炉或燃烧器3的高温烟气也被吸入烟气管路一6,两股烟气混合到设定温度,进入煤粉加热器8,热烟气与煤粉加热器8内煤粉加热管12中的煤粉换热,煤粉的加热温度可通过燃烧炉或燃烧器3的高温热烟气量进行调节;换热后的烟气通过烟气管路二34进入除尘器2进行除尘,再进入循环引风机4通过循环管路39返回出口烟气分配器5。热烟气在铁水罐铁水沟除尘罩1和铁水罐32外侧空气之间形成一层热烟幕,这样就减少了冷空气进入铁水罐铁水沟除尘罩1,烟气在铁水罐铁水沟除尘罩1内与铁水及高温辐射热能进行热交换,进一步加热烟气温度,热烟气再次被吸入烟气管路一6,循环往复。When the system is working, the gas from the outlet of the circulating induced
从高炉喷煤管线过来的煤粉进入煤粉和气体分离装置9,进行煤粉和气体分离;分离出来的气体通过旋风除尘器21除尘后进入排压管路10,然后进入煤粉集粉喷吹器11;分离出来的煤粉进入煤粉加热管12,在煤粉加热器8内与煤粉加热管12外面的热烟气进行热交换,加热后的煤粉进入煤粉集粉喷吹器11的集粉段27,通过连通管路43进入煤粉集粉喷吹器11的喷吹段28,在喷吹段28内进行流化,煤粉在喷吹加压管路16来的喷吹气体与排压管路10来的煤粉和气体分离装置9产生的气体压力共同作用下,通过喷煤枪13喷入高炉14。The pulverized coal from the blast furnace coal injection pipeline enters the pulverized coal and
本发明中的燃烧炉或燃烧器3可以一直使用,调整煤粉加热温度,也可以在高炉正常生产,煤粉加热温度稳定后停止使用。The combustion furnace or
本发明可以通过阀门一35和阀门二36的开闭,调整控制大部分或全部热烟气经过循环管路39返回出口烟气分配器5,少部分从烟筒7排出。The present invention can adjust and control most or all of the hot flue gas to return to the outlet flue gas distributor 5 through the
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110066136.2A CN112725556B (en) | 2021-01-19 | 2021-01-19 | Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110066136.2A CN112725556B (en) | 2021-01-19 | 2021-01-19 | Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas |
Publications (2)
Publication Number | Publication Date |
---|---|
CN112725556A CN112725556A (en) | 2021-04-30 |
CN112725556B true CN112725556B (en) | 2022-06-28 |
Family
ID=75592377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110066136.2A Expired - Fee Related CN112725556B (en) | 2021-01-19 | 2021-01-19 | Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112725556B (en) |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6347311A (en) * | 1986-08-18 | 1988-02-29 | Nippon Kokan Kk <Nkk> | Smelting, reducing and refining equipment |
CN100535127C (en) * | 2008-03-07 | 2009-09-02 | 山西潞安矿业(集团)有限责任公司 | Pre-heating technique of blast furnace before blowing coal powder |
CN201599815U (en) * | 2010-02-25 | 2010-10-06 | 杨永义 | Flue gas circulation heat exchange device of coal injection system |
CN102605119B (en) * | 2012-04-13 | 2016-08-03 | 孙慕文 | Coal dust conveying during a kind of pulverized coal injection in blast furnace and pre-heating technique device |
JP6012360B2 (en) * | 2012-09-20 | 2016-10-25 | 三菱重工業株式会社 | Pulverized coal blowing device, blast furnace equipment equipped with the same, and pulverized coal supply method |
CN103122398B (en) * | 2013-03-13 | 2015-01-28 | 中冶赛迪工程技术股份有限公司 | Smoke self-circulation preheating coal dust injection technology and device |
CN110129497B (en) * | 2019-05-13 | 2024-04-16 | 鞍钢集团工程技术有限公司 | Series preheating process and system for pulverized coal injection of blast furnace and air/gas of hot blast stove |
CN110607407A (en) * | 2019-09-19 | 2019-12-24 | 湖南建鑫冶金科技有限公司 | Energy-saving and yield-increasing method for preheating agglomerated materials by hot flue gas of blast furnace main channel |
-
2021
- 2021-01-19 CN CN202110066136.2A patent/CN112725556B/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN112725556A (en) | 2021-04-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN211952779U (en) | Energy-saving and environment-friendly treatment system for mixed combustion and incineration of industrial three wastes | |
CN106111889A (en) | A kind of new type high temperature reclaimed sand cooling system and exhaust heat recovering method | |
CN110669891A (en) | Gas recycling device and method for smelting reduction furnace | |
CN205717165U (en) | A kind of high-efficiency energy-saving biomass boiler | |
CN202284894U (en) | Energy-saving environment-friendly cupola furnace | |
CN104197322A (en) | Tobacco stem fluidized bed boiler | |
CN112725556B (en) | Method and device for heating pulverized coal by using blast furnace molten iron dedusting circulating hot flue gas | |
CN107796226A (en) | A kind of sintering deposit grate furnace cooling and residual heat using device and residual-heat utilization method | |
CN108680040A (en) | The efficient Distribution utilization system of sintering mine sensible heat and distribution method | |
CN211035975U (en) | Gas recycling system of smelting reduction furnace | |
CN112284147A (en) | High-temperature preheating type oxygen-enriched combustion energy-saving emission-reducing system of sand regenerating furnace for casting | |
CN203664589U (en) | Novel used sand roasting regenerative furnace | |
CN104197733B (en) | Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device and technique | |
CN112063793A (en) | Primary pure dry dedusting system of converter integrating full waste heat recovery and stable fine purification | |
CN204064005U (en) | Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device | |
CN108168292B (en) | A multifunctional and environmentally friendly BSK sintering technology shaft kiln and its use method | |
CN213543246U (en) | Cement kiln head waste heat boiler and cement line grate cooler integrated device | |
CN204494381U (en) | The air-distribution device of selective deslagging | |
CN209541168U (en) | Coal dust organic heat carrier furnace in bulk | |
CN107101219A (en) | A kind of circulation air path device of biomass boiler | |
CN211057146U (en) | Environment-friendly smoke-removing iron-smelting blast furnace | |
CN214038511U (en) | Heat-exchanging dust-removing device for combustion furnace | |
CN106399616A (en) | Radiation pipe direct reduction vertical furnace | |
CN201935384U (en) | Energy-saving and environment-friendly hot blast stove | |
CN206266647U (en) | Radiant tube is reduced directly shaft furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220628 |