WO2008037132A1 - A process for iron smelting in blast furnace using purified oxygen and coal gas and its device - Google Patents
A process for iron smelting in blast furnace using purified oxygen and coal gas and its device Download PDFInfo
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- WO2008037132A1 WO2008037132A1 PCT/CN2006/003280 CN2006003280W WO2008037132A1 WO 2008037132 A1 WO2008037132 A1 WO 2008037132A1 CN 2006003280 W CN2006003280 W CN 2006003280W WO 2008037132 A1 WO2008037132 A1 WO 2008037132A1
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- gas
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- pure oxygen
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Classifications
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/06—Making pig-iron in the blast furnace using top gas in the blast furnace process
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
-
- 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
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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
- F27D17/20—Arrangements for treatment or cleaning of waste gases
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- 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
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- 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
- C21B2100/62—Energy conversion other than by heat exchange, e.g. by use of exhaust gas in energy production
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C2100/00—Exhaust gas
- C21C2100/06—Energy from waste gas used in other processes
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/16—Sintering; Agglomerating
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/12—Dry methods smelting of sulfides or formation of mattes by gases
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- 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
Definitions
- the invention relates to a blast furnace ironmaking process in the iron and steel metallurgy industry, which mainly uses pure oxygen instead of blast furnace blast, and uses high-hydrogen gas to preheat the blast furnace into the blast furnace to replace most of the coke ironmaking process.
- the object of the present invention is to provide a new technological transformation process and equipment for the traditional blast furnace ironmaking process, namely "pure oxygen gas blast furnace ironmaking process and equipment”.
- the ore material consisting of pellets, alkaline sinter, coke, and flux is sent from the top of the furnace to the blast furnace, wherein each ton of molten iron is equipped with coke 170-200kg;
- the pure oxygen is blown into the blast furnace, and the amount of pure oxygen is 120-200 Nm 3 per ton of molten iron.
- the gas is pressurized into the blast furnace by the gas pressurized by the small-ball gas hot blast stove to reduce the metal ore.
- the temperature of the preheated gas is 900-1150 ° C, and the gas pressure is 0.1-0.6 MPa;
- the gas produced by the reduction is purified and cooled by the dust removal system, sent to the residual pressure generating device through the pipeline, reused, and then recycled to the gas tank or directly recycled.
- Pure oxygen gas blast furnace ironmaking equipment including loading system, blast furnace gravity dust collector, ceramic tube dust collector, bag dust removal device, carbon dioxide pressure swing adsorption device, residual pressure power generation device, which is characterized by opening around the blast furnace belly There are a plurality of gas injection ports and a plurality of oxygen injection ports, and a gas preheating small ball type hot blast stove is arranged outside the blast furnace furnace, and the gas ball type thermal ⁇ furnace passes through the pipeline and a plurality of gas injection ports opened around the blast furnace belly
- the gas-explosion-proof device is installed on the pipeline at the outlet end of the gas preheating ball-type hot blast stove, and a plurality of oxygen injection ports opened on the belly of the blast furnace are connected to the oxygen source through the pipeline.
- the gas generated by the reaction process of the present invention is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag dust removal device, and a carbon dioxide pressure swing adsorption device.
- the purified and cooled top gas is passed through the pipeline to the residual pressure power generation unit for reuse and recovered to the gas tank, and can also be recycled.
- the productivity of the blast furnace is greatly improved, the utilization coefficient of the blast furnace can reach 6-8 tons of iron/m 3 ⁇ D, the flux consumption is reduced by 2/3, and the slag amount is reduced by 2/3, per ton.
- the comprehensive consumption of iron can reach 492kgCE/t, and the top gas can recover electricity.
- Figure 1 is a system diagram of the apparatus of the present invention.
- Pellet ore, alkaline sinter, coke, and flux are fed into the blast furnace from the top of the furnace, wherein 180 kg of coke per ton of iron is added ; then pure oxygen is bubbled into the blast furnace, and at the same time, the ball is heated by the hot blast stove.
- the gas is injected into the blast furnace to directly reduce the pellets and iron-containing raw materials.
- the oxygen per ton of molten iron is 130Nm 3 , and the gas is preheated to 1000 ° C - 1100 ° C by a ball-type hot blast stove.
- the gas pressure is 0.2 MPa.
- the gas generated by the reaction process is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag filter and a carbon dioxide pressure swing adsorption device, and the purified and cooled top gas is passed through the pipeline to the residual pressure power generation device for reuse. It can be recycled to the gas tank. Of course, it can also be recycled.
- Pure oxygen gas blast furnace iron making equipment including feeding device 1, blast furnace 2, gravity dust collector 4, ceramic tube dust collector 5, bag filter 6, carbon dioxide pressure swing adsorption device 7, residual pressure power generation device 8, its structural characteristics a plurality of gas injection ports are respectively opened on the upper and lower sides of the blast furnace 1 and a plurality of oxygen injection ports, a gas feed coil 9 and an oxygen feed coil 3 are respectively disposed at a periphery of the abdomen, and a plurality of gas injection ports are respectively connected to the gas feed coil 9 and the plurality of oxygen injection ports are respectively connected.
- the lead pipe is connected to the oxygen feeding coil 3; a gas preheating small ball type hot blast stove 11 is disposed outside the blast furnace 2, and the gas preheating small ball type hot blast stove 11 is fed into the coil 9 through the gas pipe 12 and the gas.
- a gas explosion-proof safety device 10 is installed in conjunction with the gas pipe 12, a gas explosion-proof safety device 10 is installed.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
纯氧煤气高炉炼铁工艺和设备 技术领域: Pure oxygen gas blast furnace ironmaking process and equipment Technical field:
本发明涉及钢铁冶金行业中高炉炼铁工艺, 主要是用纯氧代替高炉 鼓风, 用高含氢煤气经预热鼓入高炉代替大部分焦炭的炼铁工艺 背景技术: The invention relates to a blast furnace ironmaking process in the iron and steel metallurgy industry, which mainly uses pure oxygen instead of blast furnace blast, and uses high-hydrogen gas to preheat the blast furnace into the blast furnace to replace most of the coke ironmaking process.
目前, 世界上 3/4的生铁和炼钢用铁水都是用传统的高炉炼铁工艺 生产的, 近代的传统高炉炼铁工艺, 由于采用富氧、 喷煤、 大型化等项 新技术, 使当代高炉炼铁技术有了长足的发展。 At present, 3/4 of the world's pig iron and steelmaking hot metal are produced by the traditional blast furnace ironmaking process. In modern times, the traditional blast furnace ironmaking process uses new technologies such as oxygen enrichment, coal injection, and large-scale production. Contemporary blast furnace ironmaking technology has made great progress.
因为高纯水煤气生产技术(见专利 200610045968.1 ))和煤气、焦炉 煤气、 天然气重整技术的发展, 工业化生产高质量、 高纯度、 高含氢、 低成本还原气体工艺已经成熟, 所以发展以上述煤气为主要还原剂的纯 氧高炉炼铁工艺已经可以实现。 ' , Because of the development of high-purity water gas production technology (see patent 200610045968.1) and the development of gas, coke oven gas and natural gas reforming technology, industrial production of high-quality, high-purity, high-hydrogen, low-cost reducing gas processes has matured, so the development of the above gas The pure oxygen blast furnace ironmaking process, which is the main reducing agent, has been achievable. ' ,
经检索未发现以煤气为还原剂, 以喷吹纯氧代替预热鼓风的纯氧煤 气高炉的工艺和设备。 The process and equipment for purifying the pure oxygen gas blast furnace with preheated blast by using pure gas as the reducing agent was not found.
发明内容: Summary of the invention:
本发明的目的在于为传统高炉炼铁工艺提供一种全新的技术改造工 艺及设备, ,即 "纯氧煤气高炉炼铁工艺和设备"。 The object of the present invention is to provide a new technological transformation process and equipment for the traditional blast furnace ironmaking process, namely "pure oxygen gas blast furnace ironmaking process and equipment".
采用的技术方案为- 纯氧煤气高炉炼铁工艺包括如下过程: The technical solution adopted is - The pure oxygen gas blast furnace iron making process includes the following processes:
1、 将由球团矿、 碱性烧结矿、 焦炭、 熔剂构成的矿料从炉顶送入高 炉中, 其中每吨铁水配焦炭 170— 200kg; 1. The ore material consisting of pellets, alkaline sinter, coke, and flux is sent from the top of the furnace to the blast furnace, wherein each ton of molten iron is equipped with coke 170-200kg;
. 2、 向高炉中鼓入纯氧, 纯氧的用量为每吨铁水 120— 200Nm3; 同时 向高炉中鼓入经小球式煤气热风炉加压预热的煤气对金属矿进行还原, 加压预热的煤气温度为 900— 1150°C , 煤气压力为 0.1— 0.6MPa; ' 2. The pure oxygen is blown into the blast furnace, and the amount of pure oxygen is 120-200 Nm 3 per ton of molten iron. At the same time, the gas is pressurized into the blast furnace by the gas pressurized by the small-ball gas hot blast stove to reduce the metal ore. The temperature of the preheated gas is 900-1150 ° C, and the gas pressure is 0.1-0.6 MPa;
3、还原产生的煤气经除尘系统进行净化降温, 通过管道送至余压发 电装置, 进行再利用, 后回收至煤气罐或直接循环使用。 3. The gas produced by the reduction is purified and cooled by the dust removal system, sent to the residual pressure generating device through the pipeline, reused, and then recycled to the gas tank or directly recycled.
纯氧煤气高炉炼铁设备, 包括上料系统、 高炉重力除尘器、 陶瓷管 式除尘器、 布袋除尘装置、 二氧化碳变压吸附装置、 余压发电装置, 其 特征是在高炉炉腹的周围开 ¾有多个煤气喷射口和多个氧气喷射口, 在 高炉炉体外设置一煤气预热小球式热风炉, 该煤气球式热 λ炉通过管路 与高炉炉腹周围开设的多个煤气喷射口相联通; 煤气预热球式热风炉出 口端的管路上装设有煤气防爆装置, 高炉炉腹上开设的多个氧气喷射口 通过管路与氧气源相联通。 , Pure oxygen gas blast furnace ironmaking equipment, including loading system, blast furnace gravity dust collector, ceramic tube dust collector, bag dust removal device, carbon dioxide pressure swing adsorption device, residual pressure power generation device, which is characterized by opening around the blast furnace belly There are a plurality of gas injection ports and a plurality of oxygen injection ports, and a gas preheating small ball type hot blast stove is arranged outside the blast furnace furnace, and the gas ball type thermal λ furnace passes through the pipeline and a plurality of gas injection ports opened around the blast furnace belly The gas-explosion-proof device is installed on the pipeline at the outlet end of the gas preheating ball-type hot blast stove, and a plurality of oxygen injection ports opened on the belly of the blast furnace are connected to the oxygen source through the pipeline. ,
本发明的反应过程所产生的煤气经重力除尘器、 陶瓷管式除尘器和 布袋除尘及二氧化碳变压吸附装置进行净化和降温。 经净化和降温的炉 顶气通过管道通至余压发电装置进行再利用后回收至煤气罐, 也可以循 环使用。 本发明采用上述工艺后, 高炉的生产率大幅度提高, 高炉的利用系 数可达 6-8吨铁 / m3 · D, 熔剂消耗量减小 2/3, 渣量减小 2/3, 每吨铁综 合消耗可达到 492kgCE/t, 炉顶煤气可回收发电。 The gas generated by the reaction process of the present invention is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag dust removal device, and a carbon dioxide pressure swing adsorption device. The purified and cooled top gas is passed through the pipeline to the residual pressure power generation unit for reuse and recovered to the gas tank, and can also be recycled. After adopting the above process, the productivity of the blast furnace is greatly improved, the utilization coefficient of the blast furnace can reach 6-8 tons of iron/m 3 · D, the flux consumption is reduced by 2/3, and the slag amount is reduced by 2/3, per ton. The comprehensive consumption of iron can reach 492kgCE/t, and the top gas can recover electricity.
附图说明: . BRIEF DESCRIPTION OF THE DRAWINGS:
图 1是本发明设备的系统图。 BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a system diagram of the apparatus of the present invention.
具体实施方式: detailed description:
实施例一 Embodiment 1
纯氧煤气高炉炼铁工艺: Pure oxygen gas blast furnace iron making process:
将球团矿、 碱性烧结矿、 焦炭、 熔剂从炉顶送入高炉中, 其中每吨 铁配焦炭 180kg;然后向高炉中鼓入纯氧,并同时将由球式热风炉加压预 热的煤气喷射至高炉内直接对球团矿和含铁原料进行还原, 每吨铁水鼓 氧量为 130Nm3, 煤气经球式热风炉加压预热到 1000°C— 1100°C, 煤气 压力为 0.2MPa。 反应过程所产生的煤气经重力除尘器、 陶瓷管式除尘器 和布袋除尘器及二氧化碳变压吸附装置进行净化降温, 经净化和降温的 炉顶气通过管道通至余压发电装置进行再利用后回收至煤气罐, 当然, 也可以循环使用。 Pellet ore, alkaline sinter, coke, and flux are fed into the blast furnace from the top of the furnace, wherein 180 kg of coke per ton of iron is added ; then pure oxygen is bubbled into the blast furnace, and at the same time, the ball is heated by the hot blast stove. The gas is injected into the blast furnace to directly reduce the pellets and iron-containing raw materials. The oxygen per ton of molten iron is 130Nm 3 , and the gas is preheated to 1000 ° C - 1100 ° C by a ball-type hot blast stove. The gas pressure is 0.2 MPa. The gas generated by the reaction process is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag filter and a carbon dioxide pressure swing adsorption device, and the purified and cooled top gas is passed through the pipeline to the residual pressure power generation device for reuse. It can be recycled to the gas tank. Of course, it can also be recycled.
纯氧煤气高炉炼铁设备, 包括上料装置 1、 高炉 2、 重力除尘器 4、 陶瓷管式除尘器 5、 布袋除尘器 6、 二氧化碳变压吸附装置 7、 余压发电 装置 8,其结构特点是在高炉 1的炉腹上下分别开设有多个煤气喷射口和 多个氧气喷射口, 腹部的外围分别设置有煤气送入盘管 9和氧气送入盘 管 3,多个煤气喷入口分别引出支管与煤气送入盘管 9相联通,多个氧气 喷入口分别引出支管与氧气送入盘管 3相联通; 在高炉 2的外部设置有 一煤气预热小球式热风炉 11, 该煤气预热小球式热风炉 11通过煤气管 12与煤气送入盘管 9相联通,煤气管 12上安装有煤气防爆安全装置 10。 Pure oxygen gas blast furnace iron making equipment, including feeding device 1, blast furnace 2, gravity dust collector 4, ceramic tube dust collector 5, bag filter 6, carbon dioxide pressure swing adsorption device 7, residual pressure power generation device 8, its structural characteristics a plurality of gas injection ports are respectively opened on the upper and lower sides of the blast furnace 1 and a plurality of oxygen injection ports, a gas feed coil 9 and an oxygen feed coil 3 are respectively disposed at a periphery of the abdomen, and a plurality of gas injection ports are respectively connected to the gas feed coil 9 and the plurality of oxygen injection ports are respectively connected. The lead pipe is connected to the oxygen feeding coil 3; a gas preheating small ball type hot blast stove 11 is disposed outside the blast furnace 2, and the gas preheating small ball type hot blast stove 11 is fed into the coil 9 through the gas pipe 12 and the gas. In conjunction with the gas pipe 12, a gas explosion-proof safety device 10 is installed.
实施例二 Embodiment 2
纯氧煤气高炉炼铁工艺: Pure oxygen gas blast furnace iron making process:
将球团矿、 碱性烧结矿、 焦炭、 熔剂从炉顶送入高炉中, 其中每吨 铁配焦炭 190kg;然后向高炉中鼓入纯氧,并同时将由球式热风炉加压预 热的煤气喷射至高炉内直接对球团矿和含铁原料进行还原, 每吨铁水鼓 氧量为 160Nm3, 煤气经球式热风炉加压预热到 1000°C— 1100°C, 煤气 压力为 0.3MPa。 反应过程所产生的煤气经重力除尘器、 陶瓷管式除尘器 和布袋除尘器及二氧化碳变压吸附装置进行净化降温, 经净化和降温的 炉顶气通过管道通至余压发电装置进行再利用后回收至煤气罐, 当然, 也可以循环使用。 Pellet ore, alkaline sinter, coke, and flux are fed into the blast furnace from the top of the furnace, wherein 190 kg of coke per ton of iron is added; then pure oxygen is bubbled into the blast furnace, and at the same time, the ball is heated by the ball-type hot blast stove. The gas is injected into the blast furnace to directly reduce the pellets and iron-containing raw materials. The oxygen content per ton of molten iron is 160Nm 3 , and the gas is preheated to 1000 ° C - 1100 ° C by a ball type hot blast stove, and the gas pressure is 0.3. MPa. The gas generated by the reaction process is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag filter and a carbon dioxide pressure swing adsorption device, and the purified and cooled top gas is passed through the pipeline to the residual pressure power generation device for reuse. It can be recycled to the gas tank. Of course, it can also be recycled.
实施例三 Embodiment 3
纯氧煤气高炉炼铁工艺: Pure oxygen gas blast furnace iron making process:
将球团矿、 碱性烧结矿、 焦炭、 熔剂从炉顶送入高炉中, 其中每吨 铁配焦炭 200kg;然后向高炉中鼓入纯氧,并同时将由球式热风炉加压预 热的煤气喷射至高炉内直接对球团矿和含铁原料进行还原, 每吨铁水鼓 氧量为 190Nm3, 煤气经球式热风炉加压预热到 1000°C— 1100°C, 煤气 压力为 0:5MPa。 反应过程所产生的煤气经重力除尘器、 陶瓷管式除尘器 和布袋除尘器及二氧化碳变压吸附装置进行净化降温, 经净化和降温的 炉顶气通过管道通至余压发电装置进行再利用后回收至煤气罐, 当然, 也可以循环使用。 Pellet ore, alkaline sinter, coke, and flux are sent from the top of the furnace to the blast furnace, wherein 200 kg of coke per ton of iron is added; then pure oxygen is bubbled into the blast furnace, and at the same time, the ball type hot blast stove is pressurized. The hot gas is injected into the blast furnace to directly reduce the pellets and iron-containing raw materials. The oxygen content per ton of molten iron is 190 Nm 3 , and the gas is preheated to 1000 ° C - 1100 ° C by a ball-type hot blast stove. It is 0:5 MPa. The gas generated by the reaction process is purified and cooled by a gravity dust remover, a ceramic tube type dust remover, a bag filter and a carbon dioxide pressure swing adsorption device, and the purified and cooled top gas is passed through the pipeline to the residual pressure power generation device for reuse. It can be recycled to the gas tank. Of course, it can also be recycled.
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/226,940 US20090095134A1 (en) | 2006-09-12 | 2006-12-05 | Process and Equipment for Blast Furnace Ironmaking Using Pure Oxygen and Gas |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2006100477209A CN1916187A (en) | 2006-09-12 | 2006-09-12 | Tecnique and euippment for making iron by using blast furnace through pure oxygen and coal gas |
| CN200610047720.9 | 2006-09-12 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2008037132A1 true WO2008037132A1 (en) | 2008-04-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2006/003280 Ceased WO2008037132A1 (en) | 2006-09-12 | 2006-12-05 | A process for iron smelting in blast furnace using purified oxygen and coal gas and its device |
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|---|---|
| US (1) | US20090095134A1 (en) |
| CN (1) | CN1916187A (en) |
| WO (1) | WO2008037132A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101792833A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for nitrogen replaced with air in blast furnace gas energy recovery system pipe network |
| CN101792834A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for gas replaced with nitrogen in blast furnace gas energy recovery system pipe network |
| CN101792831A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for nitrogen replaced with gas in blast furnace gas energy recovery system pipe network |
| CN103695665A (en) * | 2013-12-18 | 2014-04-02 | 中冶南方工程技术有限公司 | Process for recycling zinc and producing molten iron by using iron-containing zinc dust |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101519703B (en) * | 2008-02-26 | 2010-12-08 | 宝山钢铁股份有限公司 | A Low Coke Ratio Blast Furnace Ironmaking Process |
| CN101280348A (en) * | 2008-04-23 | 2008-10-08 | 沈阳东方钢铁有限公司 | High-temperature coal gas blast furnace iron-smelting process |
| LU91543B1 (en) * | 2009-03-24 | 2010-09-27 | Wurth Paul Sa | Tuyere stock arrangement for a blast furnace and method for operating a blast furnace |
| LU91559B1 (en) * | 2009-04-28 | 2010-10-29 | Wurth Paul Sa | Method for feeding a burden to a blast furnace |
| JP4743332B2 (en) * | 2009-04-30 | 2011-08-10 | Jfeスチール株式会社 | Blast furnace operation method |
| CN113718074A (en) * | 2021-09-03 | 2021-11-30 | 中冶赛迪工程技术股份有限公司 | Low-carbon blast furnace iron-making method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3955963A (en) * | 1973-05-18 | 1976-05-11 | Centre De Recherches Metallurgigues-Centrum Voor Research In De Metallurgie | Method of reducing ore |
| US4316741A (en) * | 1979-04-26 | 1982-02-23 | Krupp-Koppers Gmbh | Blast furnace process employing exchange fuel gas |
| SU1465462A1 (en) * | 1987-07-27 | 1989-03-15 | Институт черной металлургии | Method of conducting melting in blast furnace |
| JPH0261004A (en) * | 1988-08-24 | 1990-03-01 | Sumitomo Metal Ind Ltd | Blast furnace operating method |
| CN1487097A (en) * | 2003-06-23 | 2004-04-07 | 安徽工业大学 | Blast furnace iron-making technique with hydrogen-rich fuel gas, pure oxygen and thus high efficiency and low CO2 exhaust |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2192885A (en) * | 1938-03-10 | 1940-03-12 | Little Inc A | Blast furnace power system |
| BE615646A (en) * | 1961-03-27 | 1900-01-01 | ||
| US4421553A (en) * | 1980-05-06 | 1983-12-20 | Centre De Recherches Metallurgiques | Process for operating a blast furnace |
| US5582029A (en) * | 1995-10-04 | 1996-12-10 | Air Products And Chemicals, Inc. | Use of nitrogen from an air separation plant in carbon dioxide removal from a feed gas to a further process |
| US6631754B1 (en) * | 2000-03-14 | 2003-10-14 | L'air Liquide Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude | Regenerative heat exchanger and method for heating a gas therewith |
| US6406518B1 (en) * | 2000-08-21 | 2002-06-18 | Praxair Technology, Inc. | Gas separation process using ceramic membrane and regenerators |
-
2006
- 2006-09-12 CN CNA2006100477209A patent/CN1916187A/en active Pending
- 2006-12-05 WO PCT/CN2006/003280 patent/WO2008037132A1/en not_active Ceased
- 2006-12-05 US US12/226,940 patent/US20090095134A1/en not_active Abandoned
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3955963A (en) * | 1973-05-18 | 1976-05-11 | Centre De Recherches Metallurgigues-Centrum Voor Research In De Metallurgie | Method of reducing ore |
| US4316741A (en) * | 1979-04-26 | 1982-02-23 | Krupp-Koppers Gmbh | Blast furnace process employing exchange fuel gas |
| SU1465462A1 (en) * | 1987-07-27 | 1989-03-15 | Институт черной металлургии | Method of conducting melting in blast furnace |
| JPH0261004A (en) * | 1988-08-24 | 1990-03-01 | Sumitomo Metal Ind Ltd | Blast furnace operating method |
| CN1487097A (en) * | 2003-06-23 | 2004-04-07 | 安徽工业大学 | Blast furnace iron-making technique with hydrogen-rich fuel gas, pure oxygen and thus high efficiency and low CO2 exhaust |
Non-Patent Citations (2)
| Title |
|---|
| "Cyclopedia of China Metallurgy", March 2001, STEEL & METALLURGY, ISBN: 7-5024-2661-6, pages: 194 - 195 * |
| ZHOU M. AND XU Z.: "ENHANCEMENT OF ECONOMIC BENEFITS OF JIUQUAN STEEL BY USING NATURAL GAS AS A SUBSTITUTE ENERGY", RESEARCH ON IRON & STEEL, no. 4, August 2002 (2002-08-01), pages 55 - 59 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101792833A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for nitrogen replaced with air in blast furnace gas energy recovery system pipe network |
| CN101792834A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for gas replaced with nitrogen in blast furnace gas energy recovery system pipe network |
| CN101792831A (en) * | 2010-03-26 | 2010-08-04 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for nitrogen replaced with gas in blast furnace gas energy recovery system pipe network |
| CN101792833B (en) * | 2010-03-26 | 2011-06-22 | 西安陕鼓动力股份有限公司 | Automatic sweeping method for nitrogen replaced with air in blast furnace gas energy recovery system pipe network |
| CN103695665A (en) * | 2013-12-18 | 2014-04-02 | 中冶南方工程技术有限公司 | Process for recycling zinc and producing molten iron by using iron-containing zinc dust |
| CN103695665B (en) * | 2013-12-18 | 2015-04-01 | 中冶南方工程技术有限公司 | Process for recycling zinc and producing molten iron by using iron-containing zinc dust |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1916187A (en) | 2007-02-21 |
| US20090095134A1 (en) | 2009-04-16 |
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