CN117431352A - A steel smelting system and method based on hydrogen-rich reducing gas injection - Google Patents
A steel smelting system and method based on hydrogen-rich reducing gas injection Download PDFInfo
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- 239000007789 gas Substances 0.000 title claims abstract description 117
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 116
- 239000001257 hydrogen Substances 0.000 title claims abstract description 113
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 110
- 238000002347 injection Methods 0.000 title claims abstract description 27
- 239000007924 injection Substances 0.000 title claims abstract description 27
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 26
- 239000010959 steel Substances 0.000 title claims abstract description 26
- 238000003723 Smelting Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims abstract description 16
- 239000000571 coke Substances 0.000 claims abstract description 36
- 239000003245 coal Substances 0.000 claims abstract description 33
- 239000002028 Biomass Substances 0.000 claims abstract description 25
- 239000002699 waste material Substances 0.000 claims abstract description 24
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000002245 particle Substances 0.000 claims description 44
- 229920003023 plastic Polymers 0.000 claims description 23
- 239000004033 plastic Substances 0.000 claims description 23
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 20
- 229910052799 carbon Inorganic materials 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 229910045601 alloy Inorganic materials 0.000 claims description 16
- 239000000956 alloy Substances 0.000 claims description 16
- 229910000746 Structural steel Inorganic materials 0.000 claims description 15
- 229910001315 Tool steel Inorganic materials 0.000 claims description 15
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 229910052742 iron Inorganic materials 0.000 claims description 10
- 238000005266 casting Methods 0.000 claims description 9
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 7
- 230000005611 electricity Effects 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 238000005868 electrolysis reaction Methods 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 229910000677 High-carbon steel Inorganic materials 0.000 claims description 4
- 238000010891 electric arc Methods 0.000 claims description 4
- 239000003345 natural gas Substances 0.000 claims description 4
- 238000010248 power generation Methods 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 3
- 238000009628 steelmaking Methods 0.000 claims description 3
- 229910001018 Cast iron Inorganic materials 0.000 claims description 2
- 229910001021 Ferroalloy Inorganic materials 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims 3
- 239000002817 coal dust Substances 0.000 claims 2
- 238000005261 decarburization Methods 0.000 claims 2
- UICBCXONCUFSOI-UHFFFAOYSA-N n'-phenylacetohydrazide Chemical compound CC(=O)NNC1=CC=CC=C1 UICBCXONCUFSOI-UHFFFAOYSA-N 0.000 claims 2
- 238000002407 reforming Methods 0.000 claims 2
- 229920002165 CarbonCast Polymers 0.000 claims 1
- 229910000805 Pig iron Inorganic materials 0.000 claims 1
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims 1
- 229910052761 rare earth metal Inorganic materials 0.000 claims 1
- 150000002910 rare earth metals Chemical class 0.000 claims 1
- 239000000843 powder Substances 0.000 abstract description 10
- 238000005262 decarbonization Methods 0.000 abstract description 5
- 239000008188 pellet Substances 0.000 abstract description 4
- 229920000426 Microplastic Polymers 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000002411 adverse Effects 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 3
- 238000009842 primary steelmaking Methods 0.000 description 3
- UFHFLCQGNIYNRP-VVKOMZTBSA-N Dideuterium Chemical compound [2H][2H] UFHFLCQGNIYNRP-VVKOMZTBSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000009417 prefabrication Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
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- 238000004064 recycling Methods 0.000 description 2
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- 239000000126 substance Substances 0.000 description 2
- 238000005275 alloying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004177 carbon cycle Methods 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010310 metallurgical process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
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- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
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- 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
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B7/00—Blast furnaces
-
- 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
- F27D3/08—Screw feeders; Screw dischargers
-
- 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
- C21B2005/005—Selection or treatment of the reducing 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
- C21B2100/20—Increasing the gas reduction potential of recycled exhaust gases
- C21B2100/26—Increasing the gas reduction potential of recycled exhaust gases by adding additional fuel in recirculation pipes
-
- 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
- C21B2100/20—Increasing the gas reduction potential of recycled exhaust gases
- C21B2100/28—Increasing the gas reduction potential of recycled exhaust gases by separation
- C21B2100/282—Increasing the gas reduction potential of recycled exhaust gases by separation of carbon dioxide
-
- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
本发明公开了一种基于富氢还原性气体喷吹的钢铁冶炼系统和方法,包括高炉和富氢还原性气体预制炉;高炉中喷入来自富氢还原性气体预制炉的富氢还原性气体和纯氢;产生的高炉炉顶煤气则被导入富氢还原性气体预制炉进行脱碳;富氢还原性气体预制炉内包括焦丁、生物质颗粒和废塑料颗粒,同时干煤粉和纯氧也被喷吹到富氢还原性气体预制炉内以制备富氢还原性气体。
The invention discloses a steel smelting system and method based on the injection of hydrogen-rich reducing gas, which includes a blast furnace and a hydrogen-rich reducing gas pre-furnace; the blast furnace is injected with hydrogen-rich reducing gas from the hydrogen-rich reducing gas pre-furnace. and pure hydrogen; the generated blast furnace top gas is introduced into a hydrogen-rich reducing gas prefabricated furnace for decarbonization; the hydrogen-rich reducing gas prefabricated furnace includes coke, biomass pellets and waste plastic pellets, while dry coal powder and pure Oxygen is also injected into the hydrogen-rich reducing gas preheating furnace to prepare hydrogen-rich reducing gas.
Description
技术领域Technical field
本发明涉及钢铁冶炼,尤其涉及一种基于富氢还原性气体喷吹的钢铁冶炼系统和方法。The present invention relates to steel smelting, and in particular to a steel smelting system and method based on hydrogen-rich reducing gas injection.
背景技术Background technique
目前高炉冶炼铁水的主要燃料、骨架和还原剂是焦炭。焦炭是炼焦厂在煤在约1000℃的高温条件下经干馏而获得。炼焦过程会产生大量有害化学污染物,且其成本高昂,且为保证高炉的透气性,炼焦过程产生的碎焦和焦丁一般不能直接进入高炉。At present, the main fuel, skeleton and reducing agent for blast furnace smelting molten iron is coke. Coke is obtained by carbonization of coal in coking plants at high temperatures of about 1000°C. The coking process will produce a large amount of harmful chemical pollutants, and the cost is high. In order to ensure the permeability of the blast furnace, the broken coke and coke produced during the coking process generally cannot enter the blast furnace directly.
降低高炉焦比是高炉节能的关键。传统高炉冶炼中主要以向高炉喷吹低煤粉来部分代替焦炭。但大量喷煤会给高炉冶炼带来一系列不利的影响。例如煤粉会在高炉内部进行加热、分解、燃烧、造渣等一系列物理化学变化,使回旋区内反应复杂、操作困难;随着喷煤量的增加,软熔带扩大,焦炭破损严重,导致喷煤受到焦炭质量的制约;未燃煤粉的增加会使高炉软熔带、成渣带工作状态进一步恶化;且富氧大喷煤也会造成高炉“上冷下热”。Reducing blast furnace coke ratio is the key to blast furnace energy saving. In traditional blast furnace smelting, coke is partially replaced by injecting low pulverized coal into the blast furnace. However, large amounts of coal injection will bring a series of adverse effects to blast furnace smelting. For example, pulverized coal will undergo a series of physical and chemical changes such as heating, decomposition, combustion, and slagging inside the blast furnace, making the reaction in the whirling zone complex and difficult to operate. As the amount of coal injection increases, the soft melt zone expands and the coke is seriously damaged. As a result, coal injection is restricted by coke quality; the increase in unburned pulverized coal will further deteriorate the working conditions of the blast furnace's soft melt zone and slag forming zone; and large oxygen-rich coal injection will also cause the blast furnace to become "cold at the top and hot at the bottom."
另外高炉冶炼会产生高炉炉顶煤气。高炉煤气中含有CO和CO2。为回收高炉煤气中的CO,会将高炉煤气重新喷吹回高炉,然后在此之前,需要先脱除高炉煤气中的CO2,这也是一个难题。In addition, blast furnace smelting will produce blast furnace top gas. Blast furnace gas contains CO and CO 2 . In order to recover the CO in the blast furnace gas, the blast furnace gas will be injected back into the blast furnace. Before that, the CO 2 in the blast furnace gas needs to be removed, which is also a problem.
氢气具有绿色可再生、高还原性以及清洁无污染等优点。大量利用氢代替碳作为冶金过程的燃料和还原剂,反应产物是水。与传统的碳冶金相比,可从根本上减少碳排放,实现清洁生产的目标。Hydrogen has the advantages of being green and renewable, highly reducible, and clean and pollution-free. Hydrogen is widely used instead of carbon as fuel and reducing agent in metallurgical processes, and the reaction product is water. Compared with traditional carbon metallurgy, carbon emissions can be fundamentally reduced and the goal of clean production can be achieved.
与煤相比,废塑料气化产物中H2/CO的比值要远大于喷吹煤粉时的比值,更有利于铁氧化物的高温还原,但目前高炉直接喷吹塑料还处于研究阶段。Compared with coal, the H 2 /CO ratio in waste plastic gasification products is much greater than the ratio when pulverized coal is injected, which is more conducive to high-temperature reduction of iron oxides. However, direct injection of plastics in blast furnaces is still in the research stage.
另一种清洁可再生能源—生物质颗粒,本身具有较高热值以及“碳循环、碳中性”的特性。喷入高炉后既能弥补氢气导致的高炉下部热量缺失,又能节省煤炭资源,降低未燃煤粉影响高炉透气性的可能性,还不会产生多余的碳排放。然而,现存的传统风口无法实现气体与生物质颗粒的混喷。Biomass pellets, another clean renewable energy source, have high calorific value and the characteristics of "carbon cycle and carbon neutrality". After being injected into the blast furnace, it can not only make up for the heat loss in the lower part of the blast furnace caused by hydrogen, but also save coal resources, reduce the possibility of unburned pulverized coal affecting the permeability of the blast furnace, and will not produce excess carbon emissions. However, existing traditional tuyere cannot achieve mixed injection of gas and biomass particles.
发明内容Contents of the invention
有鉴于现有技术的上述缺陷,本发明提供了一种基于富氢还原性气体喷吹的钢铁冶炼系统,包括高炉和富氢还原性气体预制炉;高炉中喷入来自富氢还原性气体预制炉的富氢还原性气体和纯氢;产生的高炉炉顶煤气则循环进入富氢还原性气体预制炉进行脱碳;富氢还原性气体预制炉内的料柱包括焦丁、生物质颗粒和废塑料颗粒,同时干煤粉和纯氧也被喷吹到富氢还原性气体预制炉内以制备富氢还原性气体。In view of the above defects of the prior art, the present invention provides a steel smelting system based on the injection of hydrogen-rich reducing gas, including a blast furnace and a hydrogen-rich reducing gas prefabricated furnace; the blast furnace is injected with hydrogen-rich reducing gas from the prefabricated furnace. The hydrogen-rich reducing gas and pure hydrogen of the furnace are recycled; the generated blast furnace top gas is circulated into the hydrogen-rich reducing gas prefabricated furnace for decarbonization; the material column in the hydrogen-rich reducing gas prefabricated furnace includes coke, biomass particles and Waste plastic particles, dry coal powder and pure oxygen are also injected into the hydrogen-rich reducing gas prefabricated furnace to prepare hydrogen-rich reducing gas.
进一步地,高炉包括炼铁高炉、铸造生铁高炉、铁合金高炉。Further, the blast furnace includes an iron-making blast furnace, a cast iron blast furnace, and a ferroalloy blast furnace.
进一步地,干煤粉为富氢煤粉。Further, the dry coal powder is hydrogen-rich coal powder.
进一步地,纯氢为通过高炉、转炉煤气发电及光伏、风力、核能、水力及电网谷电制得的绿电,通过电解水方式制得,或通过焦炉煤气、天然气等富氢气体经重整纯化后制得。Furthermore, pure hydrogen is green electricity produced through blast furnace, converter gas power generation and photovoltaic, wind power, nuclear energy, hydropower and grid off-peak power. It is produced through electrolysis of water, or through heavy hydrogen-rich gases such as coke oven gas and natural gas. Prepared after purification.
进一步地,高炉生产的铁水被供给包括转炉、电弧炉在内的炼钢初炼炉,用以生产碳素结构钢、合金结构钢、低合金高强度结构钢、碳素工具钢、合金工具钢、高速工具钢、高碳铸钢件、高碳铸铁件以及不锈钢,及添加有包括稀土在内的特定合金元素的特殊用途钢材;所述特殊用途钢材包括耐海洋腐蚀钢;以及由上述钢材轧制而成的型材、板材、管材、棒材和线材。Furthermore, the molten iron produced by the blast furnace is supplied to primary steel-making furnaces including converters and electric arc furnaces to produce carbon structural steel, alloy structural steel, low-alloy high-strength structural steel, carbon tool steel, and alloy tool steel. , high-speed tool steel, high-carbon steel castings, high-carbon iron castings and stainless steel, and special-purpose steels added with specific alloying elements including rare earths; the special-purpose steels include marine corrosion-resistant steels; and rolled from the above steels Profiles, plates, tubes, rods and wires made from.
进一步地,在富氢还原性气体预制炉的入料口采用了一种双筒螺旋式布料器,包括外筒;外筒筒内的上部为螺旋式料道,下部为内筒;内筒向下延伸出外筒之下,且其内筒的长度被设置可为使出口其没入富氢还原性气体预制炉中的料柱中,在内筒延伸超出外筒的部分设置有多个均压孔,以使内筒和炉内压力均衡。Further, a double-cylinder spiral distributor is used at the feed inlet of the hydrogen-rich reducing gas prefabricated furnace, including an outer cylinder; the upper part of the outer cylinder is a spiral feed channel, and the lower part is an inner cylinder; the inner cylinder is It extends below the outer cylinder, and the length of the inner cylinder is set so that the outlet is submerged in the material column in the hydrogen-rich reducing gas prefabricated furnace. The portion of the inner cylinder extending beyond the outer cylinder is provided with multiple pressure equalizing holes. , so that the pressure in the inner cylinder and the furnace is balanced.
本发明还提供了一种基于富氢还原性气体喷吹的钢铁冶炼方法,包括步骤:The invention also provides a steel smelting method based on hydrogen-rich reducing gas injection, which includes the steps:
(1)向富氢还原性气体预制炉内加入焦丁、生物质颗粒和废塑料颗粒,同时喷入干煤粉和纯氧,燃烧制备富氢还原性气体;(1) Add coke, biomass particles and waste plastic particles into the hydrogen-rich reducing gas prefabricated furnace, spray dry coal powder and pure oxygen at the same time, and burn to prepare hydrogen-rich reducing gas;
(2)将来自富氢还原性气体预制炉内的富氢还原性气体和纯氢混合后喷入高炉;(2) Mix the hydrogen-rich reducing gas and pure hydrogen from the hydrogen-rich reducing gas prefabricated furnace and then inject it into the blast furnace;
(3)将产生的高炉炉顶煤气导入富氢还原性气体预制炉进行脱碳;(3) Introduce the generated blast furnace top gas into a hydrogen-rich reducing gas prefabricated furnace for decarbonization;
(4)同时向高炉内喷入纯氧;(4) Inject pure oxygen into the blast furnace at the same time;
(5)将高炉生产的铁水供给包括转炉、电弧炉在内的炼钢初炼炉,用以生产碳素结构钢、合金结构钢、低合金高强度结构钢、碳素工具钢、合金工具钢、高速工具钢、高碳铸钢件、高碳铸铁件以及不锈钢。(5) Supply the molten iron produced by the blast furnace to primary steelmaking furnaces including converters and electric arc furnaces to produce carbon structural steel, alloy structural steel, low alloy high-strength structural steel, carbon tool steel, and alloy tool steel , high-speed tool steel, high-carbon steel castings, high-carbon iron castings and stainless steel.
进一步地,干煤粉为富氢煤粉。Further, the dry coal powder is hydrogen-rich coal powder.
进一步地,纯氢为通过高炉、转炉煤气发电及光伏、风力、核能、水力及电网谷电制得的绿电,通过电解水方式制得,或通过焦炉煤气、天然气等富氢气体经重整纯化后制得。Furthermore, pure hydrogen is green electricity produced through blast furnace, converter gas power generation and photovoltaic, wind power, nuclear energy, hydropower and grid off-peak power. It is produced through electrolysis of water, or through heavy hydrogen-rich gases such as coke oven gas and natural gas. Prepared after purification.
进一步地,其中,在富氢还原性气体预制炉入料口采用了一种双筒螺旋式布料器,括外筒;外筒筒内的上部为螺旋式料道,下部为内筒;内筒向下延伸出外筒之下,且其内筒的长度被设置可为使出口其没入富氢还原性气体预制炉中的料柱中,同时在内筒延伸超出外筒的部分设置有多个均压孔,以使内筒和炉内压力均衡;焦丁、生物质颗粒和废塑料颗粒的混合料自上方进入螺旋式料道,在顺着螺旋式料道下落的过程中,由于焦丁的密度大,因此在惯性的作用下,其运动轨迹更靠近外筒,而生物质颗粒和废塑料颗粒密度小,其运动轨迹更靠近内筒;这样经过螺旋式料道后,使大部分焦丁从通过较短的外筒进入炉内,更早地参与炉内反应,使大部分生物质颗粒和废塑料颗粒则通过较长的内筒进入炉内,较晚地参与炉内反应。Further, a double-cylinder spiral distributor is used at the feed inlet of the hydrogen-rich reducing gas prefabricated furnace, including an outer cylinder; the upper part of the outer cylinder is a spiral feed channel, and the lower part is an inner cylinder; the inner cylinder Extends downward below the outer cylinder, and the length of the inner cylinder is set so that the outlet is submerged in the material column in the hydrogen-rich reducing gas prefabricated furnace. At the same time, the portion of the inner cylinder extending beyond the outer cylinder is provided with multiple uniform holes. Press holes to equalize the pressure in the inner cylinder and the furnace; the mixture of coke, biomass particles and waste plastic particles enters the spiral feed channel from above, and in the process of falling along the spiral feed channel, due to the The density is high, so under the action of inertia, its movement trajectory is closer to the outer cylinder, while the density of biomass particles and waste plastic particles is small, and its movement trajectory is closer to the inner cylinder; in this way, after passing through the spiral feed channel, most of the coke particles From entering the furnace through the shorter outer cylinder, they participate in the reactions in the furnace earlier, so that most of the biomass particles and waste plastic particles enter the furnace through the longer inner cylinder, and participate in the reactions in the furnace later.
本发明采用了富氢还原性气体预制炉,可以将煤粉、焦丁、生物质颗粒和废塑料颗粒等不适于直接进入高炉,但有利于减少高炉能耗的资源预制为富氢还原性气体,然后可以和氢气一起喷入高炉。其中,将煤粉预制为富氢还原性气体,可以消除喷煤对高炉炉况的不利影响;将焦丁、生物质颗粒和废塑料颗粒预制为富氢还原性气体,可以使资源得到充分的应用和回收。将高炉煤气引入富氢还原性气体预制炉,则可方便的实现高炉煤气的脱碳。更重要的是,通过富氢还原性气体预制炉对上述各种资源的综合处理统一转换为富氢还原性气体,可以实现在后续和纯氢混合喷吹时,可以根据富氢还原性气体中成分变化,由控制系统动态调整CO和H2的比值,从而实现对高炉还原性气氛和热量的控制,从而可更换的对炉矿进行控制。综上,通过对资源的统一回收转换和利用,本发明降低了高炉能耗,从而减少了钢铁冶炼的碳排放。本发明还提供了一种双筒螺旋式布料器,可使得燃烧较快的生物质颗粒和废塑料颗粒和燃烧较慢的焦丁的消耗速度趋同。这样,可以使得富氢还原性气体预制过程中,炉内料柱的原料分布更为均匀,炉内温度更为均衡。The invention adopts a hydrogen-rich reducing gas prefabrication furnace, which can prefabricate resources such as pulverized coal, coke, biomass particles and waste plastic particles that are not suitable for directly entering the blast furnace but are beneficial to reducing the energy consumption of the blast furnace into hydrogen-rich reducing gas. , which can then be injected into the blast furnace together with hydrogen. Among them, prefabricating pulverized coal into hydrogen-rich reducing gas can eliminate the adverse effects of coal injection on blast furnace conditions; prefabricating coke, biomass particles and waste plastic particles into hydrogen-rich reducing gas can fully utilize resources. Application and recycling. By introducing the blast furnace gas into the hydrogen-rich reducing gas prefabricated furnace, the decarbonization of the blast furnace gas can be easily achieved. More importantly, through the comprehensive processing of the above-mentioned various resources by the hydrogen-rich reducing gas prefabricated furnace, the unified conversion into hydrogen-rich reducing gas can be realized according to the hydrogen-rich reducing gas during the subsequent mixed injection with pure hydrogen. As the composition changes, the control system dynamically adjusts the ratio of CO and H 2 to achieve control of the reducing atmosphere and heat of the blast furnace, thereby enabling replaceable control of the furnace ore. In summary, through the unified recovery, conversion and utilization of resources, the present invention reduces blast furnace energy consumption, thereby reducing carbon emissions from steel smelting. The invention also provides a double-cylinder spiral distributor, which can make the consumption speed of biomass particles and waste plastic particles that burn faster and coke that burns slower converge. In this way, during the preproduction process of hydrogen-rich reducing gas, the distribution of raw materials in the furnace material column can be more uniform, and the temperature in the furnace can be more balanced.
以下将结合附图对本发明的构思、具体结构及产生的技术效果作进一步说明,以充分地了解本发明的目的、特征和效果。The concept, specific structure and technical effects of the present invention will be further described below in conjunction with the accompanying drawings to fully understand the purpose, features and effects of the present invention.
附图说明Description of the drawings
图1是本发明的一个较佳实施例中的基于富氢还原性气体喷吹的钢铁冶炼系统的示意图;Figure 1 is a schematic diagram of a steel smelting system based on hydrogen-rich reducing gas injection in a preferred embodiment of the present invention;
图2是本发明的一个较佳实施例中的富氢还原性气体预制炉的示意图;Figure 2 is a schematic diagram of a hydrogen-rich reducing gas prefabricated furnace in a preferred embodiment of the present invention;
图3是本发明的一个较佳实施例中的双筒螺旋式布料器的示意图;Figure 3 is a schematic diagram of a double-tube spiral distributor in a preferred embodiment of the present invention;
图4是使用了图3中的双筒螺旋式布料器的富氢还原性气体预制炉的示意图。FIG. 4 is a schematic diagram of a hydrogen-rich reducing gas prefabricated furnace using the double-cylinder spiral distributor in FIG. 3 .
具体实施方式Detailed ways
以下参考说明书附图介绍本发明的多个优选实施例,使其技术内容更加清楚和便于理解。本发明可以通过许多不同形式的实施例来得以体现,本发明的保护范围并非仅限于文中提到的实施例。The following describes multiple preferred embodiments of the present invention with reference to the accompanying drawings to make the technical content clearer and easier to understand. The present invention can be embodied in many different forms of embodiments, and the protection scope of the present invention is not limited to the embodiments mentioned herein.
本发明的一个较佳实施例中的基于富氢还原性气体喷吹的钢铁冶炼系统如图1所示,包括高炉2和富氢还原性气体预制炉1。向高炉2中喷吹来自富氢还原性气体预制炉1的富氢还原性气体、通过绿电电解获得的氢气和纯氧,进行铁水冶炼。然后高炉2生产的铁水进入炼钢工序,供给转炉、电弧炉等炼钢初炼炉,用以生产碳素结构钢、合金结构钢、低合金高强度结构钢、碳素工具钢、合金工具钢、高速工具钢、高碳铸钢件、高碳铸铁件以及不锈钢。A steel smelting system based on hydrogen-rich reducing gas injection in a preferred embodiment of the present invention is shown in Figure 1 and includes a blast furnace 2 and a hydrogen-rich reducing gas prefabricated furnace 1. The hydrogen-rich reducing gas from the hydrogen-rich reducing gas prefabricated furnace 1, hydrogen gas obtained by green electrolysis, and pure oxygen are injected into the blast furnace 2 to perform molten iron smelting. Then the molten iron produced in blast furnace 2 enters the steelmaking process and is supplied to primary steelmaking furnaces such as converters and electric arc furnaces to produce carbon structural steel, alloy structural steel, low alloy high strength structural steel, carbon tool steel, and alloy tool steel. , high-speed tool steel, high-carbon steel castings, high-carbon iron castings and stainless steel.
为预制富氢还原性气体,从富氢还原性气体预制炉1的顶部中加入焦丁、生物质颗粒和废塑料颗粒,从富氢还原性气体预制炉1的炉身处喷入干煤粉和工业纯氧,同时将高炉2的高炉煤气也引入富氢还原性气体预制炉2中。干煤粉优选为富氢煤粉。To pre-produce the hydrogen-rich reducing gas, add coke, biomass particles and waste plastic particles from the top of the hydrogen-rich reducing gas pre-furnace 1, and spray dry coal powder from the furnace body of the hydrogen-rich reducing gas pre-furnace 1 and industrial pure oxygen, and at the same time, the blast furnace gas of the blast furnace 2 is also introduced into the hydrogen-rich reducing gas prefabricated furnace 2. The dry coal powder is preferably hydrogen-rich coal powder.
本发明的一个较佳实施例中的富氢还原性气体预制炉1如图2所示,炉身下部为灰渣13,中部为焦丁11和生物质颗粒、废塑料颗粒12,和同时喷入煤粉和工业纯氧发生燃烧,生成CO和H2等富氢还原性气体,从富氢还原性气体预制炉1炉身上部排出并喷吹入高炉2。The hydrogen-rich reducing gas prefabricated furnace 1 in a preferred embodiment of the present invention is shown in Figure 2. The lower part of the furnace body is made of ash 13, and the middle part is made of coke 11 and biomass particles and waste plastic particles 12. Powdered coal and industrial pure oxygen are fed into the combustion chamber to generate hydrogen-rich reducing gases such as CO and H 2 , which are discharged from the upper part of the furnace body of the hydrogen-rich reducing gas prefabricated furnace 1 and injected into the blast furnace 2.
引入富氢还原性气体预制炉1的高炉煤气中的CO2和炉中的焦丁发生反应,还原为CO。The CO 2 in the blast furnace gas introduced into the hydrogen-rich reducing gas prefabricated furnace 1 reacts with the coke in the furnace and is reduced to CO.
本发明采用了富氢还原性气体预制炉,可以将煤粉、焦丁、生物质颗粒和废塑料颗粒等不适于直接进入高炉,但有利于减少高炉能耗的资源预制为富氢还原性气体,然后可以和氢气一起喷入高炉。其中,将煤粉预制为富氢还原性气体,可以消除喷煤对高炉炉况的不利影响;将焦丁、生物质颗粒和废塑料颗粒预制为富氢还原性气体,可以使资源得到充分的应用和回收。将高炉煤气引入富氢还原性气体预制炉,则可方便的实现高炉煤气的脱碳。更重要的是,通过富氢还原性气体预制炉对上述各种资源的综合处理统一转换为富氢还原性气体,可以实现在后续和纯氢混合喷吹时,可以根据富氢还原性气体中成分变化,由控制系统动态调整CO和H2的比值,从而实现对高炉还原性气氛和热量的控制,从而可更换的对炉矿进行控制。The invention adopts a hydrogen-rich reducing gas prefabrication furnace, which can prefabricate resources such as pulverized coal, coke, biomass particles and waste plastic particles that are not suitable for directly entering the blast furnace but are beneficial to reducing the energy consumption of the blast furnace into hydrogen-rich reducing gas. , which can then be injected into the blast furnace together with hydrogen. Among them, prefabricating pulverized coal into hydrogen-rich reducing gas can eliminate the adverse effects of coal injection on blast furnace conditions; prefabricating coke, biomass particles and waste plastic particles into hydrogen-rich reducing gas can fully utilize resources. Application and recycling. By introducing the blast furnace gas into the hydrogen-rich reducing gas prefabricated furnace, the decarbonization of the blast furnace gas can be easily achieved. More importantly, through the comprehensive processing of the above-mentioned various resources by the hydrogen-rich reducing gas prefabricated furnace, the unified conversion into hydrogen-rich reducing gas can be realized according to the hydrogen-rich reducing gas during the subsequent mixed injection with pure hydrogen. As the composition changes, the control system dynamically adjusts the ratio of CO and H 2 to achieve control of the reducing atmosphere and heat of the blast furnace, thereby enabling replaceable control of the furnace ore.
生物质颗粒和废塑料颗粒相对于焦丁而言,密度小、燃烧快,如果三者均匀布料的话,容易造成富氢还原性气体预制炉中的料柱中焦丁集聚而使得炉内温度不均,造成炉况波动,甚至发生安全事故。在根据本发明的如图3和4所示的进一步的实施例中,在富氢还原性气体预制炉1的入料口采用了一种双筒螺旋式布料器,包括外筒2。外筒2筒内的上部为螺旋式料道3,下部为内筒4。内筒4向下延伸出外筒2之下,长度使其出口没入富氢还原性气体预制炉中的料柱中。在内筒4延伸超出外筒2的部分设置有多个均压孔5,以使内筒4和炉内压力均衡,以免下料不畅。内筒4内的焦丁、生物质颗粒和废塑料颗粒的混合料自上方进入螺旋式料道3,在顺着螺旋式料道下落的过程中,由于焦丁的密度大,因此在惯性的作用下,其运动轨迹更靠近外筒,而生物质颗粒和废塑料颗粒密度小,其运动轨迹更靠近内筒。这样经过螺旋式料道后,大部分焦丁会从通过较短的外筒进入炉内,更早地参与炉内反应,而大部分生物质颗粒和废塑料颗粒则会通过较长的内筒进入炉内,且内筒的出口没入在料柱中,顺着料柱的消耗,自然下降进入料柱,故会较晚地参与炉内反应。由此实现虽然是同时进入炉内,但由于参与反应的起始时间不同,故而可使得燃烧较快的生物质颗粒和废塑料颗粒和燃烧较慢的焦丁的消耗速度趋同。这样,可以使得富氢还原性气体预制过程中,炉内料柱的原料分布更为均匀,炉内温度更为均衡。Compared with coke pellets, biomass pellets and waste plastic pellets have low density and burn quickly. If the three are evenly distributed, it will easily cause coke dices to accumulate in the material column in the hydrogen-rich reducing gas prefabricated furnace, causing the temperature inside the furnace to become unstable. All, causing fluctuations in furnace conditions and even safety accidents. In a further embodiment according to the present invention as shown in Figures 3 and 4, a double-cylinder spiral distributor is used at the feed inlet of the hydrogen-rich reducing gas prefabricated furnace 1, including an outer cylinder 2. The upper part of the outer cylinder 2 is a spiral material channel 3, and the lower part is an inner cylinder 4. The inner cylinder 4 extends downwardly below the outer cylinder 2 to such a length that its outlet is submerged into the material column in the hydrogen-rich reducing gas prefabricated furnace. A plurality of pressure equalizing holes 5 are provided in the part of the inner cylinder 4 that extends beyond the outer cylinder 2 to equalize the pressure between the inner cylinder 4 and the furnace to avoid unsmooth unloading. The mixture of coke, biomass particles and waste plastic particles in the inner cylinder 4 enters the spiral channel 3 from above. During the process of falling along the spiral channel, due to the high density of the coke, it falls under the inertial force. Under the action, its movement trajectory is closer to the outer cylinder, while biomass particles and waste plastic particles have low density, and their movement trajectory is closer to the inner cylinder. After passing through the spiral feed channel, most of the coke will enter the furnace through the shorter outer cylinder and participate in the reaction in the furnace earlier, while most of the biomass particles and waste plastic particles will pass through the longer inner cylinder. It enters the furnace, and the outlet of the inner cylinder is submerged in the material column. It will naturally descend into the material column along with the consumption of the material column, so it will participate in the reaction in the furnace later. In this way, although they enter the furnace at the same time, due to the different starting times of the reactions, the consumption speed of the biomass particles and waste plastic particles that burn faster and the coke that burns slower can be converged. In this way, during the preproduction process of hydrogen-rich reducing gas, the distribution of raw materials in the furnace material column can be more uniform, and the temperature in the furnace can be more balanced.
以上详细描述了本发明的较佳具体实施例。应当理解,本领域的普通技术人员无需创造性劳动就可以根据本发明的构思作出诸多修改和变化。因此,凡本技术领域中技术人员依本发明的构思在现有技术的基础上通过逻辑分析、推理或者有限的实验可以得到的技术方案,皆应在由权利要求书所确定的保护范围内。The preferred embodiments of the present invention are described in detail above. It should be understood that those skilled in the art can make many modifications and changes based on the concept of the present invention without creative efforts. Therefore, any technical solutions that can be obtained by those skilled in the art through logical analysis, reasoning or limited experiments based on the concept of the present invention and on the basis of the prior art should be within the scope of protection determined by the claims.
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《煤制油技术基础与应用研究》: "《煤制油技术基础与应用研究》", 31 January 2013, 上海科学技术出版社, pages: 139 - 144 * |
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WO2025036019A1 (en) * | 2023-08-15 | 2025-02-20 | 昌黎县兴国精密机件有限公司 | Steel smelting system and method based on hydrogen-rich reducing gas injection |
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