• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1. The method of operation of a blast furnace, including loading the charge through the throat, introducing carbon-containing components into the mixture, such as coal, preheating the mixture in the mine and melting in the shoulders, burning carbon materials in the tuyere zone with heated oxygen-enriched blast, blowing out liquid products from the bottom part of the hearth, the removal of gases through the top, characterized in that, in order to increase the efficiency of the blast furnace in obtaining high-quality reducing gas and reduce the cost of production; a, a gas containing C02 is introduced into the upper part of the shoulders and, at a higher temperature, while maintaining the gas temperature in the lower part of the shaft at a level, and a part of the reducing gas containing CO, H and Nj and practically free from COj, and S from the bottom of the mine on two different horizons. 2. A system for producing liquid iron and reducing gas, consisting of two blast furnaces, each of which contains a series of blast tuyeres in the upper part of the hearth, connected by trgr pipelines for transferring reducing gas from one furnace to another, characterized in that in order to improve the system’s performance in terms of the quality and quantity of smelting products produced and their cheaper production, each furnace additionally contains one 00 row of tuyeres located in the upper part of the shoulders and two rows of tuyeres located At the bottom of the shaft, up to oe, two rows of tuyeres located in the bottom of the shaft of one of the furnaces are connected to at least one row of tuyeres in the same zone of the other furnace.
    公开号:SU1138036A3
    申请号:SU823390151
    申请日:1982-02-11
    公开日:1985-01-30
    发明作者:Брюс Клэфлин Гарри
    申请人:Гарри Брюс Клэфлин (США)；
    IPC主号:
    专利说明:

    1 t
    The invention relates to ferrous metallurgy, in particular to smelting iron and producing fuel and reducing gas in blast furnaces.
    A known method for producing pig iron and reducing gas in blast furnaces, according to which metallized raw material, the charge, is charged to the furnace, and hot reducing gases obtained outside the blast furnace are introduced through tuyeres. At the same time, high-calorific gas, which is used in blast furnace smelting at another C1 J furnace, is removed through the throat.
    The closest to the proposed technical essence is the method of operation of the blast furnace, which includes loading the charge through the throat, introducing carbon-containing components, such as coal, preheating the charge in the mine and melting in the shoulders, burning coal-rich materials in the tuyere zone with heated material. -Use, the release of liquid smelting products from the lower part of the hearth, the removal of gases through the throat C2.
    The closest to the proposed technical: essence is a system for the production of liquid iron and reducing gas, consisting of two domain-ovens, each of which contains a row of blast tuyeres in the upper part of the forge connected by {{cub) | for transferring reducing gas from one furnace to another. In this case, the pipeline transports the blast furnace blast furnace gas working on metallized raw materials using reducing gas blown through the tuyere into another furnace operating on oxidized iron ore raw material tl.
    The disadvantages of this method are the low calorie content and concentration of reducing gases, the inability to regulate their composition over a wide range, which makes it difficult to use them both in blast furnace production and in other areas of production. In addition, an excellent method does not allow to control the composition of the gas in a wide range, and the preparation of reducing gases outside the blast furnace is a costly and technically difficult to implement.
    38036
    A disadvantage of the known device is its limited use, since a prerequisite for the functioning of the system 5 is the smelting in a furnace, the top gas of which is used as a reducing, metallized. bathing of raw materials, and blowing through tuyeres of natural gas or other carbon metals, since only
    If these conditions are met, the flue gas will have sufficient reduction potential. In addition, the disadvantage of the system is
    the lack of control over the amount, composition and temperature of gases in the mine, which leads to the expenditure of expensive and scarce coke on the reaction of direct reduction in a furnace operating on oxidized iron ore
    raw material All this reduces the efficiency of blast smelting and increases the cost of production of pig iron and reducing gas.
    The goal of the method is to demonstrate the efficiency of the blast furnace, while producing high-quality reducing gas and reduce the cost of production.
    The aim of the system i is to increase the efficiency of the system in terms of the quality and quantity of smelting products produced and the cheapening of their production. The goal is achieved
    the fact that according to the method of operation of the blast furnace, which includes the charge loading through the furnace, the introduction of carbon-containing components into the mixture, for example coal, preheating
    charge in the mine and melting in the shoulders, incineration. carbon {1x materials in the tuyere zone with heated blast enriched with oxygen, release of liquid smelting products from the lower part of the hearth, gas removal through the throat, gas containing COj and H20 is introduced into the upper part of the shoulders at a temperature above, while maintaining the gas temperature
    the bottom of the Mine is level, and the part of the reducing gas containing CO, N2 and practically free of CO 2, and removed 5, and 5, is removed from the lower part of the shaft in two
    different horizons.
    This goal is achieved by the fact that in a system for the production of molten iron and reducing gas, consisting of two drmen furnaces, a series of which contains a series of blast tuyeres in the upper part of the furnace, connected by pipelines to transfer the reducing gas from one furnace to another , each furnace additionally contains one row of tuyeres located in the upper part of the shoulders, and two rows of tuyeres located in the lower part of the shaft, and two rows located in the lower part of the shaft of one of the furnaces are connected at least with One row of tuyeres in the same zone of another furnace. The method is carried out as follows. Entering the gas containing COI into the upper part of the shoulders that endothermically reacts with carbon at a temperature above 1000 ° C to form CO and Hj, allows, without the use of fuel oil or direct gas or metallized raw material, to obtain a reducing gas with improved calorific value and controlled content of reducing agents in it and increase its output to the required size. At the same time, the temperature of the gases in the lower part of the bed is maintained at a level of 1000 ° C, the amount and composition of the gas in the bed, which reduces the loss of carbon to the direct reduction of oxides. On one of the horizons in the lower part of the mine, part of the gas was extracted from the blast furnace. The gas contains CO, Hj and N and is practically free from CO, and 5 with a high calorific value (1800-2500 kcal / m) The excess energy that is produced in the gases can be used for blast-furnace smelting, pyrolysis (splitting under the action of heat), cracking and it can economically replace the amount of coke oven energy that is the source of environmental pollution.On the other horizon of the lower zone of the mine part of the gaea is removed for sampling to control the composition and temperature.In addition, use this information also controlled process in the shoulders and furnace kiln. EXAMPLE In the operation mode of a blast furnace, a mixture of cheap carbon-containing materials (low-grade coal, magnesium, industrial waste, such as paper, plastic, rubber, etc.) is charged to produce gases. e.) Coke is not used. Gaseous materials for endothermic reactions containing COg and, for example, blast furnace gases, gases produced during the smelting of steel in oxygen converters, or gases from direct reduction units are introduced into the upper part of the shoulders and, if necessary, mc, through the main tuyeres. At temperatures above 1000 ° C, these gases react with carbon to form the CO and H components required for the reducing gas. In addition, they are used to control the temperature and chemical composition of the multipurpose gas. Gases are removed from the bottom of the mine at a temperature of approximately 10 ° C and sent to the consumer. Their composition and temperature are continuously monitored by samples of gas removed through the second horizon at the bottom of the charge. Pyrolysis activity in the mine above the horizons to remove gas forms a gas containing CH and other hydrocarbons, CO, CP2, Hj, H, 0, and sulfur compounds. This gas is removed through the spike plate. Liquid pig iron and spackes formed from charge materials are removed from the bottom of the furnace. The reducing gas that is removed from the lower part of the furnace is transferred through pipelines to consumers using as a reduction. solid gas, fuel for boilers, etc. The flue gas is used directly or after mixing with the multipurpose gas. The present invention allows coke consumption to be reduced to zero, producing cheap top gas with increased calorific value and multipurpose gas suitable for use in reduction units, including blast furnaces, without the use of fuel oil and natural gas. In this case, controlled operation of the blast furnace and gas composition are ensured. This device allows to obtain the required amount of reducing gas, a given composition for use in the blast furnace smelting of another furnace, as well as for the needs of other consumers. At the same time, the quantity, temperature and composition of gases in the shaft of each furnace are monitored, and the normal functioning of the system does not depend on the quality of the charge materials, cheap fuel is allowed, coke is saved by limiting the processes of direct aoccTaitpLeni. FIG. 1 shows a general circuit; FIG. -2 - diagram of blast furnaces, consumers' energy sources. The system consists of two blast furnaces, one of which (1) produces the main product - metal, and the other furnace (2) - gas. Both furnaces are equipped with four rows of tuyeres located around the periphery of the furnace, the First row of tuyeres 3 and 4 are located in the upper part of the hearth, the second row of trucks 5 and 6 are in the upper part of the shoulders. The third row of tuyeres 7 and 8 are in them. parts of the mine under the support ring and the fourth row of tuyeres 9 and 10 are also in the lower part of the mine, above the third row of tuyeres. Tuyeres of each row are united by ring manifolds 11, 12, 13 and 16 at blast furnace 1 and collectors 1А, 1.5, 17 and 18 at blast furnace 2. Ring collectors of the first pipe and tuyere are connected to air ducts 19 and 20 of hot air. coming from the air heaters 21 and 22 (Fig. 2), the oxygen-enriched air from the blower 23 is supplied to the chambers. The annular collectors 2, 3 and p of the tuyeres of each of the furnaces are connected in pairs by pipelines 24, 25 and 26, and the annular collector 2- A row of tuyeres of furnace 1, the supply of 1ai gas, was supplied with an input for the supply of endothermic gas. The pipelines connecting the collectors are equipped with bridges and a shut-off valve system that allows gas to be drawn from the common range of tuyeres 2, 3 and 4 to any of them, to blow into another 36 ryio oven or to transport to another consumer. meters of gas, as well as gas sampling devices, to determine its composition, temperature, pressure, and flow rate for each of the gas lines 27, 28, 29, 30, 31, and 32. The system operates as follows. The charge materials are loaded in the usual manner through the top furnace. When the kiln operates in gas production mode, KioKC is replaced with cheap coal, lignite, and other carbonaceous materials, such as industrial or household waste. In a blast furnace, the main product of which is metal, coke is charged in a minimum amount; required for the formation of a mobile nozzle for the drainage of liquid products of smelting and the passage of gases (210-260 kg / t of pig iron), and the ratio of metal oxide and coke is about twice as much as usual. Fluxes are also loaded in an amount sufficient to obtain the desired composition. Hot blast heated by air heaters 21 and 22 is fed through pipelines 19 and 20, is introduced into the furnace for melting metal through ring collector 16 and a series of tuyeres 5, and into the furnace for producing gas through an air duct and a series of tuyeres 6. In both In some cases, the blast is enriched with oxygen, but to varying degrees. In furnace 2, a reducing gas is formed, part of which is removed through a series of tuyeres 8 and 10, and the remaining part is introduced into furnace 1 to create a reserve of heat with a temperature below 1000 C in the lower part of the shaft and the number of reducing gases using the appropriate shut-off valves and jumpers. gases in it to ensure maximum recovery of the well-prepared oxidized charge without significant loss of carbon to direct reduction. The temperature and composition of the reducing gas is controlled by the flow rate of the incoming endothermic gas (containing H.0 and CO) introduced through tuyeres 4 and 6. The degree and character of the endothermic reactions before tuyeres 6 are adjusted on the basis of dan71
    analysis of samples taken from tuyeres 6. Gas flows passing through the collector 18 and tuyeres 4 are adjusted so that the Boudoir reaction proceeds as economically as possible. If necessary, a certain amount of gas is added to the collar gas leaving the blast furnace through the gas outlet 33, if necessary, for subsequent use in power plants or for other purposes. Part of the gas can be injected into the blast furnace
    38036.,
    for producing gas through the pipeline and the injection system before entering into the lance 4 or pipeline 17 and then into the lance 6. 5
    The use of the invention makes it possible to reduce the coke consumption to the minimum amount necessary for the drainage of liquid products of melting, replacing it with a cheap reducing gas obtained without the use of natural gas, fuel oil and metallized raw materials.
    权利要求:
    Claims (2)
    [1]
    · 1. The method of operation of a blast furnace, including loading the charge through the top, introducing carbon-containing components, for example coal, into the charge, preheating the charge in the mine and melting it on the shoulders, burning carbon materials in the tuyere zone with heated oxygen enriched blast, discharging liquid melting products from the lower part of the hearth, gas removal through the top, characterized in that, in order to increase the efficiency of the blast furnace in obtaining high-quality reducing gas and cheaper production, hnyuyu part shoulders injected gas containing C0 2 and H ^ O, at a temperature above 1000 ° C, while maintaining the temperature of the gas in the lower part of the shaft at 1000 ° C, and removing a part of the reducing gas containing CO, H 2 and N 2 and practically free of C0 g , HgO and S from the bottom of the mine at two different horizons.
    [2]
    2. A system for the production of molten iron and reducing gas, consisting of two blast furnaces, each of which contains a series of blasting tuyeres in the upper part of the hearth, connected by pipelines for transferring reducing gas from one furnace to another, characterized in that, in order to increase work efficiency § systems for the quality and quantity of produced melting products and the cost of their production, each furnace additionally contains one row of tuyeres located in the upper part of the shoulders, and two rows of tuyeres located in neither • the bottom of the shaft, and two rows of tuyeres located in the lower part of the shaft of one of the furnaces are connected to at least one row of tuyeres in the same zone of the other furnace.
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    同族专利:
    公开号 | 公开日
    WO1981003668A1|1981-12-24|
    ZA813975B|1982-06-30|
    GB2090871A|1982-07-21|
    KR830006438A|1983-09-24|
    US4381938A|1983-05-03|
    ES8300863A1|1982-11-01|
    EP0042147A1|1981-12-23|
    CA1165568A|1984-04-17|
    BR8108648A|1982-04-27|
    GB2090871B|1985-06-26|
    YU147781A|1983-12-31|
    ES503004A0|1982-11-01|
    JPS57500986A|1982-06-03|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/158,709|US4381938A|1980-06-12|1980-06-12|Multi-purpose zone controlled blast furnace and method of producing hot metal, gases and slags|
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