EP0767242A1 - Sintered steel manufacturing process - Google Patents
Sintered steel manufacturing process Download PDFInfo
- Publication number
- EP0767242A1 EP0767242A1 EP95923548A EP95923548A EP0767242A1 EP 0767242 A1 EP0767242 A1 EP 0767242A1 EP 95923548 A EP95923548 A EP 95923548A EP 95923548 A EP95923548 A EP 95923548A EP 0767242 A1 EP0767242 A1 EP 0767242A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- raw material
- hot blast
- layer
- microwaves
- surface layer
- 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.)
- Granted
Links
Images
Classifications
-
- 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
- C22B1/20—Sintering; Agglomerating in sintering machines with movable grates
- C22B1/205—Sintering; Agglomerating in sintering machines with movable grates regulation of the sintering process
-
- 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
- C22B1/20—Sintering; Agglomerating in sintering machines with movable grates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B21/00—Open or uncovered sintering apparatus; Other heat-treatment apparatus of like construction
- F27B21/06—Endless-strand sintering machines
-
- 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
- F27D99/00—Subject matter not provided for in other groups of this subclass
- F27D99/0001—Heating elements or systems
- F27D99/0006—Electric heating elements or system
- F27D2099/0028—Microwave heating
Definitions
- the present invention relates to a method of producing sintered ore to be used as raw material of iron-making in which sintered ore of high quality can be provided when iron ore is quickly dried and heated to high temperatures in a short period of time by a Dwight Lloyd type sintering machine.
- Dwight Lloyd type sintering machines have come into wide use.
- a surface layer of blended raw material is ignited in an ignition furnace, and the generated combustion gas is sucked downward, so that the combustion zone is gradually moved from an upper layer to an intermediate and to a lower layer. In this way, the entire sintering process is generally completed in 25 to 35 minutes.
- Japanese Examined Patent Publication No. 54-24682 discloses the following method of producing sintered ore.
- a hot blast feeding device between an ore feeding device for feeding raw material to pallets, and an ignition furnace.
- a blast of hot air is blown onto an upper surface of raw material so that only the temperature of an upper layer of raw material is raised, and the upper layer of raw material, the temperature of which has been raised, is successively ignited in the ignition furnace.
- raw material is sintered while the thermal shock caused in the process of ignition is reduced.
- the following effects can be provided by this method of producing sintered ore. According to this method, while the shatter test strength is maintained to be constant, the productivity can be enhanced and the unit requirement of coke breeze can be reduced, however, the product yield is a little lowered.
- Japanese Examined Patent Publication No. 57-45296 the following method of producing sintered ore is disclosed.
- a hot blast feeding device between an ore feeding device and an ignition furnace.
- a blast of hot air is blown onto an upper surface of raw material and sucked downward, so that only an upper layer of raw material is dried and then ignited in an ignition furnace.
- a hot blast feeding device After the ignition furnace, there is provided a hot blast feeding device, and a blast of hot air is fed from the hot blast feeding device and sucked downward so that a sintering reaction can be conducted.
- the above preheating sintering method when a thermal shock given to the surface layer of raw material in the ignition surface is reduced and the dried zone is extended, a moisture condensing zone is relatively reduced. Accordingly, a quantity of combustion air to be sucked after the ignition is increased, so that the sintering time can be reduced. Since the maximum temperature in the heat pattern of the preheated upper layer of raw material is raised higher than that of the upper layer of raw material which has not been preheated, the productivity, product yield and sintered ore quality can be enhanced, and further the fuel consumption and the ignition fuel consumption can be reduced.
- the pseudo particles are composed as follows.
- Raw materials of sintered ore such as iron ore, coke breeze, lime stone and so forth are previously mixing in a mixer while water is added to the mixture. Due to the foregoing, fine particles adhere onto the periphery of a core particle which is a raw material grain formed by the mixer. In this way, one pseudo particles are composed.
- the pseudo particles are made by pelletizing raw material and water, wherein a binder is added to the raw material and water when necessary.
- the particle diameter is increased when fines adhere to each other or alternatively fines adhere to rough grains.
- Raw material to be sintered the particle diameter of which has been increased, is charged into the sintering machine so that a layer of raw material of a predetermined height can be formed. After a sintering bed has been formed in this way, sintering is conducted.
- the pseudo particles collapse in the process of drying and heating the surface layer of raw material, clearances formed in the raw material to be sintered are filled with fines of the raw material. Therefore, a uniform flow of hot blast is blocked.
- a hot blast flows smoothly in some portions and does not flow smoothly in other portions. Accordingly, the surface layer of raw material is not heated uniformly in the pallet width direction. Due to the foregoing, the sintering speed fluctuates after the ignition, so that the raw material can not be sintered uniformly, which deteriorates the product yield. Unless the pseudo particles collapse, sintering is conducted uniformly, so that the yield can be enhanced.
- the present inventors made investigation in earnest into a means for drying and heating the surface layer of raw material to be sintered, in a short period of time without collapsing the pseudo particles. As a result of the investigation, they found that sintered ore of high quality can be produced at a high yield when high-frequency heating is conducted on the raw material, especially when microwaves are irradiated alone, or alternatively when microwaves and a hot blast are combined and given to the raw material to be sintered.
- microwaves are used in the present invention. It was found that the problem of collapse of pseudo particles cannot be solved as long as heating is conducted from the outside of raw material. Accordingly, from the idea of utilizing the surface layer of raw material as a heating unit, when the phenomenon of polarization, which is peculiar to microwaves, is used, it becomes possible to heat the raw material from the inside. Further, when microwaves are used, the thermal efficiency is high in principle, and it is possible to heat the raw material to be sintered in a short period of time even if the input of electric power to be given is small. Utilizing the above knowledge, the inventors succeeded in solving the above conventional problems by one effort.
- the present invention is to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 120 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; igniting the upper surface of the layer of raw material in the ignition furnace; and sintering the raw material.
- the present invention is also to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 50 to 200°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device arranged also between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
- the present invention is also to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 150 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace and simultaneously heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device also arranged between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
- the microwave heating method it is possible to quickly remove the moisture of 6 to 7 wt% contained in the blended raw material, without the collapse of the pseudo particles after pelletization. Therefore, nonuniformity of drying and heating the surface layer of raw material in the pallet width direction can be reduced. Further, it is possible to quickly preheat the blended raw material provided on the pallets to a high temperature.
- a hot blast flows smoothly in some portions and does not flow smoothly in other portions, that is, the sintering speed fluctuates. Due to the foregoing, sintering can not be conducted uniformly in the pallet width direction. However, as described before, according to the present invention, nonuniformity of sintering in the pallet width direction can be remarkably reduced.
- the microwave heating is combined with the suction of a hot blast, it is possible to quickly remove the moisture which has flowed onto the surface of the iron ore. Accordingly, while the collapse of pseudo particles is perfectly prevented, the blended raw material on the surface layer on the pallets can be more quickly heated to a high temperature.
- the productivity is enhanced and the unit requirement of fuel is reduced, and further the generation of NO x gas is reduced.
- the surface layer of raw material is defined as a region of the raw material layer formed in the thickness direction, wherein the thickness of the raw material layer is usually in a range from 350 to 500 mm, and the thickness of the surface layer is in a range within 1/10 of the thickness of the raw material layer.
- the lower layer is fed with a sufficiently large quantity of heat even when the conventional method is adopted. Accordingly, it is impossible to expect a high effect on the lower layer. Since the heat inputted onto the surface layer is successively transferred onto the layer located immediately below the surface layer, the microwave heating may be conducted only on the surface layer.
- the wavelength of microwaves used for drying and heating the surface layer of raw material on the pallets it is allowed to use the ISN bands of 2450 MHz and 915 MHz. Either of them may be selected.
- a plurality of microwave generators The capacity of each microwave generator is 5 kW or 25 kW, may be provided, and the microwaves generated by each microwave generator are collected by a wave guide and irradiated.
- the optimum range of irradiation of microwaves onto the surface layer of raw material on the pallets is from 10 to 200 kW/m 2 . The reason why the above optimum range of irradiation of microwaves is determined is described as follows.
- the range of irradiation of microwaves When the range of irradiation of microwaves is lower than 10 kW/m 2 , it is impossible to provide a sufficiently high effect of heating by microwaves. When the range of irradiation of microwaves is higher than 200 kW/m 2 , the effect of heating by microwaves reaches the upper limit.
- the optimum temperature of a hot blast blown to the raw material on the pallets is 150 to 600°C, and the blowing speed (sucking speed) of a hot blast is 0.3 to 3.0 m/sec.
- the hot blast temperature When the hot blast temperature is lower than 150°C, it is impossible to provide a sufficiently high effect of drying and heating. When the hot blast temperature is higher than 600°C, the effect of heating reaches the upper limit.
- the hot blast blowing speed is lower than 0.3 m/sec, it is impossible to provide a sufficiently high effect of drying and heating.
- the hot blast blowing speed is higher than 3.0 m/sec, the pressure of a blast of air is increased, and the raw material on the pallets contracts, which exerts a harmful influence on the sintering process.
- microwaves are irradiated before a hot blast is blown onto the surface layer of raw material on the pallets.
- the moisture in the pseudo particles of blended raw material containing iron ore, limestone and coke breeze can be made to flow quickly onto the surfaces of pseudo particles without the collapse of the pseudo particles.
- the microwave heating and the hot blast blowing are simultaneously conducted, the moisture in the blended raw material flows quickly by the action of microwave heating. Therefore, the collapse of pseudo particles caused by the hot blast heating can be prevented.
- the above method in which the microwave heating and the hot blast blowing are simultaneously conducted is very effective for preventing the collapse of pseudo particles, because the moisture flowing onto the surfaces of pseudo particles of blended raw material can be quickly evaporated.
- a method in which microwaves are irradiated after a hot blast has been blown onto the surface layer of raw material on the pallets is disadvantageous in that a portion of pseudo particles of blended raw material are collapsed in the process of heating conducted by blowing a hot blast.
- the moisture in the pseudo particles is dried from the outside to the inside by the hot blast heating method. Therefore, when the moisture inside the pseudo particles flows onto their surfaces, a portion of raw material, which has already been dried, is collapsed by the moisture. Due to the collapse of raw material, the gas permeability of the sintering bed is deteriorated and the sintering time is extended. As a result, the productivity is lowered.
- the moisture in the pseudo particles first absorbs the microwaves and heats up. Then the thus heated moisture first flows onto the surfaces of pseudo particles. Accordingly, the surfaces of pseudo particles are wet. These wet surfaces of pseudo particles are not collapsed.
- the pseudo particles are heated by blowing a hot blast after the moisture in the pseudo particles has already been dried by the microwave heating, the pseudo particles are not collapsed because no moisture evaporates in the process of blowing a hot blast.
- the reason why the surface layer of the raw material located between the raw material charging device and the ignition furnace is heated by microwaves to temperatures of 120 to 600°C is described as follows. In order to perfectly dry the blended raw material, it is necessary to heat it to temperatures of not less than 120°C. when the heating temperature exceeds 600°C, a portion of the blended raw material is overheated, so that the pseudo particles of the blended raw material start collapsing, and the gas permeability is deteriorated in the process of sintering.
- the raw material is first heated by the microwaves to temperatures of 50 to 200°C and then heated by the hot blast to temperatures of 150 to 600°C.
- heating it is possible to heat the raw material quickly.
- the raw material is heated by microwaves to temperature higher than 200°C, it is necessary to increase an amount of energy to be inputted.
- the surface layer of raw material is heated by a hot blast after that, since the temperature rising speed is not so high, the pseudo particles from which the moisture has already been evaporated do not collapse, and it is possible to heat the pseudo particles to temperatures of 150 to 600°C by inputting a smaller amount of energy.
- the reason why the heating temperature of a hot blast is determined to be 150 to 600°C is described as follows. When the heating temperature is lower than 150°C, it is impossible to provide a sufficiently high effect corresponding to the inputted energy. When the heating temperature is higher than 600°C, the effect of heating reaches the upper limit.
- the reason why the surface layer of raw material located between the raw material charging device and the ignition furnace is heated to temperatures of 150 to 600°C by both microwaves and a hot blast is that the drying and heating time can be further reduced when both microwaves and a hot blast are simultaneously used.
- the surface layer of raw material is heated to temperatures not less than 150°C, the effect of combination of microwave heating with hot blast blowing is remarkably increased.
- the surface layer of raw material is heated to temperatures lower than 150°C, the effect of combination of microwave heating with hot blast blowing is not so high.
- the temperature of the surface layer of raw material exceeds 600°C, a portion of the blended raw material is overheated by the microwaves, so that the pseudo particles of the blended raw material start collapsing.
- the surface layer of raw material it is most preferable to heat the surface layer of raw material to temperatures from 200 to 450°C. Since the blended raw material is ignited after the surface layer of raw material has been uniformly heated, it is possible for the combustion zone to spread from the upper layer to the lower layer uniformly with respect to the width direction of the raw material layer. Accordingly, the quality of sintered ore can be enhanced.
- Fig. 1 is an arrangement view of a sintering machine illustrating its general construction in accordance with the present invention.
- Blended raw material 1 to be sintered is continuously fed from the surge hopper 2 onto the pallets 6 via the drum feeder 3 and raw material charging device 5.
- the thus fed raw material 1 is laminated on the pallets 6.
- the sprocket 4 arranged on the raw material feeding side is rotated so that the pallets 6 are moved at a predetermined speed.
- waste gas is sucked by the suction blower 13 via a plurality of wind boxes 8, the main duct 9 and the dust collector 12.
- the ignition furnace 14 an upper surface of the raw material layer 7 is ignited, and operation is continuously conducted while the pallet speed is controlled so that the entire raw material layer 7 on the pallets 6 can be completely sintered before it reaches the ore discharging section.
- a microwave generator 15 Between the raw material charging device 5 and the ignition furnace 14 of the above Dwight Lloyd type sintering machine, there is provided a microwave generator 15, or alternatively there are provided a microwave generator 15 and a hot blast feeding device 16.
- the raw material layer 7 on the pallets 6 is heated in accordance with an amount of energy of the irradiated microwaves and the irradiation time.
- this hot blast feeding device 16 it is possible to introduce a hot blast discharged from the discharge pipe 18 of the cooling unit 17 composing a portion of the sintering process.
- this hot blast feeding device 16 it is possible to introduce a hot blast of gas at not lower than 100°C which has been discharged from the wind boxes 8 and passed through the waste gas introducing pipe 10, flow rate adjusting valve 11, waste gas dust collector 12' and suction blower 13'. Both the hot blast discharged from the cooling unit 17 and the waste gas of not lower than 100°C discharged from the wind boxes may be simultaneously fed to the hot blast feeding device 16. However, it is possible to feed one of than alone. It is also possible to feed the mixture of them, the temperature of which is adjusted to a predetermined value.
- the following states may be adopted. It is possible to arrange the microwave generator 15 alone. It is also possible to arrange the microwave generator 15 and the hot blast feeding device 16 in series. Although not shown in the drawing, it is possible to arrange the microwave generator in the first half of the hot blast feeding device 16, or it is also possible to arrange the microwave generators at regular intervals in the longitudinal direction of the pallets 6.
- the temperature control method for heating the raw material layer 7 on the pallets 6 by the irradiation of microwaves it is possible to adopt a method in which an amount of energy of irradiated microwaves is adjusted, and also it is possible to adopt a method in which an area of irradiation of microwaves onto the raw material layer moving at a predetermined speed is adjusted. This method may be adopted alone or combined with another method.
- Fig. 1 is an arrangement view of an example of the equipment to execute the method of the present invention.
- Fig. 2a is a graph on which the productivity, sintering time and product yield of examples and comparative examples are shown.
- Fig. 2b is a graph showing the shatter strength (SI), low temperature reduction degradation index (RDI) and consumption of generation of NO x .
- Table 1 shows a blending proportion of raw materials used in this example.
- Raw materials were blended in such a manner that various iron ores and miscellaneous raw materials such as limestone, quick lime, serpentine, scale and so forth were adjusted and blended so that SiO 2 and Al 2 O 3 in the sintered ore could be respectively 5.8% and 1.8% and so that the basicity could be 1.7.
- a ratio of returned ore was determined to be a constant value of 15% with respect to new raw material.
- a coke breeze blending ratio was determined to be a constant value of 4.0% with respect to the total 100 of new raw materials.
- Returned ore and coke breeze were blended with the above blended raw material, and then addition water of 6 to 7 wt% was added to the blended raw material and mixed by a mixer and pelletized. After that, it was put into a test pan, and the layer thickness was set at 500 mm and the negative pressure was set at a constant value of 1200 mmAq.
- Concerning the heating conducted by microwaves or the heating conducted by both microwaves and a hot blast a simulating method was adopted in which the surface layer of raw material was dried and heated before the ignition in the Dwight Lloyd type sintering machine. In Example 1, the ignition time was set at 1.5 min.
- microwaves the intensity of which was 10 kW
- microwaves the intensity of which was 10 kW
- microwaves were irradiated for 1.0 min before the ignition, so that the surface layer of raw material was heated to 150°C.
- a hot blast of 300°C was sucked for 1.0 min, so that the surface layer of raw material was heated to 350°C before the ignition, and then the surface layer of raw material was ignited for 1.5 min.
- Example 3 before the ignition, microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min, and a hot blast of 300°C was simultaneously sucked for 1.0 min, so that the surface layer of the raw material was heated to 380°C and then ignited for 1.5 min.
- the temperature of a hot blast, the sucking time of a hot blast and the heating time of microwaves are not limited to the above specific values. It was more effective that the heating time of microwaves was 0.2 to 1.5 min. Also, it was more effective that a hot blast of 200 to 400°C was sucked for 0.5 to 3 min.
- Comparative Example 1 was a conventional method in which drying and heating is not conducted before the ignition.
- Comparative Example 2 was a method in which a hot blast of 300°C was sucked for 1.0 min before ignition, and then microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min so as to heat the surface layer of raw material.
- Comparative Example 2 With respect to Examples 1, 2 and 3, sampling was conducted on the raw material on the surface layer of raw material before the ignition which had already been dried and heated, and particles, the size of which was not more than 0.5 mm, were sifted out. The weight of thus sifted particles was measured and the ratio was computed. In Comparative Example 2, the ratio of particles, the size of which was not more than 0.5 mm, was 8.0 to 9.0%. However, in Examples 1, 2 and 3, the ratio of particles, the size of which was not more than 0.5 mm, was not more than 1.0 %.
- Fig. 2a is a graph showing the productivity, sintering time and product yield obtained in the pan tests conducted in Examples 1, 2 and 3 and Comparative Examples 1 and 2.
- Fig. 2b is a graph showing the shatter strength (SI), low temperature reduction degradation index (RDI) and consumption of NO x obtained in Examples 1, 2 and 3 and Comparative Examples 1 and 2.
- the product yield in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 2 to 3%, and the sintering time including the heating time before the ignition in Examples 1, 2 and 3 of the present invention is shorter than that in Comparative Examples 1 and 2 by 1 to 3 minutes. Further, the productivity in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 0.1 to 0.25 T/H/m 2 . As can be seen in Fig.
- the shatter strength (SI) in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 1 to 1.5%
- the low temperature reduction degadation indexes (RDI) in Examples 1, 2 and 3 of the present invention are higher than those in Comparative Examples 1 and 2 by 1 to 3%.
- the NO x discharge consumption is improved by 0.02 to 0.06 Nm 3 /t-s.
- NO x generated in the sintering process is mainly composed of Fuel NO x , and the generation of NO x is suppressed when the temperature is raised, which is contrary to the phenomenon of Thermal NO x . It is considered that the generation of NO x can be reduced since the maximum temperatures of the upper and the intermediate sintering layer, which are layers from which a large amount of NO x is generated, are raised according to the method of the present invention.
- the following effects can be provided.
- the product yield can be greatly enhanced as compared with the method of the prior art.
- the productivity can be also enhanced, and SI and RDI can be improved.
- the consumption of an amount of NO x to be discharged can be greatly reduced.
- the above degree of freedom is one of the advantages of the method of the present invention. As described above, according to the present invention, it is possible to simultaneously provide effects which are not compatible with each other. Therefore, the present invention can provide great effects.
Abstract
Description
- The present invention relates to a method of producing sintered ore to be used as raw material of iron-making in which sintered ore of high quality can be provided when iron ore is quickly dried and heated to high temperatures in a short period of time by a Dwight Lloyd type sintering machine.
- In the iron and steel industry, Dwight Lloyd type sintering machines have come into wide use. In this type sintering machine, a surface layer of blended raw material is ignited in an ignition furnace, and the generated combustion gas is sucked downward, so that the combustion zone is gradually moved from an upper layer to an intermediate and to a lower layer. In this way, the entire sintering process is generally completed in 25 to 35 minutes.
- In the production process of sintered ore, the most important thing is to adopt a production method by which the productivity can be maximized while the quality of the sintered ore is maintained high, and the fuel consumption and the ignition fuel consumption can be minimized. Accordingly, in the actual operation of the sintering machine, it is desired that quantities of coke breeze and anthracite added to iron ore as fuel are reduced to as small an amount as possible, and also it is desired that quantities of coke oven gas and puevlrized coal are reduced to as small an amount as possible while the quality of the sintered ore is maintained high. However, when a blending proportion of fuel added to raw material to be sintered is simply decreased, or alternatively when a quantity of fuel used in the ignition furnace is simply decreased, it is impossible to provide good effects. When the quantity of fuel is greatly reduced, the quality of the sintered ore is deteriorated and the quantity of returned ore is increased. As a result, the fuel consumption and the ignition fuel consumption are deteriorated.
- In order to solve the above problems, for example, Japanese Examined Patent Publication No. 54-24682 discloses the following method of producing sintered ore. In a Dwight Lloyd type sintering machine, there is provided a hot blast feeding device between an ore feeding device for feeding raw material to pallets, and an ignition furnace. A blast of hot air is blown onto an upper surface of raw material so that only the temperature of an upper layer of raw material is raised, and the upper layer of raw material, the temperature of which has been raised, is successively ignited in the ignition furnace. In this way, raw material is sintered while the thermal shock caused in the process of ignition is reduced. According to the description of the above patent publication, the following effects can be provided by this method of producing sintered ore. According to this method, while the shatter test strength is maintained to be constant, the productivity can be enhanced and the unit requirement of coke breeze can be reduced, however, the product yield is a little lowered.
- According to Japanese Examined Patent Publication No. 57-45296, the following method of producing sintered ore is disclosed. In a sintering machine in which raw material is formed into layers and an upper surface of the upper layer is ignited, there is provided a hot blast feeding device between an ore feeding device and an ignition furnace. A blast of hot air is blown onto an upper surface of raw material and sucked downward, so that only an upper layer of raw material is dried and then ignited in an ignition furnace. After the ignition furnace, there is provided a hot blast feeding device, and a blast of hot air is fed from the hot blast feeding device and sucked downward so that a sintering reaction can be conducted. The following are described in the above patent publication. According to the above method, it is possible to improve various factors, which are incompatible with each other, such as an improvement of the productivity, reduction of the coke breeze consumption, improvement of the quality of sintered ore, and suppression of the generation of NOx gas. However, when only a blast of hot air is blown onto the upper surface of raw material, it is difficult to enhance the product yield greatly.
- According to the above preheating sintering method, when a thermal shock given to the surface layer of raw material in the ignition surface is reduced and the dried zone is extended, a moisture condensing zone is relatively reduced. Accordingly, a quantity of combustion air to be sucked after the ignition is increased, so that the sintering time can be reduced. Since the maximum temperature in the heat pattern of the preheated upper layer of raw material is raised higher than that of the upper layer of raw material which has not been preheated, the productivity, product yield and sintered ore quality can be enhanced, and further the fuel consumption and the ignition fuel consumption can be reduced. However, according to the above method, it is difficult to dry and heat the raw material to be sintered provided on the pallets without collapsing a portion of the pseudo particles in the blended raw material on the surface layer, the thickness of which is 5 to 50 mm. Therefore, in the process of drying and heating the surface layer of raw material, a portion of the pseudo particles are collapsed, and the nonuniformity of drying and heating is caused on the surface layer of raw material in the width direction of the pallets. Due to the above nonuniformity of drying and heating, the sintering speed fluctuates after the raw material has been ignited. As a result, it is difficult to greatly enhance the product yield, fuel consumption and ignition fuel consumption. According to the drying and heating method conducted only by sucking a hot blast downward, the space and time before the ignition furnace are limited, so that it is difficult to dry and heat the raw material to be sintered in a short period of time. Consequently, it is impossible to enhance the productivity greatly. Also, it is difficult to greatly raise the preheating temperature of raw material by sucking a hot blast. Accordingly, there is a limitation to the enhancement of the product yield. In view of the above circumstances, it is an object of the present invention to quickly dry and heat raw material to be sintered to high temperatures in a short period of time without collapsing pseudo particles on the surface layer of raw material to be sintered.
- In this case, the pseudo particles are composed as follows. Raw materials of sintered ore such as iron ore, coke breeze, lime stone and so forth are previously mixing in a mixer while water is added to the mixture. Due to the foregoing, fine particles adhere onto the periphery of a core particle which is a raw material grain formed by the mixer. In this way, one pseudo particles are composed.
- In the case of sintered ore, sintering is conducted when the fines, which adhere to the pseudo particles, and the core particles are melted with each other in a very short period of time. Therefore, it is important that the pseudo particles are held as they are without collapsing in the sintering process, especially in the drying zone.
- As described before, the pseudo particles are made by pelletizing raw material and water, wherein a binder is added to the raw material and water when necessary. The particle diameter is increased when fines adhere to each other or alternatively fines adhere to rough grains. Raw material to be sintered, the particle diameter of which has been increased, is charged into the sintering machine so that a layer of raw material of a predetermined height can be formed. After a sintering bed has been formed in this way, sintering is conducted. However, when the pseudo particles collapse in the process of drying and heating the surface layer of raw material, clearances formed in the raw material to be sintered are filled with fines of the raw material. Therefore, a uniform flow of hot blast is blocked.
- In other words, according to the method of producing sintered ore in which a hot blast is sucked, a hot blast flows smoothly in some portions and does not flow smoothly in other portions. Accordingly, the surface layer of raw material is not heated uniformly in the pallet width direction. Due to the foregoing, the sintering speed fluctuates after the ignition, so that the raw material can not be sintered uniformly, which deteriorates the product yield. Unless the pseudo particles collapse, sintering is conducted uniformly, so that the yield can be enhanced.
- The present inventors made investigation in earnest into a means for drying and heating the surface layer of raw material to be sintered, in a short period of time without collapsing the pseudo particles. As a result of the investigation, they found that sintered ore of high quality can be produced at a high yield when high-frequency heating is conducted on the raw material, especially when microwaves are irradiated alone, or alternatively when microwaves and a hot blast are combined and given to the raw material to be sintered.
- The reason why microwaves are used in the present invention is described as follows. It was found that the problem of collapse of pseudo particles cannot be solved as long as heating is conducted from the outside of raw material. Accordingly, from the idea of utilizing the surface layer of raw material as a heating unit, when the phenomenon of polarization, which is peculiar to microwaves, is used, it becomes possible to heat the raw material from the inside. Further, when microwaves are used, the thermal efficiency is high in principle, and it is possible to heat the raw material to be sintered in a short period of time even if the input of electric power to be given is small. Utilizing the above knowledge, the inventors succeeded in solving the above conventional problems by one effort.
- The present invention is to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 120 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; igniting the upper surface of the layer of raw material in the ignition furnace; and sintering the raw material.
- The present invention is also to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 50 to 200°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device arranged also between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
- The present invention is also to provide a method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 150 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace and simultaneously heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device also arranged between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
- According to the microwave heating method, it is possible to quickly remove the moisture of 6 to 7 wt% contained in the blended raw material, without the collapse of the pseudo particles after pelletization. Therefore, nonuniformity of drying and heating the surface layer of raw material in the pallet width direction can be reduced. Further, it is possible to quickly preheat the blended raw material provided on the pallets to a high temperature.
- According to the conventional method in which a hot blast is sucked downward, a hot blast flows smoothly in some portions and does not flow smoothly in other portions, that is, the sintering speed fluctuates. Due to the foregoing, sintering can not be conducted uniformly in the pallet width direction. However, as described before, according to the present invention, nonuniformity of sintering in the pallet width direction can be remarkably reduced. When the microwave heating is combined with the suction of a hot blast, it is possible to quickly remove the moisture which has flowed onto the surface of the iron ore. Accordingly, while the collapse of pseudo particles is perfectly prevented, the blended raw material on the surface layer on the pallets can be more quickly heated to a high temperature. As a result, the maximum temperature of the sintered ore layer after the ignition can be raised, and the nonuniformity of sintering speed in the pallet width direction can be reduced. Therefore, the following effects can be simultaneously provided by this method. The productivity is enhanced and the unit requirement of fuel is reduced, and further the generation of NOx gas is reduced.
- In this connection, the surface layer of raw material is defined as a region of the raw material layer formed in the thickness direction, wherein the thickness of the raw material layer is usually in a range from 350 to 500 mm, and the thickness of the surface layer is in a range within 1/10 of the thickness of the raw material layer. The reason why the microwave heating is conducted only on the surface layer of raw material is described as follows.
- In the iron ore sintering process, a blast of air or waste gas is sucked so as to cause a sintering reaction. Accordingly, on the surface layer of raw material onto which cooling air or cooling waste gas is immediately sucked, the temperature is not sufficiently raised, that is, a sufficiently large quantity of heat is not fed. When the maximum temperature of the surface layer, the thickness of which is approximately 1/10 of the raw material layer, is raised when the surface layer is heated by microwaves, the product yield of this portion can be enhanced. Further, the heat given onto the surface layer by the microwaves in this way is successively transferred to the lower layers. Accordingly, the maximum temperature, heat level and product yield of the upper and the intermediate layer can be enhanced by this transferred heat. In this case, the lower layer is fed with a sufficiently large quantity of heat even when the conventional method is adopted. Accordingly, it is impossible to expect a high effect on the lower layer. Since the heat inputted onto the surface layer is successively transferred onto the layer located immediately below the surface layer, the microwave heating may be conducted only on the surface layer.
- Concerning the wavelength of microwaves used for drying and heating the surface layer of raw material on the pallets, it is allowed to use the ISN bands of 2450 MHz and 915 MHz. Either of them may be selected. In order to ensure a necessary intensity of energy, for example, a plurality of microwave generators, The capacity of each microwave generator is 5 kW or 25 kW, may be provided, and the microwaves generated by each microwave generator are collected by a wave guide and irradiated. The optimum range of irradiation of microwaves onto the surface layer of raw material on the pallets is from 10 to 200 kW/m2. The reason why the above optimum range of irradiation of microwaves is determined is described as follows. When the range of irradiation of microwaves is lower than 10 kW/m2, it is impossible to provide a sufficiently high effect of heating by microwaves. When the range of irradiation of microwaves is higher than 200 kW/m2, the effect of heating by microwaves reaches the upper limit. The optimum temperature of a hot blast blown to the raw material on the pallets is 150 to 600°C, and the blowing speed (sucking speed) of a hot blast is 0.3 to 3.0 m/sec. When the hot blast temperature is lower than 150°C, it is impossible to provide a sufficiently high effect of drying and heating. When the hot blast temperature is higher than 600°C, the effect of heating reaches the upper limit. When the hot blast blowing speed is lower than 0.3 m/sec, it is impossible to provide a sufficiently high effect of drying and heating. When the hot blast blowing speed is higher than 3.0 m/sec, the pressure of a blast of air is increased, and the raw material on the pallets contracts, which exerts a harmful influence on the sintering process.
- The reason why microwaves are irradiated before a hot blast is blown onto the surface layer of raw material on the pallets is described as follows. When microwaves are irradiated onto the surface layer of raw material on the pallets, the moisture in the pseudo particles of blended raw material containing iron ore, limestone and coke breeze can be made to flow quickly onto the surfaces of pseudo particles without the collapse of the pseudo particles. Even when the microwave heating and the hot blast blowing are simultaneously conducted, the moisture in the blended raw material flows quickly by the action of microwave heating. Therefore, the collapse of pseudo particles caused by the hot blast heating can be prevented. The above method in which the microwave heating and the hot blast blowing are simultaneously conducted is very effective for preventing the collapse of pseudo particles, because the moisture flowing onto the surfaces of pseudo particles of blended raw material can be quickly evaporated.
- In this connection, a method in which microwaves are irradiated after a hot blast has been blown onto the surface layer of raw material on the pallets is disadvantageous in that a portion of pseudo particles of blended raw material are collapsed in the process of heating conducted by blowing a hot blast. To explain in detail, the moisture in the pseudo particles is dried from the outside to the inside by the hot blast heating method. Therefore, when the moisture inside the pseudo particles flows onto their surfaces, a portion of raw material, which has already been dried, is collapsed by the moisture. Due to the collapse of raw material, the gas permeability of the sintering bed is deteriorated and the sintering time is extended. As a result, the productivity is lowered. However, according to the method of the present invention in which the raw material is heated by microwaves or alternatively the raw material is heated by microwaves and then heated by a hot blast, the moisture in the pseudo particles first absorbs the microwaves and heats up. Then the thus heated moisture first flows onto the surfaces of pseudo particles. Accordingly, the surfaces of pseudo particles are wet. These wet surfaces of pseudo particles are not collapsed. When the pseudo particles are heated by blowing a hot blast after the moisture in the pseudo particles has already been dried by the microwave heating, the pseudo particles are not collapsed because no moisture evaporates in the process of blowing a hot blast.
- The reason why the surface layer of the raw material located between the raw material charging device and the ignition furnace is heated by microwaves to temperatures of 120 to 600°C is described as follows. In order to perfectly dry the blended raw material, it is necessary to heat it to temperatures of not less than 120°C. when the heating temperature exceeds 600°C, a portion of the blended raw material is overheated, so that the pseudo particles of the blended raw material start collapsing, and the gas permeability is deteriorated in the process of sintering.
- In the case where both microwaves and a hot blast are successively used, the raw material is first heated by the microwaves to temperatures of 50 to 200°C and then heated by the hot blast to temperatures of 150 to 600°C. When heating is conducted by the microwaves, it is possible to heat the raw material quickly. On the other hand, when the raw material is heated by microwaves to temperature higher than 200°C, it is necessary to increase an amount of energy to be inputted. When the surface layer of raw material is heated by a hot blast after that, since the temperature rising speed is not so high, the pseudo particles from which the moisture has already been evaporated do not collapse, and it is possible to heat the pseudo particles to temperatures of 150 to 600°C by inputting a smaller amount of energy. The reason why the heating temperature of a hot blast is determined to be 150 to 600°C is described as follows. When the heating temperature is lower than 150°C, it is impossible to provide a sufficiently high effect corresponding to the inputted energy. When the heating temperature is higher than 600°C, the effect of heating reaches the upper limit.
- The reason why the surface layer of raw material located between the raw material charging device and the ignition furnace is heated to temperatures of 150 to 600°C by both microwaves and a hot blast is that the drying and heating time can be further reduced when both microwaves and a hot blast are simultaneously used. When the surface layer of raw material is heated to temperatures not less than 150°C, the effect of combination of microwave heating with hot blast blowing is remarkably increased. However, when the surface layer of raw material is heated to temperatures lower than 150°C, the effect of combination of microwave heating with hot blast blowing is not so high. On the other hand, when the temperature of the surface layer of raw material exceeds 600°C, a portion of the blended raw material is overheated by the microwaves, so that the pseudo particles of the blended raw material start collapsing.
- In any case, it is most preferable to heat the surface layer of raw material to temperatures from 200 to 450°C. Since the blended raw material is ignited after the surface layer of raw material has been uniformly heated, it is possible for the combustion zone to spread from the upper layer to the lower layer uniformly with respect to the width direction of the raw material layer. Accordingly, the quality of sintered ore can be enhanced.
- Next, referring to the accompanying drawings, an example of the sintering machine to execute the present invention and its operation method will be explained below.
- Fig. 1 is an arrangement view of a sintering machine illustrating its general construction in accordance with the present invention. Blended
raw material 1 to be sintered is continuously fed from thesurge hopper 2 onto thepallets 6 via thedrum feeder 3 and raw material charging device 5. The thus fedraw material 1 is laminated on thepallets 6. While the raw material is fed in this way, the sprocket 4 arranged on the raw material feeding side is rotated so that thepallets 6 are moved at a predetermined speed. At the same time, on the lower side of thepallets 6, waste gas is sucked by thesuction blower 13 via a plurality ofwind boxes 8, themain duct 9 and thedust collector 12. In theignition furnace 14, an upper surface of theraw material layer 7 is ignited, and operation is continuously conducted while the pallet speed is controlled so that the entireraw material layer 7 on thepallets 6 can be completely sintered before it reaches the ore discharging section. - Between the raw material charging device 5 and the
ignition furnace 14 of the above Dwight Lloyd type sintering machine, there is provided amicrowave generator 15, or alternatively there are provided amicrowave generator 15 and a hotblast feeding device 16. In the case of microwave heating, theraw material layer 7 on thepallets 6 is heated in accordance with an amount of energy of the irradiated microwaves and the irradiation time. Into this hotblast feeding device 16, it is possible to introduce a hot blast discharged from thedischarge pipe 18 of the coolingunit 17 composing a portion of the sintering process. Also, into this hotblast feeding device 16, it is possible to introduce a hot blast of gas at not lower than 100°C which has been discharged from thewind boxes 8 and passed through the wastegas introducing pipe 10, flowrate adjusting valve 11, waste gas dust collector 12' and suction blower 13'. Both the hot blast discharged from the coolingunit 17 and the waste gas of not lower than 100°C discharged from the wind boxes may be simultaneously fed to the hotblast feeding device 16. However, it is possible to feed one of than alone. It is also possible to feed the mixture of them, the temperature of which is adjusted to a predetermined value. - Concerning the state in which the microwave irradiation and the hot blast blowing are combined with each other, the following states may be adopted. It is possible to arrange the
microwave generator 15 alone. It is also possible to arrange themicrowave generator 15 and the hotblast feeding device 16 in series. Although not shown in the drawing, it is possible to arrange the microwave generator in the first half of the hotblast feeding device 16, or it is also possible to arrange the microwave generators at regular intervals in the longitudinal direction of thepallets 6. Concerning the temperature control method for heating theraw material layer 7 on thepallets 6 by the irradiation of microwaves, it is possible to adopt a method in which an amount of energy of irradiated microwaves is adjusted, and also it is possible to adopt a method in which an area of irradiation of microwaves onto the raw material layer moving at a predetermined speed is adjusted. This method may be adopted alone or combined with another method. - Fig. 1 is an arrangement view of an example of the equipment to execute the method of the present invention.
- Fig. 2a is a graph on which the productivity, sintering time and product yield of examples and comparative examples are shown. Fig. 2b is a graph showing the shatter strength (SI), low temperature reduction degradation index (RDI) and consumption of generation of NOx.
- Referring to an example, the most preferred embodiment of the present invention will be explained below.
- A specific example will be explained in detail in accordance with the above exemplary equipment and the operation method.
- Table 1 shows a blending proportion of raw materials used in this example. Raw materials were blended in such a manner that various iron ores and miscellaneous raw materials such as limestone, quick lime, serpentine, scale and so forth were adjusted and blended so that SiO2 and Al2O3 in the sintered ore could be respectively 5.8% and 1.8% and so that the basicity could be 1.7. In this case, a ratio of returned ore was determined to be a constant value of 15% with respect to new raw material. A coke breeze blending ratio was determined to be a constant value of 4.0% with respect to the total 100 of new raw materials.
Table 1 Brand of raw material Blending proportion (%) Newman fine ore 10.0 Roberiver fine ore 25.0 Yandicoogina fine ore 10.0 Rio-Dose SSF powder ore 5.0 Carol fine ore 10.0 Yampi fine ore 12.5 Iscole undersized ore 6.0 Scale 5.0 Serpentine fine 2.5 Limestone fine 12.0 Quick lime 2.0 Total of new raw materials 100.0 Returned ore (outer number) 15.0 Coke breeze (outer number) 4.0 - Returned ore and coke breeze were blended with the above blended raw material, and then addition water of 6 to 7 wt% was added to the blended raw material and mixed by a mixer and pelletized. After that, it was put into a test pan, and the layer thickness was set at 500 mm and the negative pressure was set at a constant value of 1200 mmAq. Concerning the heating conducted by microwaves or the heating conducted by both microwaves and a hot blast, a simulating method was adopted in which the surface layer of raw material was dried and heated before the ignition in the Dwight Lloyd type sintering machine. In Example 1, the ignition time was set at 1.5 min. Before the ignition, microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min, so that the surface layer of raw material was heated to 150°C before the ignition. In Example 2, microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min before the ignition, so that the surface layer of raw material was heated to 150°C. After that, a hot blast of 300°C was sucked for 1.0 min, so that the surface layer of raw material was heated to 350°C before the ignition, and then the surface layer of raw material was ignited for 1.5 min. In Example 3, before the ignition, microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min, and a hot blast of 300°C was simultaneously sucked for 1.0 min, so that the surface layer of the raw material was heated to 380°C and then ignited for 1.5 min. It should be noted that the temperature of a hot blast, the sucking time of a hot blast and the heating time of microwaves are not limited to the above specific values. It was more effective that the heating time of microwaves was 0.2 to 1.5 min. Also, it was more effective that a hot blast of 200 to 400°C was sucked for 0.5 to 3 min.
- Comparative Example 1 was a conventional method in which drying and heating is not conducted before the ignition. Comparative Example 2 was a method in which a hot blast of 300°C was sucked for 1.0 min before ignition, and then microwaves, the intensity of which was 10 kW, were irradiated for 1.0 min so as to heat the surface layer of raw material.
- In Comparative Example 2, with respect to Examples 1, 2 and 3, sampling was conducted on the raw material on the surface layer of raw material before the ignition which had already been dried and heated, and particles, the size of which was not more than 0.5 mm, were sifted out. The weight of thus sifted particles was measured and the ratio was computed. In Comparative Example 2, the ratio of particles, the size of which was not more than 0.5 mm, was 8.0 to 9.0%. However, in Examples 1, 2 and 3, the ratio of particles, the size of which was not more than 0.5 mm, was not more than 1.0 %.
- Fig. 2a is a graph showing the productivity, sintering time and product yield obtained in the pan tests conducted in Examples 1, 2 and 3 and Comparative Examples 1 and 2. Fig. 2b is a graph showing the shatter strength (SI), low temperature reduction degradation index (RDI) and consumption of NOx obtained in Examples 1, 2 and 3 and Comparative Examples 1 and 2.
- As can be seen in Fig. 2a, the product yield in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 2 to 3%, and the sintering time including the heating time before the ignition in Examples 1, 2 and 3 of the present invention is shorter than that in Comparative Examples 1 and 2 by 1 to 3 minutes. Further, the productivity in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 0.1 to 0.25 T/H/m2. As can be seen in Fig. 2b, the shatter strength (SI) in Examples 1, 2 and 3 of the present invention is higher than that in Comparative Examples 1 and 2 by 1 to 1.5%, and the low temperature reduction degadation indexes (RDI) in Examples 1, 2 and 3 of the present invention are higher than those in Comparative Examples 1 and 2 by 1 to 3%. Furthermore, it can be understood that the NOx discharge consumption is improved by 0.02 to 0.06 Nm3/t-s. As described above, according to the present invention, it is possible to remarkably enhance the product characteristic, and when the technique of the present invention is executed, it is possible to provide excellent effects in the fields of operation efficiency and environment protection.
- The reason why an amount of NOx to be discharged can be reduced is that NOx generated in the sintering process is mainly composed of Fuel NOx, and the generation of NOx is suppressed when the temperature is raised, which is contrary to the phenomenon of Thermal NOx. It is considered that the generation of NOx can be reduced since the maximum temperatures of the upper and the intermediate sintering layer, which are layers from which a large amount of NOx is generated, are raised according to the method of the present invention.
- According to the method of the present invention, the following effects can be provided. The product yield can be greatly enhanced as compared with the method of the prior art. The productivity can be also enhanced, and SI and RDI can be improved. As a result, the consumption of an amount of NOx to be discharged can be greatly reduced. It is possible to change the combination of electric power of microwaves, heating time, hot blast temperature and hot blast suction time in accordance with the instruction of operation. The above degree of freedom is one of the advantages of the method of the present invention. As described above, according to the present invention, it is possible to simultaneously provide effects which are not compatible with each other. Therefore, the present invention can provide great effects.
-
- 1
- Blended raw material to be sintered
- 2
- Surge hopper
- 3
- Drum feeder
- 4
- Sprocket
- 5
- Raw material charging device
- 6
- Pallet
- 7
- Laminated raw material
- 8
- Wind box
- 9
- Main duct
- 10
- Waste gas introducing pipe
- 11
- Flow rate adjusting valve
- 12
- Waste gas dust collector
- 12'
- Waste gas dust collector
- 13
- Suction blower
- 13'
- Suction blower
- 14
- Ignition furnace
- 15
- Microwave generator
- 16
- Hot blast feeding device
- 17
- Cooler
- 18
- Waste gas pipe
Claims (3)
- A method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 120 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; igniting the upper surface of the layer of raw material in the ignition furnace; and sintering the raw material.
- A method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 50 to 200°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace; heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device also arranged between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
- A method of producing sintered ore comprising the steps of: charging raw material of sintered ore in the form of a layer; heating an upper surface of the layer of raw material to 150 to 600°C by microwaves generated by a microwave generator arranged between a raw material feeding device and an ignition furnace and simultaneously heating the upper surface of the layer of raw material to 150 to 600°C by a hot blast fed by a hot blast feeding device also arranged between the raw material feeding device and the ignition furnace; igniting the upper surface of the layer or raw material in the ignition furnace; and sintering the raw material.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16860994A JPH0814763A (en) | 1994-06-29 | 1994-06-29 | Production sintered ore |
JP168609/94 | 1994-06-29 | ||
JP16860994 | 1994-06-29 | ||
PCT/JP1995/001301 WO1996000800A1 (en) | 1994-06-29 | 1995-06-29 | Sintered steel manufacturing process |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0767242A1 true EP0767242A1 (en) | 1997-04-09 |
EP0767242A4 EP0767242A4 (en) | 1997-09-17 |
EP0767242B1 EP0767242B1 (en) | 1999-09-29 |
Family
ID=15871234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP95923548A Expired - Lifetime EP0767242B1 (en) | 1994-06-29 | 1995-06-29 | Sintered ore manufacturing process |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0767242B1 (en) |
JP (1) | JPH0814763A (en) |
KR (1) | KR100217892B1 (en) |
CN (1) | CN1048758C (en) |
BR (1) | BR9508167A (en) |
DE (1) | DE69512520T2 (en) |
WO (1) | WO1996000800A1 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101269949B (en) * | 2008-05-12 | 2010-12-01 | 北京斯蒂奇科技有限公司 | Ignition apparatus of product line for sintering porcelain granule |
JP5831413B2 (en) * | 2011-09-15 | 2015-12-09 | 新日鐵住金株式会社 | Microwave drying apparatus and microwave drying method |
KR101398345B1 (en) * | 2012-04-27 | 2014-05-22 | 주식회사 포스코 | Apparatus using induction-heating type for sintering material and method thereof |
JP6225433B2 (en) * | 2013-03-07 | 2017-11-08 | 新日鐵住金株式会社 | Drying furnace and drying method |
KR101439243B1 (en) * | 2013-07-25 | 2014-09-11 | 주식회사 포스코 | Apparatus for sintering iron-ore |
KR20170040826A (en) | 2015-10-05 | 2017-04-14 | 주식회사 포스코 | Apparatus and method for manufacturing sintered ore |
CN107504825B (en) * | 2017-08-10 | 2019-06-04 | 武汉钢铁有限公司 | The sintering process that low NOx is generated |
US20230262853A1 (en) * | 2020-06-17 | 2023-08-17 | Vale S.A. | Device for heating a material using microwaves, method for heating a material using microwaves, and systems for heating a material using microwaves |
CN113804000A (en) * | 2020-06-17 | 2021-12-17 | 宝山钢铁股份有限公司 | Microwave and hot waste gas combined heating and drying system and method for blast furnace lump ore |
CN114136095A (en) * | 2021-11-25 | 2022-03-04 | 昆明理工大学 | Microwave ignition device of sintering machine |
CN114427793B (en) * | 2022-01-11 | 2023-01-17 | 北京科技大学 | Sintering pollution-reducing and carbon-reducing system with alternating continuous circulation |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0500252A1 (en) * | 1991-02-21 | 1992-08-26 | Ontario Hydro | Method and apparatus for processing ceramics |
JPH0734141A (en) * | 1993-07-20 | 1995-02-03 | Nippon Steel Corp | Production of sintered ore |
JPH07216462A (en) * | 1994-01-28 | 1995-08-15 | Nippon Steel Corp | Production of sintered ore |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5152903A (en) * | 1974-11-06 | 1976-05-11 | Nippon Steel Corp | SHOKETSUKO SEIZOHOHO |
JPS52152802A (en) * | 1976-06-15 | 1977-12-19 | Nippon Steel Corp | Production of sintered ore |
JPS6191798U (en) * | 1984-11-21 | 1986-06-14 | ||
JPH06212293A (en) * | 1993-01-12 | 1994-08-02 | Nippon Steel Corp | Manufacture of sintered ore |
-
1994
- 1994-06-29 JP JP16860994A patent/JPH0814763A/en active Pending
-
1995
- 1995-06-29 CN CN95194317A patent/CN1048758C/en not_active Expired - Fee Related
- 1995-06-29 EP EP95923548A patent/EP0767242B1/en not_active Expired - Lifetime
- 1995-06-29 BR BR9508167A patent/BR9508167A/en not_active IP Right Cessation
- 1995-06-29 KR KR1019960707481A patent/KR100217892B1/en not_active IP Right Cessation
- 1995-06-29 DE DE69512520T patent/DE69512520T2/en not_active Expired - Fee Related
- 1995-06-29 WO PCT/JP1995/001301 patent/WO1996000800A1/en active IP Right Grant
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0500252A1 (en) * | 1991-02-21 | 1992-08-26 | Ontario Hydro | Method and apparatus for processing ceramics |
JPH0734141A (en) * | 1993-07-20 | 1995-02-03 | Nippon Steel Corp | Production of sintered ore |
JPH07216462A (en) * | 1994-01-28 | 1995-08-15 | Nippon Steel Corp | Production of sintered ore |
Non-Patent Citations (3)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 095, no. 005, 30 June 1995 & JP 07 034141 A (NIPPON STEEL CORP), 3 February 1995, * |
PATENT ABSTRACTS OF JAPAN vol. 095, no. 011, 26 December 1995 & JP 07 216462 A (NIPPON STEEL CORP), 15 August 1995, * |
See also references of WO9600800A1 * |
Also Published As
Publication number | Publication date |
---|---|
AU2806895A (en) | 1996-01-25 |
CN1154147A (en) | 1997-07-09 |
BR9508167A (en) | 1997-08-12 |
DE69512520D1 (en) | 1999-11-04 |
WO1996000800A1 (en) | 1996-01-11 |
EP0767242B1 (en) | 1999-09-29 |
KR100217892B1 (en) | 1999-09-01 |
DE69512520T2 (en) | 2000-05-04 |
EP0767242A4 (en) | 1997-09-17 |
AU685959B2 (en) | 1998-01-29 |
CN1048758C (en) | 2000-01-26 |
JPH0814763A (en) | 1996-01-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100530815B1 (en) | Metal oxide-containing green pellet for reducing furnace, method for production thereof, method for reduction thereof, and reduction facilities | |
EP0767242B1 (en) | Sintered ore manufacturing process | |
US3244507A (en) | Method of indurating ore particles | |
US3333951A (en) | Metallized pellets | |
JP5315659B2 (en) | Method for producing sintered ore | |
JP2007284744A (en) | Method for manufacturing sintered ore | |
US3313534A (en) | Method and furnace for heat treating minerals | |
KR100929182B1 (en) | Binderless briquette manufacturing method and manufacturing apparatus | |
JP3635253B2 (en) | Method for producing pellet for reducing furnace, and method for reducing metal oxide | |
CN113604662A (en) | Pellet roasting system and method based on sintering machine | |
CN111699272A (en) | Method for producing granulated sintering material | |
US3245778A (en) | Method of indurating iron ore concentrates | |
JP2000017343A (en) | Two-stage ignition type production of sintered ore | |
WO2009078662A2 (en) | Method for manufacturing binderless briquettes and apparatus for manufacturing the same | |
JP3273275B2 (en) | Sinter production method | |
EP3892744B1 (en) | Sintered ore manufacturing method | |
KR0118997B1 (en) | Method and apparatus for sintering ore | |
JPH06212293A (en) | Manufacture of sintered ore | |
CN113249566B (en) | Sintering system and method for limonite type laterite-nickel ore | |
US3288449A (en) | Apparatus for indurating ore particles | |
JP3536682B2 (en) | Sinter production method | |
JPH11106837A (en) | Production of sintered ore | |
JPH10238958A (en) | Production of sintered ore and sintering machine | |
JPH09118936A (en) | Manufacture of sintered ore | |
EP2964793B1 (en) | System for the treatment of pellet fines and/or lump ore and/or indurated pellets |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19970124 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE FR IT NL |
|
A4 | Supplementary search report drawn up and despatched |
Effective date: 19970731 |
|
AK | Designated contracting states |
Kind code of ref document: A4 Designated state(s): DE FR IT NL |
|
17Q | First examination report despatched |
Effective date: 19980406 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE FR IT NL |
|
REF | Corresponds to: |
Ref document number: 69512520 Country of ref document: DE Date of ref document: 19991104 |
|
ITF | It: translation for a ep patent filed |
Owner name: STUDIO TORTA S.R.L. |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20080626 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20080603 Year of fee payment: 14 Ref country code: DE Payment date: 20080703 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20080617 Year of fee payment: 14 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20100101 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20100226 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090630 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100101 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100101 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090629 |