CN215295745U - Lump ore pretreatment system based on distribution plate angle adjustment - Google Patents

Lump ore pretreatment system based on distribution plate angle adjustment Download PDF

Info

Publication number
CN215295745U
CN215295745U CN202120674412.9U CN202120674412U CN215295745U CN 215295745 U CN215295745 U CN 215295745U CN 202120674412 U CN202120674412 U CN 202120674412U CN 215295745 U CN215295745 U CN 215295745U
Authority
CN
China
Prior art keywords
lump ore
heat medium
storage bin
distribution plate
ore storage
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.)
Active
Application number
CN202120674412.9U
Other languages
Chinese (zh)
Inventor
赵强
魏进超
马钟琛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhongye Changtian International Engineering Co Ltd
Original Assignee
Zhongye Changtian International Engineering Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhongye Changtian International Engineering Co Ltd filed Critical Zhongye Changtian International Engineering Co Ltd
Priority to CN202120674412.9U priority Critical patent/CN215295745U/en
Application granted granted Critical
Publication of CN215295745U publication Critical patent/CN215295745U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Manufacture Of Iron (AREA)

Abstract

A lump ore pretreatment system based on distribution plate angle adjustment comprises a lump ore conveying device, a lump ore storage bin and a heat medium conveying pipeline; a distribution plate is arranged in the lump ore storage bin and is connected with the side wall of the lump ore storage bin; the lump ore storage bin is provided with a lump ore feeding hole, a lump ore discharging hole, a heat medium inlet and a heat medium outlet; the lump ore conveying device is connected to a lump ore feeding port of the lump ore storage bin; the heat medium conveying pipeline is connected to the heat medium inlet; the lump ore discharge port is connected with the feed port of the blast furnace; wherein, the distribution plate is provided with an angle adjusting device. The utility model discloses a to the shortcoming that lump ore exists of drying in the storage silo, add the distributing plate in the storage silo, improved the drying effect of lump ore in the lump ore storage silo, improve the quality of blast furnace result, practice thrift manufacturing cost simultaneously.

Description

Lump ore pretreatment system based on distribution plate angle adjustment
Technical Field
The utility model relates to a pretreatment systems, concretely relates to lump ore pretreatment systems based on distribution plate angular adjustment to high moisture, many powder lump ore belongs to steel smelting technical field.
Background
The consumption of steel as an irreplaceable structural and functional material in the industrialization process occupies more than 95 percent of the total consumption of metal in a long time. The raw pig iron materials required by the iron and steel industry are mainly provided by blast furnace smelting, and the improvement of the blast furnace smelting technology and the reduction of the cost have profound significance for promoting the development of iron and steel enterprises. The basic link of blast furnace intensified smelting is fine material operation, natural lump ore is used as one of the main components of the charging material, and the addition amount can reach 20 percent at most. Because the moisture content of the lump ore is high, after the high-moisture lump ore enters the furnace, the moisture drying needs to consume energy, the drying process needs a certain time, and the coke ratio of the blast furnace is improved, so that the air permeability of a blast furnace charge layer is influenced, the smelting cost of the blast furnace is increased, and the furnace condition is influenced to be stable. Therefore, the reduction of the moisture content of the lump ore has important significance for reducing the iron-making cost and enhancing the stability of the furnace condition. At present, lump ore drying systems have the difficult problems of high construction cost, low drying efficiency, high energy consumption and the like.
Common furnace charging materials for blast furnaces include sintered ores, pellets and natural lump ores. The reasonable blast furnace charging material structure is that the optimum matching proportion of different types of iron-containing ores is found out by adjusting the proportion of sintered ores, pellets and natural lump ores in the iron ores fed into the furnace, so that various economic and technical indexes of blast furnace smelting under the charging material structure are relatively ideal, and the consumption cost of unit pig iron smelting is relatively lowest. Research shows that the cost expenditure of iron ore and other raw material links accounts for about 60% of the total pig iron cost, the market price of lump ore is basically equal to that of fine ore, the cost price is far lower than that of sinter and pellet ore, and the improvement of the charging proportion of the lump ore is an effective measure for reducing the raw material cost of a blast furnace. At present, the charging proportion of lump ore is generally 5-15%, and the proportion is low. The reason for this is that the lump ore has a high water content of generally 8-15%, and the water content of the lump ore in rainy season in individual harbor steel mills even exceeds 20%. The problem of high moisture content exists when the lump ore enters the furnace, energy is consumed for moisture drying after the high moisture lump ore enters the furnace, a certain time is needed in the drying process, and the coke ratio of the blast furnace is improved.
Therefore, the reduction of the water content in the lump ore has important significance for reducing the iron-making cost and enhancing the stability of the furnace condition. At present, lump ore drying systems have the difficult problems of high construction cost, low drying efficiency, high energy consumption and the like.
SUMMERY OF THE UTILITY MODEL
Aiming at the problems of high water content and more powder in iron ore lump ore, the lump ore pretreatment system and method based on distribution plate angle adjustment are provided, the amount of returned water in the iron ore lump ore is generally 8-15%, and the water content of the lump ore in rainy season in individual port steel mills even exceeds 20%. After the high-powder and high-moisture lump ore is fed into the blast furnace, the powder content affects the air permeability of the blast furnace, energy is consumed for moisture drying, a certain time is needed in the drying process, and the coke ratio of the blast furnace is improved. Research shows that drying treatment of lump ore in a storage bin by using a heat medium is feasible, so that moisture of the lump ore entering a furnace can be effectively reduced, energy consumption required by drying can be greatly reduced, and the ratio of the lump ore entering the furnace can be improved to a certain extent after drying, so that the smelting cost of the blast furnace is reduced.
In addition, through research discovery, lump ore exists in the storage silo with the state of piling up, especially the existence of fine material, leads to the whole material gas permeability deviation of feed bin, and the hot gas flow can't pierce through the material body smoothly, leads to drying effect not good enough, and feed bin upper portion temperature is less than moisture dew point temperature and easily leads to the steam condensation, causes harm to dust pelletizing system moreover.
The utility model discloses to the shortcoming that lump ore deposit screening and stoving exist in the storage silo, adopt the distributing plate to realize the method of multilayer screening and roll unloading. A plurality of layers of distribution plates are arranged from top to bottom in the lump ore storage bin, each layer of distribution plate comprises a sieve plate on the upper part and a support plate on the lower part, the sieve plates of the distribution plates are in direct contact with the lump ore and are provided with sieve meshes, and fine-grained materials attached to the lump ore are sieved by the sieve plates of the distribution plates and then discharged from powder discharge ports of the distribution plates. The problem that the lump ore powder is many has been solved in setting up of multilayer area sieve mesh distribution plate in the storage silo, and the material is the rolling state in between each layer distribution plate in the storage silo, and the gas permeability of the whole storehouse body obtains greatly improving, and the heat exchange effect between the gas-solid is good. Meanwhile, hot air flow enters the storage bin from the lower part of the storage bin and is discharged to the dust removal system from the upper part of the storage bin, the hot air flow is fully distributed in the whole storage bin, moisture of lump ore is removed, and the problem of high moisture of the lump ore is solved by introducing the hot air flow.
Furthermore, the utility model discloses a handle screening of iron ore lump ore and integrative storage silo of stoving and lump ore drying time and distribution plate angle's control method. The utility model discloses to the powder that natural lump ore exists and the high difficult problem of moisture content, provided and adopted hot medium passageway and distributing plate to realize the method of multilayer screening and roll unloading, utilized the hot waste gas of steel process directly to carry out screening and dry method to the lump ore in the storage silo. Firstly, hot waste gas is introduced to increase the temperature of the storage bin, and the temperature level is stabilized for a certain time. And then, adding the lump ore materials from the upper part, falling onto a distribution plate at the top of a heat medium channel positioned in the central axis position of the storage bin, rolling from the edge of a conical distribution plate at the top onto the distribution plate on the side wall of the lump ore storage bin, then sliding from the distribution plate to a lower conical distribution plate, and so on until the lump ore slides from the lowest distribution plate to enter a lump ore discharge port of the storage bin. The sieve plate on the upper part of the distribution plate is in direct contact with lump ore and is provided with sieve pores, and fine-grained materials attached to the lump ore are sieved by the distribution plates of all layers and then are discharged from the powder discharge port of the distribution plates of all layers. Lump ore continuously rolls from each layer of conical distribution plate on the thermal medium channel and each layer of distribution plate on the side wall of the storage bin, airflow continuously enters the storage bin, the lump ore is in a flowing state and carries out gas-solid exchange with hot waste gas, and hot airflow is fully distributed in the whole storage bin, so that the powder and moisture content of the lump ore is reduced. And the airflow is discharged to a dust removal system from the upper part of the storage bin, the screened and dried lump ore is conveyed to a blast furnace feeding system from the lower part of the storage bin, and fine-grained materials under the screen are discharged and collected from powder discharge ports of all layers. And arranging a moisture detector at the feed inlet and/or the discharge outlet, and reasonably adjusting the residence time of the lump ore in the lump ore storage bin according to moisture detection data, or correspondingly adjusting the included angle between the distribution plate and the side wall of the lump ore storage bin. The utility model discloses a can increase substantially the contact efficiency of hot gas flow and lump ore, storehouse body gas permeability obtains improving, and screening and stoving effect are strengthened. The utility model discloses a popularization has good economic benefits and environmental benefit, is expected to open up a more stable efficient way for lump ore pretreatment process in the development of china.
According to the utility model provides a first embodiment provides a lump ore pretreatment systems based on distribution plate angular adjustment.
A lump ore pretreatment system based on distribution plate angle adjustment comprises a lump ore conveying device, a lump ore storage bin and a heat medium conveying pipeline. The lump ore storage bin is provided with a lump ore feeding hole, a lump ore discharging hole, a heat medium inlet and a heat medium outlet. The lump ore conveying device is connected to the lump ore feed inlet of the lump ore storage bin. The heat medium delivery pipe is connected to the heat medium inlet. The lump ore discharge port is connected with the feed inlet of the blast furnace. The inside distributing plate that is equipped with of lump ore storage silo, the distributing plate is connected with the lateral wall of lump ore storage silo. The distribution plate is provided with an angle adjusting device.
Preferably, the distribution plate comprises a screen plate and a support plate. The one end of sieve and the one end of backup pad are connected with the lateral wall of lump ore storage silo respectively, and the sieve setting is in the top of backup pad, and the sieve downward sloping sets up, and the backup pad tilt up sets up, the other end interconnect of the other end of sieve and backup pad, preferably swing joint. A lump ore blanking channel is reserved in the central axis position of the lump ore storage bin of the distribution plate. Preferably, the sieve plate, the support plate and the side wall of the lump ore storage bin form a triangular structure in the cross section in the vertical direction. Preferably, an angle adjusting device is arranged at the joint of the sieve plate and the side wall of the lump ore storage bin.
Preferably, 1-20 layers of the distribution plates are arranged in the lump ore storage bin from top to bottom, 2-10 layers of the distribution plates are preferably arranged, and 3-8 layers of the distribution plates are more preferably arranged. And an angle adjusting device is arranged on each layer of distribution plate. Preferably, the size of the lump ore blanking channel is more than 5mm, preferably more than 6mm, and more preferably more than 8 mm.
The utility model discloses in, the distribution plate sets up in the lump ore storage silo, and the distribution plate is along storage silo lateral wall evenly distributed on the horizontal direction. One or more distribution plates may be provided per layer. For example, when the number of each layer of distribution plates is 1, the distribution plates are annularly arranged in a circle and are connected with the peripheral side wall of the lump ore storage bin. When the number of the distribution plates is 2, the distribution plates are symmetrically distributed in the lump ore storage bin. When the number of the distribution plates is 4, the distribution plates are uniformly distributed along the periphery of the side wall of the lump ore storage bin.
The utility model discloses in, the one end swing joint of block ore storage silo lateral wall is being kept away from to sieve and backup pad, and the sieve is provided with angle adjusting device with the junction of block ore storage silo lateral wall, adjusts the inclination of sieve through angle adjusting device's control, and then adjusts the length of time that the block ore rolled from the sieve. The setting of angle adjusting device promptly can realize carrying out drying time's control according to the moisture content detection data or the moisture content requirement of blast furnace pan feeding.
The utility model discloses in, leave lump ore blanking passageway in the axis position of lump ore storage silo and specifically do, be the axis with the cross section center vertically virtual line of lump ore storage silo, the distribution plate leaves the space that enough lump ore passes through around the axis, forms lump ore blanking passageway, and the size of lump ore blanking passageway satisfies a plurality of lump ore and falls down simultaneously.
Preferably, a heat medium channel is further arranged at the lump ore blanking channel. The heat medium channel is also provided with a conical distribution plate. The conical surface of the conical distribution plate is provided with air holes. Preferably, the heat medium channel is provided with 1-20 layers of conical distribution plates from top to bottom, preferably 2-10 layers of conical distribution plates, and more preferably 3-8 layers of conical distribution plates. Air holes are uniformly arranged on the conical surface of each layer of conical distribution plate. Preferably, the number of layers of the conical distribution plates on the heat medium channel is the same as that of the distribution plates on the side wall of the lump ore storage bin. And the conical distribution plate is arranged above the distribution plate at the position of the same layer.
In the present invention, when the tapered distribution plate is provided with only one layer, the tapered distribution plate is provided at the top of the thermal medium channel. When the conical distribution plates on the thermal medium channel are arranged into a plurality of layers, wherein the conical distribution plate on the uppermost layer is arranged at the top of the thermal medium channel and is of a conical structure; and the other conical distribution plates are arranged on the side wall of the heat medium channel and are positioned above the distribution plates connected with the side wall of the storage bin at the same layer. Except the conical distribution plate on the uppermost layer, the conical distribution plates on the other layers are actually in a round table structure. The distributing plate that is connected with the storage silo lateral wall of same layer position specifically does, from last to being 1 st layer, 2 nd layer … … nth layer distributing plate down in proper order, and is corresponding, on the hot medium passageway, from last to being 1 st layer, 2 nd layer … … nth layer toper distributing plate down in proper order, and nth layer distributing plate and nth layer toper distributing plate are promptly in the position of one deck. Preferably, the 1 st layer of tapered distribution plate is disposed above the 1 st layer of distribution plate … … the nth layer of tapered distribution plate is disposed above the nth layer of distribution plate, and so on.
The utility model discloses add the hot medium passageway in the axis position of lump ore storage silo, be equipped with multilayer toper distributing plate on the hot medium passageway, all be equipped with the gas pocket of heating medium circulation on the conical surface of each layer toper distributing plate for the hot medium distributes evenly in the lump ore storage silo. The lump ore entering the lump ore storage bin rolls between each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, so that the air permeability in the lump ore storage bin is improved, the lump ore is more fully contacted with the heat medium, and the moisture content in the lump ore is more effectively reduced.
Preferably, sieve holes are arranged on the sieve plate of each layer of distribution plate. Preferably, each layer of distribution plate is provided with a powder discharge opening. The powder discharge port is arranged on the side wall of the lump ore storage bin and is connected with the supporting plate of the distribution plate. The gap between the sieve plate and the support plate of each layer of distribution plate forms a powder blanking channel. Preferably, the size of the sieve holes is 5-20 mm, preferably 6-15 mm, and more preferably 7-10 mm.
Preferably, the upper part of the lump ore storage bin is a heat exchange chamber provided with a distribution plate and a heat medium channel, and the lower part of the lump ore storage bin is a material collection chamber. The lump ore feed inlet is arranged on the heat exchange chamber, and the lump ore discharge outlet is arranged on the material collection chamber. Wherein: lump ore enters a heat exchange chamber of the lump ore storage bin from a lump ore feeding port, firstly rolls to a conical distribution plate at the top of a heat medium channel, rolls to a distribution plate on the side wall of the lump ore storage bin from the edge of the conical distribution plate at the top, then slides to a lower conical distribution plate from the distribution plate, and so on until the lump ore slides to a material collection chamber from the lowest distribution plate. The heat medium inlet is arranged on the material collecting chamber, and the heat medium outlet is arranged on the side part or the upper part of the heat exchange chamber. The heat medium enters the lump ore storage bin from a heat medium inlet on the material collecting chamber, directly contacts with the lump ore for heat exchange, upwards passes through the air holes on each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, and is discharged from a heat medium outlet on the heat exchange chamber.
Preferably, the upper part of the lump ore storage bin is a heat exchange chamber provided with a distribution plate and a heat medium channel, and the lower part of the lump ore storage bin is a material collection chamber. The lump ore feed inlet is arranged on the heat exchange chamber, and the lump ore discharge outlet is arranged on the material collection chamber. Wherein: lump ore enters a heat exchange chamber of the lump ore storage bin from a lump ore feeding port, firstly rolls to a conical distribution plate at the top of a heat medium channel, rolls to a distribution plate on the side wall of the lump ore storage bin from the edge of the conical distribution plate at the top, then slides to a lower conical distribution plate from the distribution plate, and so on until the lump ore slides to a material collection chamber from the lowest distribution plate. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes on the sieve plates of the distribution plates of all layers and is discharged from the powder discharge openings of all layers. The heat medium inlet is arranged on the material collecting chamber, and the heat medium outlet is arranged on the side part or the upper part of the heat exchange chamber. The heat medium enters the lump ore storage bin from a heat medium inlet on the material collecting chamber, directly contacts with the lump ore for heat exchange, upwards passes through the air holes on each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, and is discharged from a heat medium outlet on the heat exchange chamber.
Preferably, the upper part of the lump ore storage bin is a heat exchange chamber provided with a distribution plate and a heat medium channel, and the lower part of the lump ore storage bin is a material collection chamber. The lump ore feed inlet of the lump ore storage bin is arranged on the heat exchange chamber, and the lump ore discharge outlet is arranged on the material collection chamber. Wherein: lump ore enters a heat exchange chamber of the lump ore storage bin from a lump ore feeding port, firstly rolls to a conical distribution plate at the top of a heat medium channel, rolls to a distribution plate on the side wall of the lump ore storage bin from the edge of the conical distribution plate at the top, then slides to a lower conical distribution plate from the distribution plate, and so on until the lump ore slides to a material collection chamber from the lowest distribution plate. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes on the sieve plates of the distribution plates of all layers and is discharged from the powder discharge openings of all layers. The material collection chamber is provided with a heat medium inlet, each layer of distribution plate is provided with a heat medium outlet, and the heat medium outlet is positioned on the side wall of the lump ore storage bin between the sieve plate and the support plate of each layer of distribution plate. Preferably, the heat medium outlet coincides with the powder discharge port. The heat medium enters the lump ore storage bin from a heat medium inlet on the material collecting chamber, directly contacts with the lump ore for heat exchange, upwards passes through the air holes on each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, and is discharged from a heat medium outlet on each layer of distribution plate.
Preferably, the system further comprises a thermal medium guiding device. The heat medium flow guiding device is arranged in the material collecting chamber, and a heat medium flow guiding inlet and a heat medium flow guiding outlet are formed in the heat medium flow guiding device. And a heat medium inlet of the lump ore storage bin is communicated with a heat medium diversion inlet. Preferably, 1-20 heat medium diversion devices, preferably 2-5 heat medium diversion devices are arranged in the material collection chamber. And the heat medium diversion inlets of all the heat medium diversion devices are communicated with the heat medium inlet.
The utility model discloses in, be equipped with hot medium guiding device in the lump ore storage silo for the hot medium distributes evenly in the lump ore storage silo, and the contact of hot medium and lump ore is more abundant, reduces the moisture content in the lump ore more effectively. The lump ore is fully contacted with the heat medium, the drying effect of the lump ore is improved, and the moisture content in the lump ore before entering the blast furnace meets the requirement, so that the energy consumption of the blast furnace is reduced, the normal operation of blast furnace procedures is ensured, the quality of blast furnace products is improved, and the production cost is saved. The heat medium flow guiding device can adopt a structure of one (or a plurality of) heat medium flow guiding inlets and a plurality of heat medium flow guiding outlets, so that the dispersity of the heat medium is improved.
Preferably, the system further comprises a dust removal system, and the heat medium outlet is communicated to the dust removal system through a heat medium discharge pipeline.
Preferably, a first moisture detection device is arranged at a lump ore feed inlet on the lump ore storage bin.
Preferably, a second moisture detection device is arranged at the lump ore discharge port of the lump ore storage bin.
According to the utility model provides a second embodiment provides a lump ore pretreatment methods based on distribution plate angular adjustment.
A lump ore pretreatment method based on distribution plate angle adjustment comprises the following steps:
1) conveying the lump ore to be treated to a lump ore storage bin, and introducing a heat medium into the lump ore storage bin.
2) The lump ore passes through each layer of distribution plate in the lump ore storage bin to uniformly contact with a heat medium from bottom to top, and gas-solid heat exchange is carried out to obtain dry lump ore.
According to the utility model provides a third embodiment provides a lump ore pretreatment methods based on distribution plate angular adjustment.
A lump ore pretreatment method based on distribution plate angle adjustment comprises the following steps:
1) conveying the lump ore to be treated to a lump ore storage bin, and introducing a heat medium into the lump ore storage bin.
2) The lump ore passes through the heat medium channel and each layer of distribution plate in the lump ore storage bin and is uniformly contacted with the heat medium from bottom to top to carry out gas-solid heat exchange. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes on the sieve plates of the distribution plates of all layers and is discharged from the powder discharge openings of all layers. Thereby obtaining the dried large-particle-size lump ore.
Preferably, the method further comprises the steps of:
A) before the lump ore to be processed is conveyed to the lump ore storage bin, the lump ore storage bin is subjected to furnace baking treatment by adopting a heat medium, and the lump ore storage bin is preheated by the heat medium.
Preferably, the method further comprises the steps of:
3) and after heat exchange is carried out between the heat medium and the lump ore in the lump ore storage bin, the heat medium is discharged from the lump ore storage bin, and the discharged heat medium is conveyed to the dust removal system.
4) And conveying the dried large-particle-size lump ore obtained after drying and screening treatment to a blast furnace.
Preferably, a first moisture detection device is arranged at the lump ore feed inlet of the lump ore storage bin. Detecting the moisture content in the iron ore block to be treated entering the block ore storage bin through a first moisture detection device, and recording the moisture content as W0% of the amount of the compound (b). Setting the upper limit of the water content of the lump ore entering the blast furnace as W according to the condition requirements of the blast furnacemax% of the amount of the compound (b). And calculating the retention time t, h of the iron ore lump ore in the lump ore storage bin.
Figure DEST_PATH_GDA0003315409350000061
Wherein: vMediumThe flow rate of the heat medium, m/s; t isMediumThe temperature of the heat medium entering the lump ore storage bin is DEG C; k is a radical of1The retention time is a retention time adjusting constant, and the value is 0.1-1, preferably 0.2-0.8, and more preferably 0.3-0.6;
at a flow velocity V of the heat mediumMediumThe temperature of the heat medium entering the lump ore storage bin is TMediumUnder the condition, the angle between the sieve plate and the side wall of the lump ore storage bin is adjusted by an angle adjusting device arranged at the joint of the sieve plate and the side wall of the lump ore storage bin, so that the retention time of the iron ore lump ore in the lump ore storage bin is t,further controlling the water content in the granular iron ore blocks discharged from the block ore discharge port of the block ore storage bin to be lower than Wmax。
Preferably, a first moisture detection device is arranged at the lump ore feed inlet of the lump ore storage bin, and an initial included angle between the sieve plate and the side wall of the lump ore storage bin is set to be theta0And (c) degree. The first moisture detection device detects the moisture content in the lump ore entering the lump ore storage bin and records as x1. Setting the upper limit of the water content of the lump ore entering the blast furnace as W according to the condition requirements of the blast furnacemax% of the amount of the compound (b). Judgment of x1And WmaxThe real-time included angle theta between the sieve plate and the side wall of the lump ore storage bin is adjusted by an angle adjusting device arranged at the joint of the sieve plate and the side wall of the lump ore storage bin1And (c) degree. The method comprises the following steps:
when x is1≤WmaxWhen the heat medium is conveyed into the lump ore storage bin, the heat medium is stopped being conveyed into the lump ore storage bin;
when x is1When not less than 10%, theta1＝[1+k2·(x1-10％)]×θ0；
When 10% > x1At > 6%, θ1＝θ0；
When W ismax＜x1When the content is less than or equal to 6 percent, theta1＝[1-k3·(6％-x1)]×θ0；
Wherein k is2、k3Is an angle adjustment coefficient, k2Has a value range of 3-8, k3The value range of (1) to (5); wmaxLess than or equal to 4 percent; real-time detection of x1And adjusting the real-time included angle between the sieve plate and the side wall of the lump ore storage bin to be theta through an angle adjusting device1Drying the lump ore by the heat medium in the lump ore storage bin to ensure that the water content of the lump ore is lower than W before entering the blast furnacemax。
Preferably, a second moisture detection device is arranged at the lump ore discharge port of the lump ore storage bin, and an initial included angle between the sieve plate and the side wall of the lump ore storage bin is set to be theta0And (c) degree. The second moisture detection device detects the moisture content in the lump ore discharged from the lump ore storage bin and marks as x2. According toSetting the upper limit of the water content of lump ore entering the blast furnace to be W according to the requirements of blast furnace conditionsmax% of the amount of the compound (b). Judgment of x2And WmaxThe real-time included angle theta between the sieve plate and the side wall of the lump ore storage bin is adjusted by an angle adjusting device arranged at the joint of the sieve plate and the side wall of the lump ore storage bin2And (c) degree. The method comprises the following steps:
when x is2≥WmaxWhen theta is greater than theta2＝[1+k4·(x2-Wmax)]×θ0；
When 50% Wmax＜x2＜WmaxWhen theta is greater than theta2＝θ0；
When x is2≤50％WmaxWhen the temperature of the water is higher than the set temperature,
Figure DEST_PATH_GDA0003315409350000071
wherein k is4、k5Is an angle adjustment coefficient, k4Has a value range of 3-5, k5The value range of (1) to (3); wmaxLess than 6 percent; real-time detection of x2And adjusting the real-time included angle between the sieve plate and the side wall of the lump ore storage bin to be theta through an angle adjusting device2Drying the lump ore by the heat medium in the lump ore storage bin to ensure that the water content of the lump ore is lower than W before entering the blast furnacemax。
Preferably, the heat medium is a heat source generated by the steel process itself. Preferably, the heat medium is a heat source released by combustion of sintering circular cooler hot exhaust gas, blast furnace hot blast stove exhaust gas, coke oven gas/blast furnace gas/converter gas, and is preferably sintering circular cooler hot exhaust gas or blast furnace hot blast stove exhaust gas.
Preferably, the temperature of the thermal medium entering the lump ore storage bin is greater than 100 ℃, preferably greater than 150 ℃.
Preferably, the air velocity of the heat medium entering the lump ore storage bin is 0.01-3 m/s, preferably 0.02-1 m/s, and more preferably 0.03-0.5 m/s.
Preferably, the included angle between the sieve plate of the distribution plate and the side wall of the lump ore storage bin is 10-85 degrees, and preferably 20-80 degrees.
Preferably, the residence time of the lump ore in the lump ore storage bin is 0.5-24 h, preferably 1-12 h, and more preferably 2-8 h.
Preferably, the particle size of the large-particle-size lump ore is more than 5mm, preferably more than 6mm, and more preferably more than 8 mm.
The utility model provides a lump ore pretreatment systems and method based on distributing plate. The utility model discloses to the big, the many difficult problem of powder of moisture that natural lump ore exists, provided and directly adopted the lump ore storage silo to carry out dry pretreatment system and method. Drying pretreatment is carried out on the lump ore in a lump ore bin to remove moisture of the lump ore, and a heat source required for drying is preferably hot waste gas from a steel mill (such as hot waste gas generated by a blast furnace). The utility model provides a pretreatment methods is simple and easy, practical, reliable, does benefit to the engineering and popularizes and applies, compares with traditional drum drying process, the utility model discloses a ripe lump ore storage silo carries out dry pretreatment techniques, because the lump ore storage silo is a confined environment relatively, and the moisture desorption of lump ore is efficient, has solved the lump ore and has gone into stove (blast furnace) difficult problem, has improved the stove proportion and the gas permeability level of going into of blast furnace lump ore, has effectively reduced blast furnace manufacturing cost, has improved the blast furnace level of going forward. The popularization of the utility model has good economic, social and environmental benefits, and is expected to open up a more stable and efficient way for the development of the lump ore pretreatment process in China.
The utility model discloses in, natural lump ore carries to lump ore storage silo through lump ore raw materials conveyor, carries out drying and screening simultaneously in lump ore storage silo, reduces the moisture content in the lump ore, will attach to the powder screening on the lump ore simultaneously. And then conveying the lump ore subjected to particle size screening and water content reduction in the lump ore storage bin to a blast furnace for smelting.
The utility model discloses in, be equipped with the hot medium passageway in the lump ore storage silo, all be equipped with the gas pocket of heating medium circulation on the conical surface of each layer toper distributing plate of hot medium passageway for the hot medium distributes evenly in the lump ore storage silo, and the contact of hot medium and lump ore is more abundant, the more effectual moisture content that reduces in the lump ore. And then the moisture content in the lump ore before entering the blast furnace meets the requirement, thereby reducing the energy consumption of the blast furnace, ensuring the normal operation of the blast furnace process, improving the quality of blast furnace products and saving the production cost.
In the present invention, the heat medium may be hot exhaust gas with a high temperature or hot air after heat treatment. Generally, the temperature of the heat medium is higher than 100 ℃.
The utility model discloses in, utilize lump ore storage silo as place and the device to the dry process of lump ore, make full use of current equipment resource realizes the dehydration process of lump ore, does not additionally increase new equipment. Only a heat medium inlet and a heat medium outlet are required to be arranged on the original lump ore storage bin.
In the utility model, aiming at the problems of large moisture content in lump ore and low addition amount as the raw material of the blast furnace, the lump ore storage bin is adopted to carry out drying pretreatment on the lump ore, and a heat medium is conveyed to the lump ore storage bin; in the lump ore storage bin, the heat medium dries the lump ore, the moisture in the lump ore is evaporated and taken away, and the moisture is discharged out of the lump ore storage bin along with the heat medium after heat exchange, so that the aim of drying the lump ore is fulfilled.
Preferably, before the lump ore to be processed is conveyed to the lump ore storage bin, the lump ore storage bin is preheated by the heat medium, so that the internal temperature of the lump ore storage bin is increased, when the lump ore with high moisture content enters the lump ore storage bin, moisture is condensed, and the drying effect of the lump ore in the lump ore storage bin is further improved.
Preferably, after the heat medium exchanges heat with the lump ore in the lump ore storage bin, the heat medium takes away the moisture in the lump ore, and meanwhile, the heat medium can remove dust on the surface of the lump ore, so that the content of the dust in the lump ore storage bin is reduced, the air permeability of the heat medium in the lump ore storage bin is increased, and the drying efficiency is improved. Preferably, the heat medium discharged from the lump ore storage bin is subjected to dust removal treatment by a dust removal system, so that the pollution of the discharged heat medium to the environment is reduced. Meanwhile, the dust particles collected by the dust removal system can be used as sintering raw materials, and resource recycling is realized.
The utility model discloses in, set up first moisture detection device through the material feed inlet position at lump ore storage silo, moisture content in the lump ore that first moisture detection device detected to get into lump ore storage silo sets for the moisture content upper limit that gets into the lump ore in blast furnace to be Wmax% of the amount of the compound (b). The residence time of the iron ore lump ore in the lump ore storage bin can be accurately known through calculation, so that the moisture content of the lump ore before entering the blast furnace is lower than Wmax。
The utility model discloses in, be equipped with first moisture detection device in lump ore feed inlet department of lump ore storage silo, set for the initial contained angle that forms between sieve and the lump ore storage silo lateral wall, moisture content in the lump ore that first moisture detection device detected to get into lump ore storage silo sets for the moisture content upper limit that gets into the lump ore in the blast furnace to be Wmax% of the amount of the compound (b). Comparing the detected water content in the lump ore at the feed inlet with the upper limit of the water content of the lump ore entering the blast furnace, and adjusting an included angle formed between the sieve plate and the lump ore storage bin, thereby ensuring that the water content of the lump ore before entering the blast furnace is lower than Wmax。
The utility model discloses in, be equipped with second moisture detection device in lump ore discharge gate department of lump ore storage silo, set for the initial contained angle that forms between sieve and the lump ore storage silo lateral wall, the moisture content in the second moisture detection device detection lump ore storage silo discharge lump ore is set for the moisture content upper limit that gets into the lump ore in the blast furnace to be WmaxComparing the detected water content in the lump ore at the discharge port with the upper limit of the water content of the lump ore entering the blast furnace, and adjusting an included angle formed between the sieve plate and the side wall of the lump ore storage bin, thereby ensuring that the water content of the lump ore before entering the blast furnace is lower than Wmax。
The drying treatment of the lump ore in the storage bin by utilizing the hot waste gas in the steel process is feasible, the moisture of the charged lump ore can be effectively reduced, the energy consumption required by drying can be greatly reduced, and the charging proportion of the dried lump ore can be improved to a certain extent, so that the smelting cost of the blast furnace is reduced.
The problem that lump ore is not uniformly contacted with a heat medium in a lump ore storage bin is solved, the lump ore exists in the storage bin in a stacking state, particularly fine-grained materials exist, so that the air permeability of the whole materials of the storage bin is deviated, hot air flow cannot smoothly penetrate through a material body, the drying effect is poor, and the temperature of the upper part of the storage bin is lower than the dew point temperature of moisture, so that water vapor is easily condensed, and the dust removal system is damaged. The utility model discloses a to the shortcoming that lump ore deposit stoving exists in the storage silo, top-down sets up the multilayer distributing plate on the inner wall of storage silo, and the distributing plate includes the sieve on upper portion and the backup pad of lower part. Preferably, the central axis of the lump ore storage bin is provided with a heat medium channel, the heat medium channel is provided with a plurality of layers of conical distribution plates from top to bottom, and the conical surfaces of the conical distribution plates are provided with air holes for circulating heat supply media. Lump ore falls into the heat exchange chamber, firstly falls onto the conical distribution plate at the top of the heat medium channel, and falls onto the distribution plate on the side wall of the lump ore storage bin from the edge of the conical distribution plate at the top, then falls onto the conical distribution plate at the lower layer from the distribution plate, and so on until the lump ore falls into the material collection chamber from the distribution plate at the lowest layer. The heat medium inlet is arranged on the material collecting chamber, and the heat medium outlet is arranged above the heat exchange chamber. The heat medium enters the lump ore storage bin from a heat medium inlet on the material collecting chamber, directly contacts with the lump ore in the heat exchange chamber for heat exchange, then upwards passes through the distribution plates on each layer and the air holes on the conical distribution plates on each layer on the heat medium channel, and is discharged from a heat medium outlet on the heat exchange chamber. Thereby enhancing heat exchange between the gas and the solid. The air current is discharged to the dust pelletizing system from the upper part, the hot air current is fully distributed in the whole storage bin, the contact effect of the hot air current and lump ore is improved, the air permeability of the bin body is improved, and the drying effect is enhanced.
As preferred, the utility model discloses in set up the multilayer distributing plate in lump ore storage silo heat exchange chamber, wherein all be equipped with the sieve mesh on the sieve of every layer of distributing plate, the sieve of every layer of distributing plate can both play the screening effect promptly. The junction of the supporting plate of each layer of distribution plate and the side wall of the lump ore storage bin is provided with a powder discharge port. Under the condition that sieve holes are arranged on the sieve plates of the distribution plates, gaps between the sieve plates and the support plates of each layer of the distribution plates form powder blanking channels. The lump ore enters the lump ore storage bin, and while the lump ore is dried in the bin, powder attached to the lump ore enters the powder blanking channel through sieve pores on the sieve plates of the distribution plates of all layers and is then discharged from powder discharge ports of all layers. In the scheme, on one hand, the arrangement of the plurality of layers of the distribution plates in the lump ore storage bin prolongs the contact time of the heat medium and the lump ore, the contact is more uniform, the contact effect is better, the heat exchange between the heat medium and the lump ore is enhanced, and the drying effect is enhanced; on the other hand, when the drying effect of lump ore in the lump ore storage bin is improved, the multistage screening of the lump ore is realized through the arrangement of the sieve pores and the powder blanking channels on the distribution plates of all layers, namely, the powder attached to the lump ore is removed while the drying quality is ensured, and the integration of screening and drying is really realized. Generally speaking, the screening efficiency of lump ore after drying is higher, and the classification effect is better, and the lump ore after the screening is dried again, and its stoving effect also can be better, that is to say the utility model discloses in, the lump ore is sieved and is gone on simultaneously with the stoving process on the distributing plate of lump ore storage silo, and screening and stoving can play the promotion effect each other, and on the basis that single process was handled, the effect of screening and stoving is further strengthened. The utility model discloses a all be equipped with the powder bin outlet on each layer distributing plate, the powder that can in time will screen out is discharged, and then reduces dry cost, the energy saving. In this scheme, the size of sieve mesh is generally 5 ~ 20mm, preferably 6 ~ 15mm, more preferably 7 ~ 10mm, and the concrete size of sieve mesh can be adjusted as required according to operating condition. The mesh size of the sieve plate of each layer of distribution plate can also be set to different sizes as required, for example, the mesh size of the upper layer of distribution plate can be larger than the mesh size of the lower layer of distribution plate in consideration of the difference of moisture content and viscosity of the lump ore at different positions, thereby realizing the step sieving of the lump ore. In addition, the sieve mesh size of each layer of distribution plate is different, can be so that the powder of different granularities is sieve from different sieve meshes priority, avoids granule to compete mutually and gets into the sieve mesh and lead to the problem that screening efficiency is low.
Preferably, the heat medium outlet of the present invention may not be disposed above the material exchange chamber. The thermal medium outlet is arranged on the side wall of the lump ore storage bin between the upper sieve plate and the lower support plate of the distribution plate. Each layer of distribution plate is provided with a heat medium outlet. The heat medium enters the lump ore storage bin from a heat medium inlet on the material collecting chamber, directly contacts with the lump ore for heat exchange, upwards passes through the air holes on each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, and is discharged through a heat medium outlet on each layer of distribution plate. Can set up an updraft ventilator respectively in each layer hot medium exit, also can set up a total exhaust system, this exhaust system passes through pipeline and each layer hot medium export intercommunication. The hot medium enters the lump ore storage bin, and after directly contacting and exchanging heat with the lump ore, the air draft system extracts the hot medium from each layer of hot medium outlets. When the heat medium uniformly distributed in each layer of distribution plate is pumped out, the heat medium can pass through the sieve holes on the upper sieve plate of the layer of distribution plate, enter the powder blanking channel and then be discharged through the heat medium outlet. In this scheme, hot medium can pass through the sieve mesh at the exhaust in-process, and the air current passes from the sieve mesh, is favorable to bringing the powder attached to on the lump ore into the powder unloading passageway under the sieve mesh, and then strengthens the screening effect of distribution plate to the lump ore, and the gas permeability of whole lump ore storage silo obtains greatly improving, promotes screening and stoving effect from this. Further preferably, the thermal medium outlet of each layer of distribution plate may coincide with the position of the powder discharge port. The heat medium outlet is arranged at the powder discharge port, and in the process of heat medium discharge, the heat medium can also play a role in drainage, so that screened fine powder materials are taken out of the lump ore storage bin together, and the energy consumption of the system is reduced.
The utility model discloses in, change the contained angle that distribution plate sieve and lump ore storage silo lateral wall formed through angle adjusting device to change the material and get into drying and screening time in the storehouse again behind the lump ore storage silo, reduce the system energy consumption as far as possible under the prerequisite of guaranteeing dry effect.
Adopt the technical scheme provided by the utility model, can increase the interpolation proportion of lump ore in the blast furnace raw materials, through the experiment, adopt the utility model discloses a technical scheme, its addition can reach 30%. Greatly increases the dosage ratio of the lump ore in the blast furnace process, thereby reducing the operation cost of the blast furnace.
In the present invention, the height of the lump ore storage silo is 3-100m, preferably 5-80m, more preferably 10-50 m.
In the present invention, the ratio of the height of the heat exchange chamber to the length of the heat medium passage is 1:0.2 to 1, preferably 1:0.5 to 0.9, more preferably 1:0.6 to 0.8.
Compared with the prior art, the technical scheme of the utility model following beneficial technological effect has:
1. the utility model adopts the lump ore storage bin to dry the lump ore, and heat medium is conveyed to the lump ore storage bin; in the lump ore storage bin, the heat medium dries the lump ore, the moisture in the lump ore is evaporated and taken away, and the moisture is discharged out of the lump ore storage bin along with the heat medium after heat exchange, so that the aim of drying the lump ore is fulfilled.
2. The utility model discloses a to the shortcoming that the lump ore exists in the storage silo stoving, add the multilayer distributing plate at the storage silo inner wall, the lump ore rolls from each layer distributing plate and passes through, and the hot medium carries out direct heat transfer and indirect heat transfer with the lump ore simultaneously, has improved the drying effect of lump ore in the lump ore storage silo greatly; meanwhile, each layer of distribution plate is provided with a sieve mesh, a powder discharging channel and a powder discharging port, so that the multi-stage screening of the lump ore by each layer of distribution plate is realized, and small particle materials attached to the lump ore are discharged through the powder discharging ports of each layer in time, thereby reducing the drying cost and saving energy.
3. The utility model discloses a set up angle adjusting device on the distributing plate, through the contained angle control material that changes sieve and lump ore storage silo lateral wall dry and screening time in the lump ore storage silo, reduce the system energy consumption as far as under the prerequisite of guaranteeing drying effect, improve the quality of blast furnace result, practice thrift manufacturing cost simultaneously.
4. The utility model adds a heat medium channel on the central axis of the lump ore storage bin, the heat medium channel is provided with a plurality of layers of conical distribution plates, and the conical surfaces of the conical distribution plates are provided with air holes for the circulation of heat medium, so that the heat medium is uniformly distributed in the lump ore storage bin; the lump ore entering the lump ore storage bin rolls between each layer of distribution plate and each layer of conical distribution plate on the heat medium channel, so that the air permeability in the lump ore storage bin is improved, the lump ore is more fully contacted with the heat medium, and the moisture content in the lump ore is more effectively reduced.
5. The utility model integrates the screening and drying of the lump ore, improves the air permeability of the material layer in the lump ore storage bin after synchronous screening, and is beneficial to improving the drying efficiency; correspondingly, the fluidity of the materials after synchronous drying is improved, and the screening efficiency is improved; therefore, mutual promotion is realized, and the screening efficiency and the drying efficiency are improved.
Drawings
Fig. 1 is a schematic structural diagram of a lump ore pretreatment system based on distribution plate angle adjustment according to the present invention;
FIG. 2 is a schematic structural diagram of a distribution plate according to an embodiment of the present invention;
FIG. 3 is a schematic structural view of a heat medium passage provided in an embodiment of the present invention;
fig. 4 is a schematic structural view of a lump ore storage bin in an embodiment of the present invention;
FIG. 5 is a schematic structural view of sieve pores on the distribution plate according to the embodiment of the present invention;
FIG. 6 is a schematic structural view of the heat medium outlets provided on the distribution plates of each layer according to the embodiment of the present invention;
fig. 7 is a schematic structural view of a lump ore storage bin provided with a thermal medium flow guide device and a detection device according to an embodiment of the present invention;
fig. 8 is a schematic structural view of a heat medium flow guiding device according to an embodiment of the present invention.
Reference numerals: 1: a lump ore storage bin; 101: a distribution plate; 10101: a sieve plate; 1010101: screening holes; 10102: a support plate; 10103: an angle adjusting device; 10104: a powder discharge opening; 102: a lump ore feed inlet; 103: discharging a lump ore; 104: a heat medium inlet; 105: a thermal medium outlet; 106: a heat exchange chamber; 107: a material collection chamber; 108: a thermal medium passage; 10801: a conical distribution plate; 10802: air holes; 109: a thermal medium flow guide device; 10901: a heat medium diversion inlet; 10902: a heat medium diversion outlet; 2: a blast furnace; 301: a first moisture detection device; 302: a second moisture detection device; 4: a dust removal system; d1: a lump ore conveying device; l1: a thermal medium delivery conduit; l2: the heat medium is discharged out of the pipe.
Detailed Description
The technical solution of the present invention is illustrated below, and the claimed invention includes but is not limited to the following embodiments.
According to the utility model provides a first embodiment provides a lump ore pretreatment systems based on distribution plate angular adjustment.
The utility model provides a lump ore pretreatment systems based on distribution plate angle adjustment, this system includes lump ore conveyor D1, lump ore storage silo 1, thermal medium pipeline L1. The lump ore storage bin 1 is provided with a lump ore feeding port 102, a lump ore discharging port 103, a heat medium inlet 104 and a heat medium outlet 105. The lump ore conveyor D1 is connected to the lump ore feed inlet 102 of the lump ore storage bin 1. The heat medium delivery pipe L1 is connected to the heat medium inlet 104; the lump ore discharge port 103 is connected to the feed port of the blast furnace 2. The inside distributing plate 101 that is equipped with of lump ore storage silo 1, distributing plate 101 and the lateral wall of lump ore storage silo 1 are connected. The distribution plate 101 is provided with an angle adjusting device 10103. Wherein: the height of the lump ore storage bin 1 is 3-100 m.
Preferably, the distribution plate 101Comprises a sieve plate 10101 and a support plate 10102. One end of sieve 10101 and the one end of backup pad 10102 are connected with the lateral wall of lump ore storage silo 1 respectively, and sieve 10101 sets up in the top of backup pad 10102, and the downward sloping setting of sieve 10101, and backup pad 10102 tilt up sets up, and the other end of sieve 10101 and the other end interconnect of backup pad 10102, preferably swing joint. A lump ore blanking channel is reserved in the central axis position of the lump ore storage bin 1 of the distribution plate 101. Preferably, the sieve plate 10101, the support plate 10102 and the side wall of the lump ore storage bin 1 form a triangular structure in the vertical cross section. Preferably, an angle adjusting device 10103 is arranged at the joint of the sieve plate 10101 and the side wall of the lump ore storage bin 1.
Preferably, 1-20 layers of the distribution plate 101 are arranged in the lump ore storage bin 1 from top to bottom, 2-10 layers of the distribution plate 101 are preferably arranged, and 3-8 layers of the distribution plate 101 are more preferably arranged. An angle adjusting device 10103 is arranged on each layer of the distribution plate 101. Preferably, the size of the lump ore blanking channel is more than 5mm, preferably more than 6mm, and more preferably more than 8 mm.
Preferably, a heat medium channel 108 is also provided at the lump ore blanking channel. A conical distributor plate 10801 is also provided in the thermal medium passage 108. The air holes 10802 are formed on the tapered surface of the tapered distribution plate 10801.
Preferably, the heat medium channel 108 is provided with 1 to 20 layers of tapered distribution plates 10801, preferably 2 to 10 layers of tapered distribution plates 10801, and more preferably 3 to 8 layers of tapered distribution plates 10801 from top to bottom. Air holes are uniformly formed on the conical surface of each layer of conical distribution plate 10801. Preferably, the number of layers of the conical distribution plate 10801 on the heat medium channel 108 is the same as the number of layers of the distribution plate 101 on the side wall of the lump ore storage bin 1. The tapered distribution plate 10801 is disposed above the distribution plate 101 at the same level.
Preferably, sieve 10101 of each layer of distribution plate 101 is provided with sieve holes 1010101. Preferably, each layer of distribution plate 101 is provided with a powder discharge port 10104. The powder discharge port 10104 is arranged on the side wall of the lump ore storage bin 1 and is connected with the supporting plate 10102 of the distribution plate 101. The gap between the sieve plate 10101 and the support plate 10102 of each layer of distribution plate 101 forms a powder blanking channel.
Preferably, the size of the sieve opening 1010101 is 5-20 mm, preferably 6-15 mm, and more preferably 7-10 mm.
Preferably, the upper part of the lump ore storage bin 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage bin 1 is a material collection chamber 107. The lump ore feed inlet 102 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, firstly rolls to the tapered distribution plate 10801 at the top of the heat medium channel 108, and rolls to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the tapered distribution plate 10801 at the top, then slides to the tapered distribution plate 10801 at the lower layer from the distribution plate 101, and so on until the lump ore slides to the material collection chamber 107 from the distribution plate 101 at the lowest layer. The heat medium inlet is provided on the material collecting chamber 107, and the heat medium outlet 105 is provided on the side or upper portion of the heat exchange chamber 106. The heat medium enters the lump ore storage bin 1 from the heat medium inlet 104 on the material collection chamber 107, directly contacts with the lump ore for heat exchange, upwards passes through the air holes 10802 on each layer of the distribution plate 101 and each layer of the conical distribution plate 10801 on the heat medium channel 108, and is discharged from the heat medium outlet 105 on the heat exchange chamber 106.
Preferably, the upper part of the lump ore storage bin 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage bin 1 is a material collection chamber 107. The lump ore feed inlet 102 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, firstly rolls to the tapered distribution plate 10801 at the top of the heat medium channel 108, and rolls to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the tapered distribution plate 10801 at the top, then slides to the tapered distribution plate 10801 at the lower layer from the distribution plate 101, and so on until the lump ore slides to the material collection chamber 107 from the distribution plate 101 at the lowest layer. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes 1010101 on the sieve plate 10101 of each layer of the distribution plate 101 and is discharged from the powder discharge ports 10104 of each layer; the heat medium inlet is provided on the material collecting chamber 107, and the heat medium outlet 105 is provided on the side or upper portion of the heat exchange chamber 106. The heat medium enters the lump ore storage bin 1 from the heat medium inlet 104 on the material collection chamber 107, directly contacts with the lump ore for heat exchange, upwards passes through the air holes 10802 on each layer of the distribution plate 101 and each layer of the conical distribution plate 10801 on the heat medium channel 108, and is discharged from the heat medium outlet 105 on the heat exchange chamber 106.
Preferably, the upper part of the lump ore storage bin 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage bin 1 is a material collection chamber 107. The lump ore feed inlet 102 of the lump ore storage silo 1 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: the lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, and the lump oreFirstly roll to the conical distribution plate 10801 at the top of the thermal medium channel 108, roll to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the conical distribution plate 10801 at the top, then slide from the distribution plate 101 to the conical distribution plate 10801 at the lower layer, and so on until the lump ore slides from the distribution plate 101 at the lowest layer into the material collection chamber 107. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes 1010101 on the sieve plates 10101 of the distribution plates 101 in each layer and is then discharged through the powder discharge openings 10104 in each layer. The material collection chamber 107 is provided with a heat medium inlet 104, each layer of distribution plate 101 is provided with a heat medium outlet 105, and the heat medium outlet 105 is positioned on the side wall of the lump ore storage bin 1 between the sieve plate 10101 and the support plate 10102 of each layer of distribution plate 101. Preferably, the heat medium outlet 105 coincides with the powder discharge port 10104. Inlet of thermal medium from the material collection chamber 107104Enters the lump ore storage bin 1, directly contacts with the lump ore for heat exchange, then upwards passes through the air holes 10802 on the conical distribution plates 10801 on each layer of the distribution plates 101 and the heat medium channel 108 and is discharged from the heat medium outlets on the distribution plates 101 on each layer105And (4) discharging.
Preferably, the system further comprises a thermal medium guiding device 109. The heat medium flow guiding device 109 is arranged in the material collecting chamber 107, and a heat medium flow guiding inlet 10901 and a heat medium flow guiding outlet 10902 are arranged on the heat medium flow guiding device 109. Thermal medium inlet of lump ore storage bin 1104Communicating with the heat medium introduction inlet 10901. Preferably, 1 to 20 of the heat medium guiding devices 109, preferably 2 to 5 of the heat medium guiding devices 109 are arranged in the material collection chamber 107. All the heat medium flow guide inlets 10901 of the heat medium flow guide devices 109 are identical to the heat medium inlet104And (4) communicating.
Preferably, the system further comprises a dust removal system 4, a heat medium outlet105Is communicated to the dust removing system 4 through a hot medium discharge pipe L2.
Example 1
As shown in fig. 1, the lump ore pretreatment system for adjusting the angle of the distribution plate comprises a lump ore conveying device D1, a lump ore storage bin 1 and a heat medium conveying pipeline L1. The lump ore storage bin 1 is provided with a lump ore feeding hole 102, a lump ore discharging hole 103, a heat medium inlet 104 and a heat medium outlet 105; the lump ore conveyor D1 is connected to the lump ore feed inlet 102 of the lump ore storage bin 1. The heat medium delivery pipe L1 is connected to the heat medium inlet 104; the lump ore discharge port 103 is connected to the feed port of the blast furnace 2. The inside distributing plate 101 that is equipped with of lump ore storage silo 1, distributing plate 101 and the lateral wall of lump ore storage silo 1 are connected. The distribution plate 101 is provided with an angle adjusting device 10103. Wherein: the height of the lump ore storage bin 1 is 20 m.
Example 2
Example 1 was repeated, except that the distribution plate 1 was as shown in FIG. 201Comprises a sieve plate 10101 and a support plate 10102. One end of sieve 10101 and the one end of backup pad 10102 are connected with the lateral wall of lump ore storage silo 1 respectively, and sieve 10101 sets up in the top of backup pad 10102, and the downward sloping of sieve 10101 sets up, and backup pad 10102 tilt up sets up, the other end of sieve 10101 and the other end swing joint of backup pad 10102. A lump ore blanking channel is reserved in the central axis position of the lump ore storage bin 1 of the distribution plate 101. The sieve plate 10101, the support plate 10102 and the side wall of the lump ore storage bin 1 form a triangular structure in the cross section in the vertical direction. An angle adjusting device 10103 is arranged at the joint of the sieve plate 10101 and the side wall of the lump ore storage bin 1.
The lump ore storage bin 1 is internally provided with 3 layers of the distribution plates 101 from top to bottom, and each layer of the distribution plates 101 is provided with an angle adjusting device 10103. The size of the lump ore blanking channel is 10 mm.
Example 3
As shown in fig. 3, the embodiment 2 is repeated except that a heat medium channel 108 is further provided at the lump ore blanking channel. A conical distributor plate 10801 is also provided in the thermal medium passage 108. The air holes 10802 are formed on the tapered surface of the tapered distribution plate 10801.
The heat medium channel 108 is provided with a plurality of layers of conical distribution plates 10801 from top to bottom, and the conical surface of each layer of conical distribution plate 10801 is uniformly provided with air holes. The tapered distribution plate 10801 is disposed above the distribution plate 101 at the same level.
Example 4
Example 3 is repeated except that each layer of the sieve plate 10101 of the distribution plate 101 is provided with sieve holes 1010101. Each layer of distribution plate 101 is provided with a powder discharge port 10104. The powder discharge port 10104 is arranged on the side wall of the lump ore storage bin 1 and is connected with the supporting plate 10102 of the distribution plate 101. The gap between the sieve plate 10101 and the support plate 10102 of each layer of distribution plate 101 forms a powder blanking channel.
The size of the sieve hole 1010101 is 8 mm.
Example 5
As shown in fig. 4, example 3 is repeated except that the upper part of the lump ore storage silo 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage silo 1 is a material collection chamber 107. The lump ore feed inlet 102 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, firstly rolls to the tapered distribution plate 10801 at the top of the heat medium channel 108, and rolls to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the tapered distribution plate 10801 at the top, then slides to the tapered distribution plate 10801 at the lower layer from the distribution plate 101, and so on until the lump ore slides to the material collection chamber 107 from the distribution plate 101 at the lowest layer. The heat medium inlet is arranged in the material collection chamber 107 and the heat medium outlet 105 is arranged in the upper part of the heat exchange chamber 106. The heat medium enters the lump ore storage bin 1 from the heat medium inlet 104 on the material collection chamber 107, directly contacts with the lump ore for heat exchange, upwards passes through the air holes 10802 on each layer of the distribution plate 101 and each layer of the conical distribution plate 10801 on the heat medium channel 108, and is discharged from the heat medium outlet 105 on the heat exchange chamber 106.
Example 6
As shown in fig. 5, example 4 is repeated except that the upper part of the lump ore storage silo 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage silo 1 is a material collection chamber 107. The lump ore feed inlet 102 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, firstly rolls to the tapered distribution plate 10801 at the top of the heat medium channel 108, and rolls to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the tapered distribution plate 10801 at the top, then slides to the tapered distribution plate 10801 at the lower layer from the distribution plate 101, and so on until the lump ore slides to the material collection chamber 107 from the distribution plate 101 at the lowest layer. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes 1010101 on the sieve plates 10101 of the distribution plates 101 in each layer and is then discharged through the powder discharge openings 10104 in each layer. The heat medium inlet is arranged in the material collection chamber 107 and the heat medium outlet 105 is arranged in the upper part of the heat exchange chamber 106. The heat medium enters the lump ore storage bin 1 from the heat medium inlet 104 on the material collection chamber 107, directly contacts with the lump ore for heat exchange, upwards passes through the air holes 10802 on each layer of the distribution plate 101 and each layer of the conical distribution plate 10801 on the heat medium channel 108, and is discharged from the heat medium outlet 105 on the heat exchange chamber 106.
Example 7
As shown in fig. 6, example 4 is repeated except that the upper part of the lump ore storage silo 1 is a heat exchange chamber 106 provided with a distribution plate 101 and a heat medium channel 108, and the lower part of the lump ore storage silo 1 is a material collection chamber 107. The lump ore feed inlet 102 of the lump ore storage silo 1 is arranged on the heat exchange chamber 106, and the lump ore discharge outlet 103 is arranged on the material collection chamber 107. Wherein: lump ore enters the heat exchange chamber 106 of the lump ore storage bin 1 from the lump ore feed inlet 102, firstly rolls to the tapered distribution plate 10801 at the top of the heat medium channel 108, and rolls to the distribution plate 101 on the side wall of the lump ore storage bin 1 from the edge of the tapered distribution plate 10801 at the top, then slides to the tapered distribution plate 10801 at the lower layer from the distribution plate 101, and so on until the lump ore slides to the material collection chamber 107 from the distribution plate 101 at the lowest layer. Meanwhile, powder attached to the lump ore enters the powder blanking channel through the sieve holes 1010101 on the sieve plates 10101 of the distribution plates 101 in each layer and is then discharged through the powder discharge openings 10104 in each layer. The material collection chamber 107 is provided with a heat medium inlet 104, each layer of distribution plate 101 is provided with a heat medium outlet 105, and the heat medium outlet 105 is positioned on the side wall of the lump ore storage bin 1 between the sieve plate 10101 and the support plate 10102 of each layer of distribution plate 101. The heat medium outlet 105 coincides with the powder discharge port 10104. Inlet of thermal medium from the material collection chamber 107104Enters a lump ore storage bin 1 and is directly connected with the lump oreAfter heat contact and exchange, the heat medium passes through the air holes 10802 on the tapered distribution plates 10801 on the layers of the distribution plates 101 and the heat medium channels 108 and is discharged from the heat medium outlets on the layers of the distribution plates 101105And (4) discharging.
Example 8
As shown in fig. 8, example 6 is repeated except that the system further comprises a thermal medium flow guide device 109. The heat medium flow guiding device 109 is arranged in the material collecting chamber 107, and a heat medium flow guiding inlet 10901 and a heat medium flow guiding outlet 10902 are arranged on the heat medium flow guiding device 109. Thermal medium inlet of lump ore storage bin 1104Communicating with the heat medium introduction inlet 10901. The material collection chamber 107 is provided with 3 heat medium guiding devices 109. All the heat medium flow guide inlets 10901 of the heat medium flow guide devices 109 are identical to the heat medium inlet104And (4) communicating.
The system also comprises a dust removal system 4 and a heat medium outlet105Is communicated to the dust removing system 4 through a hot medium discharge pipe L2.
Example 9
As shown in fig. 7, example 8 is repeated except that a first moisture detecting device 301 is provided at the lump ore feed inlet 102 of the lump ore storage silo 1.
Example 10
Example 9 is repeated except that the lump ore discharge port 103 of the lump ore storage silo 1 is provided with a second moisture detecting device 302.
Adopt the utility model provides a lump ore pretreatment system based on distribution plate angular adjustment will carry the blast furnace through the dry big particle size lump ore that obtains after the preliminary treatment, in the raw materials that add to the blast furnace, the addition of lump ore can increase to 30%. Because the iron content in the lump ore is higher than that of the sintered ore and the pellet ore, the addition amount of the pretreated lump ore is increased in the blast furnace, and the yield of the obtained molten iron can be increased by 10-30% through the blast furnace smelting process.

Claims (43)

1. A lump ore pretreatment system based on distribution plate angle adjustment comprises a lump ore conveying device (D1), a lump ore storage bin (1) and a heat medium conveying pipeline (L1); the lump ore storage bin (1) is provided with a lump ore feeding hole (102), a lump ore discharging hole (103), a heat medium inlet (104) and a heat medium outlet (105); the lump ore conveying device (D1) is connected to the lump ore feed inlet (102) of the lump ore storage bin (1); the heat medium conveying pipeline (L1) is connected to the heat medium inlet (104); the lump ore discharge port (103) is connected to the feed port of the blast furnace (2); a distribution plate (101) is arranged in the lump ore storage bin (1), and the distribution plate (101) is connected with the side wall of the lump ore storage bin (1); an angle adjusting device (10103) is arranged on the distribution plate (101); wherein: the height of the lump ore storage bin (1) is 3-100 m.
2. The system of claim 1, wherein: the distribution plate (101) comprises a sieve plate (10101) and a support plate (10102); one end of sieve (10101) and the one end of backup pad (10102) are connected with the lateral wall of lump ore storage silo (1) respectively, and sieve (10101) set up in the top of backup pad (10102), and sieve (10101) downward sloping setting, and backup pad (10102) tilt up sets up, the other end of sieve (10101) and the other end interconnect of backup pad (10102).
3. The system of claim 2, wherein: the other end of the sieve plate (10101) is movably connected with the other end of the support plate (10102); a lump ore blanking channel is reserved in the central axis position of the lump ore storage bin (1) of the distribution plate (101).
4. The system of claim 3, wherein: the sieve plate (10101), the support plate (10102) and the side wall of the lump ore storage bin (1) form a triangular structure on the section in the vertical direction.
5. The system of claim 4, wherein: an angle adjusting device (10103) is arranged at the joint of the sieve plate (10101) and the side wall of the lump ore storage bin (1).
6. The system of claim 5, wherein: 1-20 layers of the distribution plate (101) are arranged in the lump ore storage bin (1) from top to bottom.
7. The system of claim 6, wherein: 2-10 layers of the distribution plate (101) are arranged in the lump ore storage bin (1) from top to bottom.
8. The system of claim 7, wherein: 3-8 layers of the distribution plate (101) are arranged in the lump ore storage bin (1) from top to bottom; an angle adjusting device (10103) is arranged on each layer of distribution plate (101).
9. The system of claim 8, wherein: the size of the lump ore blanking channel is larger than 5 mm.
10. The system of claim 9, wherein: the size of the lump ore blanking channel is larger than 6 mm.
11. The system of claim 10, wherein: the size of the lump ore blanking channel is larger than 8 mm.
12. The system according to any one of claims 2-11, wherein: a heat medium channel (108) is also arranged at the lump ore blanking channel; the heat medium channel (108) is also provided with a conical distribution plate (10801); air holes (10802) are arranged on the conical surface of the conical distribution plate (10801).
13. The system of claim 12, wherein: and 1-20 layers of conical distribution plates (10801) are arranged on the heat medium channel (108) from top to bottom.
14. The system of claim 13, wherein: 2-10 layers of conical distribution plates (10801) are arranged on the heat medium channel (108) from top to bottom.
15. The system of claim 14, wherein: 3-8 layers of conical distribution plates (10801) are arranged on the heat medium channel (108) from top to bottom; air holes are uniformly formed on the conical surface of each layer of conical distribution plate (10801).
16. The system of claim 15, wherein: the number of layers of the conical distribution plate (10801) on the heat medium channel (108) is the same as that of the distribution plate (101) on the side wall of the lump ore storage bin (1); the conical distribution plate (10801) is arranged above the distribution plate (101) at the same layer position.
17. The system of claim 12, wherein: sieve holes (1010101) are arranged on the sieve plate (10101) of each layer of the distribution plate (101).
18. The system according to any one of claims 13-16, wherein: sieve holes (1010101) are arranged on the sieve plate (10101) of each layer of the distribution plate (101).
19. The system of claim 17, wherein: each layer of distribution plate (101) is provided with a powder discharge port (10104); the powder discharge port (10104) is arranged on the side wall of the lump ore storage bin (1) and is connected with a support plate (10102) of the distribution plate (101); the gap between the sieve plate (10101) and the support plate (10102) of each layer of distribution plate (101) forms a powder blanking channel.
20. The system of claim 18, wherein: each layer of distribution plate (101) is provided with a powder discharge port (10104); the powder discharge port (10104) is arranged on the side wall of the lump ore storage bin (1) and is connected with a support plate (10102) of the distribution plate (101); the gap between the sieve plate (10101) and the support plate (10102) of each layer of distribution plate (101) forms a powder blanking channel.
21. The system according to claim 19 or 20, wherein: the size of the sieve pore (1010101) is 5-20 mm.
22. The system of claim 21, wherein: the size of the sieve pore (1010101) is 6-15 mm.
23. The system of claim 22, wherein: the size of the sieve pore (1010101) is 7-10 mm.
24. The system of claim 12, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
25. The system according to any one of claims 13-16, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
26. The system of any one of claims 17, 19-20, 22-23, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
27. The system of claim 18, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
28. The system of claim 21, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
29. The system of any one of claims 17, 19-20, 22-23, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) of the lump ore storage bin (1) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
30. The system of claim 18, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) of the lump ore storage bin (1) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
31. The system of claim 21, wherein: the upper part of the lump ore storage bin (1) is provided with a heat exchange chamber (106) provided with a distribution plate (101) and a heat medium channel (108), and the lower part of the lump ore storage bin (1) is provided with a material collection chamber (107); the lump ore feed inlet (102) of the lump ore storage bin (1) is arranged on the heat exchange chamber (106), and the lump ore discharge outlet (103) is arranged on the material collecting chamber (107).
32. The system of any one of claims 24, 27-28, 30-31, wherein: the system further comprises a thermal medium flow guiding device (109); the heat medium flow guiding device (109) is arranged in the material collecting chamber (107), and a heat medium flow guiding inlet (10901) and a heat medium flow guiding outlet (10902) are arranged on the heat medium flow guiding device (109); the heat medium inlet (104) of the lump ore storage bin (1) is communicated with the heat medium diversion inlet (10901).
33. The system of claim 26, wherein: the system further comprises a thermal medium flow guiding device (109); the heat medium flow guiding device (109) is arranged in the material collecting chamber (107), and a heat medium flow guiding inlet (10901) and a heat medium flow guiding outlet (10902) are arranged on the heat medium flow guiding device (109); the heat medium inlet (104) of the lump ore storage bin (1) is communicated with the heat medium diversion inlet (10901).
34. The system of claim 29, wherein: the system further comprises a thermal medium flow guiding device (109); the heat medium flow guiding device (109) is arranged in the material collecting chamber (107), and a heat medium flow guiding inlet (10901) and a heat medium flow guiding outlet (10902) are arranged on the heat medium flow guiding device (109); the heat medium inlet (104) of the lump ore storage bin (1) is communicated with the heat medium diversion inlet (10901).
35. The system of claim 32, wherein: 1-20 heat medium diversion devices (109) are arranged in the material collection chamber (107).
36. The system of claim 33, wherein: 1-20 heat medium diversion devices (109) are arranged in the material collection chamber (107).
37. The system of claim 34, wherein: 1-20 heat medium diversion devices (109) are arranged in the material collection chamber (107).
38. The system according to any one of claims 35-37, wherein: 2-5 heat medium diversion devices (109) are arranged in the material collection chamber (107); the heat medium flow guide inlets (10901) of all the heat medium flow guide devices (109) are communicated with the heat medium inlet (104); and/or
The system further comprises a dust removal system (4), and the heat medium outlet (105) is communicated to the dust removal system (4) through a heat medium discharge pipeline (L2).
39. The system of any one of claims 1-11, 13-17, 19-20, 22-24, 27-28, 30-31, 33-37, wherein: a first moisture detection device (301) is arranged at a lump ore feeding port (102) on the lump ore storage bin (1).
40. The system of claim 12, wherein: a first moisture detection device (301) is arranged at a lump ore feeding port (102) on the lump ore storage bin (1).
41. The system of claim 18, wherein: a first moisture detection device (301) is arranged at a lump ore feeding port (102) on the lump ore storage bin (1).
42. The system of claim 39, wherein: a second moisture detection device (302) is arranged at the lump ore discharge port (103) of the lump ore storage bin (1).
43. The system of claim 40 or 41, wherein: a second moisture detection device (302) is arranged at the lump ore discharge port (103) of the lump ore storage bin (1).
CN202120674412.9U 2021-04-02 2021-04-02 Lump ore pretreatment system based on distribution plate angle adjustment Active CN215295745U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202120674412.9U CN215295745U (en) 2021-04-02 2021-04-02 Lump ore pretreatment system based on distribution plate angle adjustment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202120674412.9U CN215295745U (en) 2021-04-02 2021-04-02 Lump ore pretreatment system based on distribution plate angle adjustment

Publications (1)

Publication Number Publication Date
CN215295745U true CN215295745U (en) 2021-12-24

Family

ID=79535426

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202120674412.9U Active CN215295745U (en) 2021-04-02 2021-04-02 Lump ore pretreatment system based on distribution plate angle adjustment

Country Status (1)

Country Link
CN (1) CN215295745U (en)

Similar Documents

Publication Publication Date Title
CN107226627A (en) A kind of two grades of suspension calcining devices of active powder lime
CN106556258A (en) Sintering mine sensible heat retracting device and its using method
CN115178467B (en) Lump ore pretreatment system and pretreatment method based on shaft tube type rotary kiln
CN109425231A (en) A kind of sinter air-draft-type circulating cooling system and its technique
CN207180369U (en) A kind of sintering circular-cooler distribution device
CN115164567B (en) Block ore pretreatment system and method based on angle adjustment of distribution plate
CN215278374U (en) Lump ore screening and drying integrated pretreatment system
CN215295745U (en) Lump ore pretreatment system based on distribution plate angle adjustment
CN114370757B (en) Storage bin lump ore pretreatment system and lump ore pretreatment method
CN215295755U (en) Storage silo lump ore pretreatment system
CN111306945A (en) Circular cooler with particle size screening function
CN215288919U (en) Lump ore pretreatment system based on distribution plate
CN115183564B (en) Block ore pretreatment system and method based on distribution plate
CN214496414U (en) Lump ore pretreatment system
CN107285651A (en) A kind of active powder lime suspension calcining device
CN215295787U (en) Lump ore pretreatment system based on shaft tube type rotary kiln
CN215295641U (en) Lump ore pretreatment system based on inner container type rotary kiln
CN114369714B (en) Block ore pretreatment method and treatment system
CN216716912U (en) Round roller type lump ore pretreatment system
CN113172071B (en) Solid waste and high-water-content ore based cooperative treatment process
CN114367432A (en) Lump ore screening and drying integrated pretreatment system and method
CN115164540B (en) Block ore pretreatment system and pretreatment method based on liner rotary kiln
CN211823552U (en) High-temperature continuous semi-coke drying tower
CN202725501U (en) Fines removal all-in-one machine used for dry-method classification before steam coal preparation
CN214496413U (en) Lump ore pretreatment system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant