CN215612141U - Broken waste heat recovery device of high temperature slag disc - Google Patents
Broken waste heat recovery device of high temperature slag disc Download PDFInfo
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- CN215612141U CN215612141U CN202120685516.XU CN202120685516U CN215612141U CN 215612141 U CN215612141 U CN 215612141U CN 202120685516 U CN202120685516 U CN 202120685516U CN 215612141 U CN215612141 U CN 215612141U
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Abstract
A high-temperature steel slag disc crushing waste heat recovery device comprises a liquid slag tank 1, a slag pouring machine 2, high-temperature slag 3, a slag pulling machine 4, a disc crushing bed 5, a crusher 9, a rail 24, a solid slag tank 25, a slag receiving vehicle 26, a pipeline 27, a fan 28, a heat exchanger 29 and a generator 30, liquid slag ladle 1 is on pouring sediment machine 2, and high temperature sediment 3 is in liquid slag ladle 1, and the machine of pulling out sediment 4 is at pouring sediment machine 2 lateral parts, and broken bed 5 of disc is in pouring sediment machine 2 below, and breaker 9 runs through broken bed 5 of disc and locates the track 24 top, and the sediment portion of pushing away of breaker 9 is located broken bed 5 of disc, pushes away the sediment portion and drives the high temperature slag sediment layer and remove to the export by the entry of broken bed 5 of disc, and solid-state slag ladle 25 is in broken bed 5 below of disc, and solid-state slag ladle 25 is fixed on connecing the sediment car 26, broken bed 5 of disc, fan 28, heat exchanger 29, generator 30 connect through pipeline 27.
Description
Technical Field
The utility model relates to the field of waste treatment and utilization, in particular to a high-temperature steel slag disc crushing waste heat recovery device.
Background
In recent years, the annual steel yield of China exceeds 8 hundred million tons, which accounts for about 120-140 kg of steel slag generated by producing one ton of steel, and the annual steel slag generation amount of China exceeds 1 million tons. The steel slag contains two types of resources, namely iron metal resources and inorganic materials such as calcium silicate, and has the material property of resource utilization. For a long time, iron ores in China mainly depend on imports, and resources are very short. The steel slag in China is expected to recover nearly 2000 ten thousand tons of iron resources, and inorganic materials can reach more than 8000 ten thousand tons, so that the method has great significance in resource recovery value.
The high-efficiency recovery of metal iron and inorganic material resources in the steel slag is to perform crushing separation firstly and then realize the separation of the two materials by adopting magnetic separation and other modes, thereby obtaining targeted resource utilization. The steel slag pretreatment process is a precondition for steel slag crushing and magnetic separation treatment, and realizes more efficient crushing, screening and magnetic separation of the steel slag through pretreatment under a high temperature condition.
The prior steel slag pretreatment process comprises production processes such as a hot stuffy method, a hot splashing method, a roller method, a wind quenching method and the like, wherein the hot splashing method has the problems of backward production mode, simple and extensive treatment process, serious environmental pollution, low metal resource recovery rate and the like, and is required to be eliminated as soon as possible; the roller method is only suitable for liquid steel slag with good fluidity, the treatment rate of the steel slag is less than 50%, the equipment operation cost is high, the failure is high, and the roller method is only used for a few steel enterprises in a steel system at present; the air quenching method adopts large air volume to blow off and cool the liquid steel slag into fine particles, is only suitable for treating the liquid steel slag, has low recovery rate of steel metal iron resources, and only one set of air quenching equipment is provided for domestic horse steel.
The domestic main steel slag treatment method is a hot-disintegrating method, and the process has a series of advantages of wide adaptability, good steel slag pulverization effect after hot disintegration, good slag-iron separation effect, high metal iron recovery rate, qualified tailing stability and the like. The existing hot-sealing method is divided into a pool type hot-sealing process and a pressure hot-sealing process. The tank type hot stuffy method adopts a process method of engineering mechanized operation, namely an excavator is used for slagging off and crushing the high-temperature steel slag poured into the hot stuffy tank, and the equipment level and the environmental emission need to be further improved. The crushing method has the advantages of high equipment and automation degree and the like by adopting a mechanical rolling crusher to crush the high-temperature steel slag in a pressing and hot stuffiness mode, but the investment is relatively high, the tightness is poor, and the waste heat recovery cannot be carried out by adopting a water cooling mode in the crushing process.
The slag temperature of the steel slag reaches 1600 ℃, the heat value of each ton of slag exceeds 50kg of standard coal, and a large amount of waste heat resources are contained in the slag. The annual output of steel slag in China exceeds 1 hundred million tons, if all the waste heat resources are recycled, the newly increased economic benefit can reach billions of yuan every year, and the method has huge economic market space. At present, the waste heat recovery of high-temperature slag such as metallurgical slag is still often in a test research stage, and the complete resource utilization of two slag heat resources is often difficult to realize. A large number of laboratory and industrial pilot-scale test researches are carried out at home and abroad aiming at the recovery of the waste heat of the air-quenched steel slag, but the method is improper, the recovery rate of iron resources is low, the production is discontinuous, and the comprehensive economic benefit is poor, so that the production and the application cannot be realized. In addition, smelting slag is adopted to be cooled to generate steam or hot water for heat exchange utilization, but the waste heat utilization rate is low, and the economic condition of industrial operation is not met.
Aiming at the problems of large occupied space, high system investment, incapability of recycling waste heat and the like of the existing steel slag treatment process and equipment, a novel steel slag treatment process is urgently needed to be developed. Therefore, the novel steel slag disc crushing air cooling waste heat recovery method and the novel steel slag disc crushing air cooling waste heat recovery device have the advantages of high equipment automation level, strong production continuity, high operation efficiency, small occupied space, strong tightness, low system investment, high waste heat recovery rate and the like. The technology realizes the breaking pretreatment of the high-temperature steel slag and the breakthrough of recycling the waste heat of the steel slag, and is the leap-type upgrade of the prior steel slag treatment process technical equipment.
SUMMERY OF THE UTILITY MODEL
In view of the defects of the prior art, the utility model aims to provide a high-temperature steel slag disc crushing waste heat recovery device, which replaces the traditional mode that water is used as a cooling medium for steel slag, and improves the steel slag treatment equipment level.
The technical scheme of the utility model is as follows:
the utility model relates to a high-temperature steel slag disc crushing waste heat recovery device which comprises a liquid slag tank, a slag pouring machine, high-temperature slag, a slag pulling machine, a disc crushing bed, a crusher, a rail, a solid slag tank, a slag receiving vehicle, a pipeline, a fan, a heat exchanger and a generator.
Further, the breaker includes broken axle, broken tooth, water-cooling post, rotary joint, ring gear, return pulley, and broken tooth slope sets up and forms in the crushing roller below and pushes away the sediment portion, and the water-cooling post connects the breaker through rotary joint, and the ring gear is in broken axle outside and gear connection, and the return pulley is in broken axle outer end below, the breaker main part is inside the broken bed of disc, and support and running gear are outside at the broken bed of disc.
Furthermore, broken tooth is the plate body shape, and the side rigid coupling is in crushing roller lower surface on the plate body, and when the breaker was rotatory clockwise for the broken bed of disc, the plate body was located the first quadrant and the third quadrant that the broken bed of disc radially extended face and the broken bed circumference tangent plane of disc intersected along length direction's extension face, and when the breaker was rotatory anticlockwise for the broken bed of disc, the plate body was located the broken bed of disc radially extended face and the broken bed circumference tangent plane of disc second quadrant and the fourth quadrant that intersect along length direction's extension face.
Furthermore, the included angle between the extension surface of the plate body along the length direction and the radial extension surface of the disc crushing bed is 10-80 degrees.
Further, the broken bed of disc includes slag pouring port, airtight cover, disc wall, slag blanket, bed course, end bed, wind hole, blast chamber, unloads cinder notch, water seal groove, the slag pouring port is at the top outer fringe of the broken bed upper portion airtight cover of disc, and airtight cover non-contact covers at the broken bed top of disc, and disc wall is in broken bed outside a week of disc, and slag blanket, bed course, end bed set gradually from last to down, and there is wind hole blast chamber in the end bed below the end bed, unloads cinder notch below in the middle of the end bed, and water seal groove is in the junction between airtight cover, disc wall and end bed.
Furthermore, the crushing shaft is a cross-shaped steel structure cylinder, the diameter of the crushing shaft is 800mm, the length of the crushing shaft is 3-20m, crushing teeth are arranged right below the crushing shaft, the width of the crushing teeth is 40-400mm, and the length of the crushing teeth is 400mm, 2000 mm.
Furthermore, the crusher is connected with a gear ring and a gear, the motor drives the gear to enable the crusher to rotate around the disc crushing bed, and the disc wall is connected to the crushing shaft and rotates along with the operation of the crusher.
Compared with the prior art, the utility model has the beneficial effects that:
the utility model adopts a disc crushing bed and a crusher as high-temperature steel slag cooling and crushing core equipment, adopts a fixed disc crushing bed as a steel slag treatment carrier, and rotates around the disc crushing bed by the novel crusher to efficiently crush the steel slag. In the crushing process, the high-temperature steel slag is subjected to air cooling by circulating air, and then hot air obtained by air cooling heat exchange is generated by a heat exchanger and a generator, so that the waste heat of the steel slag is effectively utilized. The slag pouring machine is adopted to perform automatic slag pouring operation, the crusher rotates at a certain speed, the crushing teeth rotate along with the crusher to crush the steel slag while realizing the effects of pushing slag and discharging. The crusher is in a cross design, a plurality of crushing teeth are arranged below the crushing shaft barrel, the crushing capacity of the equipment is high, and the steel slag treatment efficiency is high. And the high-temperature flue gas obtained by air cooling heat exchange is subjected to waste heat recovery power generation, the generation capacity per ton of slag reaches 15-40kWh, and the economic benefit of waste heat recovery is remarkable.
The utility model replaces the traditional mode that the steel slag adopts water as a cooling medium, and cancels a wet flue gas treatment device generated by a water cooling process. The process adopts circulating air to cool the high-temperature steel slag without exhausting smoke. The process equipment has the advantages of high waste heat recovery utilization rate, high treatment efficiency, good tightness, small space occupation, high automation degree and the like. The method and the device greatly improve the steel slag treatment equipment level, improve the steel slag treatment efficiency, break through the difficult problem of steel slag waste heat recycling, thoroughly solve the difficult problem of steel slag treatment process discharge, increase the comprehensive utilization benefit of the steel slag, greatly reduce public and auxiliary facility investment such as water and dust removal, effectively reduce the steel slag production operation cost, and have outstanding economic and social benefits.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
FIG. 1 is a schematic front view of a high temperature steel slag disc crushing waste heat recovery device provided by the present invention;
FIG. 2 is a schematic top view of a high temperature steel slag disk crushing waste heat recovery device provided by the present invention;
FIG. 3 is a schematic view of the arrangement of crushing shafts of the high temperature steel slag disc crushing waste heat recovery device provided by the utility model.
Detailed Description
In order to make the technical solutions of the present invention better understood, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
A high-temperature steel slag disc crushing waste heat recovery device is shown in figures 1-3, and comprises the following components: the slag removing machine comprises a liquid slag tank 1, a slag pouring machine 2, high-temperature slag 3, a slag removing machine 4, a disc crushing bed 5, a crusher 9, a rail 24, a solid slag tank 25, a slag receiving vehicle 26, a pipeline 27, a fan 28, a heat exchanger 29 and a generator 30. The liquid slag tank 1 is arranged on the slag pouring machine 2, the high-temperature slag 3 is arranged in the liquid slag tank 1, and the slag removing machine 4 is arranged on the side part of the slag pouring machine 2; the disc crushing bed 5 is arranged below the slag pouring machine 2; the main body of the crusher 9 is arranged inside the disc crushing bed 5, and the supporting and traveling mechanism is arranged outside the disc crushing bed 5 and above the track 24; the solid slag pot 25 is seated on the slag receiving vehicle 26 and is arranged below the disc crushing bed 5; the disc crushing bed 5, the fan 28, the heat exchanger 29 and the generator 30 are connected through a pipeline 27.
The disc crushing bed 5 includes: the slag pouring hole 6, the closed cover 7, the disc wall 8, the slag layer 12, the cushion layer 13, the bottom bed 14, the air hole 15, the air blowing chamber 16, the slag discharging hole 17 and the water seal tank 18. The deslagging port 6 is arranged at the top of one side of a closed cover 7 at the upper part of the disc crushing bed 5. The closed cover 7 covers the top of the disc crushing bed 5, and the disc wall 8 is arranged on the outer side of the disc crushing bed 5 for a circle; the slag layer 12 is arranged above the cushion layer 13, the cushion layer 13 is arranged above a bottom bed 14 of the disc crushing bed 5, and the bottom bed 14 is provided with wind holes 15; the blast chamber 16 is arranged below the bottom bed 14, and the slag discharge port 17 is arranged below the middle of the bottom bed 14; a water-sealed tank 18 is provided at the junction between the enclosure 7, the disc wall 8 and the bottom bed 14.
The crusher 9 comprises: crushing shaft 10, crushing teeth 11, water-cooling column 19, rotary joint 20, gear ring 21, gear 22 and bottom wheel 23. The crushing teeth 11 are connected below the crushing roller 10; the water-cooling column 19 is connected with the crusher 9 through a rotary joint 20 for water-cooling protection; the gear ring 21 is connected with the gear 22 outside the crushing shaft 10; the bottom wheel 23 is below the outer end of the crushing shaft 10.
The crushing teeth 11 are plate bodies, the upper side surfaces of the plate bodies are fixedly connected to the lower surfaces of the crushing rollers 10, when the crusher 9 rotates clockwise relative to the disc crushing bed 5, the extending surfaces of the plate bodies in the length direction are located in a first quadrant and a third quadrant, which are intersected with the circumferential tangent plane of the disc crushing bed 5, of the radial extending surfaces of the disc crushing bed 5, and when the crusher 9 rotates counterclockwise relative to the disc crushing bed 5, the extending surfaces of the plate bodies in the length direction are located in a second quadrant and a fourth quadrant, which are intersected with the circumferential tangent plane of the disc crushing bed 5, of the radial extending surfaces of the disc crushing bed 5. The included angle between the extension surface of the plate body along the length direction and the radial extension surface of the disc crushing bed 5 is 10-80 degrees.
The liquid slag pot 1 is used for containing high-temperature slag 3; the slag pouring machine 2 can automatically tip and pour slag, and the maximum tipping angle is not less than 150 degrees. The inner diameter of the upper part of the slag pouring port 4 is 2000-5000mm, and the inner diameter of the bottom part of the slag pouring port 4 is 1000-2000 mm; the external cylinder body of the slag pouring port 4 adopts a steel structure, the inner side of the cylinder body is provided with a refractory material, and the thickness of the refractory material is 100-300 mm.
The inner diameter of the slag discharging port 17 is 800-1800 mm. The outer cylinder body of the slag discharging port 17 is of a steel structure, an inorganic heat-insulating material is arranged on the outer side of the cylinder body, and the thickness of the heat-insulating material is not less than 50 mm.
The crushing shaft 10 is a cross-shaped steel structure cylinder, the diameter of the crushing shaft 10 is 300-800mm, and the length is 3-20 m; the crushing teeth 11 are arranged right below the crushing shaft 10, and the included angle between the axial direction of the crushing shaft 10 and the crushing teeth 11 is 10-80 degrees; the width of the crushing teeth 11 is 40-400mm, and the length is 400-2000 mm; the crushing shaft 10 is made of heat-resistant steel, the crushing teeth 11 are made of heat-resistant and wear-resistant steel materials, and the crushing shaft 10 and the crushing teeth 11 are cooled by water.
The bottom bed 13 is of a steel structure, the bottom of the lower bed 13 is provided with air holes 14, and the diameter of each air hole 14 is 5-50 mm. The closed cover 7 and the pipeline 27 are both made of steel structures, the exterior of the closed cover is made of inorganic heat-insulating materials, and the thickness of the inorganic heat-insulating materials is 50-200 mm. The thickness of the slag layer 12 is 150-600mm, the thickness of the cushion layer 13 is 50-300mm, the cushion layer 13 adopts solid steel slag particles, and the diameter of the solid steel slag particles is 10-100 mm.
The crusher 9 is connected with the gear ring 21 and the gear 22, the crusher 9 can rotate around the disc crushing bed 5 under the driving action of the gear 22 motor, and the crusher 9 is driven to rotate in the forward and reverse directions by adjusting the forward and reverse directions of the motor rotor. The disc wall 8 is connected to a crushing shaft 10 which rotates with the operation of the crusher 9.
The disc wall 8 is made of steel structure materials, and the inner side of the disc wall 8 is provided with refractory materials, and the thickness of the refractory materials is 50-200 mm. The air blowing chamber 16 is used for blowing air to the disc crushing bed 5 by the fan 28 to cool the high-temperature steel slag, and meanwhile, steel slag particles falling through the air holes 14 in the bottom bed 13 are collected, and the height of the air blowing chamber 16 is 500-5000 mm.
The water seal tank 18 is a steel structure water tank, the width of the water seal tank 18 is 100-600mm, the depth of the water seal tank 18 is 100-600mm, one side of the water seal tank 18 facing the disc crushing bed 5 is made of a mounting refractory material, and the thickness of the refractory material is not less than 50 mm. The fan 28 is a high temperature resistant fan, and the temperature of the hot air can be resistant to not less than 180 ℃.
The device for recycling the crushing waste heat of the high-temperature steel slag disc comprises the following steps:
(1) the liquid slag pot 1 containing the high-temperature slag 3 is lifted and placed on a slag pouring machine 2 through a travelling crane, the slag pouring machine 2 tips over the high-temperature slag 3 at a certain speed and pours the high-temperature slag 3 into a disc crushing bed 5 through a slag pouring port 6, and the high-temperature slag 3 falls on the upper part of a cushion layer 13 on a bottom bed 14 to form a slag layer 12.
(2) When deslagging, the crusher 9 drives the gear ring 21 to rotate through the gear 22, the crushing shaft 10 and the crushing teeth 11 are arranged in a non-parallel mode to form an included angle, and the crushing teeth 11 which move along with the rotation of the crusher 9 can drive the high-temperature steel slag layer 12 to move from the deslagging port 6 to the slag discharging port 17. The slag layer 12 is continuously crushed under the stirring of the crushing teeth 11 in the moving process until the requirement of the crushing granularity is met.
(3) In the treatment process, the circulating air provided by the fan 28 sequentially passes through the air blowing chamber 16, the air holes 15 in the bottom bed 14, the cushion layer 13 and the slag layer 12 to realize the heat convection of the high-temperature slag 3 until the high-temperature steel slag is cooled to a certain temperature.
(4) And (3) cooling and crushing the high-temperature slag 3 in the steps (1) to (3), discharging the high-temperature slag through the slag discharge port 17, feeding the high-temperature slag into the solid slag tank 25, and then transporting the high-temperature slag to the subsequent steel slag hot-closed treatment process through the slag receiving vehicle 26.
(5) The cold air and the slag layer 12 are converted into hot air through convection heat exchange, the hot air enters the heat exchanger 29 through the pipeline 27 to obtain pressure steam, and the steam is conveyed to the generator 30 through the pipeline 27 to generate electricity. The hot air is cooled by the heat exchanger 29 to obtain cold air, and the cold air is recycled by the fan 28 to cool the high-temperature slag 3.
Wherein, the slag pouring time of the liquid slag pot 1 is 5-60 minutes, and the treatment period is 5-60 minutes. The rotating speed of the crusher 9 is 3-60 r/h, and the treatment rate of the steel slag can be increased by increasing the rotating speed of the crusher 9, otherwise, the treatment rate of the steel slag is reduced.
Wherein the cooling air volume of the high-temperature slag 3 per ton is 1000-3The wind pressure is 2000-10000 Pa; in the blast cooling process, the processing time and the slag discharging temperature can be adjusted by increasing the air quantity of the fan 28, the processing time and the slag discharging temperature can be reduced by increasing the air quantity, and otherwise, the processing time and the slag discharging temperature are increased.
Wherein, the mass proportion of the steel slag with the particle size less than 200mm after the high-temperature slag 3 is cooled and crushed exceeds 80 percent; the temperature of the treated steel slag is controlled to be 300-1000 ℃, the cooling, solidification and crushing of the steel slag can be realized, and a certain amount of heat can be reserved for subsequent hot disintegration.
Wherein, the temperature of the cooling air provided by the fan 28 is 25-200 ℃, and the temperature of the hot air formed by the convection heat exchange of the slag layer 12 formed by the high-temperature slag 3 is 250-600 ℃. The hot air is cooled to 100-200 ℃ through heat exchange by a heat exchanger 29, and then the high-temperature slag 3 is circularly cooled by a fan 28. Saturated steam obtained by heat exchange of the hot air through the heat exchanger 29 is conveyed to the generator 30 for power generation, and the power generation amount per ton of steel slag is 15-40 kWh. Wherein, the solid or semi-solid high-temperature slag 3 with poor fluidity is subjected to slag-pulling operation by a slag-pulling machine 4, and the solidified high-temperature slag 3 is pulled into a disc crushing bed 5 uniformly.
In the description herein, references to the description of the term "one embodiment," "some embodiments," "an illustrative embodiment," "an example," "a specific example," or "some examples" or the like mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the utility model. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
While embodiments of the utility model have been shown and described, it will be understood by those of ordinary skill in the art that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the utility model, the scope of which is defined by the claims and their equivalents.
Claims (8)
1. A high-temperature steel slag disc crushing waste heat recovery device comprises a liquid slag tank (1), a slag pouring machine (2), high-temperature slag (3), a slag pulling machine (4), a disc crushing bed (5), a crusher (9), a rail (24), a solid slag tank (25), a slag receiving vehicle (26), a pipeline (27), a fan (28), a heat exchanger (29) and a generator (30), and is characterized in that the liquid slag tank (1) is arranged on the slag pouring machine (2), the high-temperature slag (3) is arranged in the liquid slag tank (1), the slag pulling machine (4) is arranged on the side part of the slag pouring machine (2), the disc crushing bed (5) is arranged below the slag pouring machine (2), the crusher (9) penetrates through the disc crushing bed (5) and is arranged above the rail (24), a slag pushing part of the crusher (9) is arranged in the disc crushing bed (5), and drives a high-temperature steel slag layer to move from an inlet to an outlet of the disc crushing bed (5), the solid slag pot (25) is arranged below the disc crushing bed (5), the solid slag pot (25) is fixed on the slag receiving vehicle (26), and the disc crushing bed (5), the fan (28), the heat exchanger (29) and the generator (30) are connected through a pipeline (27).
2. The high-temperature steel slag disc crushing waste heat recovery device according to claim 1, wherein the crusher (9) comprises a crushing shaft (10), crushing teeth (11), a water cooling column (19), a rotary joint (20), a gear ring (21), a gear (22) and a bottom wheel (23), the crushing teeth (11) are obliquely arranged below the crushing shaft (10) to form a slag pushing part, the water cooling column (19) is connected with the crusher (9) through the rotary joint (20), the gear ring (21) is connected with the gear (22) on the outer side of the crushing shaft (10), the bottom wheel (23) is arranged below the outer end of the crushing shaft (10), the main body of the crusher (9) is arranged inside the disc crushing bed (5), and a supporting and traveling mechanism is arranged outside the disc crushing bed (5).
3. The high-temperature steel slag disc crushing waste heat recovery device as claimed in claim 2, wherein the crushing teeth (11) are plate-shaped, the upper side surface of the plate body is fixedly connected to the lower surface of the crushing shaft (10), when the crusher (9) rotates clockwise relative to the disc crushing bed (5), the extension surfaces of the plate body along the length direction are located in a first quadrant and a third quadrant where the radial extension surface of the disc crushing bed (5) intersects with the circumferential tangent plane of the disc crushing bed (5), and when the crusher (9) rotates counterclockwise relative to the disc crushing bed (5), the extension surfaces of the plate body along the length direction are located in a second quadrant and a fourth quadrant where the radial extension surface of the disc crushing bed (5) intersects with the circumferential tangent plane of the disc crushing bed (5).
4. The high-temperature steel slag disc crushing waste heat recovery device as claimed in claim 3, wherein the included angle between the extension surface of the plate body along the length direction and the radial extension surface of the disc crushing bed (5) is 10-80 degrees.
5. The high-temperature steel slag disc crushing waste heat recovery device according to claim 1, wherein the disc crushing bed (5) comprises a slag pouring port (6), a closed cover (7), a disc wall (8), a slag layer (12), a cushion layer (13), a bottom bed (14), an air hole (15), an air blowing chamber (16), a slag discharging port (17) and a water sealing groove (18), the slag pouring port (6) is arranged at the outer edge of the top of the closed cover (7) at the upper part of the disc crushing bed (5), the closed cover (7) covers the top of the disc crushing bed (5) in a non-contact manner, the disc wall (8) is arranged on the outer side of the disc crushing bed (5) in a circle, the slag layer (12), the cushion layer (13) and the bottom bed (14) are sequentially arranged from top to bottom, the air hole (15) is arranged in the bottom bed (14) and the air blowing chamber (16) is arranged below the bottom bed (14), the slag discharging port (17) is arranged below the middle of the bottom bed (14), and the water sealing groove (18) is arranged in the closed cover (7), The junction between the disc wall (8) and the bottom bed (14).
6. The high-temperature steel slag disc crushing waste heat recovery device as claimed in claim 2, wherein the crushing shaft (10) is a cross-shaped steel structure cylinder, the diameter of the crushing shaft (10) is 300-800mm, and the length is 3-20 m.
7. The high-temperature steel slag disc crushing waste heat recovery device as claimed in claim 2, wherein the crushing teeth (11) are arranged under the crushing shaft (10), the width of the crushing teeth (11) is 40-400mm, and the length of the crushing teeth is 400-2000 mm.
8. The high-temperature steel slag disc crushing waste heat recovery device as claimed in claim 5, wherein the crusher (9) is connected with a gear ring (21) and a gear (22), the motor drives the gear (22) to enable the crusher (9) to rotate around the disc crushing bed (5), and the disc wall (8) is connected to the crushing shaft (10) and rotates along with the operation of the crusher (9).
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112958246A (en) * | 2021-04-02 | 2021-06-15 | 中冶节能环保有限责任公司 | High-temperature steel slag disc crushing waste heat recovery device and method |
| CN116287494A (en) * | 2023-03-15 | 2023-06-23 | 山西航金环保科技有限公司 | Energy-saving and environment-friendly treatment method for high-temperature liquid steel slag |
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2021
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112958246A (en) * | 2021-04-02 | 2021-06-15 | 中冶节能环保有限责任公司 | High-temperature steel slag disc crushing waste heat recovery device and method |
| CN112958246B (en) * | 2021-04-02 | 2024-01-09 | 中冶节能环保有限责任公司 | High-temperature steel slag disc crushing waste heat recovery device and method |
| CN116287494A (en) * | 2023-03-15 | 2023-06-23 | 山西航金环保科技有限公司 | Energy-saving and environment-friendly treatment method for high-temperature liquid steel slag |
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