WO2023184962A1 - Drum quick-cooling dry treatment device for blast furnace slag for use in waste heat recovery - Google Patents

Drum quick-cooling dry treatment device for blast furnace slag for use in waste heat recovery Download PDF

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Publication number
WO2023184962A1
WO2023184962A1 PCT/CN2022/128585 CN2022128585W WO2023184962A1 WO 2023184962 A1 WO2023184962 A1 WO 2023184962A1 CN 2022128585 W CN2022128585 W CN 2022128585W WO 2023184962 A1 WO2023184962 A1 WO 2023184962A1
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Prior art keywords
cooling
slag
drum
blast furnace
furnace slag
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PCT/CN2022/128585
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French (fr)
Chinese (zh)
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凌祥
黄博厚
刘威宏
包恒兴
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南京工业大学
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Publication of WO2023184962A1 publication Critical patent/WO2023184962A1/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • C21B3/08Cooling slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/052Apparatus features including rotating parts
    • C21B2400/056Drums whereby slag is poured on or in between
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/08Treatment of slags originating from iron or steel processes with energy recovery

Definitions

  • the invention belongs to the technical field of metallurgical high-temperature slag treatment, and specifically relates to a blast furnace slag drum quick-cooling dry treatment device that separates slag from water, has a cooling tube that is not in direct contact with the slag, and is used for waste heat recovery.
  • Blast furnace slag is the main by-product of the iron and steel metallurgical industry. Under the current production process conditions, more than 0.3t of blast furnace slag is produced for every 1t of pig iron produced. Its temperature is around 1450 ⁇ 1550°C. Each ton of slag contains about 1.8MJ of waste heat. For recycling. China is currently the world's largest steel producer. In 2020, the country's total pig iron production was 887.524 million tons. According to the industry average, it is estimated that 266 million tons of slag will be produced. The heat contained in it is equivalent to the burning of 16.365 million tons of standard coal (1 The heat generated by the combustion of a ton of standard coal is 29307.6kJ).
  • the methods for treating high-temperature slag mainly include wet method and dry method.
  • the wet method that is, the water quenching method, is currently the most widely used method. Although this method has the advantages of small particle size and high vitreous content, it wastes a lot of water resources and high-grade heat energy, and also produces sulfur-containing gas and pollutes the environment.
  • Dry methods include rotary cup method, drum method, rotating disk method, etc., which mainly achieve the purpose of granulating slag through the dual effects of centrifugal force and air cooling.
  • the present invention provides a blast furnace slag drum quick-cooling dry processing device for waste heat recovery.
  • the cooling granulation drum is composed of an inner and outer cylinder. Both ends of the inner and outer cylinder are sealed, and the middle closed cavity is filled. Thermal medium. The coolant flows in a closed cooling coil, which is buried in the heat transfer medium between the inner and outer cylinders.
  • the high-temperature slag adheres to the surface of the outer cylinder, and the heat is transferred from the heat-conducting medium between the inner and outer cylinders to the cooling tubes buried in it, and is taken away by the coolant in the cooling tubes.
  • the high-temperature slag quickly cools to about 600°C to form a glassy state.
  • the cooling granulating drum continues to rotate. When it rotates to a certain angle, the two intermeshing outer drums squeeze and crush the slag, and the slag falls into the heat exchanger to recover waste heat.
  • a blast furnace slag drum quick-cooling dry treatment device for waste heat recovery which is characterized in that it includes a blast furnace slag tank installed on a bracket, several sets of cooling granulation drums and heat exchangers;
  • the high-temperature molten slag flows downward through the adjustable-width slot set at the bottom of the blast furnace slag tank and adheres to the outer wall of the cooling granulation drum.
  • the high-temperature molten slag is cooled into glassy slag.
  • the glassy slag is arranged in several groups in the vertical direction.
  • the cooling granulation roller is squeezed and crushed in sequence, and finally enters the heat exchanger for waste heat recovery;
  • each cooling granulation roller is arranged in pairs, and each cooling granulation roller includes an outer cylinder, an inner cylinder and a cooling coil.
  • the closed space formed between the outer cylinder and the inner cylinder is filled with heat-conducting medium, so The cooling coil is embedded in the heat transfer medium.
  • the inner layer of the blast furnace slag tank is an insulating coating
  • the middle layer is a high-temperature resistant material
  • the outer layer is thermally insulated.
  • the surface of the outer cylinder is processed with crushing gear teeth, and two outer cylinders in the same group mesh with each other.
  • the inner cylinder is axially penetrated by a main shaft, and the main shaft is driven by a driving motor, thereby driving the rotation of the entire cooling and granulating drum.
  • the cooling liquid flows in the cooling coil, and the cooling liquid flows into the cooling coil through the cooling liquid inflow pipe, the inflow main pipe and the inflow branch pipe, and the cooling liquid in the cooling coil flows out through the outflow branch pipe and the cooling liquid outflow pipe in sequence;
  • the main inflow pipe is fixedly sleeved on the part of the main shaft that extends out of the inner cylinder, and the coolant inflow pipe is connected to the main inflow pipe through the inflow rotary joint;
  • the main shaft is partially hollow, and the outflow branch pipe is connected to the main inflow pipe through the hollow part of the main shaft and the outflow rotary joint.
  • the cooling liquid outflow pipes are connected; wherein, the cooling liquid inflow pipe, the inflow rotary joint and the cooling liquid outflow pipe do not rotate with the main shaft.
  • an expansion chamber is provided on one side of the cooling granulation drum. Two expansion chambers in the same group are arranged in a staggered manner. The expansion chamber is connected to the closed space between the outer cylinder and the inner cylinder and is used to accommodate the expansion of the heat-conducting medium. the subsequent volume.
  • thermal conductive medium is tin or graphite mixed with ceramic glue.
  • the heat exchanger is placed directly below the cooling granulation drum, and the slag crushed by the cooling granulation drum enters the heat exchanger through the collection port.
  • the heat exchanger is provided with an oscillation mechanism.
  • the beneficial effects of the invention are: when the device is working, the slag vitrification and slag granulation collection processes are carried out simultaneously to realize continuous production; the cooling liquid and the slag are completely separated, and the cooling tube is not in direct contact with the slag to avoid It eliminates the leakage of coolant due to thermal fatigue damage of the cooling pipe, essentially eliminating the risk of contact between the coolant and the slag; it can efficiently recycle the slag, effectively reducing the serious waste of high-quality waste heat resources of liquid slag, and the heat energy recovery efficiency reaches 70%, which is of great significance to the waste heat recovery and efficient utilization of high-temperature slag.
  • Figure 1 is a schematic structural diagram of the blast furnace slag drum rapid cooling dry processing device of the present invention.
  • Figure 2a is a schematic structural diagram of a blast furnace slag tank according to the present invention.
  • Figure 2b is a schematic structural diagram of the notch at the bottom of the blast furnace slag tank according to the present invention.
  • Figure 3 is a schematic structural diagram of the cooling granulation drum of the present invention.
  • Figure 4a is a cross-sectional view of the flow path of the cooling coil in the cooling granulation drum of the present invention.
  • Figure 4b is a schematic diagram of the flow path of the cooling coil in the cooling granulation drum of the present invention.
  • Figure 5 is a schematic diagram of the present invention's operation of granulating and crushing slag.
  • the reference signs are as follows: 1-blast furnace slag tank; 1.1-notch; 2-bracket; 3-driving motor; 4-cooling granulating drum; 4.1-coolant outflow pipe; 4.2 outflow rotary joint; 4.3 inflow rotary joint; 4.4 Coolant inflow pipe; 4.5 inflow main pipe; 4.6-cooling coil; 4.7-outflow branch pipe; 4.8-inflow branch pipe; 4.9-outer cylinder; 4.10-heat transfer medium; 4.11-expansion chamber; 4.12-inner cylinder; 4.13-spindle; 5 -Heat Exchanger.
  • the blast furnace slag drum quick-cooling dry processing device shown in Figure 1 includes a blast furnace slag tank 1, a bracket 2, a drive motor 3, a cooling granulating drum 4 and a heat exchanger 5.
  • the blast furnace slag tank 1 is placed at the bottom of the high-temperature slag pool, and the cooling granulation drum 4 is used to quickly cool the liquid slag flowing down from the blast furnace slag tank 1 to vitrify and pulverize it.
  • a cooling coil 4.6 is arranged in the cooling granulation drum 4, and the coolant is in the cooling coil 4.6.
  • the molten slag rapidly cools down under the action of the coolant in the coil and forms a glassy state that adheres to the surface of the cooling granulation drum 4.
  • the cooling granulating drum 4 is driven by the drive motor 3, which adopts a reduction motor, which can adjust the motor speed according to the slag flow and temperature.
  • the reduction motor is fixed on the machine base through the machine feet.
  • the cooling granulating drum 4 continues to rotate. When it rotates to a certain angle, the glassy slag attached to the surface of the cooling granulating drum 4 is extruded and crushed by the intermeshing surfaces of the cooling granulating drum 4, forming a The powder then falls into heat exchanger 5.
  • the structure of the blast furnace slag tank 1 is shown in Figures 2a and 2b.
  • the inner layer of the blast furnace slag tank 1 is an insulating coating, the middle is a high-temperature resistant material, and the outer layer is thermally insulated.
  • the bottom of the blast furnace slag tank 1 is provided with an adjustable-width slot 1.1, which can adjust the opening to control the flow of high-temperature slag and ensure that the high-temperature slag can form a uniform film on the surface of the cooling granulation drum 4.
  • the structure of the cooling granulation drum 4 is shown in Figure 3.
  • a cooling coil 4.6 is arranged inside the cooling granulation drum 4, and the cooling coil 4.6 is spirally arranged between the outer cylinder 4.9 and the inner cylinder 4.12.
  • the space between the outer cylinder 4.9 and the inner cylinder 4.12 is filled with heat transfer medium 4.10, and the cooling coil 4.6 is buried in the heat transfer medium 4.10.
  • the inner cylinder 4.12 is axially penetrated by a main shaft 4.13.
  • the main shaft 4.13 is driven by the drive motor 3, which in turn drives the rotation of the entire cooling and granulating drum 4. Coolant continues to flow in the cooling coil 4.6.
  • the coolant flows into the cooling coil 4.6 through the coolant inflow pipe 4.4, the main inflow pipe 4.5 and the inflow branch pipe 4.8.
  • the coolant in the cooling coil 4.6 flows out through the outflow branch pipe 4.7 and the coolant in sequence. Outflow from tube 4.1.
  • the flow trajectory of the coolant in the pipe is shown in Figures 4a and 4b.
  • the inflow main pipe 4.5 is fixedly sleeved on the part of the main shaft 4.13 extending out of the inner cylinder 4.12, and the coolant inflow pipe 4.4 is connected to the inflow main pipe 4.5 through the inflow rotary joint 4.3.
  • One end of the spindle 4.13 has a hole, and the formed hollow portion serves as a section of flow path for the coolant.
  • the outflow branch pipe 4.7 is connected to the hollow part of the spindle 4.13, and the orifice is connected to the coolant outflow pipe 4.1 through the outflow rotary joint 4.2.
  • Thermal conductive medium 4.10 requires the use of thermal conductive materials with good heat transfer properties, which can be tin, graphite mixed with ceramic glue, etc.
  • the melting point of tin is 231.89°C
  • the cooling granulation drum 4 operates at a temperature of about 600°C, so tin will undergo a phase change from solid to liquid, while the boiling point of tin is 2260°C, which is much higher than the working temperature, so it is very Stable and will not cause danger of boiling.
  • the thermal conductive medium 4.10 is a metal such as tin
  • an expansion cavity 4.11 needs to be provided on one side of the cooling granulation drum 4 to avoid the phase change of the thermal conductive material causing volume expansion and damage to the drum.
  • the working principle of the cooling granulation drum 4 is: the coolant continuously enters the cooling coil 4.6 from the coolant inflow pipe 4.4, and flows out from the coolant outflow pipe 4.1.
  • the high-temperature molten slag flows to the surface of the outer cylinder 4.9, the high-temperature molten slag exchanges heat with the coolant in the cooling coil 4.6 through the heat transfer medium 4.10.
  • the high-temperature molten slag quickly cools down to form a glassy state, and the heated coolant flows out through the coolant.
  • the cooling granulating drum 4 rotates under the control of the drive motor 3.
  • the drum speed can be adjusted according to the amount of slag and the cooling speed.
  • the cooling granulating drum 4 rotates to a certain angle, the high-temperature slag cools to form a glassy state, and the glassy slag adheres to it.
  • the roller On the surface of the outer cylinder 4.9, as the roller continues to rotate to the meshing position of the two outer cylinders 4.9, it is then crushed and granulated.
  • FIG. 5 An implementation example of the present invention is shown in Figure 5.
  • the blast furnace slag tank 1 is connected to the slag pool.
  • High-temperature molten slag flows along the blast furnace slag tank 1.
  • the width of the slot 1.1 can be adjusted according to the production speed.
  • several sets of cooling granulation rollers 4 are arranged in the lower part of the slag tank. Two cooling granulation rollers 4 form a group. N groups can be set according to needs.
  • the specific operation process of the blast furnace slag drum quick-cooling dry treatment device is as follows:
  • Liquid high-temperature slag enters the blast furnace slag tank 1 at the bottom of the slag pool, flows down to the surface of the cooling granulation drum 4 through the slot 1.1 at the bottom of the blast furnace slag tank 1, and the coolant flows in the closed cooling coil 4.6, and the cooling coil 4.6
  • the heat transfer medium 4.10 buried in the closed space of the inner and outer cylinders exchanges heat with the slag on the surface of the outer cylinder 4.9, thereby achieving complete separation of the coolant and the slag.
  • the cooling coil 4.6 is not in direct contact with the slag.
  • the molten slag adheres to the surface of the outer cylinder 4.9, and the heat is transferred from the heat transfer medium 4.10 between the inner and outer cylinders to the cooling coil 4.6 buried in it. It is taken away by the coolant in the cooling coil 4.6, and the molten slag quickly cools to about 600°C to form Glassy state.
  • the glassy slag adheres to the surface of the cooling granulating drum 4 and continues to rotate as the drum continues to rotate. When it reaches the meshing point of the two outer cylinders 4.9, it is granulated into powder under the action of the crushing teeth machined on the surface of the outer cylinder 4.9.
  • the granulated slag enters Heat exchanger 5 recovers waste heat.
  • the heat exchanger 5 is equipped with an oscillation mechanism to prevent powder from clogging the channel. When the device is working, slag granulation and waste heat recovery can be carried out simultaneously, realizing continuous operation of the device.

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Abstract

A drum quick-cooling dry treatment device for blast furnace slag for use in waste heat recovery, comprising a blast furnace slag trough, multiple sets of cooling granulation drums and a heat exchanger. The cooling granulation drum comprises an inner drum, an outer drum, a cooling coil and a heat conduction medium. The closed space between the inner drum and the outer drum is filled with the heat conduction medium. The cooling coil is embedded in the heat conduction medium in the closed space between the inner drum and the outer drum and is completely isolated from the slag. When the device works, the drum rotates, the slag flows naturally down from a width-adjustable notch at the bottom of the blast furnace slag trough and is attached to the surface of the outer drum. Heat is transferred from the heat conduction medium between the inner drum and the outer drum to the cooling coil embedded therein, and is taken away by a coolant in the cooling coil. The slag is rapidly cooled into a vitreous state, is crushed by the outer drum of an engaged gear roller, and enters the heat exchanger for waste heat recovery. During work, molten slag vitrification and slag granulation collection are carried out simultaneously to realize continuous production. The slag can be efficiently recycled, and the waste of high-quality waste heat resources of the liquid slag is effectively reduced.

Description

一种用于余热回收的高炉渣滚筒快冷式干法处理装置A blast furnace slag drum quick-cooling dry treatment device for waste heat recovery 技术领域Technical field
本发明属于冶金高温熔渣处理技术领域,具体涉及一种炉渣与水分离、冷却管不与炉渣直接接触且用于余热回收的高炉渣滚筒快冷式干法处理装置。The invention belongs to the technical field of metallurgical high-temperature slag treatment, and specifically relates to a blast furnace slag drum quick-cooling dry treatment device that separates slag from water, has a cooling tube that is not in direct contact with the slag, and is used for waste heat recovery.
背景技术Background technique
高炉渣是钢铁冶金工业的主要副产品,在现有的生产工艺条件下,每生产1t生铁约产生0.3t以上高炉渣,其温度在1450~1550℃左右,每吨炉渣约含有1.8MJ的余热可供回收利用。中国目前是全球最大的钢铁生产国,2020年,全国生铁生产总量88752.4万吨,依照行业平均水平预估产生2.66亿吨炉渣,其所含的热量相当于1636.5万吨标准煤燃烧量(1吨标准煤燃烧所产生的热量为29307.6kJ),如果能有效回收利用高温炉渣中的热能,将减少数万吨C02、SO 2和H 2S等大气污染物。目前处理高温炉渣的方法主要包括湿法和干法两种。湿法即水淬法,是目前使用最为广泛的一种方法。该方法虽然具有粒度小和玻璃体含量高等优点,但是大量浪费水资源与高品位热能,同时还会产生含硫气体,污染环境。干法包括转杯法、滚筒法、转盘法等,主要通过离心力与风冷的双重作用达到粒化熔渣的目的。传统的干法处理方式由于风冷效率低下及高温熔渣流态的不可控性,最终产品质量欠佳,能用于水泥生产的玻璃颗粒含量相对较低,且该法设备结构复杂,稳定性不佳。 Blast furnace slag is the main by-product of the iron and steel metallurgical industry. Under the current production process conditions, more than 0.3t of blast furnace slag is produced for every 1t of pig iron produced. Its temperature is around 1450~1550℃. Each ton of slag contains about 1.8MJ of waste heat. For recycling. China is currently the world's largest steel producer. In 2020, the country's total pig iron production was 887.524 million tons. According to the industry average, it is estimated that 266 million tons of slag will be produced. The heat contained in it is equivalent to the burning of 16.365 million tons of standard coal (1 The heat generated by the combustion of a ton of standard coal is 29307.6kJ). If the heat energy in high-temperature slag can be effectively recycled, tens of thousands of tons of atmospheric pollutants such as CO2, SO2 , and H2S will be reduced. At present, the methods for treating high-temperature slag mainly include wet method and dry method. The wet method, that is, the water quenching method, is currently the most widely used method. Although this method has the advantages of small particle size and high vitreous content, it wastes a lot of water resources and high-grade heat energy, and also produces sulfur-containing gas and pollutes the environment. Dry methods include rotary cup method, drum method, rotating disk method, etc., which mainly achieve the purpose of granulating slag through the dual effects of centrifugal force and air cooling. Due to the low efficiency of air cooling and the uncontrollability of high-temperature slag flow patterns, the traditional dry processing method results in poor final product quality. The content of glass particles that can be used for cement production is relatively low, and the equipment structure of this method is complex and unstable. Not good.
发明内容Contents of the invention
本发明针对现有技术中的不足,提供一种用于余热回收的高炉渣滚筒快冷式干法处理装置。装置运行时,高温熔渣通过高炉渣槽底部的槽口向下流动,附着在下方的冷却粒化滚筒上,冷却粒化滚筒由内外筒组成,内外筒两端密封,中间封闭空腔内填充导热介质。冷却液在封闭的冷却盘管中流动,冷却盘管埋在内外筒之间的导热介质中。高温熔渣附着在外筒表面,热量由内外筒之间的导热介质传递给埋在其中的冷却管,由冷却管中冷却液带走,高温熔渣迅速降温至600℃左右形成玻璃态。冷却粒化滚筒继续旋转,当转至一定角度时,两个相互啮合的外筒挤压粉碎炉渣,炉渣下落进入换热器实现余热回收。In view of the deficiencies in the prior art, the present invention provides a blast furnace slag drum quick-cooling dry processing device for waste heat recovery. When the device is running, high-temperature molten slag flows downward through the slot at the bottom of the blast furnace slag tank and adheres to the cooling granulation drum below. The cooling granulation drum is composed of an inner and outer cylinder. Both ends of the inner and outer cylinder are sealed, and the middle closed cavity is filled. Thermal medium. The coolant flows in a closed cooling coil, which is buried in the heat transfer medium between the inner and outer cylinders. The high-temperature slag adheres to the surface of the outer cylinder, and the heat is transferred from the heat-conducting medium between the inner and outer cylinders to the cooling tubes buried in it, and is taken away by the coolant in the cooling tubes. The high-temperature slag quickly cools to about 600°C to form a glassy state. The cooling granulating drum continues to rotate. When it rotates to a certain angle, the two intermeshing outer drums squeeze and crush the slag, and the slag falls into the heat exchanger to recover waste heat.
为实现上述目的,本发明采用以下技术方案:In order to achieve the above objects, the present invention adopts the following technical solutions:
一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于,包括安装在支架上的高炉渣槽、若干组冷却粒化滚筒和换热器;A blast furnace slag drum quick-cooling dry treatment device for waste heat recovery, which is characterized in that it includes a blast furnace slag tank installed on a bracket, several sets of cooling granulation drums and heat exchangers;
高温熔渣通过高炉渣槽底部设置的可调宽度的槽口向下流动并附着在冷却粒化滚筒外壁,高温熔渣被冷却成玻璃态的炉渣,玻璃态的炉渣被若干组沿垂直方向布置的冷却粒化滚筒依 次挤压粉碎,最终进入换热器进行余热回收;The high-temperature molten slag flows downward through the adjustable-width slot set at the bottom of the blast furnace slag tank and adheres to the outer wall of the cooling granulation drum. The high-temperature molten slag is cooled into glassy slag. The glassy slag is arranged in several groups in the vertical direction. The cooling granulation roller is squeezed and crushed in sequence, and finally enters the heat exchanger for waste heat recovery;
其中,所述冷却粒化滚筒两两一组,每个冷却粒化滚筒包括外筒、内筒和冷却盘管,所述外筒和内筒之间形成的封闭空间内填充有导热介质,所述冷却盘管埋藏在导热介质中。Wherein, the cooling granulation rollers are arranged in pairs, and each cooling granulation roller includes an outer cylinder, an inner cylinder and a cooling coil. The closed space formed between the outer cylinder and the inner cylinder is filled with heat-conducting medium, so The cooling coil is embedded in the heat transfer medium.
为优化上述技术方案,采取的具体措施还包括:In order to optimize the above technical solutions, specific measures taken also include:
进一步地,所述高炉渣槽内层为绝热涂层,中间为耐高温材料,外层进行保温处理。Further, the inner layer of the blast furnace slag tank is an insulating coating, the middle layer is a high-temperature resistant material, and the outer layer is thermally insulated.
进一步地,所述外筒表面加工有粉碎轮齿,同组的两个外筒相互啮合。Further, the surface of the outer cylinder is processed with crushing gear teeth, and two outer cylinders in the same group mesh with each other.
进一步地,所述内筒轴向贯穿有主轴,所述主轴由驱动电机驱动,进而带动整个冷却粒化滚筒的转动。Furthermore, the inner cylinder is axially penetrated by a main shaft, and the main shaft is driven by a driving motor, thereby driving the rotation of the entire cooling and granulating drum.
进一步地,所述冷却盘管中流动冷却液,冷却液依次通过冷却液流入管、流入总管和流入支管流入冷却盘管,冷却盘管中的冷却液依次通过流出支管和冷却液流出管流出;所述流入总管固定套设在主轴伸出内筒外的部分,所述冷却液流入管通过流入旋转接头与流入总管相连;主轴部分中空,所述流出支管通过主轴的中空部分和流出旋转接头与冷却液流出管相连;其中,所述冷却液流入管、流入旋转接头和冷却液流出管不随主轴转动。Further, the cooling liquid flows in the cooling coil, and the cooling liquid flows into the cooling coil through the cooling liquid inflow pipe, the inflow main pipe and the inflow branch pipe, and the cooling liquid in the cooling coil flows out through the outflow branch pipe and the cooling liquid outflow pipe in sequence; The main inflow pipe is fixedly sleeved on the part of the main shaft that extends out of the inner cylinder, and the coolant inflow pipe is connected to the main inflow pipe through the inflow rotary joint; the main shaft is partially hollow, and the outflow branch pipe is connected to the main inflow pipe through the hollow part of the main shaft and the outflow rotary joint. The cooling liquid outflow pipes are connected; wherein, the cooling liquid inflow pipe, the inflow rotary joint and the cooling liquid outflow pipe do not rotate with the main shaft.
进一步地,所述冷却粒化滚筒的一侧设置有膨胀腔,同组的两个膨胀腔错位布置,所述膨胀腔与外筒和内筒之间的封闭空间连通,用于容纳导热介质膨胀后的体积。Further, an expansion chamber is provided on one side of the cooling granulation drum. Two expansion chambers in the same group are arranged in a staggered manner. The expansion chamber is connected to the closed space between the outer cylinder and the inner cylinder and is used to accommodate the expansion of the heat-conducting medium. the subsequent volume.
进一步地,所述导热介质为锡或混合有陶瓷胶的石墨。Further, the thermal conductive medium is tin or graphite mixed with ceramic glue.
进一步地,所述换热器置于冷却粒化滚筒的正下方,被冷却粒化滚筒粉碎后的炉渣通过收集口进入换热器,换热器设置有震荡机构。Further, the heat exchanger is placed directly below the cooling granulation drum, and the slag crushed by the cooling granulation drum enters the heat exchanger through the collection port. The heat exchanger is provided with an oscillation mechanism.
本发明的有益效果是:本装置工作时,熔渣玻璃化和熔渣粒化收集过程同时进行,实现连续化生产;实现了冷却液与炉渣的完全分离,冷却管不与炉渣直接接触,避免了冷却管因热疲劳损坏导致冷却液泄露,从本质上杜绝了冷却液与炉渣接触的风险;可对熔渣进行高效的回收,有效减少液态熔渣高品质余热资源严重浪费,热能回收效率达70%,对高温熔渣的余热回收及高效利用有着重大意义。The beneficial effects of the invention are: when the device is working, the slag vitrification and slag granulation collection processes are carried out simultaneously to realize continuous production; the cooling liquid and the slag are completely separated, and the cooling tube is not in direct contact with the slag to avoid It eliminates the leakage of coolant due to thermal fatigue damage of the cooling pipe, essentially eliminating the risk of contact between the coolant and the slag; it can efficiently recycle the slag, effectively reducing the serious waste of high-quality waste heat resources of liquid slag, and the heat energy recovery efficiency reaches 70%, which is of great significance to the waste heat recovery and efficient utilization of high-temperature slag.
附图说明Description of drawings
图1为本发明高炉渣滚筒快冷式干法处理装置的结构示意图。Figure 1 is a schematic structural diagram of the blast furnace slag drum rapid cooling dry processing device of the present invention.
图2a为本发明高炉渣槽的结构示意图。Figure 2a is a schematic structural diagram of a blast furnace slag tank according to the present invention.
图2b为本发明高炉渣槽底部槽口的结构示意图。Figure 2b is a schematic structural diagram of the notch at the bottom of the blast furnace slag tank according to the present invention.
图3为本发明冷却粒化滚筒的结构示意图。Figure 3 is a schematic structural diagram of the cooling granulation drum of the present invention.
图4a为本发明冷却粒化滚筒中冷却盘管的流道剖视图。Figure 4a is a cross-sectional view of the flow path of the cooling coil in the cooling granulation drum of the present invention.
图4b为本发明冷却粒化滚筒中冷却盘管的流道示意图。Figure 4b is a schematic diagram of the flow path of the cooling coil in the cooling granulation drum of the present invention.
图5为本发明对炉渣进行粒化粉碎的工作示意图。Figure 5 is a schematic diagram of the present invention's operation of granulating and crushing slag.
附图标记如下:1-高炉渣槽;1.1-槽口;2-支架;3-驱动电机;4-冷却粒化滚筒;4.1-冷却液流出管;4.2流出旋转接头;4.3流入旋转接头;4.4冷却液流入管;4.5流入总管;4.6-冷却盘管;4.7-流出支管;4.8-流入支管;4.9-外筒;4.10-导热介质;4.11-膨胀腔;4.12-内筒;4.13-主轴;5-换热器。The reference signs are as follows: 1-blast furnace slag tank; 1.1-notch; 2-bracket; 3-driving motor; 4-cooling granulating drum; 4.1-coolant outflow pipe; 4.2 outflow rotary joint; 4.3 inflow rotary joint; 4.4 Coolant inflow pipe; 4.5 inflow main pipe; 4.6-cooling coil; 4.7-outflow branch pipe; 4.8-inflow branch pipe; 4.9-outer cylinder; 4.10-heat transfer medium; 4.11-expansion chamber; 4.12-inner cylinder; 4.13-spindle; 5 -Heat Exchanger.
具体实施方式Detailed ways
现在结合附图对本发明作进一步详细的说明。The present invention will now be described in further detail with reference to the accompanying drawings.
如图1所示的高炉渣滚筒快冷式干法处理装置,包括高炉渣槽1、支架2、驱动电机3、冷却粒化滚筒4和换热器5。高炉渣槽1置于高温熔渣池底部,冷却粒化滚筒4用于将从高炉渣槽1流下的液态熔渣快速冷却玻璃化并粉碎。工作时,当高温液态熔渣经熔渣池底部的高炉渣槽1流下后,附着在冷却粒化滚筒4表面,冷却粒化滚筒4内布置冷却盘管4.6,冷却液在冷却盘管4.6中持续流动,熔渣在盘管内冷却液作用下迅速降温形成玻璃态附着于冷却粒化滚筒4表面。冷却粒化滚筒4由驱动电机3驱动,驱动电机3采用减速电机,可根据熔渣流量与温度调节电机转速,减速电机通过机脚固定在机座上。在驱动电机3的控制下,冷却粒化滚筒4继续转动,当转至一定角度时,附着于冷却粒化滚筒4表面的玻璃态炉渣被相互啮合的冷却粒化滚筒4表面挤压粉碎,形成粉末,随后下落进入换热器5。The blast furnace slag drum quick-cooling dry processing device shown in Figure 1 includes a blast furnace slag tank 1, a bracket 2, a drive motor 3, a cooling granulating drum 4 and a heat exchanger 5. The blast furnace slag tank 1 is placed at the bottom of the high-temperature slag pool, and the cooling granulation drum 4 is used to quickly cool the liquid slag flowing down from the blast furnace slag tank 1 to vitrify and pulverize it. During operation, when high-temperature liquid slag flows down through the blast furnace slag tank 1 at the bottom of the slag pool, it adheres to the surface of the cooling granulation drum 4. A cooling coil 4.6 is arranged in the cooling granulation drum 4, and the coolant is in the cooling coil 4.6. Continuously flowing, the molten slag rapidly cools down under the action of the coolant in the coil and forms a glassy state that adheres to the surface of the cooling granulation drum 4. The cooling granulating drum 4 is driven by the drive motor 3, which adopts a reduction motor, which can adjust the motor speed according to the slag flow and temperature. The reduction motor is fixed on the machine base through the machine feet. Under the control of the drive motor 3, the cooling granulating drum 4 continues to rotate. When it rotates to a certain angle, the glassy slag attached to the surface of the cooling granulating drum 4 is extruded and crushed by the intermeshing surfaces of the cooling granulating drum 4, forming a The powder then falls into heat exchanger 5.
高炉渣槽1的结构如图2a和2b所示,高炉渣槽1的内层为绝热涂层,中间为耐高温材料,外层进行保温处理。高炉渣槽1的底部设置有可调宽度的槽口1.1,能调节开度以控制高温熔渣的流量,确保高温熔渣能在冷却粒化滚筒4表面形成均匀的膜。The structure of the blast furnace slag tank 1 is shown in Figures 2a and 2b. The inner layer of the blast furnace slag tank 1 is an insulating coating, the middle is a high-temperature resistant material, and the outer layer is thermally insulated. The bottom of the blast furnace slag tank 1 is provided with an adjustable-width slot 1.1, which can adjust the opening to control the flow of high-temperature slag and ensure that the high-temperature slag can form a uniform film on the surface of the cooling granulation drum 4.
冷却粒化滚筒4的结构如图3所示,冷却粒化滚筒4内部布置着冷却盘管4.6,冷却盘管4.6螺旋布置在外筒4.9和内筒4.12之间。外筒4.9和内筒4.12间充满着导热介质4.10,冷却盘管4.6埋在导热介质4.10中。内筒4.12轴向贯穿有主轴4.13,主轴4.13由驱动电机3驱动,进而带动整个冷却粒化滚筒4的转动。冷却盘管4.6中持续流动冷却液,冷却液依次通过冷却液流入管4.4、流入总管4.5和流入支管4.8流入冷却盘管4.6,冷却盘管4.6中的冷却液依次通过流出支管4.7和冷却液流出管4.1流出。管道内冷却液的流动轨迹如图4a和4b所示。The structure of the cooling granulation drum 4 is shown in Figure 3. A cooling coil 4.6 is arranged inside the cooling granulation drum 4, and the cooling coil 4.6 is spirally arranged between the outer cylinder 4.9 and the inner cylinder 4.12. The space between the outer cylinder 4.9 and the inner cylinder 4.12 is filled with heat transfer medium 4.10, and the cooling coil 4.6 is buried in the heat transfer medium 4.10. The inner cylinder 4.12 is axially penetrated by a main shaft 4.13. The main shaft 4.13 is driven by the drive motor 3, which in turn drives the rotation of the entire cooling and granulating drum 4. Coolant continues to flow in the cooling coil 4.6. The coolant flows into the cooling coil 4.6 through the coolant inflow pipe 4.4, the main inflow pipe 4.5 and the inflow branch pipe 4.8. The coolant in the cooling coil 4.6 flows out through the outflow branch pipe 4.7 and the coolant in sequence. Outflow from tube 4.1. The flow trajectory of the coolant in the pipe is shown in Figures 4a and 4b.
具体地,流入总管4.5固定套设在主轴4.13伸出内筒4.12的部分,冷却液流入管4.4通过流入旋转接头4.3与流入总管4.5相连。主轴4.13的一端开孔,形成的中空部分作为冷却液的一段流道。流出支管4.7连接主轴4.13的中空部分,孔口处通过流出旋转接头4.2与冷却液流出管4.1相连。主轴4.13转动时,冷却液流入管4.4、流入旋转接头4.3和冷却液 流出管4.1不随之转动。Specifically, the inflow main pipe 4.5 is fixedly sleeved on the part of the main shaft 4.13 extending out of the inner cylinder 4.12, and the coolant inflow pipe 4.4 is connected to the inflow main pipe 4.5 through the inflow rotary joint 4.3. One end of the spindle 4.13 has a hole, and the formed hollow portion serves as a section of flow path for the coolant. The outflow branch pipe 4.7 is connected to the hollow part of the spindle 4.13, and the orifice is connected to the coolant outflow pipe 4.1 through the outflow rotary joint 4.2. When the spindle 4.13 rotates, the coolant inflow pipe 4.4, the inflow rotary joint 4.3 and the coolant outflow pipe 4.1 do not rotate accordingly.
导热介质4.10要求选用具有良好传热性能的导热材料,可以为锡、混合有陶瓷胶的石墨等。锡的熔点为231.89℃,冷却粒化滚筒4工作时温度在600℃左右,所以锡会发生相变,由固态变成液态,而锡的沸点为2260℃,远远高于工作温度,所以很稳定不会发生沸腾产生危险。因此,当导热介质4.10为锡等金属时,由于工作时相变导致体积变化,需在冷却粒化滚筒4一侧设置膨胀腔4.11,避免导热材料相变导致体积膨胀破坏滚筒。Thermal conductive medium 4.10 requires the use of thermal conductive materials with good heat transfer properties, which can be tin, graphite mixed with ceramic glue, etc. The melting point of tin is 231.89°C, and the cooling granulation drum 4 operates at a temperature of about 600°C, so tin will undergo a phase change from solid to liquid, while the boiling point of tin is 2260°C, which is much higher than the working temperature, so it is very Stable and will not cause danger of boiling. Therefore, when the thermal conductive medium 4.10 is a metal such as tin, due to the volume change caused by the phase change during operation, an expansion cavity 4.11 needs to be provided on one side of the cooling granulation drum 4 to avoid the phase change of the thermal conductive material causing volume expansion and damage to the drum.
冷却粒化滚筒4的工作原理为:冷却液持续地从冷却液流入管4.4进入冷却盘管4.6,从冷却液流出管4.1流出。当高温熔渣流至外筒4.9表面时,高温熔渣通过导热介质4.10与冷却盘管4.6内的冷却液进行换热,高温熔渣迅速降温形成玻璃态,被加热的冷却液经冷却液流出管4.1流出。冷却粒化滚筒4在驱动电机3的控制下转动,滚筒转速可根据炉渣量与冷却速度进行调节,当冷却粒化滚筒4转至一定角度后,高温熔渣冷却形成玻璃态,玻璃态炉渣附着于外筒4.9表面,随滚筒继续转动至两外筒4.9啮合位置,然后被粉碎粒化。The working principle of the cooling granulation drum 4 is: the coolant continuously enters the cooling coil 4.6 from the coolant inflow pipe 4.4, and flows out from the coolant outflow pipe 4.1. When the high-temperature molten slag flows to the surface of the outer cylinder 4.9, the high-temperature molten slag exchanges heat with the coolant in the cooling coil 4.6 through the heat transfer medium 4.10. The high-temperature molten slag quickly cools down to form a glassy state, and the heated coolant flows out through the coolant. Outflow from tube 4.1. The cooling granulating drum 4 rotates under the control of the drive motor 3. The drum speed can be adjusted according to the amount of slag and the cooling speed. When the cooling granulating drum 4 rotates to a certain angle, the high-temperature slag cools to form a glassy state, and the glassy slag adheres to it. On the surface of the outer cylinder 4.9, as the roller continues to rotate to the meshing position of the two outer cylinders 4.9, it is then crushed and granulated.
本发明的实施案例如图5所示,高炉渣槽1连接渣池,高温熔渣沿高炉渣槽1流动,高炉渣槽1底部开设有槽口1.1,可以根据生产速度调节槽口1.1的宽度控制熔渣流量,渣槽下部布置有若干组冷却粒化滚筒4,两个冷却粒化滚筒4为一组,可以根据需求设置N组,高温熔渣在接触到第一组冷却粒化滚筒4后迅速降温形成玻璃态,然后依次经过N组冷却粒化滚筒4进行粉碎,粉碎后形成的均匀粉末落入换热器5,完成余热回收。An implementation example of the present invention is shown in Figure 5. The blast furnace slag tank 1 is connected to the slag pool. High-temperature molten slag flows along the blast furnace slag tank 1. There is a slot 1.1 at the bottom of the blast furnace slag tank 1. The width of the slot 1.1 can be adjusted according to the production speed. To control the flow of slag, several sets of cooling granulation rollers 4 are arranged in the lower part of the slag tank. Two cooling granulation rollers 4 form a group. N groups can be set according to needs. When the high-temperature slag comes into contact with the first group of cooling granulation rollers 4 Then it is quickly cooled to form a glassy state, and then passed through N groups of cooling granulation rollers 4 for crushing. The uniform powder formed after crushing falls into the heat exchanger 5 to complete waste heat recovery.
高炉渣滚筒快冷式干法处理装置的具体操作过程如下:The specific operation process of the blast furnace slag drum quick-cooling dry treatment device is as follows:
液态高温熔渣进入熔渣池底部的高炉渣槽1,经高炉渣槽1底部的槽口1.1流下至冷却粒化滚筒4表面,冷却液在封闭的冷却盘管4.6中流动,冷却盘管4.6埋藏在内外筒密闭空间中的导热介质4.10里,通过导热介质4.10与外筒4.9表面的熔渣换热,实现了冷却液与熔渣的完全分离,冷却盘管4.6不与熔渣直接接触,熔渣附着在外筒4.9表面,热量由内外滚筒之间的导热介质4.10传递给埋在其中的冷却盘管4.6,由冷却盘管4.6中的冷却液带走,熔渣迅速降温至600℃左右形成玻璃态。玻璃态炉渣附着在冷却粒化滚筒4表面,随滚筒继续转动,当转至两外筒4.9啮合处时,在外筒4.9表面加工的粉碎齿的作用下粒化形成粉末,经粒化的炉渣进入换热器5进行余热回收。换热器5设置有震荡机构,可以避免粉末堵塞通道。该装置工作时,熔渣粒化和余热回收可同时进行,实现了装置的连续运行。Liquid high-temperature slag enters the blast furnace slag tank 1 at the bottom of the slag pool, flows down to the surface of the cooling granulation drum 4 through the slot 1.1 at the bottom of the blast furnace slag tank 1, and the coolant flows in the closed cooling coil 4.6, and the cooling coil 4.6 The heat transfer medium 4.10 buried in the closed space of the inner and outer cylinders exchanges heat with the slag on the surface of the outer cylinder 4.9, thereby achieving complete separation of the coolant and the slag. The cooling coil 4.6 is not in direct contact with the slag. The molten slag adheres to the surface of the outer cylinder 4.9, and the heat is transferred from the heat transfer medium 4.10 between the inner and outer cylinders to the cooling coil 4.6 buried in it. It is taken away by the coolant in the cooling coil 4.6, and the molten slag quickly cools to about 600°C to form Glassy state. The glassy slag adheres to the surface of the cooling granulating drum 4 and continues to rotate as the drum continues to rotate. When it reaches the meshing point of the two outer cylinders 4.9, it is granulated into powder under the action of the crushing teeth machined on the surface of the outer cylinder 4.9. The granulated slag enters Heat exchanger 5 recovers waste heat. The heat exchanger 5 is equipped with an oscillation mechanism to prevent powder from clogging the channel. When the device is working, slag granulation and waste heat recovery can be carried out simultaneously, realizing continuous operation of the device.
需要注意的是,发明中所引用的如“上”、“下”、“左”、“右”、“前”、“后”等的用语,亦仅为便于叙述的明了,而非用以限定本发明可实施的范围,其相对关系的改变或调整,在无实质变更技术内容下,当亦视为本发明可实施的范畴。It should be noted that terms such as "upper", "lower", "left", "right", "front", "back", etc. cited in the invention are only for convenience of description and are not used to To limit the implementable scope of the present invention, changes or adjustments in relative relationships shall also be regarded as the implementable scope of the present invention as long as the technical content is not substantially changed.
以上仅是本发明的优选实施方式,本发明的保护范围并不仅局限于上述实施例,凡属于本发明思路下的技术方案均属于本发明的保护范围。应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理前提下的若干改进和润饰,应视为本发明的保护范围。The above are only preferred embodiments of the present invention. The protection scope of the present invention is not limited to the above-mentioned embodiments. All technical solutions that fall under the idea of the present invention belong to the protection scope of the present invention. It should be pointed out that for those of ordinary skill in the art, several improvements and modifications without departing from the principle of the present invention should be regarded as the protection scope of the present invention.

Claims (8)

  1. 一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于,包括安装在支架(2)上的高炉渣槽(1)、若干组冷却粒化滚筒(4)和换热器(5);A blast furnace slag drum quick-cooling dry treatment device for waste heat recovery, which is characterized by including a blast furnace slag tank (1) installed on a bracket (2), several sets of cooling granulation drums (4) and heat exchangers device(5);
    高温熔渣通过高炉渣槽(1)底部设置的可调宽度的槽口(1.1)向下流动并附着在冷却粒化滚筒(4)外壁,高温熔渣被冷却成玻璃态的炉渣,玻璃态的炉渣被若干组沿垂直方向布置的冷却粒化滚筒(4)依次挤压粉碎,最终进入换热器(5)进行余热回收;The high-temperature molten slag flows downward through the adjustable-width slot (1.1) provided at the bottom of the blast furnace slag tank (1) and adheres to the outer wall of the cooling granulation drum (4). The high-temperature molten slag is cooled into glassy slag. The glassy slag The slag is sequentially squeezed and crushed by several sets of cooling granulation rollers (4) arranged in the vertical direction, and finally enters the heat exchanger (5) for waste heat recovery;
    其中,所述冷却粒化滚筒(4)两两一组,每个冷却粒化滚筒(4)包括外筒(4.9)、内筒(4.12)和冷却盘管(4.6),所述外筒(4.9)和内筒(4.12)之间形成的封闭空间内填充有导热介质(4.10),所述冷却盘管(4.6)埋藏在导热介质(4.10)中。Wherein, the cooling granulation rollers (4) are grouped in pairs. Each cooling granulation roller (4) includes an outer cylinder (4.9), an inner cylinder (4.12) and a cooling coil (4.6). The outer cylinder (4.6) The closed space formed between 4.9) and the inner cylinder (4.12) is filled with heat-conducting medium (4.10), and the cooling coil (4.6) is buried in the heat-conducting medium (4.10).
  2. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述高炉渣槽(1)内层为绝热涂层,中间为耐高温材料,外层进行保温处理。A blast furnace slag drum quick-cooling dry processing device for waste heat recovery as claimed in claim 1, characterized in that: the inner layer of the blast furnace slag tank (1) is an insulating coating, and the middle is a high-temperature resistant material. The outer layer is insulated.
  3. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述外筒(4.9)表面加工有粉碎轮齿,同组的两个外筒(4.9)相互啮合。A blast furnace slag drum quick-cooling dry processing device for waste heat recovery as claimed in claim 1, characterized in that: the surface of the outer cylinder (4.9) is processed with crushing gear teeth, and the two outer cylinders in the same group (4.9) Intermeshing.
  4. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述内筒(4.12)轴向贯穿有主轴(4.13),所述主轴(4.13)由驱动电机(3)驱动,进而带动整个冷却粒化滚筒(4)的转动。A blast furnace slag drum quick-cooling dry treatment device for waste heat recovery as claimed in claim 1, characterized in that: the inner cylinder (4.12) has a main shaft (4.13) axially penetrating through it, and the main shaft (4.13 ) is driven by the driving motor (3), which in turn drives the rotation of the entire cooling granulating drum (4).
  5. 如权利要求4所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述冷却盘管(4.6)中流动冷却液,冷却液依次通过冷却液流入管(4.4)、流入总管(4.5)和流入支管(4.8)流入冷却盘管(4.6),冷却盘管(4.6)中的冷却液依次通过流出支管(4.7)和冷却液流出管(4.1)流出;所述流入总管(4.5)固定套设在主轴(4.13)伸出内筒(4.12)外的部分,所述冷却液流入管(4.4)通过流入旋转接头(4.3)与流入总管(4.5)相连;主轴(4.13)部分中空,所述流出支管(4.7)通过主轴(4.13)的中空部分和流出旋转接头(4.2)与冷却液流出管(4.1)相连;其中,所述冷却液流入管(4.4)、流入旋转接头(4.3)和冷却液流出管(4.1)不随主轴(4.13)转动。A blast furnace slag roller quick-cooling dry processing device for waste heat recovery as claimed in claim 4, characterized in that: cooling liquid flows in the cooling coil (4.6), and the cooling liquid flows through the cooling liquid inflow pipe in sequence. (4.4), the inflow main pipe (4.5) and the inflow branch pipe (4.8) flow into the cooling coil (4.6), and the coolant in the cooling coil (4.6) flows out through the outflow branch pipe (4.7) and the coolant outflow pipe (4.1) in sequence; The inflow main pipe (4.5) is fixedly sleeved on the part of the main shaft (4.13) that extends out of the inner cylinder (4.12), and the coolant inflow pipe (4.4) is connected to the inflow main pipe (4.5) through the inflow rotary joint (4.3); The main shaft (4.13) is partially hollow, and the outflow branch pipe (4.7) is connected to the coolant outflow pipe (4.1) through the hollow part of the main shaft (4.13) and the outflow rotary joint (4.2); wherein, the coolant inflow pipe (4.4) , the inflow rotary joint (4.3) and the coolant outflow pipe (4.1) do not rotate with the main shaft (4.13).
  6. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述冷却粒化滚筒(4)的一侧设置有膨胀腔(4.11),同组的两个膨胀腔(4.11)错位布置,所述膨胀腔(4.11)与外筒(4.9)和内筒(4.12)之间的封闭空间连通,用于容纳导热介质(4.10)膨胀后的体积。A blast furnace slag drum quick-cooling dry processing device for waste heat recovery as claimed in claim 1, characterized in that: an expansion chamber (4.11) is provided on one side of the cooling granulation drum (4), and The two expansion chambers (4.11) of the set are arranged in a staggered manner. The expansion chamber (4.11) is connected to the closed space between the outer cylinder (4.9) and the inner cylinder (4.12) and is used to accommodate the expanded volume of the heat transfer medium (4.10). .
  7. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在于:所述导热介质(4.10)为锡或混合有陶瓷胶的石墨。A blast furnace slag drum quick-cooling dry processing device for waste heat recovery as claimed in claim 1, characterized in that: the heat transfer medium (4.10) is tin or graphite mixed with ceramic glue.
  8. 如权利要求1所述的一种用于余热回收的高炉渣滚筒快冷式干法处理装置,其特征在 于:所述换热器(5)置于冷却粒化滚筒(4)的正下方,被冷却粒化滚筒(4)粉碎后的炉渣通过收集口进入换热器(5),换热器(5)设置有震荡机构。A blast furnace slag drum quick-cooling dry processing device for waste heat recovery according to claim 1, characterized in that: the heat exchanger (5) is placed directly below the cooling granulation drum (4), The slag crushed by the cooling granulation drum (4) enters the heat exchanger (5) through the collection port, and the heat exchanger (5) is equipped with an oscillation mechanism.
PCT/CN2022/128585 2022-04-02 2022-10-31 Drum quick-cooling dry treatment device for blast furnace slag for use in waste heat recovery WO2023184962A1 (en)

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CN117208345B (en) * 2023-11-09 2024-01-23 江苏履信新材料科技有限公司 Flaking packaging system for molten salt production

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