WO1995015929A1 - Slag granulation method and container by air crushing - Google Patents

Slag granulation method and container by air crushing Download PDF

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Publication number
WO1995015929A1
WO1995015929A1 PCT/CN1994/000098 CN9400098W WO9515929A1 WO 1995015929 A1 WO1995015929 A1 WO 1995015929A1 CN 9400098 W CN9400098 W CN 9400098W WO 9515929 A1 WO9515929 A1 WO 9515929A1
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WO
WIPO (PCT)
Prior art keywords
slag
gas
pool
tundish
granulator
Prior art date
Application number
PCT/CN1994/000098
Other languages
French (fr)
Chinese (zh)
Inventor
Yongzhi Li
Tianfu Geng
Kaiji Li
Shirong Xia
Yi Peng
Bin Ye
Guomin Hu
Changjian Miao
Shuqi Lai
Shimin Li
Zhenqiang Zhou
Original Assignee
Chengdu Iron & Steel Works
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 Chengdu Iron & Steel Works filed Critical Chengdu Iron & Steel Works
Priority to AU11901/95A priority Critical patent/AU683520B2/en
Publication of WO1995015929A1 publication Critical patent/WO1995015929A1/en

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Classifications

    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/02Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
    • B01J2/04Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
    • 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
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • 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
    • C21B2400/026Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/062Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/066Receptacle features where the slag is treated
    • C21B2400/072Tanks to collect the slag, e.g. water tank

Definitions

  • the invention relates to a method and a device for granulating slag, in particular to a method and a device for granulating and granulating copper slag. Background technique
  • Japanese Patent No. 8120.061 discloses a technology for blowing slag of a converter with compressed air and cooling it with water. Utilizing this patent, it is sprayed under water pressure of 0.7Mpa, water-cooled, the granulation rate reaches 91%, and the air consumption is 500-1000N Vt slag.
  • Chinese Patent No. 882 11 276 ⁇ 7 discloses a steel slag wind granulation device, which is composed of a tundish, a granulator, and a pool.
  • the bottom of the tundish and the flow slot have a certain slope.
  • the granulator uses compressed air as the air source, and the front side is arranged with a sparge-shaped spray hole.
  • the steel slag ladle needs to be hoisted and tilted to the tundish by a crane.
  • the working conditions are harsh, unsafe, and the productivity is not high.
  • the granulator with nozzles arranged in a ⁇ shape has a high air consumption and a low utilization rate of compressed air.
  • Gas is used as the gas source of the granulator.
  • the residual molten steel is severely oxidized during granulation.
  • the air pollution is serious and an air compressor and a gas supply line need to be installed.
  • the gas source investment is large.
  • the purpose of the present invention is to provide a method and a device for slag gas granulation with simple process, saving investment, convenient operation, safe and reliable, saving energy, eliminating environmental pollution and high productivity.
  • the slag gas granulation method according to the present invention includes the following steps:
  • crushed liquid slag droplets are cooled and solidified during forward flight, forming spherical slag particles, which are scattered in the sediment pool for further cooling;
  • the slag gas granulation device includes: a slag bag overturning device, a tundish, a granulator, a pool, a slag retaining wall and a gas source; a slag bag overturning mechanism for liquid
  • the slag is tipped to the tundish; the liquid slag flows out of the tundish.
  • the granulator is located below the tundish and is connected to an air source. The slag breaks and falls into the pool.
  • the pore diameter of the bottom row of the spray holes is larger than the pore diameters of both sides.
  • the angle of the centerline of the vertical apertures on both sides can be varied from 0-120 °.
  • the slag gas granulation device of the present invention further includes a dust removal device.
  • the device is composed of a water pipe arranged around the water pool, and a plurality of spray holes are distributed on the water pipe, and a dustproof leather is added to the pool.
  • the overturning mechanism provided by the slag gas granulation device of the present invention is used to overturn the slag containing bag, so that the slag therein is poured into the tundish.
  • the tipping mechanism further includes a slag bag supporting mechanism and a positioning device for preventing the slag bag from tipping over and falling off.
  • the slag gas granulation device of the present invention is further provided with a slag retaining wall to prevent the slag from flowing into the pool and causing an explosion, and the slag retaining wall is located between the granulator and the pool.
  • FIG. 1 is a general layout diagram of the present invention
  • Figure 2 is a top view of Figure 1, (remove dust prevention leather);
  • Figure 3 shows the dump bag tilting mechanism of the device of the present invention
  • FIG. 4 is a top view of FIG. 3;
  • Figure 5 shows the structure of the slag pack of the device of the present invention
  • FIG. 6 is a U-shaped structure of the granulating nozzle of the device of the present invention.
  • Fig. 7 shows a u-shaped structure of the granulator nozzle holes of the device of the present invention. Detailed description of the examples ⁇
  • the gas source of the granulator uses a large amount of surplus nitrogen or steam from a metallurgical plant, and compressed air can also be used. Nitrogen has the effect of preventing oxidation of residual metal in the slag.
  • the granulator uses nitrogen, and the working pressure of compressed nitrogen is 0.2-0.6Mpa, the gas consumption is 30-50Nm 3 / t, and the ability to treat slag is 2- 3, 5t / min. 0
  • a slag granulation device includes a slag bag tilting mechanism 1, a slag bag 2, a tundish 3, a granulator 9, a pool 4, a slag retaining wall 7, Dedusting device 6, air source 8.
  • the tipping mechanism as shown in FIG. 3, is mainly composed of three parts, that is, a slag bag supporting mechanism 10, a tipping frame 16, and a hydraulic tipping system.
  • a support ear 12 is provided on the upper end of the support 10, and a supporting shaft 13 of the tilting frame 16 is placed in the supporting ear 12.
  • the tilting frame 16 is further provided with a positioning base 17 and another supporting ear is formed on the positioning base 17.
  • the hydraulic system is hinged under the tilting frame through the piston rod of the hydraulic cylinder 19, and the iris of the hydraulic cylinder 19 and the support 20 are hinged.
  • the slag pack 2 has a shaft 21 and positioning 4 to 22, and the positioning shaft cooperates with the supporting ears on the positioning base 17 on the tilting frame.
  • a tundish 3 is provided on the tundish 3.
  • Figures 6 and 7 show that the nozzles of the granulator of the present invention are U-shaped and! ⁇ -Shaped arrangement.
  • the hole diameters 23 of the nozzle holes provided on the side 24 of the granulator 9 which are directly opposite to the slag are not the same.
  • the holes in the bottom row of the holes with a ⁇ -shaped or W-shaped arrangement are larger in diameter than the vertical holes on both sides. Changes between ⁇ 4-14.
  • the angle between the centerlines of the vertical apertures on both sides can be between 0-120. Changes within range.
  • the dust-removing device 6 of the present invention is provided at the periphery of the pool 4.
  • the device is composed of a water pipe 11, and water spray holes are arranged in the water pipe 11.
  • a slag retaining wall 7 is provided on the side of the pool 4 near the granulator.
  • the slag retaining wall is a water-cooled steel jacket. Because of its location between the tundish slag tank and the pool, when special conditions occur, such as sudden power failure Can avoid slag flow Into the pool to completely eliminate the hidden danger of explosion.
  • the water pipe 11 sprays water to form a water curtain around the pool.
  • the cooling and solidification process of the crushed liquid slag droplets is performed in the water curtain, which effectively prevents dust pollution. Adding a dust cover to the outside of the entire pool can effectively prevent water mist and dust mist from spreading and protect the environment.
  • the slag pack 2, the tundish 3, and the tipping mechanism 1 are located on a platform.
  • the cylinder of the hydraulic cylinder 19 is hinged with the support 20 located in the pit.
  • the granulator 9 is provided on the side wall of the platform.
  • a slag retaining wall is arranged between the tundish slag slag tank and the pool.
  • the water consumption is very small, and only the amount of water consumed by evaporation needs to be replenished into the pond. There is no sewage discharge and no secondary pollution will be caused.
  • the optimal gas consumption is 40-60Nm 3 / t slag, while the Fukuyama Iron and Steel Plant in Japan consumes 500-1000Nm 3 / t.
  • the gas source can use a large surplus of nitrogen or steam from the metallurgical plant (compressed air can also be used).
  • the use of nitrogen or steam can prevent the oxidation of residual metals in the slag, which can not only reduce environmental pollution, but also improve the recovery rate of residual metals. It can save a lot of energy and improve the comprehensive benefit of the steel mill.
  • Granulated steel slag is convenient for comprehensive utilization. It is an ideal substitute for the production of cement clinker. With small grains and easy grinding, it is very popular among cement plants.
  • steel slag can also be used as sintering raw material or blast furnace flux, and it can also be used as agricultural phosphate fertilizer after wind crushing in the early stage.
  • the device of the invention is simple, the design is advanced, and the effect is remarkable.
  • the hydraulic tipping mechanism and slag pack are safe and reliable, improving working conditions and productivity.
  • the granulators with different apertures and the spray holes in a "U" or shaped arrangement are scientifically and rationally designed, regardless of whether it is slag or metal liquid, which can be safely granulated and dispersed into the slag pool, with low gas consumption and granulation The rate is high.
  • the slag retaining wall can completely avoid the hidden danger of explosion of slag when it encounters water in the event of a power outage or gas outage.
  • the dust removal device improves the working environment and significantly reduces the dust content in the air.
  • the process and the device of the invention have low investment, high productivity, low energy consumption, comprehensive economic benefits and
  • the environmental protection effect is good, and it can be widely applied to the treatment of converter slag, open hearth, electric furnace steel slag, blast furnace smelting slag and non-ferrous smelting slag in metallurgical industry.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Furnace Details (AREA)
  • Manufacture Of Iron (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

The present invention provides a granulation container and method, which comprises tilting mechanism (1) of sludge ladle, sludge ladle (2), tundish (3), granulator (9), water tank (4), barrier wall (7), jet device (6) of cold water for dust elimination and air current (8). The molten slag is poured into the tundish from the sludge ladle by the means of the tilting mechanism. The molten slag flows down from a slag launder of the tundish and then is dispersed by compressed air from small holes which are arranged in the form of or | 1 before the granulator enters into the device for dust elimination to cool and set. The set slag drops into the water tank. The slag particles in the water tank are moved away by a clamshell.

Description

炉渣气碎粒化方法和装置 技术领域  Method and device for slag gas granulation
本发明涉及炉渣的粒化方法及装置, 尤其是铜渣的气碎粒化方法与 装置。 背景技术  The invention relates to a method and a device for granulating slag, in particular to a method and a device for granulating and granulating copper slag. Background technique
现有的冶金炉渣多采用水碎、 热闷、 热泼或水冷弃渣等处理方法。 如日本专利第 8120. 061号公开了一种将转炉的熔渣用压缩空气吹, 用水 冷的技术。 利用该项专利, 在 0. 7Mpa的空气压力下喷吹、 水冷, 粒化率 达到 91% , 耗气量 500 -1000N Vt渣。  Most of the existing metallurgical slags are treated by water crushing, hot stuffing, hot splashing or water cooling. For example, Japanese Patent No. 8120.061 discloses a technology for blowing slag of a converter with compressed air and cooling it with water. Utilizing this patent, it is sprayed under water pressure of 0.7Mpa, water-cooled, the granulation rate reaches 91%, and the air consumption is 500-1000N Vt slag.
中国专利第 88211276· 7号公开了一种钢渣风碎粒化装置, 该装置由 中间包, 粒化器、 水池构成。 中间包的底和流槽有一定斜度, 其粒化器 使用压缩空气作气源, 正面排列有呈 Η形的喷孔。 Chinese Patent No. 882 11 276 · 7 discloses a steel slag wind granulation device, which is composed of a tundish, a granulator, and a pool. The bottom of the tundish and the flow slot have a certain slope. The granulator uses compressed air as the air source, and the front side is arranged with a sparge-shaped spray hole.
但以上现有技术存在下列不足:  However, the above existing technologies have the following disadvantages:
1.钢渣包需用行车吊挂倾翻到中间包, 工作条件恶劣, 不安全, 生 产率不高。  1. The steel slag ladle needs to be hoisted and tilted to the tundish by a crane. The working conditions are harsh, unsafe, and the productivity is not high.
2.喷孔呈 Η形排列的粒化器耗气量较高, 压缩空气利用率不高。 2. The granulator with nozzles arranged in a Η shape has a high air consumption and a low utilization rate of compressed air.
3. 气作为粒化器的气源, 使粒化时残留钢水氧化严重, 空气污染 严重并需要安装空气压缩机及供气管线, 气源投资较大。  3. Gas is used as the gas source of the granulator. The residual molten steel is severely oxidized during granulation. The air pollution is serious and an air compressor and a gas supply line need to be installed. The gas source investment is large.
4.中间包流渣槽与水池之间无安全挡墙, 在特殊情况下存在安全隐 患。  4. There is no safety retaining wall between the tundish slag tank and the pool, and there are hidden safety hazards in special cases.
5.未设置除尘系统, 风碎操作时对环境的污染较严重。 发明的公开  5. There is no dust removal system, and the environmental pollution is severe during windbreak operation. Disclosure of invention
本发明的目的是提供一种工艺简单, 投资节省, 搡作方便, 安全可 靠, 节约能源, 消除环境污染, 生产率高的炉渣气碎粒化方法和装置。  The purpose of the present invention is to provide a method and a device for slag gas granulation with simple process, saving investment, convenient operation, safe and reliable, saving energy, eliminating environmental pollution and high productivity.
根据本发明的炉渣气碎粒化方法包括以下步骤:  The slag gas granulation method according to the present invention includes the following steps:
1)将盛满液态冶金渣的盛渣包吊装到倾翻机构的支承架上, 倾翻机 构将盛渣包逐渐倾翻, 液渣被倒入中间包, 侬靠重力作用液渣从中间包 的流渣槽流出;  1) The slag bag full of liquid metallurgical slag is hoisted to the support frame of the tipping mechanism. The tipping mechanism gradually tilts the slag bag, and the liquid slag is poured into the tundish. Outflow of slag tank;
2)在炉渣从流液槽流出后, 气源的压缩气体从粒化器的喷孔喷出将 流渣击碎; 2) After the slag flows out of the flow tank, the compressed gas from the gas source is ejected from the nozzle of the granulator Slag crushing
3)击碎的液渣滴通过水池周边的除尘装置除尘;  3) The crushed liquid slag drops are removed by the dust removal device around the pool;
4)击碎后的液渣滴在向前飞行中冷却和凝固, 形成球状渣粒, 撒落 在沉渣水池中进一步冷却;  4) The crushed liquid slag droplets are cooled and solidified during forward flight, forming spherical slag particles, which are scattered in the sediment pool for further cooling;
5)用抓斗将水池中的渣粒捞出运走。  5) Use a grab to remove the slag particles from the pool.
根据本发明的炉渣气碎粒化方法, 气源采用压缩氮气或蒸汽, 气源 的工作压力为 0. 2- 0. 6Mpa, 生产每吨粒化渣的耗气量为 30 - 100Nm3/to 根据本发明的炉渣气碎粒化装置包括: 一盛渣包倾翻装置, 一中间 包, 一粒化器, 一水池, 一挡渣墙及气源; 盛渣包倾翻机构用于将液渣 倾翻至中间包; 液渣由中间包流出, 粒化器位于中间包下方并与一气源 相连, 粒化器的前面有呈 ϋ 形或 "形排列的喷孔以喷出高速气流将液渣 击碎并落入水池。 According to the slag gas granulation method of the present invention, compressed gas or compressed gas is used as the gas source, and the working pressure of the gas source is 0.2 to 0.6 Mpa, and the gas consumption per ton of granulated slag is 30-100Nm 3 / t o The slag gas granulation device according to the present invention includes: a slag bag overturning device, a tundish, a granulator, a pool, a slag retaining wall and a gas source; a slag bag overturning mechanism for liquid The slag is tipped to the tundish; the liquid slag flows out of the tundish. The granulator is located below the tundish and is connected to an air source. The slag breaks and falls into the pool.
本发明的粒化器, 其喷孔的底排孔径大于两边孔径。 两边竖排孔径 中心线的夹角可在 0 - 120° 范围内变化。  In the granulator of the present invention, the pore diameter of the bottom row of the spray holes is larger than the pore diameters of both sides. The angle of the centerline of the vertical apertures on both sides can be varied from 0-120 °.
本发明的炉渣气碎粒化装置还包括一除尘装置。 该装置由布置于水 池周边的水管构成, 水管上分布有若干喷孔, 水池上加有防尘革。  The slag gas granulation device of the present invention further includes a dust removal device. The device is composed of a water pipe arranged around the water pool, and a plurality of spray holes are distributed on the water pipe, and a dustproof leather is added to the pool.
本发明的炉渣气碎粒化装置所提供的倾翻机构用于倾翻盛渣包, 使 其中的炉渣倒入中间包。 该倾翻机构进一步包括一盛渣包支承机构和防 止盛渣包倾翻及脱落的定位装置。  The overturning mechanism provided by the slag gas granulation device of the present invention is used to overturn the slag containing bag, so that the slag therein is poured into the tundish. The tipping mechanism further includes a slag bag supporting mechanism and a positioning device for preventing the slag bag from tipping over and falling off.
本发明的炉渣气碎粒化装置, 为防止炉渣流进水池发生爆炸还设置 有挡渣墙, 该挡渣墙位于粒化器与水池之间。 附图的说明  The slag gas granulation device of the present invention is further provided with a slag retaining wall to prevent the slag from flowing into the pool and causing an explosion, and the slag retaining wall is located between the granulator and the pool. Description of the drawings
下面参照附图对本发明的实施例做详细说明。  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
图 1是本发明的总体布置图;  FIG. 1 is a general layout diagram of the present invention;
图 2是图 1的俯视图, (去掉防止尘革) ;  Figure 2 is a top view of Figure 1, (remove dust prevention leather);
图 3 示出了本发明装置的盛渣包倾翻机构;  Figure 3 shows the dump bag tilting mechanism of the device of the present invention;
图 4是图 3的俯视图;  4 is a top view of FIG. 3;
图 5 示出了本发明装置的盛渣包的结构;  Figure 5 shows the structure of the slag pack of the device of the present invention;
图 6 为本发明装置的粒化器喷孔呈 U 形的结构;  FIG. 6 is a U-shaped structure of the granulating nozzle of the device of the present invention;
图 7 为本发明装置的粒化器喷孔呈 u形的结构。 实施例的详细说明 ■  Fig. 7 shows a u-shaped structure of the granulator nozzle holes of the device of the present invention. Detailed description of the examples ■
当装满熔渣的盛渣包 2用行车吊放在倾翻架 1上后, 启动液压缸 19, 盛渣包逐渐倾翻, 熔渣被倒入中间包 3内。 倒入中间包的熔渣依靠重力 的作用通过中间包的流渣褙 28流到粒化器 9前方, 粒化器内喷射出的高 速气流将熔渣击碎, 由于表面张力的作用, 被击碎的液渣滴很快在防尘 水幕内冷却和凝固, 形成粒度为 2mm左右的球状颗粒, 撒落在沉渣水池 4中。 抓斗 5将完全冷却凝固的渣粒从水池 4中捞出, 用运输工具运走。 When the slag bag 2 filled with slag is hoisted on the tilting frame 1 by a crane, the hydraulic cylinder 19 is started, The slag package gradually tipped, and the slag was poured into the tundish 3. The slag poured into the tundish flows through the tundish slag 28 to the front of the granulator 9 by the action of gravity. The high-speed air flow ejected from the granulator crushes the slag. Due to the effect of surface tension, it is hit The broken liquid slag droplets are quickly cooled and solidified in the dust-proof water curtain, forming spherical particles with a particle size of about 2 mm, which are scattered in the sediment pool 4 . Grab 5 removes the completely cooled and solidified slag from pool 4 and removes it by transport.
在本发明所提供的炉渣粒化方法中, 粒化器的气源使用冶金工厂大 量富余的氮气或蒸汽, 也可以使用压缩空气。 氮气具有可防止炉渣残余 金属氧化的作用。 在本发明的实施例中, 粒化器使用氮气, 压缩氮气的 工作压力为 0. 2 - 0. 6Mpa, 耗气量为 30-50Nm3/t, 处理炉渣的能力为 2- 3, 5t/min0 In the slag granulation method provided by the present invention, the gas source of the granulator uses a large amount of surplus nitrogen or steam from a metallurgical plant, and compressed air can also be used. Nitrogen has the effect of preventing oxidation of residual metal in the slag. In the embodiment of the present invention, the granulator uses nitrogen, and the working pressure of compressed nitrogen is 0.2-0.6Mpa, the gas consumption is 30-50Nm 3 / t, and the ability to treat slag is 2- 3, 5t / min. 0
根据本发明的一个实施例所提供的炉渣粒化装置如图所示, 包括盛 渣包倾翻机构 1, 盛渣包 2, 中间包 3, 粒化器 9, 水池 4, 挡渣墙 7, 除尘 装置 6, 气源 8。 该倾翻机构, 如图 3所示, 主要由三大部分組成, 即盛 渣包支承机构 10, 倾翻架 16以及液压倾翻系统。 支承 10上端设置有支承 耳 12, 倾翻架 16的支轴 13置于支承耳 12内, 倾翻架 16上还设有定位座 17, 并在定位座 17上形成另一支承耳。 液压系统, 通过液压缸 19的活塞杆铰 接于倾 架的下面, 液压缸 19的虹体与支座 20铰接。 盛渣包 2上有轴 21, 及定位 4~ώ22, 该定位轴与倾翻架上的定位座 17上的支承耳配合。 当盛 渣包 2被放到倾翻架 16上时, 通过启动液压系统, 餃接于倾翻架 16下面的 液压缸 I9的活塞向上运动, 使整个倾翻架在支承耳 12内转动, 这时置放 在倾翻架上的盛渣包随着倾翻架的转动而逐渐倾翻, 炉渣随即逐渐倾倒 在中间包内。 由于支承耳 12前端有凸起, 该凸起可以起到定位的作用, 可保证盛渣包在倾翻过程中不脱离倾翻机构。 As shown in the figure, a slag granulation device according to an embodiment of the present invention includes a slag bag tilting mechanism 1, a slag bag 2, a tundish 3, a granulator 9, a pool 4, a slag retaining wall 7, Dedusting device 6, air source 8. The tipping mechanism, as shown in FIG. 3, is mainly composed of three parts, that is, a slag bag supporting mechanism 10, a tipping frame 16, and a hydraulic tipping system. A support ear 12 is provided on the upper end of the support 10, and a supporting shaft 13 of the tilting frame 16 is placed in the supporting ear 12. The tilting frame 16 is further provided with a positioning base 17 and another supporting ear is formed on the positioning base 17. The hydraulic system is hinged under the tilting frame through the piston rod of the hydraulic cylinder 19, and the iris of the hydraulic cylinder 19 and the support 20 are hinged. The slag pack 2 has a shaft 21 and positioning 4 to 22, and the positioning shaft cooperates with the supporting ears on the positioning base 17 on the tilting frame. When the slag pack 2 is placed on the tipping frame 16, by starting the hydraulic system, the piston of the hydraulic cylinder I 9 connected to the bottom of the tipping frame 16 moves upward, so that the entire tipping frame rotates within the support ear 12. At this time, the slag bag placed on the tipping rack gradually tipped with the rotation of the tipping rack, and the slag was gradually poured into the tundish. Because the front end of the support ear 12 has a protrusion, the protrusion can play a positioning role, and can ensure that the slag pack does not leave the tipping mechanism during the tipping process.
中间包 3上设有流渣槽 28。  A tundish 3 is provided on the tundish 3.
图 6和图 7示出了本发明粒化器喷孔呈 U型和!^形排列的结构。 在粒 化器 9正对流渣的一面 24上设置的喷孔孔径 23大小不一致, 一般来说呈 ϋ 形或 W形排列的孔的底排横孔的孔径比两边竖孔的孔径大, 孔径一般在 Φ 4-14廳之间变化。 两边竖排孔径的中心线夹角可以在 0 - 120。 范围之 内变化。  Figures 6 and 7 show that the nozzles of the granulator of the present invention are U-shaped and! ^ -Shaped arrangement. The hole diameters 23 of the nozzle holes provided on the side 24 of the granulator 9 which are directly opposite to the slag are not the same. Generally, the holes in the bottom row of the holes with a ϋ-shaped or W-shaped arrangement are larger in diameter than the vertical holes on both sides. Changes between Φ 4-14. The angle between the centerlines of the vertical apertures on both sides can be between 0-120. Changes within range.
如图 1所示, 本发明的除尘装置 6设置在水池 4的周边, 该装置由水 管 11构成, 并在水管 11上排布有喷水孔。 在水池 4靠近粒化器的一边设 有挡渣墙 7, 该挡渣墙为一水冷钢套, 由于其位置在中间包流渣槽与水 池之间, 当特殊情况发生如突然停电、 断气的情况下, 可以避免液渣流 进水池, 彻底消除爆炸隐患。 在搡作时, 水管 11喷出水, 围绕水池形成 水幕, 击碎后的液渣滴的冷却和凝固过程在水幕内进行, 有效地防止了 粉尘污染。 在整个水池上外方加设一个防尘罩, 可以有效地防止水雾、 尘雾扩散、 保护环境。 As shown in FIG. 1, the dust-removing device 6 of the present invention is provided at the periphery of the pool 4. The device is composed of a water pipe 11, and water spray holes are arranged in the water pipe 11. A slag retaining wall 7 is provided on the side of the pool 4 near the granulator. The slag retaining wall is a water-cooled steel jacket. Because of its location between the tundish slag tank and the pool, when special conditions occur, such as sudden power failure Can avoid slag flow Into the pool to completely eliminate the hidden danger of explosion. During the operation, the water pipe 11 sprays water to form a water curtain around the pool. The cooling and solidification process of the crushed liquid slag droplets is performed in the water curtain, which effectively prevents dust pollution. Adding a dust cover to the outside of the entire pool can effectively prevent water mist and dust mist from spreading and protect the environment.
根据本发明的实施例, 盛渣包 2、 中间包 3、 倾翻机构 1位于一平台 上, 液压缸 19的缸体与位于地坑的支座 20铰接, 粒化器 9设置在平台侧 壁流渣槽下面, 挡渣墙设置在中间包流渣槽与水池之间。  According to the embodiment of the present invention, the slag pack 2, the tundish 3, and the tipping mechanism 1 are located on a platform. The cylinder of the hydraulic cylinder 19 is hinged with the support 20 located in the pit. The granulator 9 is provided on the side wall of the platform. Below the slag slag tank, a slag retaining wall is arranged between the tundish slag slag tank and the pool.
本发明所提供的炉渣气碎粒化方法和装置具有以下优点:  The slag gas granulation method and device provided by the present invention have the following advantages:
1.工艺非常简单, 占地面积小, 投资小。 在处理液渣量相同的前提 下所用主体设备的投资仅相当已有工艺的十分之一到几十分之一。  1. The process is very simple, the floor space is small, and the investment is small. Under the premise of the same amount of liquid slag treatment, the investment of the main equipment used is only one tenth to several tenths of the existing process.
2.处理能力大, 粒化彻底。 每分钟可处理熔渣 2 - 3. 5t。 处理后的渣 粒直径为 0. 1 - 6匪, 大部分颗粒小于 21^ 从中间包流出的熔渣 95%均能 粒化。 粒化后的渣粒容易粉化加工。  2. Large processing capacity and complete granulation. It can process slag 2-3.5t per minute. The diameter of the slag after treatment is 0.1 to 6 bands. Most of the particles are less than 21 ^ 95% of the slag flowing out of the tundish can be granulated. The granulated slag particles are easily powdered.
3.用水量极小, 只需向池内补充因蒸发而消耗的水量即可, 无污水 外排, 不会造成二次污染。  3. The water consumption is very small, and only the amount of water consumed by evaporation needs to be replenished into the pond. There is no sewage discharge and no secondary pollution will be caused.
4.安全可靠。 由于粒化器距水池有一定的安全距离, 其间设置有挡 渣墙对付突发事故。 彻底消除了爆炸伤人的隐患。 独特的液压倾翻机构 使工人在远距离控制倾翻液渣, 安全性好, 改善了劳动条件和强度。 4. Safe and reliable. Because the granulator has a certain safety distance from the pool, a slag retaining wall is set up to cope with the accident. The potential danger of injury from the explosion was completely eliminated. The unique hydraulic tipping mechanism enables workers to control the tipping of liquid slag at a long distance, with good safety and improved working conditions and intensity.
5.耗气量少, 能耗低。 最佳耗气量为 40 - 60Nm3/t渣, 而日本福山 钢铁厂的耗气量为 500 - 1000Nm3/t。 气源可使用冶金工厂大量富余的氮气 或蒸汽 (也可使用压缩空气) 。 使用氮气或蒸汽并可防止炉渣中残余金 属的氧化, 不仅可以减轻对环境的污染, 又可提高残余金属的回收率。 可大量节约能源, 提高钢厂的综合效益。 5. Low air consumption and low energy consumption. The optimal gas consumption is 40-60Nm 3 / t slag, while the Fukuyama Iron and Steel Plant in Japan consumes 500-1000Nm 3 / t. The gas source can use a large surplus of nitrogen or steam from the metallurgical plant (compressed air can also be used). The use of nitrogen or steam can prevent the oxidation of residual metals in the slag, which can not only reduce environmental pollution, but also improve the recovery rate of residual metals. It can save a lot of energy and improve the comprehensive benefit of the steel mill.
6.粒化钢渣便于综合利用。 是生产水泥熟料的理想代用品, 加上粒 小易磨, 深受水泥厂的欢迎。 此外, 钢渣还可做烧结原料或高炉熔剂, 前期渣风碎后, 也可做农用磷肥。  6. Granulated steel slag is convenient for comprehensive utilization. It is an ideal substitute for the production of cement clinker. With small grains and easy grinding, it is very popular among cement plants. In addition, steel slag can also be used as sintering raw material or blast furnace flux, and it can also be used as agricultural phosphate fertilizer after wind crushing in the early stage.
本发明的设备简单, 设计先进, 效果显著。 液压倾翻机构和盛渣包 安全、 可靠, 改善了劳动条件, 提高了生产率。 有不同孔径, 且喷孔呈 "U" 或 形布置的粒化器设计科学合理, 不论是炉渣或金属液体 都能使之安全粒化, 分散落入积渣水池中, 耗气量小, 粒化率高。 挡渣 墙能在出现停电、 停气等偶然情况时彻底避免炉渣遇水爆炸隐患。 除尘 装置改善了工作环境, 明显降低了空气中的含尘量。  The device of the invention is simple, the design is advanced, and the effect is remarkable. The hydraulic tipping mechanism and slag pack are safe and reliable, improving working conditions and productivity. The granulators with different apertures and the spray holes in a "U" or shaped arrangement are scientifically and rationally designed, regardless of whether it is slag or metal liquid, which can be safely granulated and dispersed into the slag pool, with low gas consumption and granulation The rate is high. The slag retaining wall can completely avoid the hidden danger of explosion of slag when it encounters water in the event of a power outage or gas outage. The dust removal device improves the working environment and significantly reduces the dust content in the air.
本发明的工艺及装置投资省, 生产率高, 能耗低, 综合经济效益和 环保效果好, 可广泛适用于冶金行业的转炉、 平炉、 电炉的钢渣, 高炉 炼铗及有色冶炼炉渣的处理。 The process and the device of the invention have low investment, high productivity, low energy consumption, comprehensive economic benefits and The environmental protection effect is good, and it can be widely applied to the treatment of converter slag, open hearth, electric furnace steel slag, blast furnace smelting slag and non-ferrous smelting slag in metallurgical industry.

Claims

权利要求书 Claim
1. 炉渣气碎粒化装置包括一盛渣包倾翻装置 (1) , 一中间包(3) , —粒 化器(9), 一水池(4), 一挡渣墙 (7)及气源; 所述盛渣包倾翻装置(1)用 于将液渣倾翻至中间包(2), 液渣由所述中间包流出, 所述粒化器位于 中间包下方并与一气源相连, 粒化器的前面有呈 U形或 u形排列的喷孔 以喷出高速气流将液渣击碎并落入水池。 1. Slag gas granulation device includes a slag bag tilting device (1), a tundish (3), a granulator (9), a pool (4), a slag wall (7) and gas The slag container tilting device (1) is used to tip liquid slag to a tundish (2), the slag flows out of the tundish, the granulator is located below the tundish and is connected to an air source Connected, the granulator has U-shaped or U-shaped spray holes in front of it to spray high-speed air flow to crush the liquid residue and fall into the pool.
2. 如权利要求 1 所述的炉渣气碎粒化装置, 其中所述喷孔的底排孔径 大于两边孔径, 两边竖排孔径中心线的夹角可在 0 - 120。 范围内变化。 2. The slag gas granulating device according to claim 1, wherein the hole diameter of the bottom row of the spray holes is larger than the hole diameters on both sides, and the angle between the centerlines of the vertical row hole diameters on both sides can be in the range of 0-120. Within range.
3. 如权利要求 1或 2所述的炉渣气碎粒化装置, 还包括一除尘装置(6), 3. The slag gas granulation device according to claim 1 or 2, further comprising a dust removal device (6),
4. 如权利要求 3所述的炉渣气碎粒化装置, 所述除尘装置(6)进一步包 括布置在水池边的, 分布有小孔的喷水管和设置在水池上外方的防尘軍。 4. The slag gas granulation device according to claim 3, the dust removal device (6) further comprises a water spray pipe with small holes distributed on the side of the pool, and a dust-proof army arranged outside the pool .
5. 如权利要求 1, 所述的炉渣气碎粒化装置, 所述盛渣包倾翻机构(1) 进一步包括一盛渣包支承机构和防止盛渣包倾翻及脱落的定位装置。 5. The slag gas granulation device according to claim 1, wherein the slag bag tilting mechanism (1) further comprises a slag bag support mechanism and a positioning device for preventing the slag bag from tipping over and falling off.
6. 如权利要求 1所述的炉渣气碎粒化装置, 所述挡渣墙(7), 位于粒化 器(9)与水池(4)之间。 6. The slag gas granulation device according to claim 1, wherein the slag retaining wall (7) is located between the granulator (9) and the pool (4).
7. 炉渣气碎粒化方法, 包括以下步骤: 7. Slag gas granulation method includes the following steps:
1)将盛满液态冶金渣的盛渣包吊装到倾翻机构的支承架上, 倾翻机 构将盛渣包逐渐倾翻, 液渣被倒入中间包, 侬靠重力作用液渣从中间包 的流法槽流出;  1) The slag bag full of liquid metallurgical slag is hoisted to the support frame of the tipping mechanism. The tipping mechanism gradually tilts the slag bag, and the liquid slag is poured into the tundish. Outflow trough;
2)在炉渣从流渣槽流出后, 气源的压缩气体从粒化器的喷孔喷出将 流渣击碎;  2) After the slag flows out of the slag tank, the compressed gas from the gas source is ejected from the nozzle of the granulator to crush the slag;
3)击碎的液渣滴通过水池周边的除尘装置除尘;  3) The crushed liquid slag drops are removed by the dust removal device around the pool;
4)击碎后的液渣滴在向前飞行中冷却和凝固, 形成球状渣粒, 撒落 在沉渣水池中进一步冷却。  4) The crushed liquid slag droplets are cooled and solidified during forward flight, forming spherical slag particles, which are scattered in the sediment pool for further cooling.
5 )用抓斗将水池中的渣粒捞出运走。 5) Use a grab to remove the slag particles from the pool.
8. 如权利要求 7所迷的炉渣气碎粒化方法, 所述气源的工作压力为 0. 2 - 0. 6Mpa, 使用压缩氮气或蒸汽。 Slag 8. The method of gas nibs fans claim 7, wherein the working pressure of the gas source 0. 2 - 0. 6Mpa, using compressed nitrogen or steam.
9. 如权利要求 8所述的炉渣气碎粒化方法, 所述气源使用压缩空气。  9. The slag gas granulation method according to claim 8, wherein the gas source uses compressed air.
PCT/CN1994/000098 1993-12-11 1994-12-09 Slag granulation method and container by air crushing WO1995015929A1 (en)

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CN101660012B (en) * 2009-09-25 2012-07-18 阳谷祥光铜业有限公司 Anhydrous granulating technique of metallurgical slag and device thereof
CN101886149A (en) * 2010-07-08 2010-11-17 无锡市东方环境工程设计研究所有限公司 High temperature liquid slag recovery method
CN101886148A (en) * 2010-07-08 2010-11-17 无锡市东方环境工程设计研究所有限公司 Method for recovering high-temperature molten slag
CN102329902B (en) * 2011-10-15 2016-09-07 杜天宇 A kind of device structure of metallurgical gas-water continuous quenching
CN103710479B (en) * 2014-01-17 2016-05-18 中冶华天工程技术有限公司 Steel slag water quenching treatment system
CN115418420B (en) * 2022-09-26 2023-07-25 马鞍山钢铁股份有限公司 Treatment device and treatment method for improving wind-break slagging of steel slag

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