CN201321481Y - Novel pellet cooling device - Google Patents
Novel pellet cooling device Download PDFInfo
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- CN201321481Y CN201321481Y CNU2008202324240U CN200820232424U CN201321481Y CN 201321481 Y CN201321481 Y CN 201321481Y CN U2008202324240 U CNU2008202324240 U CN U2008202324240U CN 200820232424 U CN200820232424 U CN 200820232424U CN 201321481 Y CN201321481 Y CN 201321481Y
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- 238000001816 cooling Methods 0.000 title claims abstract description 47
- 239000008188 pellet Substances 0.000 title claims abstract description 36
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000000463 material Substances 0.000 claims abstract description 19
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 14
- 239000002184 metal Substances 0.000 claims abstract description 12
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 7
- 239000010959 steel Substances 0.000 claims abstract description 7
- 239000011449 brick Substances 0.000 claims abstract description 5
- 239000007921 spray Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 230000036760 body temperature Effects 0.000 claims 1
- 238000010276 construction Methods 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 abstract description 6
- 239000002918 waste heat Substances 0.000 abstract description 6
- 230000003647 oxidation Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 230000009469 supplementation Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 239000003973 paint Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 239000000109 continuous material Substances 0.000 description 3
- 238000001465 metallisation Methods 0.000 description 3
- 238000011946 reduction process Methods 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Manufacture And Refinement Of Metals (AREA)
Abstract
新型金属化球团冷却装置,采用补充氮气循环冷却方式,它包括冷却机机体、进料器、进气管、链箅机及出料器。特征在于:机体表面为金属框架结构,内衬高温段和低温段耐火砖,机体高温端连接进料器,低温端连接出料器,进料器与出料器相对水平面向下倾斜,链箅机位于进料器和出料器之间的机体内,机体顶部设有出气孔,排出来的废气,经锅炉余热回收后,再返回冷却机循环利用。另一侧设有人孔,以便于操作人员检修。机体一侧沿料行进方向设有多排进气管,进气管与补充氮气后的循环气体输送总管相连。本实用新型可进行热量回收、防止金属化球团氧化、具有排矿连续性及维修方便的特点。适用于钢铁行业金属化球团的冷却。
The new metallized pellet cooling device adopts the supplementary nitrogen circulation cooling method, which includes the cooling machine body, feeder, intake pipe, chain grate machine and discharger. The characteristics are: the surface of the body is a metal frame structure, lined with refractory bricks in the high temperature section and the low temperature section, the high temperature end of the body is connected to the feeder, and the low temperature end is connected to the discharge device, the relative horizontal plane of the feeder and the discharge device is inclined downward, and the chain grate The machine is located in the body between the feeder and the discharger. There is an air outlet on the top of the body. The exhaust gas is recovered by the waste heat of the boiler and then returned to the cooling machine for recycling. There is a manhole on the other side for easy maintenance by operators. One side of the body is provided with multiple rows of intake pipes along the direction of material travel, and the intake pipes are connected to the main pipe of circulating gas after nitrogen supplementation. The utility model can recover heat, prevent oxidation of metallized pellets, and has the characteristics of continuous ore discharge and convenient maintenance. Suitable for cooling metallized pellets in the steel industry.
Description
所属技术领域 Technical field
本实用新型属于冶金行业的冷却装置,主要用于钢铁行业金属化球团的冷却。The utility model belongs to a cooling device in the metallurgical industry, which is mainly used for cooling metallized pellets in the iron and steel industry.
背景技术 Background technique
转底炉直接还原工艺生产金属化球团(直接还原铁)是最近三十年间发展起来的炼铁新工艺。由于这一工艺无需燃料的制备和原料的深加工,对合理利用自然资源、保护人类环境有积极作用,因而受到冶金行业的普遍关注。冷却是该工艺的一个重要工序,1000℃的球团降至300℃以下,回收其余热,防止球团的再次氧化,保证产品的金属化率,对于转底炉生产的节能降耗及后道工序高炉或转炉或电炉能耗的降低有着重要的意义。The production of metallized pellets (direct reduced iron) by rotary hearth furnace direct reduction process is a new ironmaking process developed in the last thirty years. Because this process does not require the preparation of fuel and the deep processing of raw materials, it has a positive effect on the rational use of natural resources and the protection of the human environment, so it has received widespread attention from the metallurgical industry. Cooling is an important process of the process. The pellets at 1000°C are reduced to below 300°C, and the remaining heat is recovered to prevent the re-oxidation of the pellets and ensure the metallization rate of the product. The reduction of energy consumption in process blast furnace or converter or electric furnace is of great significance.
为了连续生产,国外金属化球团的冷却方式主要是间接水冷式敞口冷却,余热损失较大,冷却水进出口温度仅相差15℃左右。我国现有的转底炉直接还原工艺的冷却设施是由北京科技大学开发的间接水冷式振动冷却机,其结构简单,但冷却效果较差,进出口冷却水温差小,热量无法回收利用,且金属化球团暴露在空气之中,容易导致球团表层被二次氧化,影响产品的最终金属化率。为了进一步降低球团的氧化,日本将低浓度氮气引入间接水冷式冷却筒,通过不断补充氮气来实现减少球团金属化率降低的目的,但是余热仍无法回收利用,且球团在冷却筒冷却翻动前进过程中出现大量的粉末,影响了产品的质量和产量。For continuous production, the cooling method of foreign metallized pellets is mainly indirect water-cooled open cooling, the waste heat loss is relatively large, and the temperature difference between the inlet and outlet of cooling water is only about 15°C. The cooling facility of the existing rotary hearth furnace direct reduction process in my country is an indirect water-cooled vibrating cooler developed by Beijing University of Science and Technology. Its structure is simple, but the cooling effect is poor. Metallized pellets are exposed to the air, which easily leads to secondary oxidation of the pellet surface, which affects the final metallization rate of the product. In order to further reduce the oxidation of the pellets, Japan introduces low-concentration nitrogen into the indirect water-cooled cooling cylinder to achieve the purpose of reducing the metallization rate of the pellets by continuously replenishing nitrogen, but the waste heat cannot be recycled, and the pellets are cooled in the cooling cylinder A large amount of powder appears during the turning process, which affects the quality and output of the product.
发明内容 Contents of the invention
鉴于目前国内外现有金属化球团冷却设备的缺陷,根据转底炉及其它直接还原铁生产的实际需要,本实用新型提供一种可进行热量回收、防止金属化球团氧化、具有排矿连续性及维修方便的金属化球团冷却装置。In view of the defects of existing metallized pellet cooling equipment at home and abroad, according to the actual needs of rotary hearth furnace and other direct reduced iron production, the utility model provides a cooling device capable of heat recovery, preventing oxidation of metallized pellets, and has the function of ore discharge. Continuity and maintenance-friendly metallized pellet cooling device.
新型金属化球团冷却装置,采用补充氮气循环冷却方式,它由冷却机机体(11)、进料器(1)、进气总管(12)、进气支管(13)、链篦机(6)及出料器(9)组成。其特征在于,机体(11)外表面为金属框架结构,内衬高温段和低温段不同的耐火砖,机体高温端连接进料器(1),低温端连接出料器(9),链篦机(6)位于进料器(1)和出料器(9)之间的机体(11)内,机体顶部设有出气孔(4),排出来的废气,经锅炉余热回收后,再返回冷却机循环利用。The new metallized pellet cooling device adopts the supplementary nitrogen circulation cooling method, which consists of a cooler body (11), a feeder (1), an air intake main pipe (12), an air intake branch pipe (13), and a chain grate (6 ) and the discharger (9). It is characterized in that the outer surface of the body (11) is a metal frame structure, lined with refractory bricks of different high-temperature sections and low-temperature sections, the high-temperature end of the body is connected to the feeder (1), the low-temperature end is connected to the discharger (9), and the chain grate The machine (6) is located in the body (11) between the feeder (1) and the discharger (9). The top of the body is provided with an air outlet (4). Cooler recycling.
优选的,在机体一侧沿料行进方向设有多个进气孔(16),进气孔(16)与进气支管(13)相连,进气支管(13)和氮气补充管(15)与进气总管(12)相连,另一侧设有人孔(14),便于检修。Preferably, a plurality of air inlets (16) are provided along the material advancing direction on one side of the machine body, and the air inlets (16) are connected with the air inlet branch pipe (13), and the air inlet branch pipe (13) and the nitrogen supplementary pipe (15) It is connected with the intake manifold (12), and the other side is provided with a manhole (14) for easy maintenance.
所述进料器(1)由进料漏斗(18)和圆辊布料器(10)组成,进料漏斗为耐热不锈钢结构,内衬以耐高温耐磨喷涂料喷涂,进料漏斗(18)的倾斜底板上设置导料筋条(17),倾斜底板下部与圆辊布料器(10)连接。The feeder (1) is composed of a feed funnel (18) and a round roller distributor (10). The feed funnel is a heat-resistant stainless steel structure, and the inner lining is sprayed with high temperature and wear-resistant spray paint. The feed funnel (18 ) on the inclined base plate is provided with material guide ribs (17), and the inclined base plate bottom is connected with the round roller distributor (10).
所述出料器(9)由出料漏斗(19)和活动闸板(8)组成,出料漏斗为钢结构,以耐热耐磨喷涂料喷涂,出料漏斗倾斜底板上设置导料筋条(17),出料漏斗上设置活动闸板(8),活动闸板(8)一端与冷却机机体(11)相连,另一端与物料(2)表面相接;人孔(14)处以厚钢板覆盖,平时用螺母将钢板和机体紧密连接在一起。The discharge device (9) is composed of a discharge funnel (19) and a movable gate (8). The discharge funnel is a steel structure, sprayed with heat-resistant and wear-resistant spray paint, and the inclined bottom plate of the discharge funnel is provided with guide ribs Bar (17), the discharge funnel is provided with a movable gate (8), one end of the movable gate (8) is connected with the cooling machine body (11), and the other end is connected with the surface of the material (2); the manhole (14) is provided with Covered with thick steel plate, the steel plate and the machine body are tightly connected together with nuts at ordinary times.
所述冷却机机体一侧的相邻两进气支管(13)之间的间距为0.5-4.0米。The distance between two adjacent intake branch pipes (13) on one side of the cooling machine body is 0.5-4.0 meters.
所述的冷却机机体一侧的进气支管(13)数量为5~50个。The number of intake branch pipes (13) on one side of the cooling machine body is 5-50.
所述进料器(1)相对水平面向下倾斜,进料器的进料漏斗(18)底边与圆辊布料器(10)中心轴线垂直方向的倾斜角度为15-45°。The feeder (1) is inclined downward relative to the horizontal plane, and the inclination angle between the bottom edge of the feeding funnel (18) of the feeder and the vertical direction of the central axis of the round roller distributor (10) is 15-45°.
所述的出料器(9)相对水平面向下倾斜,所述的出料器的活动闸板(8)与冷却机机体(11)的夹角为0~60°。The discharger (9) is inclined downward relative to the horizontal plane, and the included angle between the movable gate (8) of the discharger and the cooling machine body (11) is 0-60°.
进料器与出料器相对水平面向下倾斜,便于顺利进料和排料,连续物料自然堆积形成的料堆对进料口和出料口可以起到自封闭的作用。The relative horizontal plane of the feeder and the discharger is inclined downward, which is convenient for feeding and discharging smoothly. The stockpile formed by the natural accumulation of continuous materials can play a self-sealing effect on the inlet and outlet.
本实用新型球团冷却装置,进料器下部设圆辊布料器,出料器下部紧接运转链板机,保证了物料的连续流动;连续物料自然堆积及负压操作实现了进料端及出料端的自密封,同时出料器设有活动闸板,与冷却机机体夹角为0~60°,亦起到密封的作用;采用氮气为冷却气体,既起到了冷却的作用,还有效避免了金属化球团的氧化,保证了产品的质量;排出来的废气,经锅炉余热回收,使余热得到再利用。本实用新型结构合理、易于生产、安装和维护,使用后可以完全满足转底炉直接还原工艺及其它直接还原铁生产工艺的产品冷却需求,对于转底炉工艺的全面推广及国内外直接还原铁生产工艺的发展具有极大的推动意义。In the pellet cooling device of the utility model, the lower part of the feeder is equipped with a round roller distributor, and the lower part of the discharger is connected to the running chain plate machine, which ensures the continuous flow of materials; the natural accumulation of continuous materials and negative pressure operation realize the feeding end and The discharge end is self-sealing, and at the same time, the discharge device is equipped with a movable gate, and the angle between the discharge device and the cooling machine body is 0-60°, which also plays the role of sealing; nitrogen is used as the cooling gas, which not only plays the role of cooling, but also effectively The oxidation of the metallized pellets is avoided, and the quality of the product is guaranteed; the exhaust gas is recovered by the waste heat of the boiler, so that the waste heat can be reused. The utility model has a reasonable structure, is easy to produce, install and maintain, and can fully meet the product cooling requirements of the rotary hearth furnace direct reduction process and other direct reduced iron production processes after use. The development of production technology has great promotion significance.
附图说明 Description of drawings
图1是本实用新型的截面示意图;Fig. 1 is a schematic cross-sectional view of the utility model;
图2是本实用新型进气管方向机体平面示意图;Fig. 2 is a schematic plan view of the body of the utility model in the direction of the intake pipe;
图3是本实用新型进气管俯视示意图;Fig. 3 is a top view schematic diagram of the utility model intake pipe;
图4是本实用新型进料器平面图;Fig. 4 is a plan view of the utility model feeder;
图5是本实用新型进料器侧面图;Fig. 5 is a side view of the utility model feeder;
图6是本实用新型出料器平面图;Fig. 6 is a plan view of the discharge device of the present utility model;
图7是本实用新型出料器侧面图;Fig. 7 is a side view of the utility model discharger;
图8是本实用新型人孔平面示意图;Fig. 8 is a schematic plan view of the utility model manhole;
1、进料器 2、物料 3、金属外壳 4、出气孔 5、耐火砖层 6、链篦机 7、链篦机支架 8、活动闸板 9、出料器 10、圆辊布料器 11、机体 12、进气总管 13、进气支管 14、人孔 15、氮气补充管 16、进气孔 17、导料筋条 18、进料漏斗 19、出料漏斗1. Feeder 2. Material 3. Metal shell 4.
具体实施方式 Detailed ways
实施例1:Example 1:
年产10万吨金属化球团的新型金属化球团冷却装置为补充氮气循环冷却方式,主要由冷却机机体11、进气总管12、进气支管13、进料器1、链篦机6、出料器9组成。The new metallized pellet cooling device with an annual output of 100,000 tons of metallized pellets is a supplementary nitrogen circulation cooling method. ,
冷却机机体11表面为金属框架结构,长11m.宽2.5m,高1.8m。内衬高温段和低温段不同的耐火砖。冷却机高温端连接进料器1的进料漏斗18,漏斗容积0.4m3,漏斗18为耐热不锈钢结构,内衬用耐高温耐磨喷涂料喷涂而成,进料漏斗18的倾斜底板上设置耐热耐磨合金堆焊的导料筋条17进行料的斜向疏导,下部以圆辊布料器10将料均匀布于链篦机6上,进料漏斗18底边与圆辊布料器10中心轴线水平垂直方向成45°倾斜角,链篦机长8m,宽1.5m。冷却机11低温端连接出料漏斗19,出料漏斗19为钢结构,以耐热耐磨喷涂料喷涂,出料漏斗19的倾斜底板上采用耐热耐磨合金堆焊的导料筋条17进行料的斜向疏导,出料漏斗19顶板采用活动闸板8,活动闸板8与冷却机机体11夹角为35°。冷却机机体一侧的进气支管13和氮气补充管15与进气总管12相连。进气支管13间距离1.0米。进气支管13数量8个。冷却机机体顶部出来的废气,经锅炉余热回收后,再返回冷却机循环利用。The surface of the cooling
温度为900~1100℃的物料2经进料器1,在圆辊布料器10的连续带动下均匀布在链篦机6上,并匀速向出料器9方向移动。在此过程中,从进气孔16进来的低温氮气进入到物料层,与物料2发生直接热交换。物料2经冷却后温度降至200~300℃,经出料器9落至链板机上,通过链板机的连续转动,实现设备的连续稳定出料。连续物料自然堆积及负压操作实现了进料端及出料端的自密封,同时出料器设有活动闸板,与冷却机机体夹角为0~60°,亦起到密封的作用。The material 2 with a temperature of 900-1100°C passes through the
实施例2:Example 2:
年产20万吨金属化球团的新型金属化球团冷却装置为补充氮气循环冷却方式,主要装备及结构同实例1.The new metallized pellet cooling device with an annual output of 200,000 tons of metallized pellets is a supplementary nitrogen circulation cooling method. The main equipment and structure are the same as in Example 1.
冷却机机体表面为金属框架结构,长12m.宽1.5m,高1.8m。进料器底边与圆辊布料器中心轴线水平垂直方向角度为30°,链篦机长10m,宽1.5m。活动闸板与冷却机机体夹角为45°。进气支管间距离1.0米。进气支管数量10个The surface of the cooling machine body is a metal frame structure, 12m long, 1.5m wide, and 1.8m high. The horizontal and vertical angle between the bottom edge of the feeder and the central axis of the round roller distributor is 30°, and the length of the chain grate is 10m, and the width is 1.5m. The angle between the movable ram and the body of the cooling machine is 45°. The distance between the intake branch pipes is 1.0 meters. The number of intake branch pipes is 10
实施例3:Example 3:
年产30万吨金属化球团的新型金属化球团冷却装置为补充氮气循环冷却方式,主要装备及结构同实例1.The new metallized pellet cooling device with an annual output of 300,000 tons of metallized pellets is a supplementary nitrogen circulation cooling method, and the main equipment and structure are the same as in Example 1.
冷却机机体表面为金属框架结构,长14m.宽3m,高2m。进料器底边与圆辊布料器中心轴线水平垂直方向角度为30°,链篦机长12m,宽2m。活动闸板与冷却机机体夹角为45°。进气支管间距离0.8米。进气支管数量15个。The body surface of the cooling machine is a metal frame structure, 14m long, 3m wide, and 2m high. The horizontal and vertical angle between the bottom edge of the feeder and the central axis of the round roller distributor is 30°, the length of the chain grate is 12m, and the width is 2m. The angle between the movable ram and the body of the cooling machine is 45°. The distance between the intake branch pipes is 0.8 meters. The number of intake branch pipes is 15.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNU2008202324240U CN201321481Y (en) | 2008-12-22 | 2008-12-22 | Novel pellet cooling device |
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| CNU2008202324240U CN201321481Y (en) | 2008-12-22 | 2008-12-22 | Novel pellet cooling device |
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| CN201321481Y true CN201321481Y (en) | 2009-10-07 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102586532A (en) * | 2012-03-08 | 2012-07-18 | 江苏沙钢集团有限公司 | Direct reduction iron cooling device |
| CN102818027A (en) * | 2012-08-05 | 2012-12-12 | 许静 | Sealing riding wheel group |
| CN103088213A (en) * | 2011-11-04 | 2013-05-08 | 中冶长天国际工程有限责任公司 | Device and method for cooling direct reduction iron |
| CN104457084A (en) * | 2014-12-25 | 2015-03-25 | 山东钢铁股份有限公司 | Rapid cooling method for high-temperature materials |
| CN104913652A (en) * | 2015-05-20 | 2015-09-16 | 中南大学 | Shaft furnace pellet clinker waste heat recycling method and device |
| CN107208168A (en) * | 2015-02-03 | 2017-09-26 | 株式会社神户制钢所 | Method and device for producing reduced iron |
| CN111504059A (en) * | 2020-04-16 | 2020-08-07 | 江苏中意建筑材料有限公司 | A cooler for clinker from rotary kiln |
| CN113295010A (en) * | 2021-01-05 | 2021-08-24 | 中冶长天国际工程有限责任公司 | Sintering precooling device |
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- 2008-12-22 CN CNU2008202324240U patent/CN201321481Y/en not_active Expired - Fee Related
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| CN103088213A (en) * | 2011-11-04 | 2013-05-08 | 中冶长天国际工程有限责任公司 | Device and method for cooling direct reduction iron |
| CN103088213B (en) * | 2011-11-04 | 2015-09-09 | 中冶长天国际工程有限责任公司 | A kind of device and method cooling direct-reduction iron block |
| CN102586532B (en) * | 2012-03-08 | 2014-06-25 | 江苏沙钢集团有限公司 | Direct reduction iron cooling device |
| CN102586532A (en) * | 2012-03-08 | 2012-07-18 | 江苏沙钢集团有限公司 | Direct reduction iron cooling device |
| CN102818027B (en) * | 2012-08-05 | 2015-01-14 | 许静 | Sealing riding wheel group |
| CN102818027A (en) * | 2012-08-05 | 2012-12-12 | 许静 | Sealing riding wheel group |
| CN104457084A (en) * | 2014-12-25 | 2015-03-25 | 山东钢铁股份有限公司 | Rapid cooling method for high-temperature materials |
| CN107208168A (en) * | 2015-02-03 | 2017-09-26 | 株式会社神户制钢所 | Method and device for producing reduced iron |
| CN107208168B (en) * | 2015-02-03 | 2019-05-21 | 株式会社神户制钢所 | Method and device for producing reduced iron |
| CN104913652A (en) * | 2015-05-20 | 2015-09-16 | 中南大学 | Shaft furnace pellet clinker waste heat recycling method and device |
| CN104913652B (en) * | 2015-05-20 | 2016-11-30 | 中南大学 | A kind of method of Shaft Furnace Pelletizing Process grog waste heat recovery and device thereof |
| CN111504059A (en) * | 2020-04-16 | 2020-08-07 | 江苏中意建筑材料有限公司 | A cooler for clinker from rotary kiln |
| CN111504059B (en) * | 2020-04-16 | 2021-12-10 | 江苏中意建筑材料有限公司 | Cooler for kiln-discharging clinker of rotary kiln |
| CN113295010A (en) * | 2021-01-05 | 2021-08-24 | 中冶长天国际工程有限责任公司 | Sintering precooling device |
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