CN118361950A - A vertical tank reduction furnace for producing magnesium metal - Google Patents
A vertical tank reduction furnace for producing magnesium metal Download PDFInfo
- Publication number
- CN118361950A CN118361950A CN202410788421.9A CN202410788421A CN118361950A CN 118361950 A CN118361950 A CN 118361950A CN 202410788421 A CN202410788421 A CN 202410788421A CN 118361950 A CN118361950 A CN 118361950A
- Authority
- CN
- China
- Prior art keywords
- vertical tank
- silo
- base
- tank
- reduction furnace
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 230000009467 reduction Effects 0.000 title claims abstract description 39
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 238000004519 manufacturing process Methods 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000000835 fiber Substances 0.000 claims description 19
- 229910052749 magnesium Inorganic materials 0.000 claims description 11
- 239000011777 magnesium Substances 0.000 claims description 11
- 239000008188 pellet Substances 0.000 claims description 11
- 238000007789 sealing Methods 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 4
- 239000000428 dust Substances 0.000 abstract description 6
- 239000000779 smoke Substances 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract description 2
- 239000002893 slag Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 239000003500 flue dust Substances 0.000 description 5
- 239000003546 flue gas Substances 0.000 description 5
- 238000003723 Smelting Methods 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 101000827703 Homo sapiens Polyphosphoinositide phosphatase Proteins 0.000 description 2
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 2
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000005272 metallurgy Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B1/00—Shaft or like vertical or substantially vertical furnaces
- F27B1/02—Shaft or like vertical or substantially vertical furnaces with two or more shafts or chambers, e.g. multi-storey
- F27B1/04—Combinations or arrangements of shafts
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/20—Obtaining alkaline earth metals or magnesium
- C22B26/22—Obtaining magnesium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/04—Dry methods smelting of sulfides or formation of mattes by aluminium, other metals or silicon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B1/00—Shaft or like vertical or substantially vertical furnaces
- F27B1/10—Details, accessories or equipment specially adapted for furnaces of these types
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B1/00—Shaft or like vertical or substantially vertical furnaces
- F27B1/10—Details, accessories or equipment specially adapted for furnaces of these types
- F27B1/20—Arrangements of devices for charging
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B1/00—Shaft or like vertical or substantially vertical furnaces
- F27B1/10—Details, accessories or equipment specially adapted for furnaces of these types
- F27B1/21—Arrangements of devices for discharging
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27M—INDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
- F27M2003/00—Type of treatment of the charge
- F27M2003/16—Treatment involving a chemical reaction
- F27M2003/165—Reduction
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
技术领域Technical Field
本发明属于生产金属镁用还原炉技术领域,尤其涉及一种用于生产金属镁的竖罐还原炉。The invention belongs to the technical field of reduction furnaces for producing metallic magnesium, and in particular relates to a vertical tank reduction furnace for producing metallic magnesium.
背景技术Background technique
镁是一种化学性质活泼的碱土金属,在工业上,金属镁冶炼方法有热还原法、电解法、电熔法、气相冶金法和溶剂冶金法,其中,热还原法为主流的冶炼方法,热还原法炼镁主要是指皮江法炼镁。传统的皮江法炼镁采用横罐还原炉,还原炉的横罐水平放置于炉膛内部,生产时将球团料加入横罐中,随后球团料在1200℃的温度进行还原,待反应结束时,取出结晶器后需要扒除料罐内部的渣料。由于横罐的设置只能采用人工扒渣,因此横罐生产的连续性极差,受高温和粉尘等影响,扒渣作业环境非常恶劣。此外,由于横罐长期受高温环境影响,在横罐跨度较大时,极易出现向下的弯曲变形,因此,横罐结构不仅会影响罐体的使用寿命,还不利于罐体的大型化发展,不利于设备产能的提升。Magnesium is an alkaline earth metal with active chemical properties. In industry, the methods for smelting magnesium metal include thermal reduction, electrolysis, electric melting, gas phase metallurgy and solvent metallurgy. Among them, thermal reduction is the mainstream smelting method. Thermal reduction magnesium smelting mainly refers to the Pijiang method. The traditional Pijiang method for magnesium smelting uses a horizontal tank reduction furnace. The horizontal tank of the reduction furnace is placed horizontally inside the furnace. During production, the pellets are added to the horizontal tank, and then the pellets are reduced at a temperature of 1200°C. When the reaction is completed, the slag inside the tank needs to be removed after the crystallizer is taken out. Since the horizontal tank can only be manually slag-scraped, the continuity of horizontal tank production is extremely poor. Affected by high temperature and dust, the slag-scraping operation environment is very harsh. In addition, since the horizontal tank is affected by the high temperature environment for a long time, it is very easy to bend downward when the span of the horizontal tank is large. Therefore, the horizontal tank structure not only affects the service life of the tank body, but also is not conducive to the large-scale development of the tank body and the improvement of equipment production capacity.
竖罐还原炉解决了上述横罐还原炉存在的问题,当前已在工业生产中成功应用。现有竖罐还原炉如图1-3所示,竖罐6由上部抽真空装置6-1、冷却水套6-2、罐体6-3、下部变径口6-4和出渣口6-5组成。中心管9位于竖罐6内部,装炉时,使用天车将球团料8装在竖罐6与中心管9之间的腔体内,高温烟气和粉尘从竖罐6上部大量、快速、无组织溢出。在出炉时,使用天车吊起中心管9,同时打开出渣口6-5,渣料向下流出,此时,高温烟气和粉尘从竖罐6上部大量、快速、无组织溢出。上述装出炉作业使得车间作业环境恶化。此外,由于渣料在高温状态下的粘结性使得竖罐6和中心管9之间粘结,造成中心管9无法拔出,需要将竖罐6、中心管9及渣料全部吊出,更换新的竖罐6和中心管9,这样不仅会影响竖罐还原炉的生产连续性,还会缩短竖罐的使用寿命。The vertical tank reduction furnace solves the problems existing in the above-mentioned horizontal tank reduction furnace and has been successfully applied in industrial production. The existing vertical tank reduction furnace is shown in Figure 1-3. The vertical tank 6 is composed of an upper vacuum device 6-1, a cooling water jacket 6-2, a tank body 6-3, a lower reducer 6-4 and a slag outlet 6-5. The central tube 9 is located inside the vertical tank 6. When loading the furnace, a crane is used to load the pellet material 8 into the cavity between the vertical tank 6 and the central tube 9. High-temperature flue gas and dust overflow from the upper part of the vertical tank 6 in large quantities, quickly and unorganized. When unloading, a crane is used to lift the central tube 9, and the slag outlet 6-5 is opened at the same time, and the slag flows downward. At this time, high-temperature flue gas and dust overflow from the upper part of the vertical tank 6 in large quantities, quickly and unorganized. The above-mentioned loading and unloading operations deteriorate the workshop working environment. In addition, due to the adhesion of the slag at high temperature, the vertical tank 6 and the central tube 9 are adhered to each other, making it impossible to pull out the central tube 9. The vertical tank 6, the central tube 9 and the slag need to be lifted out and replaced with new vertical tanks 6 and central tubes 9. This will not only affect the production continuity of the vertical tank reduction furnace, but also shorten the service life of the vertical tank.
另一方面,在吊出中心管9出渣时,由于无法封闭竖罐顶部的炉盖,高温烟气和粉尘从上部溢出,同时,在装料时,物料落入竖罐中,高温烟气和粉尘也会从上部溢出,车间生产操作环境恶劣,由于炉顶结构复杂,且存在天车作业,因此不具备烟气和粉尘的收集处理条件。On the other hand, when the central tube 9 is lifted out to discharge the slag, the furnace cover on the top of the vertical tank cannot be closed, and high-temperature flue gas and dust overflow from the upper part. At the same time, when loading, the material falls into the vertical tank, and high-temperature flue gas and dust also overflow from the upper part. The production and operating environment of the workshop is poor. Due to the complex structure of the furnace top and the existence of an overhead crane operation, the conditions for collecting and treating flue gas and dust are not met.
发明内容Summary of the invention
鉴于现有技术的上述缺点、不足,本发明提供一种用于生产金属镁的竖罐还原炉,通过将竖罐底部设置为底部直口结构,配合可升降的料仓组合体,实现集中备料,解决了现行竖罐还原炉装、出炉时车间烟气和粉尘无组织排放问题,提高了金属镁竖罐还原炉的连续、稳定和环保生产。In view of the above-mentioned shortcomings and deficiencies of the prior art, the present invention provides a vertical tank reduction furnace for producing metallic magnesium. By setting the bottom of the vertical tank as a bottom straight-mouth structure and cooperating with a liftable silo assembly, centralized material preparation is achieved, thereby solving the problem of unorganized emissions of workshop smoke and dust during loading and unloading of the current vertical tank reduction furnace, and improving the continuous, stable and environmentally friendly production of the metallic magnesium vertical tank reduction furnace.
为了达到上述目的,本发明采用的主要技术方案包括:In order to achieve the above object, the main technical solutions adopted by the present invention include:
一种用于生产金属镁的竖罐还原炉,包括竖罐,所述竖罐包括直筒状的罐体,所述罐体的底部为内径与上部罐体内径相同的底部直口,所述竖罐还原炉还包括料仓组合体,所述料仓组合体包括呈直筒状的上部仓体和下部仓体,所述上部仓体底部制有底座,所述下部仓体套置于上部仓体及底座的外部,上部仓体及底座相对于下部仓体升降移动,上部仓体的外径小于竖罐的内径,生产时,上部仓体内部设置中心管,所述中心管外壁与上部仓体内壁之间填充有球团料,料仓组合体置于竖罐底部,上部仓体及底座相对于下部仓体向上升起时,上部仓体置于竖罐内,生产结束后,上部仓体下降至下部仓体内部。A vertical tank reduction furnace for producing metallic magnesium comprises a vertical tank, the vertical tank comprises a straight cylindrical tank body, the bottom of the tank body is a bottom straight opening with the same inner diameter as the inner diameter of the upper tank body, the vertical tank reduction furnace also comprises a silo assembly, the silo assembly comprises a straight cylindrical upper silo body and a lower silo body, the bottom of the upper silo body is provided with a base, the lower silo body is sleeved on the outside of the upper silo body and the base, the upper silo body and the base are lifted and moved relative to the lower silo body, the outer diameter of the upper silo body is smaller than the inner diameter of the vertical tank, during production, a central tube is arranged inside the upper silo body, pellet material is filled between the outer wall of the central tube and the inner wall of the upper silo body, the silo assembly is placed at the bottom of the vertical tank, when the upper silo body and the base are lifted upward relative to the lower silo body, the upper silo body is placed in the vertical tank, after production is completed, the upper silo body descends to the inside of the lower silo body.
进一步地,所述上部仓体内侧底部设有带环形凹槽的纤维垫,该环形凹槽直径与中心管直径相匹配,中心管置于上部仓体内部时,中心管底部置于纤维垫的环形凹槽内。Furthermore, a fiber pad with an annular groove is provided at the bottom inner side of the upper warehouse body, the diameter of the annular groove matches the diameter of the central tube, and when the central tube is placed inside the upper warehouse body, the bottom of the central tube is placed in the annular groove of the fiber pad.
进一步地,所述底座与下部仓体之间密封设置,上部仓体通过气动升降装置相对于下部仓体升降移动。Furthermore, a seal is arranged between the base and the lower warehouse body, and the upper warehouse body is lifted and moved relative to the lower warehouse body by a pneumatic lifting device.
进一步地,所述底座接近上部仓体的一端制有底座颈部,底座颈部为向底座纵向中轴线凹陷的环形凹槽,所述底座颈部内设有纤维密封圈,上部仓体置于竖罐内时,纤维密封圈对竖罐与底座之间的缝隙密封。Furthermore, a base neck is formed at one end of the base close to the upper storage body, and the base neck is an annular groove recessed toward the longitudinal center axis of the base. A fiber sealing ring is provided in the base neck. When the upper storage body is placed in the vertical tank, the fiber sealing ring seals the gap between the vertical tank and the base.
进一步地,所述底座为中空结构。Furthermore, the base is a hollow structure.
进一步地,所述料仓组合体通过轨道机构送入或送出竖罐底部。Furthermore, the silo assembly is sent into or out of the bottom of the vertical tank via a track mechanism.
本发明的有益效果是:本发明的金属镁竖罐还原炉通过将竖罐底部设置为底部直口,配合料仓组合体中上部仓体的升降实现装出炉作业,装出炉过程短,并且不会产生粉尘,提高了竖罐还原炉的生产连续性、稳定性,还可以大幅改善劳动作业环境。装炉前集中备料,出炉后的物料可进行集中出料,解决了现行竖罐还原炉装、出炉时车间烟气和粉尘无组织排放问题,出炉时的高温物料还可以在集中出料时采用余热回收装置进行余热回用。通过设置纤维垫,避免了竖罐与中心管的粘接问题。The beneficial effects of the present invention are as follows: the magnesium metal vertical tank reduction furnace of the present invention realizes the loading and unloading operations by setting the bottom of the vertical tank as a straight bottom mouth, and coordinating the lifting of the upper bin body in the silo assembly. The loading and unloading process is short and does not generate dust, thereby improving the production continuity and stability of the vertical tank reduction furnace and greatly improving the working environment. The materials are centrally prepared before loading the furnace, and the materials can be centrally discharged after being discharged, which solves the problem of unorganized workshop smoke and dust emissions during the current vertical tank reduction furnace loading and unloading. The high-temperature materials when discharged can also be recycled by using a waste heat recovery device during centralized discharge. By providing a fiber mat, the bonding problem between the vertical tank and the center tube is avoided.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为现有竖罐还原炉结构示意图;FIG1 is a schematic diagram of the structure of an existing vertical tank reduction furnace;
图2为现有竖罐还原炉中竖罐的结构示意图;FIG2 is a schematic diagram of the structure of a vertical tank in an existing vertical tank reduction furnace;
图3为现有竖罐还原炉中中心管的结构示意图;FIG3 is a schematic diagram of the structure of a central tube in an existing vertical tank reduction furnace;
图4为本发明竖罐还原炉结构示意图;FIG4 is a schematic diagram of the structure of a vertical tank reduction furnace according to the present invention;
图5为本发明竖罐还原炉中竖罐的结构示意图;FIG5 is a schematic diagram of the structure of a vertical tank in a vertical tank reduction furnace of the present invention;
图6为本发明上部仓体升起时的料仓组合体结构示意图;FIG6 is a schematic diagram of the structure of the silo assembly when the upper silo body of the present invention is raised;
图7为本发明上部仓体下降时的料仓组合体结构示意图。FIG. 7 is a schematic diagram of the structure of the silo assembly when the upper silo body of the present invention is lowered.
图中:1、炉顶;2、炉膛;3、炉头;4、蓄热式烧嘴;5、炉底;6、竖罐;6-1、抽真空装置;6-2、冷却水套;6-3、罐体;6-4、下部变径口;6-5、出渣口;6-6、底部直口;7、结晶器;8、球团料;9、中心管;9-1、逸出口;9-2、管体;10、料仓组合体;10-1、上部仓体;10-2、底座颈部;10-3、底座;10-4、下部仓体;11、钢立柱;12、纤维垫;13、纤维密封圈;14、轨道机构。In the figure: 1. furnace roof; 2. furnace chamber; 3. burner head; 4. regenerative burner; 5. furnace bottom; 6. vertical tank; 6-1. vacuum device; 6-2. cooling water jacket; 6-3. tank body; 6-4. lower reducer; 6-5. slag outlet; 6-6. bottom straight outlet; 7. crystallizer; 8. pellet material; 9. center tube; 9-1. escape outlet; 9-2. tube body; 10. silo assembly; 10-1. upper silo body; 10-2. base neck; 10-3. base; 10-4. lower silo body; 11. steel column; 12. fiber mat; 13. fiber sealing ring; 14. track mechanism.
具体实施方式Detailed ways
为了更好的解释本发明,以便于理解,下面结合附图,通过具体实施方式,对本发明作详细描述。In order to better explain the present invention and facilitate understanding, the present invention is described in detail below through specific implementation modes in conjunction with the accompanying drawings.
一种用于生产金属镁的竖罐还原炉,如图4所示,包括竖罐6,竖罐6置于炉膛2内部,炉膛2顶部为炉顶1,炉膛2两侧为炉头3,炉头3上设有若干蓄热式烧嘴4,炉膛2底部为炉底5,炉底5底部与钢立柱11固定相连,竖罐6内部设有结晶器7,竖罐6上部设有抽真空装置6-1、冷却水套6-2。如图5所示,所述竖罐6包括直筒状的罐体6-3,所述罐体6-3的底部为内径与上部罐体内径相同的底部直口6-6。所述竖罐还原炉还包括料仓组合体10,所述料仓组合体10包括呈直筒状的上部仓体10-1和下部仓体10-4,所述上部仓体10-1底部制有底座10-3,所述下部仓体10-4套置于上部仓体10-1及底座10-3的外部,上部仓体10-1及底座10-3可相对于下部仓体10-4升降移动,上部仓体10-1的外径小于竖罐6的内径。具体地,所述底座10-3与下部仓体10-4之间密封设置,上部仓体10-1可通过气动升降装置相对于下部仓体10-4升降移动。气动升降装置对下部仓体10-4充气或放气,使上部仓体10-1实现上升或下降。上部仓体10-1升起时状态参见图6,上部仓体10-1下降时状态参见图7。具体地,所述底座10-3接近上部仓体10-1的一端制有底座颈部10-2,底座颈部10-2为向底座10-3纵向中轴线凹陷的环形凹槽,所述底座颈部10-2内设有纤维密封圈13,上部仓体10-1置于竖罐6内时,纤维密封圈13对竖罐6与底座10-3之间的缝隙密封,用以减少竖罐6内部热量的散失。具体地,所述底座10-3可以为中空结构,在保证其基本强度的前提下,以降低底座10-3的重量及制作成本。A vertical tank reduction furnace for producing magnesium metal, as shown in FIG4, includes a vertical tank 6, which is placed inside a furnace 2, the top of the furnace 2 is a furnace top 1, the two sides of the furnace 2 are furnace heads 3, a plurality of regenerative burners 4 are arranged on the furnace head 3, the bottom of the furnace 2 is a furnace bottom 5, the bottom of the furnace bottom 5 is fixedly connected to a steel column 11, a crystallizer 7 is arranged inside the vertical tank 6, and a vacuum device 6-1 and a cooling water jacket 6-2 are arranged on the upper part of the vertical tank 6. As shown in FIG5, the vertical tank 6 includes a straight cylindrical tank body 6-3, and the bottom of the tank body 6-3 is a bottom straight mouth 6-6 with an inner diameter the same as the inner diameter of the upper tank body. The vertical tank reduction furnace also includes a silo assembly 10, which includes an upper silo body 10-1 and a lower silo body 10-4 in a straight cylindrical shape. A base 10-3 is formed at the bottom of the upper silo body 10-1, and the lower silo body 10-4 is sleeved on the outer portion of the upper silo body 10-1 and the base 10-3. The upper silo body 10-1 and the base 10-3 can be lifted and moved relative to the lower silo body 10-4, and the outer diameter of the upper silo body 10-1 is smaller than the inner diameter of the vertical tank 6. Specifically, the base 10-3 and the lower silo body 10-4 are sealed, and the upper silo body 10-1 can be lifted and moved relative to the lower silo body 10-4 by a pneumatic lifting device. The pneumatic lifting device inflates or deflates the lower silo body 10-4 to enable the upper silo body 10-1 to rise or fall. The state of the upper warehouse body 10-1 when it is raised is shown in FIG6 , and the state of the upper warehouse body 10-1 when it is lowered is shown in FIG7 . Specifically, the base 10-3 is formed with a base neck 10-2 at one end close to the upper warehouse body 10-1, and the base neck 10-2 is an annular groove recessed toward the longitudinal center axis of the base 10-3. A fiber sealing ring 13 is provided inside the base neck 10-2. When the upper warehouse body 10-1 is placed in the vertical tank 6, the fiber sealing ring 13 seals the gap between the vertical tank 6 and the base 10-3 to reduce the heat loss inside the vertical tank 6. Specifically, the base 10-3 can be a hollow structure, so as to reduce the weight and manufacturing cost of the base 10-3 while ensuring its basic strength.
生产时,上部仓体10-1内部设置中心管9,如图3所示,中心管9包括管体9-2,所述管体9-2上制有镁蒸汽的逸出口9-1。所述中心管9外壁与上部仓体10-1内壁之间填充有球团料8,为了对上部仓体10-1内部的中心管9限位以及便于生产后中心管9与上部仓体10-1的分离,所述上部仓体10-1内侧底部设有带环形凹槽的纤维垫12,该环形凹槽直径与中心管9直径相匹配,中心管9置于上部仓体10-1内部时,中心管9底部置于纤维垫12的环形凹槽内。料仓组合体10置于竖罐6底部,上部仓体10-1及底座10-3相对于下部仓体10-4向上升起时,上部仓体10-1置于竖罐6内,使球团料8位于炉膛2内,底座10-3置于炉底5处,生产结束后,上部仓体10-1下降至下部仓体10-4内部。所述料仓组合体10可通过轨道机构14送入或送出竖罐6底部,实现料仓组合体10的输运。During production, a central tube 9 is arranged inside the upper warehouse body 10-1. As shown in FIG3 , the central tube 9 includes a tube body 9-2, and the tube body 9-2 is provided with an escape port 9-1 for magnesium vapor. The space between the outer wall of the central tube 9 and the inner wall of the upper warehouse body 10-1 is filled with pellet material 8. In order to limit the position of the central tube 9 inside the upper warehouse body 10-1 and to facilitate the separation of the central tube 9 from the upper warehouse body 10-1 after production, a fiber mat 12 with an annular groove is arranged at the bottom of the inner side of the upper warehouse body 10-1. The diameter of the annular groove matches the diameter of the central tube 9. When the central tube 9 is placed inside the upper warehouse body 10-1, the bottom of the central tube 9 is placed in the annular groove of the fiber mat 12. The silo assembly 10 is placed at the bottom of the vertical tank 6. When the upper silo 10-1 and the base 10-3 are raised relative to the lower silo 10-4, the upper silo 10-1 is placed in the vertical tank 6 so that the pellet material 8 is located in the furnace 2. The base 10-3 is placed at the furnace bottom 5. After the production is completed, the upper silo 10-1 is lowered to the inside of the lower silo 10-4. The silo assembly 10 can be sent into or out of the bottom of the vertical tank 6 through the track mechanism 14 to realize the transportation of the silo assembly 10.
采用本发明还原炉的金属镁生产方法,包括如下步骤:The method for producing magnesium metal using the reduction furnace of the present invention comprises the following steps:
步骤S01、在底座颈部10-2内设置纤维密封圈13,将上部仓体10-1装配在下部仓体10-4内部,将装配后的料仓组合体10置于装、出料工位处。Step S01, set a fiber sealing ring 13 in the base neck 10-2, assemble the upper silo body 10-1 inside the lower silo body 10-4, and place the assembled silo assembly 10 at the loading and unloading station.
步骤S02、中心管9置于纤维垫12的环形凹槽内,将中心管9连同纤维垫12装入位于装、出料工位的料仓组合体10的上部仓体10-1内部,将球团料8装入上部仓体10-2与中心管9之间的腔体中。Step S02, the center tube 9 is placed in the annular groove of the fiber mat 12, and the center tube 9 together with the fiber mat 12 are loaded into the upper silo body 10-1 of the silo assembly 10 located at the loading and unloading station, and the pellet material 8 is loaded into the cavity between the upper silo body 10-2 and the center tube 9.
步骤S03、竖罐6上部安装结晶器7,盖上竖罐6顶部炉盖;轨道机构14带动备料完毕的料仓组合体10至工作位,即竖罐6的正下方,采用气动升降装置将上部仓体10-2上升至竖罐6内部,使球团料8位于炉膛2内,底座10-3置于炉底5处,进入生产状态。Step S03, install the crystallizer 7 on the top of the vertical tank 6, and cover the top of the vertical tank 6; the track mechanism 14 drives the prepared silo assembly 10 to the working position, that is, directly below the vertical tank 6, and adopts a pneumatic lifting device to raise the upper silo body 10-2 to the inside of the vertical tank 6, so that the pellet material 8 is located in the furnace 2, and the base 10-3 is placed at the furnace bottom 5, entering the production state.
步骤S04、生产周期结束后,打开竖罐6顶部炉盖,取出结晶器7;采用气动升降装置将上部仓体10-2从竖罐6内部下降至下部料仓10-4中;轨道机构14带动料仓组合体10至装、出料工位处,进行封闭条件下的出料作业。Step S04, after the production cycle is completed, open the furnace cover on the top of the vertical tank 6 and take out the crystallizer 7; use a pneumatic lifting device to lower the upper bin body 10-2 from the inside of the vertical tank 6 to the lower bin 10-4; the track mechanism 14 drives the bin assembly 10 to the loading and unloading station to perform unloading operations under closed conditions.
本发明的金属镁竖罐还原炉通过将竖罐6底部设置为底部直口6-6,配合料仓组合体10中上部仓体10-1的升降实现装出炉作业,装出炉过程短,并且不会产生粉尘,提高了竖罐还原炉的生产连续性,还可以大幅改善劳动作业环境。装、出料作业都在特定车间进行集中处理,出炉时的高温物料还可以在集中出料时采用余热回收装置进行余热回用。通过设置纤维垫12,避免了竖罐6与中心管9的粘接问题。The magnesium vertical tank reduction furnace of the present invention realizes the loading and unloading operation by setting the bottom of the vertical tank 6 as a bottom straight mouth 6-6 and coordinating the lifting of the upper bin body 10-1 in the bin assembly 10. The loading and unloading process is short and does not generate dust, thereby improving the production continuity of the vertical tank reduction furnace and greatly improving the working environment. The loading and unloading operations are all centrally processed in a specific workshop, and the high-temperature materials when discharged from the furnace can also be recycled by using a waste heat recovery device during centralized unloading. By setting the fiber mat 12, the bonding problem between the vertical tank 6 and the central tube 9 is avoided.
尽管上面已经示出和描述了本发明的实施例,可以理解的是,上述实施例是示例性的,不能理解为对本发明的限制,本领域的普通技术人员对上述实施例进行改动、修改、替换和变型均属于本发明的范围内。Although the embodiments of the present invention have been shown and described above, it is to be understood that the above embodiments are illustrative and are not to be construed as limitations on the present invention. Alterations, modifications, substitutions and variations of the above embodiments by a person skilled in the art are all within the scope of the present invention.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202410788421.9A CN118361950B (en) | 2024-06-19 | 2024-06-19 | A vertical tank reduction furnace for producing magnesium metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202410788421.9A CN118361950B (en) | 2024-06-19 | 2024-06-19 | A vertical tank reduction furnace for producing magnesium metal |
Publications (2)
Publication Number | Publication Date |
---|---|
CN118361950A true CN118361950A (en) | 2024-07-19 |
CN118361950B CN118361950B (en) | 2024-10-18 |
Family
ID=91885094
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202410788421.9A Active CN118361950B (en) | 2024-06-19 | 2024-06-19 | A vertical tank reduction furnace for producing magnesium metal |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN118361950B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118705885A (en) * | 2024-08-27 | 2024-09-27 | 沈阳铝镁设计研究院有限公司 | A magnesium metal vertical reduction furnace and a method for loading and unloading the furnace |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040072410A (en) * | 2003-02-12 | 2004-08-18 | 이명준 | Method to replace briquet for boiler and thereof apparatus |
CN101666509A (en) * | 2009-09-14 | 2010-03-10 | 罗子焱 | Pot mounting device of biomass semi-gasifier |
JP2021014977A (en) * | 2019-07-15 | 2021-02-12 | 張偉萍 | Auxiliary equipment that completely burns coke in the stove |
CN217785827U (en) * | 2022-05-27 | 2022-11-11 | 济南易航新材料科技有限公司 | A magnesium extraction furnace and its complete set of magnesium smelting equipment |
-
2024
- 2024-06-19 CN CN202410788421.9A patent/CN118361950B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040072410A (en) * | 2003-02-12 | 2004-08-18 | 이명준 | Method to replace briquet for boiler and thereof apparatus |
CN101666509A (en) * | 2009-09-14 | 2010-03-10 | 罗子焱 | Pot mounting device of biomass semi-gasifier |
JP2021014977A (en) * | 2019-07-15 | 2021-02-12 | 張偉萍 | Auxiliary equipment that completely burns coke in the stove |
CN217785827U (en) * | 2022-05-27 | 2022-11-11 | 济南易航新材料科技有限公司 | A magnesium extraction furnace and its complete set of magnesium smelting equipment |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118705885A (en) * | 2024-08-27 | 2024-09-27 | 沈阳铝镁设计研究院有限公司 | A magnesium metal vertical reduction furnace and a method for loading and unloading the furnace |
Also Published As
Publication number | Publication date |
---|---|
CN118361950B (en) | 2024-10-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN118361950B (en) | A vertical tank reduction furnace for producing magnesium metal | |
CN107663588B (en) | A method for continuous smelting of carbonized slag | |
CN108050848B (en) | A kind of continuous electric forge furnace of high temperature | |
KR20120074927A (en) | Apparatus for manufacturing magnesium | |
CN106431024A (en) | Method for preparing titanium carbide slag | |
CN102936648B (en) | Method for producing rich-titanium material by using microwave kiln, independent container and ilmenite pressing blocks | |
CN203893655U (en) | Vacuum heating furnace | |
CN106702172A (en) | Soldering copper slag tank with refractory lining | |
CN101033511B (en) | A metal magnesium smelting furnace | |
CN210856202U (en) | Liquid metal smelting system | |
CN114231694B (en) | Device and method for heating waste steel by utilizing hot stuffy waste heat of steel slag | |
CN111690817A (en) | Novel airtight protective cover device of electroslag furnace | |
CN102943142A (en) | Solid-state reduction ilmenite pressing block for producing titanium-rich material and preparation method and application thereof | |
CN218539317U (en) | Casting type directional solidification device for industrial silicon | |
CN217785827U (en) | A magnesium extraction furnace and its complete set of magnesium smelting equipment | |
CN201778058U (en) | Vacuum refining furnace | |
CN113817926B (en) | Efficient energy-saving bottom magnesium-discharging smelting device | |
CN115060073A (en) | High-temperature atmosphere sintering furnace for extra-large ceramic parts and sintering method thereof | |
CN201092582Y (en) | Slag discharging device for metal vacuum smelting reduction still | |
CN209639495U (en) | Continuous feeding electric arc furnace for steelmaking | |
CN206607268U (en) | Swinging support refers to vertical shaft scrap steel preheating system | |
CN207525311U (en) | One kind is placed in material boat in horizontal positioned magnesium vacuum reduction tank | |
CN201459211U (en) | Vacuum smelting reduction tank barrel | |
CN115448306B (en) | Tandem graphitizing furnace and discharging method | |
CN118147457A (en) | A heat storage type vertical tank reduction furnace magnesium smelting device and process method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |