CN200988859Y - Oxygen bottom blowing melting furnace - Google Patents
Oxygen bottom blowing melting furnace Download PDFInfo
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- CN200988859Y CN200988859Y CN200620158487.7U CN200620158487U CN200988859Y CN 200988859 Y CN200988859 Y CN 200988859Y CN 200620158487 U CN200620158487 U CN 200620158487U CN 200988859 Y CN200988859 Y CN 200988859Y
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- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 69
- 239000001301 oxygen Substances 0.000 title claims abstract description 69
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 238000007664 blowing Methods 0.000 title claims description 19
- 238000002844 melting Methods 0.000 title description 4
- 230000008018 melting Effects 0.000 title description 4
- 150000002926 oxygen Chemical class 0.000 claims description 6
- 238000003723 Smelting Methods 0.000 abstract description 29
- 238000009423 ventilation Methods 0.000 abstract description 14
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 238000000034 method Methods 0.000 description 26
- 239000000779 smoke Substances 0.000 description 11
- 238000005245 sintering Methods 0.000 description 10
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 239000003517 fume Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 240000005561 Musa balbisiana Species 0.000 description 1
- 235000018290 Musa x paradisiaca Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241001062472 Stokellia anisodon Species 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000009510 drug design Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 239000010959 steel 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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Abstract
本实用新型氧气底吹熔炼炉,其提供了一种新型高效节能的熔炼炉,该炉身底部设有数个氧枪口,该氧枪口处设有氧枪装置,该氧枪装置由外层套管、若干个内层套管套合而成,该若干个内层套管依次嵌套,该内层套管外侧设有若干通气槽,该内层套管中心形成有通孔,此新型熔炼炉,合理的组织了各层通道上的通气量,并且保持合理的高的气流速度,明显降低供氧压力,有利于化学发应剧烈高效的进行。
The utility model oxygen bottom-blown smelting furnace provides a new high-efficiency and energy-saving smelting furnace. The bottom of the furnace body is provided with several oxygen gun ports, and the oxygen gun ports are provided with an oxygen lance device. The oxygen lance device consists of an outer layer The casing and several inner layer casings are sleeved together. The several inner layer casings are nested in sequence. There are a number of ventilation grooves on the outside of the inner layer casing. A through hole is formed in the center of the inner layer casing. This new type The smelting furnace reasonably organizes the ventilation volume on the channels of each layer, and maintains a reasonable high air velocity, significantly reduces the oxygen supply pressure, and is conducive to the intense and efficient chemical reaction.
Description
技术领域technical field
本实用新型涉及用于冶金行业冶金设备,特别是指一种新型的熔炼炉。The utility model relates to metallurgical equipment used in the metallurgical industry, in particular to a novel melting furnace.
背景技术Background technique
传统的炼铅工艺主要有烧结锅-鼓风炉流程和烧结机-鼓风炉流程。这两种方法主要是将铅精矿用烧结的方法通过鼓风炉还原熔炼。烧结锅-鼓风炉流程在生产应用中存在严重的环保问题,烧结过程中产生的SO2烟气由于无法回收利用而全部排空,对大气环境造成严重污染,同时烧结过程中大量的返粉作业又造成铅烟尘的低空弥散,带来铅烟尘的环境污染。烧结机-鼓风炉流程,产出的烟气SO2含量低,国内普遍采用的制酸工艺中实际生产转化率只有80%左右,尾气排放仍然达不到环保要求,而且硫酸产品质量不高。国外有TOPSOE制酸技术,但是技术软硬件费用昂贵,经济上极不合理,并且该流程同样存在烧结过程大量返尘作业造成的铅烟尘的低空弥散问题,环保问题仍然无法解决。另外,这两种烧结方法,烧结过程中产生的氧化反应热都无法回收利用,冶炼过程能耗高。目前,国外比较成熟先进的炼铅工艺还有Kivicet法、QSL法、顶吹浸没熔炼法,它们都较好地解决了铅冶炼过程中的环保问题,但是实施费用高、基建投资大、经济效益较差。Traditional lead smelting processes mainly include sintering pot-blast furnace process and sintering machine-blast furnace process. These two methods mainly use the method of sintering the lead concentrate to reduce and smelt through the blast furnace. The sintering pot-blast furnace process has serious environmental protection problems in production and application. The SO2 flue gas generated during the sintering process is completely emptied because it cannot be recycled, causing serious pollution to the atmospheric environment. At the same time, a large number of powder returning operations during the sintering process have caused The low-altitude dispersion of lead fume brings environmental pollution of lead fume. Sintering machine-blast furnace process, the output flue gas SO 2 content is low, the actual production conversion rate in the acid production process commonly used in China is only about 80%, the tail gas emission still does not meet the environmental protection requirements, and the quality of sulfuric acid products is not high. There is TOPSOE acid production technology in foreign countries, but the technical software and hardware are expensive and economically unreasonable, and this process also has the problem of low-altitude dispersion of lead fumes caused by a large number of dust-returning operations during the sintering process, and the environmental protection problem still cannot be solved. In addition, in these two sintering methods, the oxidation reaction heat generated during the sintering process cannot be recycled, and the energy consumption of the smelting process is high. At present, there are more mature and advanced lead smelting processes in foreign countries, such as Kivicet method, QSL method, and top-blowing immersion smelting method. poor.
实用新型内容Utility model content
在实践过程中,氧气底吹熔炼炉在铅冶炼及铜冶炼方面正发挥越来越大的作用,尤其是在铅冶炼领域业已取得不菲的业绩。氧气底吹熔炼炉是对传统铅(铜)冶炼工艺的重大改进。In practice, oxygen bottom-blown smelting furnaces are playing an increasingly important role in lead smelting and copper smelting, especially in the field of lead smelting, which has achieved remarkable results. Oxygen bottom-blown smelting furnace is a major improvement to the traditional lead (copper) smelting process.
本实用新型的目的在于提供一种带有氧枪装置的氧气底吹熔炼炉,使得现行的氧气底吹熔炼工艺更具能耗低、污染少、操作环境好等突出优点。The purpose of this utility model is to provide an oxygen bottom-blown smelting furnace with an oxygen lance device, so that the current oxygen bottom-blown smelting process has the outstanding advantages of low energy consumption, less pollution, and good operating environment.
本实用新型的氧气底吹熔炼炉采用的技术方案在于:The technical solution adopted by the oxygen bottom-blowing smelting furnace of the present utility model is:
一种氧气底吹熔炼炉,包含有炉身,该炉身底部设置有数个氧枪口,该氧枪口出设置有氧枪装置;An oxygen bottom blowing smelting furnace, comprising a furnace body, the bottom of the furnace body is provided with several oxygen lance ports, and the oxygen lance ports are provided with an oxygen lance device;
其中,该氧枪装置由外层套管、若干个内层套管套合而成,该若干个内层套管依次嵌套,该内层套管外侧设有若干通气槽,该内层套管中心形成有通孔;Wherein, the oxygen lance device is composed of an outer layer sleeve and several inner layer sleeves, and the several inner layer sleeves are nested sequentially. There are several ventilation grooves on the outside of the inner layer sleeve. A through hole is formed in the center of the tube;
其中,该每个内层套管的通气槽的截面面积互不相同;Wherein, the cross-sectional areas of the ventilation grooves of each inner casing are different from each other;
其中,该每个内层套管的通气槽的数量互不相同;Wherein, the number of ventilation grooves of each inner casing is different from each other;
其中,该若干个内层套管的个数为2~5个;Wherein, the number of the several inner casings is 2 to 5;
其中,该氧枪口设置在炉底中心线-30°~+30°;Wherein, the oxygen lance is set at -30°~+30° on the center line of the furnace bottom;
其中,该氧枪口为单排设置;Wherein, the oxygen muzzle is arranged in a single row;
其中,该氧枪口为双排设置;Among them, the oxygen muzzle is set in double rows;
过在氧气底吹熔炼炉底部设置的氧枪口上装设氧枪装置,氧气从炉内熔池底部喷入,使炉内的熔体处于剧烈翻腾搅动状态。使得化学反应速度更为剧烈,反应完全,大大提高了化学反应的速率,优化了的枪口设计,使得炉子的使用寿命增长而且经济合理,有效克服了现有的氧枪装置使用寿命短、需要氧气压力高、作业率底、动力消耗大等缺点。By installing an oxygen lance device on the oxygen lance port at the bottom of the oxygen bottom-blown smelting furnace, oxygen is injected from the bottom of the molten pool in the furnace, so that the melt in the furnace is in a state of violent tumbling and stirring. It makes the chemical reaction speed more intense, the reaction is complete, and the chemical reaction rate is greatly improved. The optimized muzzle design makes the service life of the furnace longer and economical and reasonable, effectively overcoming the short service life of the existing oxygen lance device and the need for Disadvantages such as high oxygen pressure, low operating rate, and large power consumption.
附图说明Description of drawings
图1为本实用新型氧气底吹熔炼炉的主视图;Fig. 1 is the front view of the utility model oxygen bottom blowing smelting furnace;
图2为本实用新型氧气底吹熔炼炉的侧视图;Fig. 2 is the side view of the utility model oxygen bottom blowing smelting furnace;
图3为本实用新型氧气底吹熔炼炉的氧枪口装设位置图;Fig. 3 is the installation position diagram of the oxygen muzzle of the oxygen bottom blowing smelting furnace of the present utility model;
图4为本实用新型氧气底吹熔炼炉的氧枪装置的剖面结构示意图。Fig. 4 is a schematic cross-sectional structure diagram of the oxygen lance device of the oxygen bottom blowing smelting furnace of the present invention.
具体实施方式Detailed ways
本实用新型氧气底吹熔炼炉是氧气底吹熔炼工艺的核心设备,如图1~图2所示,它是由可绕水平轴转动的炉身10、托轮装置b和传动装置a等主要部件所组成,其中该传动装置a连接发电机1。炉身10为卧式圆筒外形,钢制外壳内砌筑优质镁铬砖,可以根据需要转动任意角度。支撑装置b可以满足炉身10回转和热胀冷缩的需要,上部设有出烟口4和加料口5,本氧气底吹熔炼炉的出烟口装置具有特殊的设计结构,在使用过程中无烟尘泄漏无块状粘结。即使在炉身转动过程,也可使出烟口无烟气外泄。这是由于出烟口结构的合理设计与固定连接的香蕉罩的作用。出烟口无块状粘结主要是在设计中充分考虑了避免结块的方法和以优良材质的水套做烟气通道,使出烟口内表面无法形成结块。在炉体一端设出渣口8另一端设金属放出口2及氧油烧嘴口3。上部的出烟口4与烟罩相接。两端各设有一台燃烧器7,设在出渣口端的燃烧器,用于开炉升温、临时保温及需要热量供给炉体的情况,另一端的燃烧器主要用于热工的锅炉直升烟道,其可能产生的结块落到本炉内,用此燃烧器将其熔化。另外,炉身10一端设置有氧油烧嘴口,上部设有探料口6。The utility model oxygen bottom-blown smelting furnace is the core equipment of the oxygen bottom-blown smelting process, as shown in Fig. components, where the transmission a is connected to the generator 1. Furnace body 10 is a horizontal cylindrical shape, and high-quality magnesia-chrome bricks are built in the steel shell, which can be rotated at any angle as required. The support device b can meet the needs of the furnace body 10 rotation and thermal expansion and contraction. The upper part is provided with a smoke outlet 4 and a feeding port 5. The smoke outlet device of this oxygen bottom blowing smelting furnace has a special design structure. During use No smoke leakage, no lumpy sticking. Even in the process of rotating the furnace body, there is no leakage of smoke from the smoke outlet. This is due to the rational design of the smoke outlet structure and the effect of the fixedly connected banana cover. The lack of block-like adhesion at the smoke outlet is mainly because the method of avoiding agglomeration has been fully considered in the design and the water jacket of good material is used as the flue gas channel, so that no agglomeration can be formed on the inner surface of the smoke outlet. One end of the furnace body is provided with a slag discharge port 8 and the other end is provided with a metal discharge port 2 and an oxygen oil burner port 3 . The smoke outlet 4 on the top is connected with the smoke hood. There is a burner 7 at each end. The burner at the slag outlet is used for heating up the furnace, temporary heat preservation and heat supply to the furnace body. The burner at the other end is mainly used for thermal boiler direct heating. The flue, its possible agglomerates fall into the furnace, where it is melted with this burner. In addition, an oxygen oil burner port is provided at one end of the furnace body 10 , and a material detection port 6 is provided at the upper part.
本实用新型的重点在于:于炉身10上设置有数个氧枪口9,该氧枪口设置在炉底中心线-30°~+30°之间,通常为双排设置,根据不同反应的需要也可以为单排设置,该氧枪口内部有氧枪装置11。The key points of the present utility model are: several oxygen muzzles 9 are arranged on the furnace body 10, and the oxygen muzzles are arranged between -30°~+30° on the center line of the furnace bottom, and are usually arranged in double rows. It can also be arranged in a single row if required, and there is an oxygen lance device 11 inside the oxygen lance.
如图4所示,该氧气装置11,是由一外层套管111和内层套管组成,该内层套管由第一内层套管121、第二内层套管122及第三内层套管123组成,每个套管中心形成有通孔13,其上对应设有第一通气槽124、第二通气槽125、第三通气槽126,各个通气槽的截面面积不同,且各个内层套管设置的通气槽的数量也根据反应的需要互不相同,以保证供应不同量的气体,合理的分配各层通道的通气量,通常,第一通气槽124为氮及水雾通道,第二通气槽125、第三通气槽126和中心通孔输送氧气。As shown in Figure 4, the oxygen device 11 is composed of an
炉料通过炉顶加料口5或端头的抛料机将配制好的炉料抛入炉内,散落在熔池表面。氧气通过氧气喷枪从炉内熔池底部喷入,使炉内的熔体处于剧烈翻腾搅动状态。落入熔池的炉料迅速被熔体卷入并熔化,因尔发生急剧的化学反应,形成金属(或锍)和熔渣。所形成的产物因其重度不同而在沉降区沉降分离形成金属层和渣层,二者分别从不同的放出口放出。氧气底吹熔炼过程为自热反应过程。The prepared charge is thrown into the furnace through the charging port 5 on the top of the furnace or the throwing machine at the end, and scattered on the surface of the molten pool. Oxygen is injected from the bottom of the molten pool in the furnace through an oxygen lance, so that the melt in the furnace is in a state of violent tumbling and stirring. The charge falling into the molten pool is quickly engulfed and melted by the melt, so a sharp chemical reaction occurs to form metal (or matte) and slag. The formed product settles and separates in the settling zone due to its different gravity to form a metal layer and a slag layer, which are released from different outlets respectively. The oxygen bottom-blown smelting process is an autothermal reaction process.
的理化反应更为充分、完全,有利于化学反映剧烈高效的进行。氧气底吹熔炼炉熔炼过程是在一个几乎完全密封状态下进行的,所以可以得到较高二氧化硫浓度的烟气以利制酸处理,同时也使车间环境达到无烟少尘的良好环保要求。由于优化了枪口设计,保证炉子的寿命增长而且经济合理。另外由于各内层套管外侧的通气槽的数量和面积不同,合理的组织了各层通道的通气量,保持了合理高的气流速度,同时使得气流比较分散,增加了气体与溶体的反应面积,有利于化学反映剧烈高效的进行,使得供氧压力明显降低。具体从数据上讲:本实用新型氧枪后其使用中寿命一般可达30天以上,大大的提高了氧气底吹熔炼炉的作业率,另外,本实用新型的氧枪装置使用的氧气压力仅为(0.6-0.8MPa)大大降低了动力消耗,本实用新型氧气底吹炼熔炉是一种新型高效的熔炼炉。The physical and chemical reactions are more complete and complete, which is conducive to the intense and efficient chemical reactions. The smelting process of the oxygen bottom-blown smelting furnace is carried out in an almost completely sealed state, so the flue gas with a high concentration of sulfur dioxide can be obtained to facilitate acid treatment, and at the same time, the workshop environment can meet the good environmental protection requirements of no smoke and less dust. Due to the optimized design of the muzzle, the life of the furnace is guaranteed to be increased and the economy is reasonable. In addition, because the number and area of the ventilation grooves on the outside of each inner casing are different, the ventilation volume of each layer of channels is reasonably organized, and a reasonable high air velocity is maintained. At the same time, the air flow is relatively dispersed, and the reaction area between the gas and the solution is increased. , which is conducive to the intense and efficient chemical reaction, so that the oxygen supply pressure is significantly reduced. Specifically speaking from the data: the service life of the oxygen lance of the present utility model can generally reach more than 30 days, which greatly improves the operation rate of the oxygen bottom blowing smelting furnace. In addition, the oxygen pressure used by the oxygen lance device of the present utility model is only (0.6-0.8MPa) greatly reduces power consumption, the utility model oxygen bottom blowing melting furnace is a new type of high-efficiency melting furnace.
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101871725A (en) * | 2010-07-07 | 2010-10-27 | 中南大学 | Horizontal bottom-blown molten pool desulfurization furnace and oxidative desulfurization method for lead-containing materials |
| CN101915504A (en) * | 2010-08-23 | 2010-12-15 | 董兰田 | Oxygen-enriched bottom-blown double-port matte-feeding tilting furnace |
| CN102230091A (en) * | 2011-06-13 | 2011-11-02 | 中国恩菲工程技术有限公司 | Oxygen-enriched bottom-blown matte smelting furnace and oxygen-enriched bottom-blown matte smelting technology |
| CN102242277A (en) * | 2011-06-13 | 2011-11-16 | 中国恩菲工程技术有限公司 | Oxygen-rich bottom blown copper smelter and oxygen-rich bottom blown technology for extraction of copper |
| CN103498057A (en) * | 2013-10-12 | 2014-01-08 | 河南豫光金铅股份有限公司 | Device and method for bottom-blowing reduction lead refining with little disturbance of bottom lead |
| CN104018007A (en) * | 2013-02-28 | 2014-09-03 | 中国恩菲工程技术有限公司 | Nickel matte bottom-blowing refining process and nickel matte bottom-blowing refining device |
| CN106086459A (en) * | 2016-08-30 | 2016-11-09 | 安阳市岷山有色金属有限责任公司 | A kind of oxygen bottom-blowing direct-reduction lead smelting process |
| CN107460340A (en) * | 2017-07-31 | 2017-12-12 | 河南豫光金铅股份有限公司 | A kind of quick blow-in method of copper bottom-blown smelting stove |
| CN107739778A (en) * | 2017-11-27 | 2018-02-27 | 中航上大高温合金材料有限公司 | A kind of steel ladle bottom argon blowing device and its refining stirring means |
| CN109628754A (en) * | 2019-02-03 | 2019-04-16 | 包头华鼎铜业发展有限公司 | Copper making continuous-blowing furnace oxygen lance nozzle |
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2006
- 2006-11-16 CN CN200620158487.7U patent/CN200988859Y/en not_active Expired - Lifetime
Cited By (14)
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| CN101871725A (en) * | 2010-07-07 | 2010-10-27 | 中南大学 | Horizontal bottom-blown molten pool desulfurization furnace and oxidative desulfurization method for lead-containing materials |
| CN101915504A (en) * | 2010-08-23 | 2010-12-15 | 董兰田 | Oxygen-enriched bottom-blown double-port matte-feeding tilting furnace |
| CN101915504B (en) * | 2010-08-23 | 2012-04-25 | 董兰田 | Oxygen-enriched bottom-blowing double-port sulfonium-discharging inclined smelting furnace |
| CN102230091A (en) * | 2011-06-13 | 2011-11-02 | 中国恩菲工程技术有限公司 | Oxygen-enriched bottom-blown matte smelting furnace and oxygen-enriched bottom-blown matte smelting technology |
| CN102242277A (en) * | 2011-06-13 | 2011-11-16 | 中国恩菲工程技术有限公司 | Oxygen-rich bottom blown copper smelter and oxygen-rich bottom blown technology for extraction of copper |
| CN102242277B (en) * | 2011-06-13 | 2012-10-10 | 中国恩菲工程技术有限公司 | Oxygen-rich bottom blown copper smelter and oxygen-rich bottom blown technology for extraction of copper |
| CN104018007B (en) * | 2013-02-28 | 2018-01-16 | 中国恩菲工程技术有限公司 | Nickel matte bottom blowing converting process and nickel matte bottom blowing blowing device |
| CN104018007A (en) * | 2013-02-28 | 2014-09-03 | 中国恩菲工程技术有限公司 | Nickel matte bottom-blowing refining process and nickel matte bottom-blowing refining device |
| CN103498057A (en) * | 2013-10-12 | 2014-01-08 | 河南豫光金铅股份有限公司 | Device and method for bottom-blowing reduction lead refining with little disturbance of bottom lead |
| CN106086459A (en) * | 2016-08-30 | 2016-11-09 | 安阳市岷山有色金属有限责任公司 | A kind of oxygen bottom-blowing direct-reduction lead smelting process |
| CN107460340A (en) * | 2017-07-31 | 2017-12-12 | 河南豫光金铅股份有限公司 | A kind of quick blow-in method of copper bottom-blown smelting stove |
| CN107739778A (en) * | 2017-11-27 | 2018-02-27 | 中航上大高温合金材料有限公司 | A kind of steel ladle bottom argon blowing device and its refining stirring means |
| CN107739778B (en) * | 2017-11-27 | 2019-03-22 | 中航上大高温合金材料有限公司 | A kind of steel ladle bottom argon blowing device and its refining stirring means |
| CN109628754A (en) * | 2019-02-03 | 2019-04-16 | 包头华鼎铜业发展有限公司 | Copper making continuous-blowing furnace oxygen lance nozzle |
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Assignee: Chengzhou City Jingui Silver Co., Ltd. Assignor: China Enfi Engineering Technology Co., Ltd. Contract record no.: 2010110000102 Denomination of utility model: Oxygen gun device for oxygen bottom-blowing smelting furnace Granted publication date: 20071212 License type: Common License Record date: 20100803 |
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