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CN116481316A - Redox integrated metallurgical furnace - Google Patents

Redox integrated metallurgical furnace Download PDF

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Publication number
CN116481316A
CN116481316A CN202310448484.5A CN202310448484A CN116481316A CN 116481316 A CN116481316 A CN 116481316A CN 202310448484 A CN202310448484 A CN 202310448484A CN 116481316 A CN116481316 A CN 116481316A
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CN
China
Prior art keywords
furnace
oxidation
reduction
siphon
redox
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.)
Pending
Application number
CN202310448484.5A
Other languages
Chinese (zh)
Inventor
张红
曾国礼
张朝波
付光
马绍斌
尹为波
兰国辉
刘殿传
张特
肖毕高
李永凤
张路飞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yunnan Chihong Zinc and Germanium Co Ltd
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Yunnan Chihong Zinc and Germanium Co Ltd
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.)
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Publication date
Application filed by Yunnan Chihong Zinc and Germanium Co Ltd filed Critical Yunnan Chihong Zinc and Germanium Co Ltd
Priority to CN202310448484.5A priority Critical patent/CN116481316A/en
Publication of CN116481316A publication Critical patent/CN116481316A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B19/00Combinations of different kinds of furnaces that are not all covered by any single one of main groups F27B1/00 - F27B17/00
    • F27B19/02Combinations of different kinds of furnaces that are not all covered by any single one of main groups F27B1/00 - F27B17/00 combined in one structure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/30Arrangements for extraction or collection of waste gases; Hoods therefor
    • F27D17/302Constructional details of ancillary components, e.g. waste gas conduits or seals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/15Tapping equipment; Equipment for removing or retaining slag
    • F27D3/1545Equipment for removing or retaining slag
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27MINDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
    • F27M2003/00Type of treatment of the charge
    • F27M2003/16Treatment involving a chemical reaction
    • F27M2003/165Reduction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27MINDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
    • F27M2003/00Type of treatment of the charge
    • F27M2003/16Treatment involving a chemical reaction
    • F27M2003/167Oxydation
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacture Of Iron (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to an oxidation-reduction integrated smelting furnace, which comprises an integrated furnace body, wherein the interior of the furnace body is divided into an oxidation furnace and a reduction furnace through a furnace wall, and the upper end of the furnace wall is lower than the inner top wall of the furnace body; the inner bottom of the oxidation furnace is higher than the inner bottom of the reduction furnace, and a siphon component is arranged between the reduction furnace and the oxidation furnace; the upper section of the furnace body is provided with a flue gas pipeline, the upper end of the oxidation furnace is provided with a feeding port and a slag detection port, and the upper end of the reduction furnace is provided with an auxiliary material port and a lead detection port. The integrated metallurgical furnace can shorten the process flow of traditional lead smelting, integrate two sets of environment smoke collection and dust collection needed by oxidation and reduction, reduce the investment cost of factories and save the labor cost.

Description

氧化还原一体式冶金炉Redox integrated metallurgical furnace

技术领域technical field

本发明属于冶炼技术领域,具体的说,涉及一种氧化还原一体式冶炼炉。The invention belongs to the technical field of smelting, and in particular relates to an oxidation-reduction integrated smelting furnace.

背景技术Background technique

近年来,火法炼铅模式逐渐由高含铅物料向低含铅或其他渣物料转变,原先的部分炉型随之而变,逐渐由两段炼铅过度到一段氧化、一段还原的炼铅模式,但是,两台冶金炉的人员构成不变,所需设备、占地面积等也不会改变。再随着环保压力的增加,火法炼铅的生产经营面临着巨大的挑战,要如何压缩成本、扩大经济效益,成为企业生死存亡的威胁。In recent years, the mode of pyrometallurgical lead smelting has gradually changed from materials with high lead content to materials with low lead content or other slag materials, and some of the original furnace types have changed accordingly, gradually transitioning from two-stage lead smelting to one-stage oxidation and one-stage reduction. However, the personnel composition of the two metallurgical furnaces remains unchanged, and the required equipment and floor space will not change. With the increasing pressure of environmental protection, the production and operation of pyrometallurgy is facing huge challenges. How to reduce costs and expand economic benefits has become a threat to the survival of enterprises.

本发明可以在当前最新的炼铅模式下,进一步压缩投资及人工成本,大大降低企业的运行成本,在相同产能的情况下,占据非常明显的经济优势,将会成为未来炼铅、甚至其他冶炼行业的首选炉型。The present invention can further reduce the investment and labor costs under the current latest lead smelting mode, and greatly reduce the operating cost of the enterprise. Under the same production capacity, it occupies a very obvious economic advantage, and will become the preferred furnace type for lead smelting and even other smelting industries in the future.

发明内容Contents of the invention

为了克服背景技术中存在的问题,本发明提供了一种氧化还原一体式冶炼炉。In order to overcome the problems in the background technology, the present invention provides a redox integrated smelting furnace.

为实现上述目的,本发明是通过如下技术方案实现的:To achieve the above object, the present invention is achieved through the following technical solutions:

一种氧化还原一体式冶炼炉,包括一体式的炉体,所述炉体内部通过炉墙分隔成氧化炉和还原炉,所述炉墙的上端低于炉体的内顶壁;所述氧化炉的内底高于还原炉的内底,还原炉和氧化炉之间设有虹吸组件;所述炉体上部段设有烟气管道,氧化炉上端设有投料口和探渣口,还原炉上端设有辅料口和探铅口。An oxidation-reduction integrated smelting furnace, comprising an integrated furnace body, the interior of the furnace body is divided into an oxidation furnace and a reduction furnace by a furnace wall, the upper end of the furnace wall is lower than the inner top wall of the furnace body; the inner bottom of the oxidation furnace is higher than the inner bottom of the reduction furnace, and a siphon component is arranged between the reduction furnace and the oxidation furnace; a flue gas pipeline is provided on the upper part of the furnace body, a feeding port and a slag detection port are provided at the upper end of the oxidation furnace, and an auxiliary material port and a lead detection port are provided at the upper end of the reduction furnace.

进一步的,所述的烟气管道位于炉墙的正上方,氧化炉和还原炉各占一半烟气管道。Further, the flue gas pipeline is located directly above the furnace wall, and the oxidation furnace and the reduction furnace each occupy half of the flue gas pipeline.

进一步的,所述的虹吸组件包括放渣虹吸井、第一虹吸通道和渣溜槽;所述放渣虹吸井设置在氧化炉的外壁上,第一虹吸通道的一端伸入至氧化炉的底部,另一端连通放渣虹吸井;放渣虹吸井通过渣溜槽连通还原炉。Further, the siphon assembly includes a slag discharge siphon well, a first siphon channel and a slag chute; the slag discharge siphon well is arranged on the outer wall of the oxidation furnace, one end of the first siphon channel extends to the bottom of the oxidation furnace, and the other end communicates with the slag discharge siphon well; the slag discharge siphon well communicates with the reduction furnace through the slag chute.

进一步的,所述氧化炉底部呈漏斗状往第一虹吸通道处倾斜。Further, the bottom of the oxidation furnace is funnel-shaped and slopes toward the first siphon channel.

进一步的,所述的还原炉外壁上设有放铅虹吸井,放铅虹吸井通过倾斜向下的第二虹吸通道连接至还原炉底部,所述还原炉底部呈漏斗状往第二虹吸通道的下端口处倾斜。Further, the outer wall of the reduction furnace is provided with a lead-discharging siphon well, and the lead-discharging siphon well is connected to the bottom of the reduction furnace through a second sloping downward siphon passage, and the bottom of the reduction furnace is funnel-shaped and slopes toward the lower port of the second siphon passage.

进一步的,所述氧化炉的虹吸井高度为1.5m,高于还原炉正常熔炼熔池高度0.5m,确保氧化炉熔池向还原炉内流动。Further, the height of the siphon well of the oxidation furnace is 1.5m, which is 0.5m higher than the normal melting pool height of the reduction furnace, so as to ensure that the oxidation furnace melt pool flows into the reduction furnace.

进一步的,所述氧化炉与还原炉连通的渣溜槽倾斜角度为15度,可以实现熔渣的自行流淌。Further, the inclination angle of the slag chute connecting the oxidation furnace and the reduction furnace is 15 degrees, which can realize the voluntary flow of molten slag.

进一步的,所述氧化炉和还原炉的侧面设有预留事故排渣管。Further, the sides of the oxidation furnace and the reduction furnace are provided with reserved emergency slagging pipes.

进一步的,所述还原炉的底部呈漏斗状往第二虹吸通道处倾斜。Further, the bottom of the reduction furnace is funnel-shaped and slopes toward the second siphon channel.

本发明的有益效果:使用本发明所述的一体式冶金路可缩短传统铅冶炼的工艺流程,将氧化和还原原需两套的环境集烟、收尘合二为一,可降低工厂投资成本,节约人工成本。Beneficial effects of the present invention: the use of the integrated metallurgical road of the present invention can shorten the process flow of traditional lead smelting, and combine the two sets of environments for oxidation and reduction into one for smoke collection and dust collection, which can reduce factory investment costs and save labor costs.

附图说明Description of drawings

图1是本发明的俯视图;Fig. 1 is a top view of the present invention;

图2是本发明中氧化炉的结构示意图。Fig. 2 is a structural schematic diagram of an oxidation furnace in the present invention.

图中,1、炉体;2、炉墙;3、氧化炉;4、还原炉;5、虹吸组件;501、放渣虹吸井;502、第一虹吸通道;503、渣溜槽;6、烟气管道;7、投料口;8、辅料口;9、放铅虹吸井;10、第二虹吸通道;11、事故排渣管;12、探渣口;13、探铅口。In the figure, 1, furnace body; 2, furnace wall; 3, oxidation furnace; 4, reduction furnace; 5, siphon assembly; 501, slag discharge siphon well; 502, first siphon channel; 503, slag chute;

具体实施方式Detailed ways

为了使本发明的目的、技术方案和有益效果更加清楚,下面将对本发明的优选实施例进行详细的说明,以方便技术人员理解。In order to make the purpose, technical solutions and beneficial effects of the present invention clearer, the preferred embodiments of the present invention will be described in detail below, so as to facilitate the understanding of the skilled person.

实施例,一种氧化还原一体式冶炼炉,参照附图1-2,包括一体式的炉体1,所述炉体1内部通过炉墙2分隔成氧化炉3和还原炉4,所述炉墙2的上端低于炉体1的内顶壁;所述氧化炉3的内底比还原炉4的内底高0.5m,还原炉4和氧化炉3之间设有虹吸组件5;通过虹吸组件5将氧化炉3中的熔渣输送至还原炉4,所述炉体1上部段设有烟气管道6,氧化炉3上端设有投料口7和探渣口12,还原炉4上端设有辅料口8和探铅口13。An embodiment, an oxidation-reduction integrated smelting furnace, with reference to accompanying drawings 1-2, includes an integrated furnace body 1, the interior of the furnace body 1 is divided into an oxidation furnace 3 and a reduction furnace 4 by a furnace wall 2, the upper end of the furnace wall 2 is lower than the inner top wall of the furnace body 1; the inner bottom of the oxidation furnace 3 is 0.5m higher than the inner bottom of the reduction furnace 4, and a siphon assembly 5 is provided between the reduction furnace 4 and the oxidation furnace 3; the slag in the oxidation furnace 3 is transported to the reduction furnace 4 through the siphon assembly 5. A flue gas pipeline 6 is provided, a feeding port 7 and a slag detection port 12 are provided at the upper end of the oxidation furnace 3 , and an auxiliary material port 8 and a lead detection port 13 are provided at the upper end of the reduction furnace 4 .

在一实施例中,所述的烟气管道6位于炉墙2的正上方,氧化炉3和还原炉4各占一半烟气管道6,两段炉体1共用一套余热锅炉来吸收烟气中的热量、共用一套除尘设备来处理烟气中烟尘,可节省建设投资成本。In one embodiment, the flue gas pipeline 6 is located directly above the furnace wall 2, the oxidation furnace 3 and the reduction furnace 4 each occupy half of the flue gas pipeline 6, and the two furnace bodies 1 share a set of waste heat boilers to absorb the heat in the flue gas and a set of dust removal equipment to treat the smoke in the flue gas, which can save construction investment costs.

在一实施例中,所述的虹吸组件5包括放渣虹吸井501、第一虹吸通道502和渣溜槽503;所述放渣虹吸井501设置在氧化炉3的外壁上;第一虹吸通道502通过140mm*140mm的耐火砖砌筑而成,其一端伸入至氧化炉3的底部,另一端连通放渣虹吸井501;放渣虹吸井501通过渣溜槽503连通还原炉4。In one embodiment, the siphon assembly 5 includes a slag discharge siphon well 501, a first siphon channel 502 and a slag chute 503; the slag discharge siphon well 501 is arranged on the outer wall of the oxidation furnace 3; the first siphon channel 502 is made of 140mm*140mm refractory bricks, one end of which extends into the bottom of the oxidation furnace 3, and the other end communicates with the slag discharge siphon well 501; Furnace 4.

在一实施例中,所述氧化炉3底部呈漏斗状往第一虹吸通道502处倾斜。In one embodiment, the bottom of the oxidation furnace 3 is funnel-shaped and slopes toward the first siphon channel 502 .

在一实施例中,所述的还原炉4外壁上设有放铅虹吸井9,放铅虹吸井9通过倾斜向下的第二虹吸通道10连接至还原炉4底部,所述还原炉4底部呈漏斗状往第二虹吸通道10的下端口处倾斜。第二虹吸通道10通过140mm*140mm的耐火砖砌筑而成。In one embodiment, the outer wall of the reduction furnace 4 is provided with a lead-discharging siphon well 9, and the lead-discharging siphon well 9 is connected to the bottom of the reduction furnace 4 through a second siphon channel 10 inclined downward. The second siphon channel 10 is built by refractory bricks of 140mm*140mm.

在一实施例中,所述氧化炉3的虹吸井高度为1.5m,高于还原炉4正常熔炼熔池高度0.5m,确保氧化炉3熔池向还原炉4内流动。In one embodiment, the height of the siphon well of the oxidation furnace 3 is 1.5 m, which is 0.5 m higher than the normal melting pool height of the reduction furnace 4 , so as to ensure that the molten pool of the oxidation furnace 3 flows into the reduction furnace 4 .

在一实施例中,渣溜槽503倾斜角度为15度,可以实现熔渣的自行流淌。In one embodiment, the inclination angle of the slag chute 503 is 15 degrees, so that the slag can flow by itself.

在一实施例中,所述氧化炉3和还原炉4的侧面设有预留事故排渣管11。In one embodiment, the sides of the oxidation furnace 3 and the reduction furnace 4 are provided with reserved emergency slagging pipes 11 .

在一实施例中,所述还原炉4的底部呈漏斗状往第二虹吸通道10处倾斜。In one embodiment, the bottom of the reduction furnace 4 is funnel-shaped and slopes toward the second siphon channel 10 .

最后说明的是,以上优选实施例仅用于说明本发明的技术方案而非限制,尽管通过上述优选实施例已经对本发明进行了详细的描述,但本领域技术人员应当理解,可以在形式上和细节上对其作出各种各样的改变,而不偏离本发明权利要求书所限定的范围。Finally, it is noted that the above preferred embodiments are only used to illustrate the technical solutions of the present invention and are not limiting. Although the present invention has been described in detail through the above preferred embodiments, those skilled in the art should understand that various changes can be made to it in form and details without departing from the scope defined by the claims of the present invention.

Claims (9)

1. An oxidation-reduction integrated smelting furnace is characterized in that: the furnace comprises an integrated furnace body, wherein the interior of the furnace body is divided into an oxidation furnace and a reduction furnace through a furnace wall, and the upper end of the furnace wall is lower than the inner top wall of the furnace body; the inner bottom of the oxidation furnace is higher than the inner bottom of the reduction furnace, and a siphon component is arranged between the reduction furnace and the oxidation furnace; the upper section of the furnace body is provided with a flue gas pipeline, the upper end of the oxidation furnace is provided with a feeding port and a slag detection port, and the upper end of the reduction furnace is provided with an auxiliary material port and a lead detection port.
2. The redox integrated smelting furnace of claim 1, wherein: the flue gas pipeline is positioned right above the furnace wall, and the oxidation furnace and the reduction furnace respectively occupy half of the flue gas pipeline.
3. The redox integrated smelting furnace of claim 1, wherein: the siphon assembly comprises a slag discharging siphon well, a first siphon channel and a slag chute; the slag discharging siphon well is arranged on the outer wall of the oxidation furnace, one end of the first siphon channel extends into the bottom of the oxidation furnace, and the other end of the first siphon channel is communicated with the slag discharging siphon well; the slag discharging siphon well is communicated with the reduction furnace through a slag chute.
4. A redox integrated smelting furnace according to claim 3, wherein: the bottom of the oxidation furnace is inclined towards the first siphon channel in a funnel shape.
5. The redox integrated smelting furnace of claim 1, wherein: the outer wall of the reduction furnace is provided with a lead discharging siphon well, the lead discharging siphon well is connected to the bottom of the reduction furnace through a second siphon channel which is inclined downwards, and the bottom of the reduction furnace is inclined towards the lower port of the second siphon channel in a funnel shape.
6. The redox integrated smelting furnace of claim 1, wherein: the height of the siphon well of the oxidation furnace is 1.5m, which is 0.5m higher than the height of the normal smelting pool of the reduction furnace.
7. The redox integrated smelting furnace of claim 1, wherein: the sides of the oxidation furnace and the reduction furnace are provided with reserved accident slag discharging pipes.
8. A redox integrated smelting furnace according to claim 3, wherein: the inclination angle of the slag chute is 15 degrees.
9. The redox integrated smelting furnace of claim 5, wherein: the bottom of the reduction furnace is inclined towards the second siphon channel in a funnel shape.
CN202310448484.5A 2023-04-24 2023-04-24 Redox integrated metallurgical furnace Pending CN116481316A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101200777A (en) * 2007-09-24 2008-06-18 云南锡业集团(控股)有限责任公司 Method and equipment for continuous smelting of lead sulfide concentrate
CN201628476U (en) * 2010-03-23 2010-11-10 中国瑞林工程技术有限公司 Direct lead smelting furnace
CN201909535U (en) * 2011-01-26 2011-07-27 云南铜业科技发展股份有限公司 Infinity smelting furnace
CN103146936A (en) * 2013-03-25 2013-06-12 湖南金旺铋业股份有限公司 Oxygen-rich redox furnace
CN106403595A (en) * 2016-11-22 2017-02-15 江苏省冶金设计院有限公司 Oxidation-reduction roasting integrated rotary hearth furnace
CN106996695A (en) * 2016-01-22 2017-08-01 中国恩菲工程技术有限公司 A kind of metallurgical furnace
CN111457735A (en) * 2020-04-15 2020-07-28 中国恩菲工程技术有限公司 Integrated pyrometallurgical furnace and method for treating zinc leaching slag

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101200777A (en) * 2007-09-24 2008-06-18 云南锡业集团(控股)有限责任公司 Method and equipment for continuous smelting of lead sulfide concentrate
CN201628476U (en) * 2010-03-23 2010-11-10 中国瑞林工程技术有限公司 Direct lead smelting furnace
CN201909535U (en) * 2011-01-26 2011-07-27 云南铜业科技发展股份有限公司 Infinity smelting furnace
CN103146936A (en) * 2013-03-25 2013-06-12 湖南金旺铋业股份有限公司 Oxygen-rich redox furnace
CN106996695A (en) * 2016-01-22 2017-08-01 中国恩菲工程技术有限公司 A kind of metallurgical furnace
CN106403595A (en) * 2016-11-22 2017-02-15 江苏省冶金设计院有限公司 Oxidation-reduction roasting integrated rotary hearth furnace
CN111457735A (en) * 2020-04-15 2020-07-28 中国恩菲工程技术有限公司 Integrated pyrometallurgical furnace and method for treating zinc leaching slag

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Application publication date: 20230725