WO2020057266A1 - Copper smelting device - Google Patents

Copper smelting device Download PDF

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Publication number
WO2020057266A1
WO2020057266A1 PCT/CN2019/098643 CN2019098643W WO2020057266A1 WO 2020057266 A1 WO2020057266 A1 WO 2020057266A1 CN 2019098643 W CN2019098643 W CN 2019098643W WO 2020057266 A1 WO2020057266 A1 WO 2020057266A1
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WIPO (PCT)
Prior art keywords
furnace body
copper
layer
smelting device
slag
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PCT/CN2019/098643
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French (fr)
Chinese (zh)
Inventor
李锋
尉克俭
黎敏
陆金忠
李建辉
曹珂菲
郝小红
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中国恩菲工程技术有限公司
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Priority to EA202090703A priority Critical patent/EA202090703A1/en
Publication of WO2020057266A1 publication Critical patent/WO2020057266A1/en

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0026Pyrometallurgy
    • C22B15/0028Smelting or converting
    • C22B15/003Bath smelting or converting
    • 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

Definitions

  • the present disclosure relates to the field of non-ferrous metallurgy, and in particular, to a copper smelting device.
  • the fixed side-blown melting furnace that has been put into operation is only 100,000 t / a copper, and the largest side-blown furnace currently designed is only 200,000 t / a copper, which has not yet been put into operation. If the annual output is 300,000 to 500,000
  • the t / a copper scale that is, the annual processing of copper concentrates of 1.5 to 2 million t / a, usually requires at least two side-blown copper production lines, covering a large area, large equipment, large investment, large number of operators, and high operating costs.
  • One of the main objectives of the present disclosure is to overcome at least one of the drawbacks of the related art and provide a copper smelting device to meet the needs of large-scale processing of concentrates.
  • a copper smelting device which includes a furnace body, a charging port, a smoke outlet, a slag outlet, a copper grate, and a primary air vent.
  • a copper grate layer and slag are sequentially arranged from bottom to top in the furnace.
  • a feeding port is provided on the top wall of the furnace body; a smoke outlet is provided on the top wall of the furnace body; a slag outlet is provided on one end of the furnace body; The end of the furnace body opposite to the slag outlet, the copper grate opening is located at the bottom of the copper grate layer; the primary air outlet is located on the corresponding side wall of the slag layer of the furnace body, and is used for The slag layer is blown with oxygen-enriched air, and the widthwise dimension of the inner side wall corresponding to the slag layer is greater than 2.5m and less than or equal to 4.5m.
  • the dimension in the height direction of the inner cavity of the furnace body is 6m to 8m.
  • a widthwise dimension of the gas layer is 4.1m-7m.
  • a blowing pressure of the primary tuyere is 0.12 MPa to 0.3 MPa.
  • the copper smelting device further includes a secondary air outlet disposed on a side wall corresponding to the gas layer.
  • the number of the primary air vents is plural, and the distance between adjacent primary air vents is 500-600 mm.
  • a partition wall is provided in an inner cavity of the copper smelting device along a width direction, and the partition wall divides the inner cavity into a melting zone and a settlement zone, and the partition wall and the There is a space between the top walls of the furnace body.
  • the length of the melting zone is 12m-20m.
  • the settling area is provided with a heating electrode and / or a burner for holding or heating the settling area.
  • the width dimension of the inner side wall corresponding to the slag layer of the copper smelting device is greater than 2.5 m and less than or equal to 4.5 m, which can expand single furnace processing Concentrate scale, which improves labor efficiency and reduces operating costs.
  • Fig. 1 is a plan view of a copper smelting device according to an exemplary embodiment.
  • Fig. 2 is a cross-sectional view taken along the line A-A of the copper smelting apparatus in Fig. 1.
  • Fig. 3 is a B-B sectional view of the copper smelting apparatus in Fig. 1.
  • a copper smelting device which includes a furnace body 100, a charging port 101, a smoke outlet 106, a slag outlet 102, a copper grate 103, and a primary air outlet 104.
  • a copper rhenium layer 112, a slag layer 113, and a gas layer 114 are sequentially arranged from bottom to top.
  • the copper rhenium layer 112 is located at the bottom of the inner cavity of the furnace body 100, and on the corresponding side wall of the copper rhenium layer 112.
  • a copper gate 103 may be provided, and the copper gate 103 may be located at the bottom of the copper gate layer 112.
  • the copper gate 103 may be disposed at an end of one end of the furnace body 100.
  • the feeding port 101 may be disposed on the top wall of the furnace body 100, and there may be multiple feeding ports 101 distributed on the top wall.
  • the feeding port 101 may be 3-6.
  • the slag outlet 102 may be disposed at an end of the furnace body 100 opposite to the copper grate 103.
  • the primary air outlet 104 is located on a side wall corresponding to the slag layer 113 of the furnace body 100, and can be used to blow oxygen-rich air into the slag layer 113.
  • the width of the inner side wall corresponding to the slag layer 113 The dimension of the direction W is greater than 2.5 m and less than or equal to 4.5 m.
  • the concentration of the oxygen-enriched air is 70% to 95%, but is not limited thereto, and may be selected according to actual needs.
  • the blowing pressure of the primary tuyere 104 is 0.12 MPa to 0.3 MPa, and the pressure can increase the stirring intensity of the middle melt of the furnace body 100 in the width direction W and increase the blast of oxygen-enriched air. Pressure can overcome the resistance of the melt and increase the penetration depth of the blast.
  • there may be multiple primary air outlets 104 and the interval between adjacent primary air outlets 104 may be 500mm-600mm, such as but not limited to 550mm or 600mm.
  • a diameter of the air outlet of the primary air outlet 104 may be 38 mm-54 mm, such as but not limited to 45 mm or 50 mm, or 52 mm.
  • the number of the primary air outlets 104 may be 48-80, such as but not limited to 50, 55, 60, 65, 70, 75, and may be based on actual conditions. Need to choose.
  • the copper smelting device provided by the present disclosure can be a side-blown furnace, capable of processing 1 to 2 million t / a of concentrate in a single furnace body, and a copper production scale of 200,000 to 500,000 t / a.
  • the length direction L is the direction defined by the double arrow in FIG. 1
  • the height direction H is the direction of the double arrow in FIG. 2
  • the width direction W defined in the present disclosure is the direction of the double arrow in FIG. 3.
  • Direction It can be understood that when the picture in the illustration is rotated, the defined width direction W and height direction H are also rotated by corresponding angles.
  • the projection of the furnace body 100 in the width direction W may be that the upper gas layer structure width is greater than the lower slag layer structure width.
  • the dimension of the width direction W of the gas layer 114 may be 4.1m-7m.
  • the outer shell of the furnace body 100 may be a steel structure, and the inner lining may be formed of a refractory material.
  • the top of the furnace body 100 may be provided with a feeding opening 101 and a smoke outlet 106.
  • the feeding opening 101 can be set on the center line of the furnace body 100, but is not limited thereto, and can also be arranged near the two side walls according to actual needs.
  • a primary air outlet 104 and a secondary air outlet 105 may be provided on a side wall of the furnace body 100, wherein the primary air outlet 104 is on both sides of the furnace body 100, and the primary air outlet 104 may be provided on a slag layer 113.
  • the secondary air outlet 105 may be disposed on the top wall and the side wall of the furnace body 100, and the secondary air outlet 105 may correspond to the gas layer 114.
  • a cooling element may be provided on the side wall of the furnace body 100, the partition wall 107, and the end wall of the settlement area 111.
  • a copper water jacket 115 may be provided on the side wall.
  • the copper water jacket 115 may be provided with a cooling medium therein, such as but not limited to, the cooling medium may be water.
  • a copper nozzle 103 may be provided at one end of the furnace body 100, and a slag outlet 102 and a burner port 109 may be provided at the other end of the furnace body 100.
  • the burner port 109 may be disposed above the slag outlet 102.
  • the dimension H of the inner cavity height of the furnace body 100 may be 6 m to 8 m.
  • the length of the melting zone may be 12m-20m.
  • the copper smelting device further includes a secondary air outlet 105 disposed on a side wall corresponding to the gas layer 114.
  • the copper smelting device further includes a smoke outlet 106 provided on the top wall of the furnace body 100.
  • the internal cavity of the copper smelting device may be provided with a partition wall 107 along the width direction W.
  • the partition wall 107 divides the internal cavity into a melting area 110 and a settlement area 111, and the partition wall 107 and the furnace body 100. There are spaces between the top walls.
  • the smelting zone 110 and the settling zone 111 are arranged horizontally. With continuous feeding and smelting, the smelting slag generated after smelting can directly flow into the settling zone 111, and the copper slag and slag are separated in the settling zone 111.
  • the sedimentation region 111 is provided with a heating electrode for keeping or heating the sedimentation region 111.
  • the heating electrode may be a graphite electrode 108, but not the same. For the limit, you can choose according to your needs.
  • the settling area 111 may further be provided with a burner, and the burner may be provided in the burner port 109.
  • the copper concentrate After the copper concentrate is mixed with the flux, coal and other returned materials, it can be conveyed to the furnace top of the furnace body 100 through a belt, added to the furnace body 100 through the charging port 101, and 70% to 95% of the rich air is blown through the primary air port 104.
  • 111 is discharged from the slag outlet 102 after being separated from the copper matte. Air is blown into the secondary tuyere 105 for burning the monomer sulfur and carbon monoxide in the flue gas.
  • the flue gas is discharged from the upper gas outlet 106, enters the ascending flue, and the waste heat boiler is sent to the acid production after cooling and dust removal.
  • the melting temperature in the furnace body 100 can be 1200 ° C to 1300 ° C
  • the depth of the molten pool can be 2000mm to 2800mm
  • the grade of copper grate is 55% to 78%
  • the slag contains Cu 0.6% to 2.5%
  • the bed energy rate in the melting zone is concentrate
  • the amount is 60 ⁇ 90t / m2.d.
  • the oxygen-material ratio is related to the copper ⁇ grade
  • the slag containing Cu is also related to the copper ⁇ grade.
  • the furnace hearth of the smelting zone can be estimated.
  • the area is based on the length of the slag layer 113 in the melting zone of the furnace.
  • the width of the slag layer 113 in the melting zone is calculated.
  • the width of the slag layer 113 in the melting zone is 2.5m-4.5m.
  • blower volume can be achieved by increasing the number of tuyeres, increasing the diameter of the tuyere and increasing the pressure of oxygen-enriched air.
  • the melting strength is 80t / m 2 .d.
  • the furnace area of the slag layer 113 in the melting zone is 38m 2 .
  • the size is 15m
  • the width of the furnace body of the slag layer 113 is 2.5m
  • the primary air outlet 104 pressure is 0.12MPa-0.15MPa
  • the primary air outlet 104 spacing is 600mm
  • the primary air outlet 104 number is 48
  • the primary air outlet 104 diameter is 40mm
  • the feeding opening The number of 101 is 3, the blast oxygen concentration is 85%
  • the melt temperature is 1220 °C ⁇ 1280 °C
  • the depth of the molten pool is 2500mm
  • the height of the furnace bottom to the furnace top is 7000mm
  • the gas layer structure in the furnace body 100 is along the width direction
  • the size of W is 4100mm.
  • the smelting strength is 75t / m 2 .d
  • the furnace area of the slag layer 113 in the melting zone is 48m 2
  • the size of the slag layer 113 in the melting zone is 16m along the length direction L.
  • the width of the furnace body of the slag layer 113 is 3.0m
  • the pressure of the primary air outlet 104 is 0.15MPa-0.20MPa
  • the spacing of the primary air outlet 104 is 600mm
  • the number of the primary air outlet 104 is 52
  • the diameter of the primary air outlet 104 is 45mm
  • the feeding opening 101 The number is 3, the blast oxygen-rich concentration is 85%
  • the melt temperature is 1220 °C -1280 °C
  • the melt pool depth is 2500mm
  • the furnace height from the furnace bottom to the furnace top is 7200mm
  • the gas layer structure in the furnace body 100 is along the width direction W
  • the dimensions are 4800mm.
  • the smelting furnace area of the slag layer 113 is 63m 2
  • L dimension along the longitudinal direction of the melting of the slag layer 113 is 18m
  • the slag layer The furnace body width of 113 is 3.5m
  • the primary air outlet 104 pressure is 0.15MPa-0.25MPa
  • the primary air outlet 104 spacing is 600mm
  • the number of primary air outlets 104 is 60
  • the primary air outlet 104 diameter is 48mm
  • the number of feed openings 101 is 4
  • the blast air oxygen-rich concentration is 80% -85%
  • the melt temperature is 1220 °C -1280 °C
  • the melt pool depth is 2500mm
  • the furnace height from the furnace bottom to the furnace top is 7500mm
  • the gas layer structure in the furnace body 100 is 5600mm in the width direction. .
  • the melting strength is 72t / m 2 .d
  • the furnace area of the slag layer 113 in the melting zone is 76m 2
  • the size of the slag layer 113 in the melting zone along the length direction L is 19m.
  • the slag layer The furnace body width of 113 is 4.0m, the pressure of the primary air outlet 104 is 0.18MPa-0.30MPa, the spacing of the primary air outlet 104 is 600mm, the number of primary air outlets 104 is 62, the diameter of the primary air outlet 104 is 50mm, and the number of feeding openings There are five blast air oxygen-rich concentrations of 80% to 85%, melt temperature of 1220 ° C to 1280 ° C, melt pool depth of 2500mm, furnace height from the bottom to the top of the furnace, 7800mm, and the gas layer structure in the furnace body 100 along the width direction W The dimensions are 6400mm.
  • the melting strength is 67t / m 2 .d
  • the furnace area of the slag layer 113 in the melting zone is 90m 2
  • the size of the slag layer 113 in the melting zone along the length direction L is 20m.
  • the furnace body width of 113 is 4.5m
  • the pressure of the primary air outlet 104 is 0.18MPa-0.30MPa
  • the spacing of the primary air outlet 104 is 600mm
  • the number of primary air outlets 104 is 66
  • the diameter of the primary air outlet 104 is 54mm
  • the number of the feeding openings 101 There are six blast air oxygen-rich concentrations of 80% to 85%, melt temperature of 1220 ° C to 1280 ° C, melt pool depth of 2500mm, furnace height from furnace bottom to furnace top of 8000mm, and the gas layer structure in the furnace body 100 along the width direction W
  • the dimensions are 7000mm.
  • the side-blow furnace of the present disclosure adopts a wide furnace body and a blast furnace structure, which can reduce the length of the furnace body, reduce the number of furnace body feeding openings, expand the vertical sectional area of the furnace, reduce the flue gas flow rate, reduce the dust rate, and the smoke outlet.
  • the size is more reasonable.
  • the amount of copper concentrate processed by a single side blowing furnace of the present disclosure is equal to the processing amount of two side blowing furnaces in the related art.
  • the single side-blowing furnace occupies less floor space, less corresponding equipment, saves investment, saves manpower, and improves labor productivity. In comparison, economic benefits will be better.
  • one large side-blown smelting furnace system is used than the two small side-blown smelting furnace systems.

Abstract

A copper smelting device, comprising a furnace body (100), a feeding port (101), a smoke outlet (106), a slag outlet (102), a copper matte port (103), and a primary air vent (104). A copper matte layer (112), a slag layer (113), and a gas layer (114) are sequentially arranged in the furnace body (100) from bottom to top. The feeding port (101) is arranged on a top wall of the furnace body (100). The smoke outlet (106) is arranged on the top wall of the furnace body (100). The slag outlet (102) is arranged at one end of the furnace body (100). The copper matte port (103) is arranged at an end of the furnace body (100) opposite to the slag outlet (102), and the copper matte port (103) is located at the bottom of the copper matte layer (112). The primary air vent (104) is located on a side wall of the furnace body corresponding to the slag layer (113), and is used to blow oxygen-enriched air into the slag layer (113). The dimensions in the width-wise direction of the inner wall corresponding to the slag layer (113) are greater than 2.5 m and less than or equal to 4.5 m so as to expand the scale of single furnace processing of concentrates, thereby improving labor efficiency and reducing operating costs.

Description

铜熔炼装置Copper melting plant
交叉引用cross reference
本公开要求于2018年9月21日提交的申请号为201811109807.3、名称为“铜熔炼装置”的中国专利申请的优先权,该中国专利申请的全部内容通过引用全部并入本文。This disclosure claims priority from a Chinese patent application filed on September 21, 2018 with an application number of 201811109807.3, entitled "Copper Smelting Device", the entire contents of which are incorporated herein by reference.
技术领域Technical field
本公开涉及一种有色冶金领域,具体而言,涉及一种铜熔炼装置。The present disclosure relates to the field of non-ferrous metallurgy, and in particular, to a copper smelting device.
背景技术Background technique
目前,已投入运行的固定式侧吹熔炼炉只有铜10万t/a规模级,目前设计的最大侧吹炉也只有20万t/a铜,还未投入运行,如果年产30~50万t/a铜规模,即年处理铜精矿150~200万t/a,通常至少需要两条侧吹炼铜生产线,占地面积大,设备多,投资大,操作人员多,运营成本高。由于目前已投入运行的固定式侧吹炉规格小,精矿处理能力小,不能满足单台侧吹炉即单系列处理大规模精矿能力的需要,一定程度上限制了侧吹炼铜技术的发展和推广。At present, the fixed side-blown melting furnace that has been put into operation is only 100,000 t / a copper, and the largest side-blown furnace currently designed is only 200,000 t / a copper, which has not yet been put into operation. If the annual output is 300,000 to 500,000 The t / a copper scale, that is, the annual processing of copper concentrates of 1.5 to 2 million t / a, usually requires at least two side-blown copper production lines, covering a large area, large equipment, large investment, large number of operators, and high operating costs. Due to the small specifications of the fixed side-blown furnaces that have been put into operation at present and the small concentrate processing capacity, they cannot meet the needs of a single side-blown furnace, that is, a single series of large-scale concentrate processing capacity, which has limited the side-blown copper technology to a certain extent. Development and promotion.
在所述背景技术部分公开的上述信息仅用于加强对本公开的背景的理解,因此它可以包括不构成对本领域普通技术人员已知的相关技术的信息。The above information disclosed in the background section is only used to enhance the understanding of the background of the present disclosure, so it may include information that does not constitute related technology known to those of ordinary skill in the art.
公开内容Public content
本公开的一个主要目的在于克服上述相关技术的至少一种缺陷,提供一种铜熔炼装置,以满足大规模处理精矿的需求。One of the main objectives of the present disclosure is to overcome at least one of the drawbacks of the related art and provide a copper smelting device to meet the needs of large-scale processing of concentrates.
为实现上述公开目的,本公开采用如下技术方案:In order to achieve the above disclosure purpose, the present disclosure adopts the following technical solutions:
根据本公开的一个方面,提供一种铜熔炼装置,包括炉体、加料口、出烟口、出渣口、铜锍口以及一次风口,炉体内自下而上依次设置有铜锍层、渣层以及气体层;加料口设置于所述炉体的顶壁上;出烟口设置于所述炉体的顶壁上;出渣口设置于所述炉体的一端;铜锍口设置于所述炉体的与所述出渣口相对的一端,所述铜锍口位于所述铜锍层的底部;一次风口位于所述炉体的所述渣层对应的侧壁上,用于向所述渣层鼓入富氧空气,所述渣层对应的内侧壁的宽度方向的尺寸为大于2.5m且小于或者等于4.5m。According to an aspect of the present disclosure, a copper smelting device is provided, which includes a furnace body, a charging port, a smoke outlet, a slag outlet, a copper grate, and a primary air vent. A copper grate layer and slag are sequentially arranged from bottom to top in the furnace. Layer and gas layer; a feeding port is provided on the top wall of the furnace body; a smoke outlet is provided on the top wall of the furnace body; a slag outlet is provided on one end of the furnace body; The end of the furnace body opposite to the slag outlet, the copper grate opening is located at the bottom of the copper grate layer; the primary air outlet is located on the corresponding side wall of the slag layer of the furnace body, and is used for The slag layer is blown with oxygen-enriched air, and the widthwise dimension of the inner side wall corresponding to the slag layer is greater than 2.5m and less than or equal to 4.5m.
根据本公开的一具体实施方式,其中所述炉体内腔高度方向的尺寸为6m至8m。According to a specific embodiment of the present disclosure, the dimension in the height direction of the inner cavity of the furnace body is 6m to 8m.
根据本公开的一具体实施方式,其中所述气体层的宽度方向的尺寸为4.1m-7m。According to a specific embodiment of the present disclosure, a widthwise dimension of the gas layer is 4.1m-7m.
根据本公开的一具体实施方式,其中所述一次风口的鼓风压力为0.12MPa至0.3MPa。According to a specific embodiment of the present disclosure, a blowing pressure of the primary tuyere is 0.12 MPa to 0.3 MPa.
根据本公开的一具体实施方式,其中所述铜熔炼装置还包括二次风口,设置于所述气体层对应的侧壁上。According to a specific embodiment of the present disclosure, the copper smelting device further includes a secondary air outlet disposed on a side wall corresponding to the gas layer.
根据本公开的一具体实施方式,其中所述一次风口的数量为多个,相邻的所述一次风口的间距为500-600mm。According to a specific embodiment of the present disclosure, the number of the primary air vents is plural, and the distance between adjacent primary air vents is 500-600 mm.
根据本公开的一具体实施方式,其中所述铜熔炼装置的内腔沿宽度方向设置有隔墙,所述隔墙将所述内腔分隔为熔炼区和沉降区,所述隔墙与所述炉体的顶壁之间具有间隔。According to a specific embodiment of the present disclosure, a partition wall is provided in an inner cavity of the copper smelting device along a width direction, and the partition wall divides the inner cavity into a melting zone and a settlement zone, and the partition wall and the There is a space between the top walls of the furnace body.
根据本公开的一具体实施方式,其中所述熔炼区的长度为12m-20m。According to a specific embodiment of the present disclosure, the length of the melting zone is 12m-20m.
根据本公开的一具体实施方式,其中所述沉降区设置有用于对所述沉降区进行保温或者加热的加热电极和/或燃烧器。According to a specific embodiment of the present disclosure, the settling area is provided with a heating electrode and / or a burner for holding or heating the settling area.
由上述技术方案可知,本公开的铜熔炼装置的优点和积极效果在于:铜熔炼装置的渣层对应的内侧壁的宽度方向的尺寸为大于2.5m且小于或者等于4.5m,能够扩大单炉处理精矿的规模,从而提高劳动效率,降低运营成本。It can be known from the above technical solution that the advantages and positive effects of the copper smelting device of the present disclosure are that the width dimension of the inner side wall corresponding to the slag layer of the copper smelting device is greater than 2.5 m and less than or equal to 4.5 m, which can expand single furnace processing Concentrate scale, which improves labor efficiency and reduces operating costs.
本公开中通过以下参照附图对优选实施例的说明,本公开的上述以及其它目的、特征和优点将更加明显。The above and other objects, features, and advantages of the present disclosure will be more apparent through the following description of the preferred embodiments with reference to the accompanying drawings.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
通过结合附图考虑以下对本公开的优选实施例的详细说明,本公开的各种目标、特征和优点将变得更加显而易见。附图仅为本公开的示范性图解,并非一定是按比例绘制。在附图中,同样的附图标记始终表示相同或类似的部件。其中:Various objectives, features, and advantages of the present disclosure will become more apparent by considering the following detailed description of the preferred embodiments of the present disclosure in conjunction with the accompanying drawings. The drawings are merely exemplary illustrations of the disclosure, and are not necessarily drawn to scale. In the drawings, the same reference numerals always refer to the same or similar parts. among them:
图1是根据一示例性实施方式示出的一种铜熔炼装置俯视图。Fig. 1 is a plan view of a copper smelting device according to an exemplary embodiment.
图2是图1中的铜熔炼装置的A-A剖视图。Fig. 2 is a cross-sectional view taken along the line A-A of the copper smelting apparatus in Fig. 1.
图3是图1中的铜熔炼装置的B-B剖视图。Fig. 3 is a B-B sectional view of the copper smelting apparatus in Fig. 1.
其中,附图标记说明如下:Among them, the reference signs are described as follows:
100、炉体;         101、加料口;100. Furnace body 101. Feeding port;
102、出渣口;       103、铜锍口;102. Slag outlet; 103. Copper outlet;
104、一次风口;     105、二次风口;104. Primary air outlet 105; Secondary air outlet;
106、出烟口;       107、隔墙;106. Smoke outlet; 107. Partition wall;
108、石墨电极;     109、燃烧器口;108. Graphite electrode 109: Burner port;
110、熔炼区;       111、沉降区;110. Smelting area 111. Settlement area
112、铜锍层;       113、渣层;112. Copper slag layer; 113 slag layer;
114、气体层;       115、铜水套;114. Gas layer; 115. Copper water jacket;
L、长度方向;       W、宽度方向;L, length direction W, width direction;
H、高度方向。H. Height direction.
具体实施方式detailed description
现在将参考附图更全面地描述示例实施方式。然而,示例实施方式能够以多种形式实施,且不应被理解为限于在此阐述的实施方式;相反,提供这些实施方式使得本公开将全面和完整,并将示例实施方式的构思全面地传达给本领域的技术人员。图中相同的附图标记表示相同或类似的结构,因而将省略它们的详细描述。Example embodiments will now be described more fully with reference to the accompanying drawings. However, the example embodiments can be implemented in various forms and should not be construed as limited to the embodiments set forth herein; rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the concept of the example embodiments To those skilled in the art. The same reference numerals in the drawings denote the same or similar structures, and thus their detailed descriptions will be omitted.
参照图1至图3,根据本公开的一个方面,提供一种铜熔炼装置,包括炉体100、加料口101、出烟口106、出渣口102、铜锍口103以及一次风口104。炉体100内自下而上依次设置有铜锍层112、渣层113以及气体层114,其中铜锍层112位于炉体100的内腔的底部,在该铜锍层112对应的侧壁上可以设置有铜锍口103,该铜锍口103可以位于该铜锍层112的底部。根据本公开的一具体实施方式,其中铜锍口103可以设置于炉体100一端的端部。根据本公开的一具体实施方式,其中加料口101可以设置于炉体100的顶壁上,该加料口101可以为多个,分布在顶壁上,例如但不限于,该加料口101可以为3-6个。1 to 3, according to an aspect of the present disclosure, a copper smelting device is provided, which includes a furnace body 100, a charging port 101, a smoke outlet 106, a slag outlet 102, a copper grate 103, and a primary air outlet 104. In the furnace body 100, a copper rhenium layer 112, a slag layer 113, and a gas layer 114 are sequentially arranged from bottom to top. The copper rhenium layer 112 is located at the bottom of the inner cavity of the furnace body 100, and on the corresponding side wall of the copper rhenium layer 112. A copper gate 103 may be provided, and the copper gate 103 may be located at the bottom of the copper gate layer 112. According to a specific embodiment of the present disclosure, the copper gate 103 may be disposed at an end of one end of the furnace body 100. According to a specific embodiment of the present disclosure, the feeding port 101 may be disposed on the top wall of the furnace body 100, and there may be multiple feeding ports 101 distributed on the top wall. For example, but not limited to, the feeding port 101 may be 3-6.
继续参照图1至图3,根据本公开的一具体实施方式,其中出渣口102可以设置于炉体100的与铜锍口103相对一端。根据本公开的一具体实施方式,其中一次风口104位于炉体100的渣层113对应的侧壁上,可以用于向渣层113鼓入富氧空气,渣层113对应的内侧壁的沿宽度方向W的尺寸为大于2.5m且小于或者等于4.5m。根据本公开的一具体实施方式,其中富氧空气的浓度为70%~95%,但不以此为限,可以根据实际需要选择。根据本公开的一具体实施方式,其中一次风口104的鼓风压力为0.12MPa至0.3MPa,该压力可以提高炉体100沿宽度方向W的中部熔体的搅拌强度,提高富氧空气的鼓风压力,可以克服熔体的阻力,提高了鼓风的穿透深度。根据本公开的一具体实施方式,其中一次风口104可以为多个,相邻的一次风口104的间距可以为500mm-600mm,例如但不限于可以为550mm,或者为600mm。根据本公开的一具体实施方式,其中该一次风口104的风口直径可以为38mm-54mm,例如但不限于可以为45mm或者为50mm,或者52mm。 根据本公开的一具体实施方式,其中该一次风口104的数量可以为48-80个,例如但不限于可以为50个,55个,60个,65个,70个,75个,可以根据实际需要进行选择。本公开提供的铜熔炼装置,可以为侧吹炉,能够实现单炉体处理精矿100-200万t/a,产铜规模达到20-50万t/a。With continued reference to FIGS. 1 to 3, according to a specific embodiment of the present disclosure, the slag outlet 102 may be disposed at an end of the furnace body 100 opposite to the copper grate 103. According to a specific embodiment of the present disclosure, the primary air outlet 104 is located on a side wall corresponding to the slag layer 113 of the furnace body 100, and can be used to blow oxygen-rich air into the slag layer 113. The width of the inner side wall corresponding to the slag layer 113 The dimension of the direction W is greater than 2.5 m and less than or equal to 4.5 m. According to a specific embodiment of the present disclosure, the concentration of the oxygen-enriched air is 70% to 95%, but is not limited thereto, and may be selected according to actual needs. According to a specific embodiment of the present disclosure, the blowing pressure of the primary tuyere 104 is 0.12 MPa to 0.3 MPa, and the pressure can increase the stirring intensity of the middle melt of the furnace body 100 in the width direction W and increase the blast of oxygen-enriched air. Pressure can overcome the resistance of the melt and increase the penetration depth of the blast. According to a specific embodiment of the present disclosure, there may be multiple primary air outlets 104, and the interval between adjacent primary air outlets 104 may be 500mm-600mm, such as but not limited to 550mm or 600mm. According to a specific embodiment of the present disclosure, a diameter of the air outlet of the primary air outlet 104 may be 38 mm-54 mm, such as but not limited to 45 mm or 50 mm, or 52 mm. According to a specific embodiment of the present disclosure, the number of the primary air outlets 104 may be 48-80, such as but not limited to 50, 55, 60, 65, 70, 75, and may be based on actual conditions. Need to choose. The copper smelting device provided by the present disclosure can be a side-blown furnace, capable of processing 1 to 2 million t / a of concentrate in a single furnace body, and a copper production scale of 200,000 to 500,000 t / a.
在未做相反说明的情况下,长度方向L为图1中的双箭头限定的方向,高度方向H为图2中的双箭头的方向,本公开限定的宽度方向W为图3中双箭头限定的方向。可以理解的是,在图示中的图片旋转的情况下,限定的宽度方向W和高度方向H也旋转相应的角度。Unless otherwise stated, the length direction L is the direction defined by the double arrow in FIG. 1, the height direction H is the direction of the double arrow in FIG. 2, and the width direction W defined in the present disclosure is the direction of the double arrow in FIG. 3. Direction. It can be understood that when the picture in the illustration is rotated, the defined width direction W and height direction H are also rotated by corresponding angles.
继续参照图1至图3,炉体100在宽度方向W上的投影可以为上部气体层结构宽度大于下部渣层结构宽度。根据本公开的一具体实施方式,其中气体层114的宽度方向W的尺寸可以为4.1m-7m。炉体100的外壳可以为钢结构,内衬可以由耐火材料构成。炉体100顶部可以设有加料口101和出烟口106。加料口101可以设置在炉体100中心线上,但不以此为限,根据实际需要也可以靠近两侧壁布置。根据本公开的一具体实施方式,其中炉体100的侧壁上可以设置一次风口104和二次风口105,其中一次风口104在炉体100双侧部,该一次风口104可以设置在渣层113,二次风口105可以设置在炉体100的顶壁和侧壁,该二次风口105可以对应于气体层114。With continued reference to FIGS. 1 to 3, the projection of the furnace body 100 in the width direction W may be that the upper gas layer structure width is greater than the lower slag layer structure width. According to a specific embodiment of the present disclosure, the dimension of the width direction W of the gas layer 114 may be 4.1m-7m. The outer shell of the furnace body 100 may be a steel structure, and the inner lining may be formed of a refractory material. The top of the furnace body 100 may be provided with a feeding opening 101 and a smoke outlet 106. The feeding opening 101 can be set on the center line of the furnace body 100, but is not limited thereto, and can also be arranged near the two side walls according to actual needs. According to a specific embodiment of the present disclosure, a primary air outlet 104 and a secondary air outlet 105 may be provided on a side wall of the furnace body 100, wherein the primary air outlet 104 is on both sides of the furnace body 100, and the primary air outlet 104 may be provided on a slag layer 113. The secondary air outlet 105 may be disposed on the top wall and the side wall of the furnace body 100, and the secondary air outlet 105 may correspond to the gas layer 114.
根据本公开的一具体实施方式,其中在炉体100侧壁、隔墙107和沉降区111的端墙可以设有冷却元件,例如但不限于,侧壁上可以设置有铜水套115,该铜水套115内可以设置有冷却介质,例如但不限于,冷却介质可以为水。在炉体100一端可以设置铜锍口103,在炉体100另一端可以设置出渣口102和燃烧器口109,其中燃烧器口109可以设置于出渣口102的上方。According to a specific embodiment of the present disclosure, a cooling element may be provided on the side wall of the furnace body 100, the partition wall 107, and the end wall of the settlement area 111. For example, but not limited to, a copper water jacket 115 may be provided on the side wall. The copper water jacket 115 may be provided with a cooling medium therein, such as but not limited to, the cooling medium may be water. A copper nozzle 103 may be provided at one end of the furnace body 100, and a slag outlet 102 and a burner port 109 may be provided at the other end of the furnace body 100. The burner port 109 may be disposed above the slag outlet 102.
根据本公开的一具体实施方式,其中炉体100内腔高度方向H的尺寸可以为6m至8m。根据本公开的一具体实施方式,其中熔炼区的长度可以为12m-20m。根据本公开的一具体实施方式,其中铜熔炼装置还包括二次风口105,设置于气体层114对应的侧壁上。根据本公开的一具体实施方式,其中铜熔炼装置还包括设置于炉体100顶壁上的出烟口106。According to a specific embodiment of the present disclosure, the dimension H of the inner cavity height of the furnace body 100 may be 6 m to 8 m. According to a specific embodiment of the present disclosure, the length of the melting zone may be 12m-20m. According to a specific embodiment of the present disclosure, the copper smelting device further includes a secondary air outlet 105 disposed on a side wall corresponding to the gas layer 114. According to a specific embodiment of the present disclosure, the copper smelting device further includes a smoke outlet 106 provided on the top wall of the furnace body 100.
根据本公开的一具体实施方式,其中铜熔炼装置的内腔沿宽度方向W可以设置有隔墙107,隔墙107将内腔分隔为熔炼区110和沉降区111,隔墙107与炉体100的顶壁之间具有间隔。该熔炼区110和沉降区111水平排列,随着不断加料熔炼,经熔炼后产生的熔炼渣直接可以自流入沉降区111中,在沉降区111完成铜锍和渣的分离。According to a specific embodiment of the present disclosure, the internal cavity of the copper smelting device may be provided with a partition wall 107 along the width direction W. The partition wall 107 divides the internal cavity into a melting area 110 and a settlement area 111, and the partition wall 107 and the furnace body 100. There are spaces between the top walls. The smelting zone 110 and the settling zone 111 are arranged horizontally. With continuous feeding and smelting, the smelting slag generated after smelting can directly flow into the settling zone 111, and the copper slag and slag are separated in the settling zone 111.
根据本公开的一具体实施方式,其中沉降区111设置有用于对沉降区111进行保温或 者加热的加热电极,根据本公开的一具体实施方式,其中加热电极可以为石墨电极108,但不以此为限,可以根据需要进行选择。根据本公开的一具体实施方式,其中沉降区111还可以设置有燃烧器,该燃烧器可以设置于燃烧器口109中。According to a specific embodiment of the present disclosure, the sedimentation region 111 is provided with a heating electrode for keeping or heating the sedimentation region 111. According to a specific embodiment of the present disclosure, the heating electrode may be a graphite electrode 108, but not the same. For the limit, you can choose according to your needs. According to a specific embodiment of the present disclosure, the settling area 111 may further be provided with a burner, and the burner may be provided in the burner port 109.
铜精矿与熔剂、煤及其他返料配好料后可以通过皮带输送到炉体100的炉顶,通过加料口101加入到炉体100内,一次风口104鼓入70%~95%的富氧空气,一次风口104的鼓风压力0.12MPa~0.3MPa,物料在熔池内进行氧化脱硫、熔化、造渣等化学反应,产生的铜锍从铜锍口103虹吸或打眼排出,残渣在沉降区111与铜锍沉降分离后从出渣口102排出。二次风口105鼓入空气,用于燃烧烟气中的单体硫及一氧化碳,烟气由上部的出烟口106排出,进入上升烟道、余热锅炉经降温除尘后送制酸。炉体100内的熔炼温度可以为1200℃~1300℃,熔池深度可以为2000mm~2800mm,铜锍品位55%~78%,渣含Cu0.6%~2.5%,熔炼区床能率为精矿量60~90t/m2.d,氧料比与铜锍品位有关,渣含Cu与铜锍品位也有关联。After the copper concentrate is mixed with the flux, coal and other returned materials, it can be conveyed to the furnace top of the furnace body 100 through a belt, added to the furnace body 100 through the charging port 101, and 70% to 95% of the rich air is blown through the primary air port 104. Oxygen air, primary air outlet 104 blowing pressure of 0.12MPa ~ 0.3MPa, the material undergoes chemical reactions such as oxidative desulfurization, melting and slagging in the molten pool. 111 is discharged from the slag outlet 102 after being separated from the copper matte. Air is blown into the secondary tuyere 105 for burning the monomer sulfur and carbon monoxide in the flue gas. The flue gas is discharged from the upper gas outlet 106, enters the ascending flue, and the waste heat boiler is sent to the acid production after cooling and dust removal. The melting temperature in the furnace body 100 can be 1200 ° C to 1300 ° C, the depth of the molten pool can be 2000mm to 2800mm, the grade of copper grate is 55% to 78%, the slag contains Cu 0.6% to 2.5%, and the bed energy rate in the melting zone is concentrate The amount is 60 ~ 90t / m2.d. The oxygen-material ratio is related to the copper 锍 grade, and the slag containing Cu is also related to the copper 锍 grade.
具体可根据不同规模的精矿处理量,如100-200万t/a精矿量,和一定的熔炼区床能率,一般为精矿量60-90t/m2.d,估算出熔炼区炉膛的面积,根据设定炉体的熔炼区渣层113长度,一般小于20m,推算出熔炼区渣层113宽度,熔炼区渣层113宽度为2.5m-4.5m,再根据熔炼区渣层113的宽度,确定渣层风口鼓风压力,鼓风压力0.12MPa-0.3MPa,鼓风量的增加可以通过增加风口数,增加风口直径和提高富氧空气压力来实现。Specifically, according to the concentrate processing capacity of different scales, such as 1 to 2 million t / a concentrate, and a certain smelting zone bed energy rate, generally 60 to 90 t / m2.d of concentrate, the furnace hearth of the smelting zone can be estimated. The area is based on the length of the slag layer 113 in the melting zone of the furnace. Generally, the width of the slag layer 113 in the melting zone is calculated. The width of the slag layer 113 in the melting zone is 2.5m-4.5m. , Determine the slag layer tuyere blower pressure, blower pressure 0.12MPa-0.3MPa, the increase of blower volume can be achieved by increasing the number of tuyeres, increasing the diameter of the tuyere and increasing the pressure of oxygen-enriched air.
具体实施方式一:Specific Embodiment One:
年处理100万吨(万t)铜精矿时,熔炼强度按精矿量80t/m 2.d,熔炼区渣层113的炉体面积为38m 2,熔炼区渣层113沿长度方向L的尺寸为15m,渣层113的炉体内宽度为2.5m,一次风口104压力为0.12MPa-0.15MPa,一次风口104间距为600mm,一次风口104数量为48个,一次风口104直径为40mm,加料口101的数量为3个,鼓风富氧浓度85%,熔体温度1220℃~1280℃,熔池深度2500mm,炉底到炉顶的炉膛高度为7000mm,炉体100内气体层结构沿宽度方向W的尺寸为4100mm。 When processing 1 million tons (10,000 tons) of copper concentrate annually, the melting strength is 80t / m 2 .d. The furnace area of the slag layer 113 in the melting zone is 38m 2 . The size is 15m, the width of the furnace body of the slag layer 113 is 2.5m, the primary air outlet 104 pressure is 0.12MPa-0.15MPa, the primary air outlet 104 spacing is 600mm, the primary air outlet 104 number is 48, the primary air outlet 104 diameter is 40mm, and the feeding opening The number of 101 is 3, the blast oxygen concentration is 85%, the melt temperature is 1220 ℃ ~ 1280 ℃, the depth of the molten pool is 2500mm, the height of the furnace bottom to the furnace top is 7000mm, and the gas layer structure in the furnace body 100 is along the width direction The size of W is 4100mm.
具体实施方式二:Specific implementation mode two:
年处理120万吨(万t)铜精矿时,熔炼强度按75t/m 2.d,熔炼区渣层113炉体面积为48m 2,熔炼区渣层113的沿长度方向L的尺寸为16m,渣层113的炉体内宽度为3.0m,一次风口104压力为0.15MPa-0.20MPa,一次风口104间距为600mm,一次风口104的 数量为52个,一次风口104的直径为45mm,加料口101的数量为3个,鼓风富氧浓度为85%,熔体温度1220℃-1280℃,熔池深度2500mm,炉底到炉顶的炉膛高度7200mm,炉体100内气体层结构沿宽度方向W的尺寸为4800mm。 When processing 1.2 million tons (10,000 tons) of copper concentrate annually, the smelting strength is 75t / m 2 .d, the furnace area of the slag layer 113 in the melting zone is 48m 2 , and the size of the slag layer 113 in the melting zone is 16m along the length direction L. The width of the furnace body of the slag layer 113 is 3.0m, the pressure of the primary air outlet 104 is 0.15MPa-0.20MPa, the spacing of the primary air outlet 104 is 600mm, the number of the primary air outlet 104 is 52, the diameter of the primary air outlet 104 is 45mm, and the feeding opening 101 The number is 3, the blast oxygen-rich concentration is 85%, the melt temperature is 1220 ℃ -1280 ℃, the melt pool depth is 2500mm, the furnace height from the furnace bottom to the furnace top is 7200mm, and the gas layer structure in the furnace body 100 is along the width direction W The dimensions are 4800mm.
具体实施方式三:Specific implementation mode three:
年处理150万t铜精矿时,熔炼强度按72t/m 2.d,熔炼区渣层113的炉体面积为63m 2,熔炼区渣层113的沿长度方向L的尺寸为18m,渣层113的炉体内宽度为3.5m,一次风口104压力为0.15MPa-0.25MPa,一次风口104间距为600mm,一次风口104数量为60个,一次风口104直径为48mm,加料口101的数量为4个,鼓风富氧浓度80%-85%,熔体温度1220℃-1280℃,熔池深度2500mm,炉底到炉顶的炉膛高度7500mm,炉体100内气体层结构沿宽度方向W尺寸为5600mm。 Time for 150 million t copper concentrate smelting strength press 72t / m 2 .d, the smelting furnace area of the slag layer 113 is 63m 2, L dimension along the longitudinal direction of the melting of the slag layer 113 is 18m, the slag layer The furnace body width of 113 is 3.5m, the primary air outlet 104 pressure is 0.15MPa-0.25MPa, the primary air outlet 104 spacing is 600mm, the number of primary air outlets 104 is 60, the primary air outlet 104 diameter is 48mm, and the number of feed openings 101 is 4 The blast air oxygen-rich concentration is 80% -85%, the melt temperature is 1220 ℃ -1280 ℃, the melt pool depth is 2500mm, the furnace height from the furnace bottom to the furnace top is 7500mm, and the gas layer structure in the furnace body 100 is 5600mm in the width direction. .
具体实施方式四:Specific implementation four:
年处理180万t铜精矿时,熔炼强度按72t/m 2.d,熔炼区渣层113的炉体面积为76m 2,熔炼区渣层113的沿长度方向L的尺寸为19m,渣层113的炉体内宽度为4.0m,一次风口104的压力为0.18MPa-0.30MPa,一次风口104的间距为600mm,一次风口104的数量为62个,一次风口104的直径为50mm,加料口的数量为5个,鼓风富氧浓度80%-85%,熔体温度1220℃-1280℃,熔池深度2500mm,炉底到炉顶的炉膛高度7800mm,炉体100内气体层结构沿宽度方向W的尺寸为6400mm。 When processing 1.8 million tons of copper concentrate annually, the melting strength is 72t / m 2 .d, the furnace area of the slag layer 113 in the melting zone is 76m 2 , and the size of the slag layer 113 in the melting zone along the length direction L is 19m. The slag layer The furnace body width of 113 is 4.0m, the pressure of the primary air outlet 104 is 0.18MPa-0.30MPa, the spacing of the primary air outlet 104 is 600mm, the number of primary air outlets 104 is 62, the diameter of the primary air outlet 104 is 50mm, and the number of feeding openings There are five blast air oxygen-rich concentrations of 80% to 85%, melt temperature of 1220 ° C to 1280 ° C, melt pool depth of 2500mm, furnace height from the bottom to the top of the furnace, 7800mm, and the gas layer structure in the furnace body 100 along the width direction W The dimensions are 6400mm.
具体实施方式五:Specific implementation five:
年处理200万t铜精矿时,熔炼强度按67t/m 2.d,熔炼区渣层113的炉体面积为90m 2,熔炼区渣层113的沿长度方向L的尺寸为20m,渣层113的炉体内宽度为4.5m,一次风口104压力为0.18MPa-0.30MPa,一次风口104的间距为600mm,一次风口104的数量为66个,一次风口104的直径为54mm,加料口101的数量为6个,鼓风富氧浓度80%~85%,熔体温度1220℃~1280℃,熔池深度2500mm,炉底到炉顶的炉膛高度8000mm,炉体100内气体层结构沿宽度方向W的尺寸为7000mm。 When processing 2 million tons of copper concentrate annually, the melting strength is 67t / m 2 .d, the furnace area of the slag layer 113 in the melting zone is 90m 2 , and the size of the slag layer 113 in the melting zone along the length direction L is 20m. The furnace body width of 113 is 4.5m, the pressure of the primary air outlet 104 is 0.18MPa-0.30MPa, the spacing of the primary air outlet 104 is 600mm, the number of primary air outlets 104 is 66, the diameter of the primary air outlet 104 is 54mm, and the number of the feeding openings 101 There are six blast air oxygen-rich concentrations of 80% to 85%, melt temperature of 1220 ° C to 1280 ° C, melt pool depth of 2500mm, furnace height from furnace bottom to furnace top of 8000mm, and the gas layer structure in the furnace body 100 along the width direction W The dimensions are 7000mm.
本公开的侧吹炉采用宽炉体、高炉膛结构形式,可以减少炉体的长度,减少炉体加料口的数量,扩大炉膛立式截面积,降低烟气流速,减少烟尘率,出烟口的大小尺寸更合理。The side-blow furnace of the present disclosure adopts a wide furnace body and a blast furnace structure, which can reduce the length of the furnace body, reduce the number of furnace body feeding openings, expand the vertical sectional area of the furnace, reduce the flue gas flow rate, reduce the dust rate, and the smoke outlet. The size is more reasonable.
尽管炉体宽时,鼓风压力也提高,动能消耗增加,但用本公开的单台侧吹炉处理的铜 精矿的量等于相关技术中的两台侧吹炉的处理量,因此本公开的单台侧吹炉较现有的两台侧吹炉,占地面积少,相应的设备少,投资省,节省人力,提高劳动生产率,相比较而言,经济效益会更好。Although when the furnace body is wide, the blast pressure is also increased, and the kinetic energy consumption is increased, the amount of copper concentrate processed by a single side blowing furnace of the present disclosure is equal to the processing amount of two side blowing furnaces in the related art. Compared with the existing two side-blowing furnaces, the single side-blowing furnace occupies less floor space, less corresponding equipment, saves investment, saves manpower, and improves labor productivity. In comparison, economic benefits will be better.
处理相同规模的铜精矿,采用一台大型侧吹熔炼炉系统比两台小型侧吹熔炼炉系统,相应的冶炼系统土建及设备等投资节省约2.0亿人民币(土建3500万元、设备16500万元),每年折旧费为1515万元(3500/25+16500/12=1515万元),操作人员少120人,工资7.5万元/人.年,工资900万元,因鼓风压力提高增加的费用220万元(500度/h×8000h×0.55元/度=220万元),每年节省费用约1515+900-220=2195万元,折合每吨铜55元。For processing copper concentrates of the same scale, one large side-blown smelting furnace system is used than the two small side-blown smelting furnace systems. The corresponding investment in smelting system civil construction and equipment can save about 200 million yuan (35 million yuan for civil construction and 165 million for equipment). Yuan), the annual depreciation fee is 15.15 million yuan (3500/25 + 16500/12 = 15.15 million yuan), 120 operators are less, and the salary is 75,000 yuan / person. The annual salary is 9 million yuan, which is increased due to the increase in air pressure. The cost is 2.2 million yuan (500 degrees / h × 8000h × 0.55 yuan / degree = 2.2 million yuan), and the annual cost savings are about 1515 + 900-220 = 21.95 million yuan, equivalent to 55 yuan per ton of copper.
所描述的特征、结构或特性可以以任何合适的方式结合在一个或更多实施方式中。在上面的描述中,提供许多具体细节从而给出对本公开的实施方式的充分理解。然而,本领域技术人员将意识到,可以实践本公开的技术方案而没有所述特定细节中的一个或更多,或者可以采用其它的方法、组件、材料等。在其它情况下,不详细示出或描述公知结构、材料或者操作以避免模糊本公开的各方面。The described features, structures, or characteristics may be combined in any suitable manner in one or more embodiments. In the above description, many specific details are provided to give a full understanding of the embodiments of the present disclosure. However, those skilled in the art will realize that the technical solutions of the present disclosure may be practiced without one or more of the specific details, or other methods, components, materials, etc. may be adopted. In other instances, well-known structures, materials, or operations have not been shown or described in detail to avoid obscuring aspects of the present disclosure.

Claims (9)

  1. 一种铜熔炼装置,包括:A copper smelting device includes:
    炉体,所述炉体内自下而上依次设置有铜锍层、渣层以及气体层;A furnace body, which is provided with a copper grate layer, a slag layer, and a gas layer in order from bottom to top;
    加料口,设置于所述炉体的顶壁上;A feeding port is arranged on the top wall of the furnace body;
    出烟口,设置于所述炉体的顶壁上;The smoke outlet is arranged on the top wall of the furnace body;
    出渣口,设置于所述炉体的一端;A slag outlet is provided at one end of the furnace body;
    铜锍口,设置于所述炉体的与所述出渣口相对的一端,所述铜锍口位于所述铜锍层的底部;A copper gate is disposed at an end of the furnace body opposite to the slag outlet, and the copper gate is located at the bottom of the copper gate layer;
    一次风口,位于所述炉体的所述渣层对应的侧壁上,用于向所述渣层鼓入富氧空气,所述渣层对应的内侧壁的宽度方向的尺寸为大于2.5m且小于或者等于4.5m。The primary air vent is located on the side wall corresponding to the slag layer of the furnace body, and is used to blow oxygen-enriched air into the slag layer. The width dimension of the inner side wall corresponding to the slag layer is greater than 2.5m and Less than or equal to 4.5m.
  2. 如权利要求1所述的铜熔炼装置,其中,所述炉体内腔高度方向的尺寸为6m至8m。The copper smelting device according to claim 1, wherein the size in the height direction of the cavity inside the furnace is 6m to 8m.
  3. 如权利要求1所述的铜熔炼装置,其中,所述气体层的宽度方向的尺寸为4.1m-7m。The copper smelting device according to claim 1, wherein a widthwise dimension of the gas layer is 4.1m-7m.
  4. 如权利要求1至3中任一项所述的铜熔炼装置,其中,所述一次风口的鼓风压力为0.12MPa至0.3MPa。The copper smelting device according to any one of claims 1 to 3, wherein a blowing pressure of the primary tuyere is 0.12 MPa to 0.3 MPa.
  5. 如权利要求1所述的铜熔炼装置,其中,所述铜熔炼装置还包括二次风口,设置于所述气体层对应的侧壁上。The copper smelting device according to claim 1, wherein the copper smelting device further comprises a secondary tuyere disposed on a side wall corresponding to the gas layer.
  6. 如权利要求1所述的铜熔炼装置,其中,所述一次风口的数量为多个,相邻的所述一次风口的间距为500~600mm。The copper smelting device according to claim 1, wherein the number of the primary air vents is plural, and the distance between adjacent primary air vents is 500-600 mm.
  7. 如权利要求1所述的铜熔炼装置,其中,所述铜熔炼装置的内腔沿宽度方向设置有隔墙,所述隔墙将所述内腔分隔为熔炼区和沉降区,所述隔墙与所述炉体的顶壁之间具有间隔。The copper smelting device according to claim 1, wherein an inner cavity of the copper smelting device is provided with a partition wall in a width direction, and the partition wall divides the internal cavity into a melting area and a settlement area, and the partition wall There is a distance from the top wall of the furnace body.
  8. 如权利要求7所述的铜熔炼装置,其中,所述熔炼区的长度为12m-20m。The copper smelting device according to claim 7, wherein the length of the smelting zone is 12m-20m.
  9. 如权利要求7所述的铜熔炼装置,其中,所述沉降区设置有用于对所述沉降区进行保温或者加热的加热电极和/或燃烧器。The copper smelting device according to claim 7, wherein the settling zone is provided with a heating electrode and / or a burner for holding or heating the settling zone.
PCT/CN2019/098643 2018-09-21 2019-07-31 Copper smelting device WO2020057266A1 (en)

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