CN2738889Y - Sulfuric acid residual separating-purifying-sorting apparatus - Google Patents

Sulfuric acid residual separating-purifying-sorting apparatus Download PDF

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CN2738889Y
CN2738889Y CN 200420076632 CN200420076632U CN2738889Y CN 2738889 Y CN2738889 Y CN 2738889Y CN 200420076632 CN200420076632 CN 200420076632 CN 200420076632 U CN200420076632 U CN 200420076632U CN 2738889 Y CN2738889 Y CN 2738889Y
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sulfuric acid
spiral
spiral chute
ore
separation
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张一敏
刘惠中
陈铁军
刘涛
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Wuhan University of Science and Engineering WUSE
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Wuhan University of Science and Engineering WUSE
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Abstract

The utility model relates to a sulfuric acid residual separating-purifying-sorting apparatus. The utility model has the technical proposal that an ore separator [1] and an ore feeding groove [3] are fixedly connected and mounted on an upper bracket [2]; the upper bracket [2] is fixedly connected with a spiral groove column [4], and a spiral chute [5] is fixedly connected with the spiral groove column [4]; the upper end of the spiral chute [5] is located under the upper bracket [2], and the lower end of the spiral chute [5] is connected with an ore cutting groove [6]; the ore cutting groove [6] is connected with an ore receiving bucket [7]. The inner side of the spiral chute [5] is equipped with a transversal wash tub pipe [8] which is externally connected with high-pressure water source, and the inner side of the transversal wash tub pipe [8] is provided with a plurality of water outlet holes. The transversal wash tub pipe [8] is in pipe spiral shape. This equipment breaks through the traditional theoretic limit that the ratio of height to diameter can not less than 0.45, and adopts the ultra-limit ratio of height to diameter that h/d = 0.33-0.40; thus the sulfuric acid residual separating-purifying-sorting apparatus has the advantages of simple operation, low energy consumption, high recovery rate, low cost, stable running and without generating secondary pollution, etc. The sulfuric acid residual separating-purifying-sorting apparatus can also be widely used for resources processing of lower grade tailings, metalliferous solid slag, low-density non-metal materials, metal mine debris and chemical fine materials.

Description

一种硫酸渣分离提纯分选设备Separation, purification and sorting equipment for sulfuric acid slag

一、技术领域1. Technical field

本实用新型属于资源化处理设备。尤其涉及一种硫酸渣分离提纯的分选设备。The utility model belongs to resource processing equipment. In particular, it relates to a sorting device for separating and purifying sulfuric acid slag.

二、背景技术2. Background technology

国外对硫酸渣的利用已有近百年历史,一些工业发达国家虽未间断过对硫酸渣的研究,但到目前为止,对硫酸渣的处理技术并无重大突破。其原因主要是生产工艺复杂、过程控制困难、产品指标不稳以及利用率偏低、运行成本过高等问题所致。究其原因,设备是制约硫酸渣资源化发展的主要因素。由于长期没有针对硫酸渣分选的专门设备,通常是以不同的分选工艺,借助原有的传统设备进行分选,这些工艺和设备虽然在一定程度上能够分选硫酸渣,但并不完全适合硫酸渣的分选特点,其结果导致分选效率低下,产品质量不稳,运行成本过高和工艺过程复杂等问题出现。The use of sulfuric acid slag has a history of nearly a hundred years in foreign countries. Although some industrially developed countries have not stopped the research on sulfuric acid slag, so far, there has been no major breakthrough in the treatment technology of sulfuric acid slag. The reasons are mainly due to the complex production process, difficult process control, unstable product indicators, low utilization rate, and high operating costs. The reason is that equipment is the main factor restricting the development of sulfuric acid slag resources. Since there is no special equipment for sorting sulfuric acid slag for a long time, different sorting processes are usually used for sorting with the help of original traditional equipment. Although these processes and equipment can sort sulfuric acid slag to a certain extent, they are not completely It is suitable for the separation characteristics of sulfuric acid slag, and the result is low separation efficiency, unstable product quality, high operating cost and complicated process.

最常用于硫酸渣分选的传统螺旋溜槽(丘继存,选矿学,冶金工业出版社,1987北京),其作用是对目的矿物进行初步富集,为下步分选工艺提供粗精矿。出于对物料密度和回收粒度下限等因素的考虑,该设备距径比h/D变化一般在0.45~0.8之间,下限值不超过0.45,通常取0.5~0.6倍。这样可保证颗粒粒度较粗、目的矿物与非目的矿之间密度差较大的矿物在紊流流膜和流变力场中得到连续分选,而不致“堆溜”和“掏溜”。但当将该传统设备用于硫酸渣分选时,由于硫酸渣中的目的矿物(含铁矿物)和非目的矿物(残硫载体、硫铁矿连生体和二氧化硅等脉石矿物)之间的密度差极小(通常为0.1-0.2%之间),在这种小密度差之下,当溜槽螺距h与溜槽直径D之比为0.45~0.8这一常规距径比时,硫酸渣无法进行有效分离。此时,硫酸渣中的目的矿物和非目的矿物在螺旋流体的流变力场中相互混合一起被甩向溜槽外侧,最终成为尾矿。The most commonly used traditional spiral chute for the separation of sulfuric acid slag (Qiu Jicun, Mineral Processing, Metallurgical Industry Press, 1987 Beijing), its function is to initially enrich the target minerals and provide rough concentrate for the next step of separation process. Considering factors such as material density and the lower limit of recycled particle size, the aspect ratio h/D of the equipment generally changes between 0.45 and 0.8, and the lower limit does not exceed 0.45, usually 0.5 to 0.6 times. This can ensure that the minerals with coarse particle size and large density difference between the target minerals and non-target minerals can be continuously separated in the turbulent flow film and rheological force field without "stacking" and "slipping". But when this traditional equipment is used for the separation of sulfuric acid slag, due to the purpose minerals (iron-containing minerals) and non-purpose minerals (residual sulfur carrier, pyrite joints and gangue minerals such as silicon dioxide) in the sulfuric acid slag The density difference between them is extremely small (usually between 0.1-0.2%). Under this small density difference, when the ratio of the chute pitch h to the chute diameter D is the conventional aspect ratio of 0.45-0.8, the sulfuric acid Slag cannot be effectively separated. At this time, the target minerals and non-target minerals in the sulfuric acid slag are mixed with each other in the rheological force field of the spiral fluid and thrown to the outside of the chute, and finally become tailings.

三、发明内容本实用新型的目的是提供一种操作简单、能耗低、回收率高、成本低、运行稳定、不产生二次污染的硫酸渣分离提纯分选设备。该设备还可广泛用于其它低品位尾渣、含金属固体废渣、低密度非金属物料、金属矿山尾矿和化工微细物料的分选提纯、富集分离、综合回收等资源化处理。3. Summary of the invention The purpose of this utility model is to provide a sulfuric acid slag separation, purification and sorting equipment with simple operation, low energy consumption, high recovery rate, low cost, stable operation and no secondary pollution. The equipment can also be widely used in other low-grade tailings, metal-containing solid waste, low-density non-metallic materials, metal mine tailings and chemical fine materials for separation and purification, enrichment separation, comprehensive recovery and other resource treatment.

为实现上述目的,本实用新型所采取的技术方案是:将分矿器与给矿槽固定连接并安装在上支架上,上支架与螺旋槽支柱固定连接,螺旋溜槽与螺旋槽支柱固定连接,螺旋溜槽的上端位于上支架下、下端与截矿槽相接,截矿槽和接矿斗连接,在螺旋溜槽的内侧设置有横向冲洗水管。In order to achieve the above purpose, the technical solution adopted by the utility model is: the ore separator is fixedly connected with the ore feeding trough and installed on the upper bracket, the upper bracket is fixedly connected with the spiral groove pillar, and the spiral chute is fixedly connected with the spiral groove pillar, The upper end of the spiral chute is located under the upper support, and the lower end is connected with the ore-cutting chute, and the ore-cutting chute is connected with the ore-connecting hopper, and a horizontal flushing water pipe is arranged on the inner side of the spiral chute.

横向冲洗水管外接高压水源,内侧开有若干出水孔,其形状为管式螺旋状。螺旋溜槽为1~4头。螺旋溜槽的螺旋片高h与外径D之比为:h/D=0.33~0.40。螺旋溜槽是由玻璃纤维增强塑料或玻璃钢制成,内衬为刚玉型耐磨材料。The horizontal flushing water pipe is externally connected to a high-pressure water source, and there are a number of water outlet holes inside, which are in the shape of a tubular spiral. There are 1 to 4 spiral chutes. The ratio of the spiral height h of the spiral chute to the outer diameter D is: h/D=0.33~0.40. The spiral chute is made of glass fiber reinforced plastic or fiberglass, and the lining is corundum type wear-resistant material.

由于采用上述技术方案,本实用新型突破了距径比不能小于0.45的传统理论极限,采用了h/D=0.33~0.40的超极限距径比设计,使之具有操作简单、能耗低、回收率高等显著特点;在增大螺旋槽直径后仍可对微细粒矿物进行有效回收;提高了小密度差硫酸渣的分选效率。增加了横向冲洗水的设计,不产生二次污染,提高了单机富集比。Due to the adoption of the above technical scheme, the utility model breaks through the traditional theoretical limit that the aspect ratio cannot be less than 0.45, and adopts an ultra-limit aspect ratio design of h/D=0.33~0.40, which makes it easy to operate, low in energy consumption, and recyclable. Notable features such as high efficiency; after increasing the diameter of the spiral groove, it can still effectively recover fine-grained minerals; it improves the separation efficiency of sulfuric acid slag with small density difference. The design of horizontal flushing water is added, no secondary pollution occurs, and the enrichment ratio of a single machine is improved.

本实用新型不仅适合于硫酸渣的处理,还可广泛用于其它低品位尾渣、含金属固体废渣、低密度非金属物料、金属矿山尾矿和化工微细物料的资源化处理。The utility model is not only suitable for the treatment of sulfuric acid slag, but also can be widely used in resource treatment of other low-grade tailings, metal-containing solid waste, low-density non-metallic materials, metal mine tailings and chemical fine materials.

四、附图说明4. Description of drawings

图1是本实用新型的一种结构示意图;Fig. 1 is a kind of structural representation of the utility model;

图2是本实用新型的冲洗水管设置示意图。Fig. 2 is a schematic diagram of the arrangement of the flushing water pipe of the present invention.

五、具体实施方式5. Specific implementation

本实施方式的结构如图1所示,将分矿器[1]与给矿槽[3]固定连接并安装在上支架[2]上,上支架[2]与螺旋槽支柱[4]固定连接,螺旋溜槽[5]与螺旋槽支柱[4]固定连接,螺旋溜槽[5]的上端位于上支架[2]下、下端与截矿槽[6]相接,截矿槽[6]和接矿斗[7]连接,在螺旋溜槽[5]的内侧设置有横向冲洗水管[8],横向冲洗水管[8]外接高压水源,在横向冲洗水管[8]的内侧开有若干出水孔,横向冲洗水管[8]形状为管式螺旋状。The structure of this embodiment is shown in Figure 1, the ore separator [1] is fixedly connected with the ore feeder [3] and installed on the upper bracket [2], and the upper bracket [2] is fixed with the spiral groove pillar [4] Connection, the spiral chute [5] is fixedly connected with the spiral chute pillar [4], the upper end of the spiral chute [5] is positioned at the bottom of the upper bracket [2], and the lower end is connected with the cutting groove [6], the cutting groove [6] and The ore hopper [7] is connected, and a horizontal flushing water pipe [8] is arranged on the inner side of the spiral chute [5]. The horizontal flushing water pipe [8] is shaped as a tubular spiral.

本实施例采用的螺旋溜槽[5]为3头,断面曲线采用复合立方抛物线断面曲线,上部断面曲线的横向下斜角大于下部。螺旋片高h与外径D之比为:h/D=0.35。螺旋溜槽[5]由玻璃纤维增强塑料或玻璃钢制成,内衬为刚玉型耐磨材料。The spiral chute [5] that the present embodiment adopts is 3, and section curve adopts composite cubic parabolic section curve, and the lateral downslope angle of top section curve is greater than bottom. The ratio of the height h of the helix to the outer diameter D is: h/D=0.35. The spiral chute [5] is made of fiberglass reinforced plastics or FRP, and the lining is a corundum type wear-resistant material.

本实施例突破了距径比不能小于0.45的传统理论极限,采用了h/D=0.35的超极限距径比设计,使之具有操作简单、能耗低、回收率高等特点;在增大螺旋槽直径后仍可对微细粒矿物进行有效回收,提高了小密度差硫酸渣的分选效率。增加了横向冲洗水的设计,不产生二次污染,提高了单机富集比。该设备还可广泛用于其它低品位尾渣、含金属固体废渣、低密度非金属物料、金属矿山尾矿和化工微细物料的资源化处理。This embodiment breaks through the traditional theoretical limit that the aspect ratio cannot be less than 0.45, and adopts the ultra-limit aspect ratio design of h/D=0.35, so that it has the characteristics of simple operation, low energy consumption, and high recovery rate; The fine-grained minerals can still be effectively recovered after the diameter of the tank is increased, which improves the separation efficiency of sulfuric acid slag with small density difference. The design of horizontal flushing water is added, no secondary pollution occurs, and the enrichment ratio of a single machine is improved. The equipment can also be widely used in resource treatment of other low-grade tailings, metal-containing solid waste, low-density non-metallic materials, metal mine tailings and chemical fine materials.

Claims (5)

1、一种硫酸渣分离提纯分选设备,其特征在于将分矿器[1]与给矿槽[3]固定连接并安装在上支架[2]上,上支架[2]与螺旋槽支柱[4]固定连接,螺旋溜槽[5]与螺旋槽支柱[4]固定连接,螺旋溜槽[5]的上端位于上支架[2]下、下端与截矿槽[6]相接,截矿槽[6]和接矿斗[7]连接,在螺旋溜槽[5]的内侧设置有横向冲洗水管[8]。1. Separation, purification and sorting equipment for sulfuric acid slag, characterized in that the ore separator [1] is fixedly connected with the ore feed tank [3] and installed on the upper bracket [2], and the upper bracket [2] is connected with the spiral groove pillar [4] Fixed connection, the spiral chute [5] is fixedly connected with the spiral chute pillar [4], the upper end of the spiral chute [5] is located under the upper support [2], and the lower end is connected with the cutting groove [6]. [6] is connected with the ore receiving hopper [7], and the inboard of the spiral chute [5] is provided with a horizontal flushing water pipe [8]. 2、根据权利要求1所述的硫酸渣分离提纯分选设备,其特征在于所述的横向冲洗水管[8]外接高压水源,在横向冲洗水管[8]的内侧开有若干出水孔,横向冲洗水管[8]形状为管式螺旋状。2. Sulfuric acid slag separation, purification and sorting equipment according to claim 1, characterized in that the horizontal flushing water pipe [8] is externally connected to a high-pressure water source, and there are several water outlet holes on the inner side of the horizontal flushing water pipe [8] for horizontal flushing. Water pipe [8] shape is tubular spiral. 3、根据权利要求1所述的硫酸渣分离提纯分选设备,其特征在于所述的螺旋溜槽[5]为1~4头。3. Separation, purification and sorting equipment for sulfuric acid slag according to claim 1, characterized in that there are 1 to 4 spiral chutes [5]. 4、根据权利要求1所述的硫酸渣分离提纯分选设备,其特征在于所述的螺旋溜槽[5]的螺旋片高h与外径D之比为:h/D=0.33~0.40。4. Separation, purification and sorting equipment for sulfuric acid slag according to claim 1, characterized in that the ratio of the height h of the spiral sheet of the spiral chute [5] to the outer diameter D is: h/D=0.33-0.40. 5、根据权利要求3所述的硫酸渣分离提纯分选设备,其特征在于所述的螺旋溜槽[5]由玻璃纤维增强塑料或玻璃钢制成,内衬为刚玉型耐磨材料。5. Sulfuric acid slag separation, purification and sorting equipment according to claim 3, characterized in that said spiral chute [5] is made of glass fiber reinforced plastic or fiberglass, and the lining is corundum wear-resistant material.
CN 200420076632 2004-09-17 2004-09-17 Sulfuric acid residual separating-purifying-sorting apparatus Expired - Lifetime CN2738889Y (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103599842A (en) * 2013-11-11 2014-02-26 宁德市康鑫矿山设备设计研发有限公司 Large tower-type spiral concentrator
CN104923381A (en) * 2015-06-30 2015-09-23 辽宁科技大学 Complex force field spiral chute for ore dressing
CN105880032A (en) * 2016-05-09 2016-08-24 武汉科技大学 Middle-low grade collophanite heavy floating combined sorting method
CN106000619A (en) * 2016-05-20 2016-10-12 武汉科技大学 Method for obtaining vanadium from vanadium-containing stone coal through gravity separation and pre-concentration

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103599842A (en) * 2013-11-11 2014-02-26 宁德市康鑫矿山设备设计研发有限公司 Large tower-type spiral concentrator
CN104923381A (en) * 2015-06-30 2015-09-23 辽宁科技大学 Complex force field spiral chute for ore dressing
CN105880032A (en) * 2016-05-09 2016-08-24 武汉科技大学 Middle-low grade collophanite heavy floating combined sorting method
CN106000619A (en) * 2016-05-20 2016-10-12 武汉科技大学 Method for obtaining vanadium from vanadium-containing stone coal through gravity separation and pre-concentration

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