CN2738889Y - Sulfuric acid residual separating-purifying-sorting apparatus - Google Patents
Sulfuric acid residual separating-purifying-sorting apparatus Download PDFInfo
- Publication number
- 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
- Authority
- CN
- China
- Prior art keywords
- sulfuric acid
- spiral
- spiral chute
- ore
- separation
- 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.)
- Expired - Lifetime
Links
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 239000002893 slag Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000000926 separation method Methods 0.000 claims description 15
- 238000011010 flushing procedure Methods 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 7
- 239000011152 fibreglass Substances 0.000 claims description 5
- 229910052593 corundum Inorganic materials 0.000 claims description 3
- 239000010431 corundum Substances 0.000 claims description 3
- 239000002184 metal Substances 0.000 abstract description 7
- 229910052751 metal Inorganic materials 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000007769 metal material Substances 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 238000012545 processing Methods 0.000 abstract description 3
- 229910052755 nonmetal Inorganic materials 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 13
- 239000011707 mineral Substances 0.000 description 13
- 238000013461 design Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 239000002910 solid waste Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
Images
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420076632 CN2738889Y (en) | 2004-09-17 | 2004-09-17 | Sulfuric acid residual separating-purifying-sorting apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420076632 CN2738889Y (en) | 2004-09-17 | 2004-09-17 | Sulfuric acid residual separating-purifying-sorting apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2738889Y true CN2738889Y (en) | 2005-11-09 |
Family
ID=35353957
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200420076632 Expired - Lifetime CN2738889Y (en) | 2004-09-17 | 2004-09-17 | Sulfuric acid residual separating-purifying-sorting apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2738889Y (en) |
Cited By (4)
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 |
-
2004
- 2004-09-17 CN CN 200420076632 patent/CN2738889Y/en not_active Expired - Lifetime
Cited By (4)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101773873B (en) | Slime separation method and equipment | |
CN102172559A (en) | Tungsten and tin recovery concentration method combining centrifugal concentration with floatation | |
CN103480502B (en) | Three-product cyclone microbubble floatation column screening installation and method | |
CN105880032B (en) | A kind of re-flotation combined sorting method of low-grade collophosphate ore | |
CN106733205A (en) | The Efficient beneficiation method of troilite in lead zinc flotation tailing | |
CN101507946A (en) | Double tail-removing gravity-flotation combined sorting method and device | |
CN206701482U (en) | A kind of new elutriation magnetic separator | |
CN103041931A (en) | Particle size differentiation flotation column type sorting device and method | |
CN102343309A (en) | Machine-column combined three-section floating equipment | |
CN110882851B (en) | Beneficiation system and beneficiation method for sulfide ore | |
CN2738889Y (en) | Sulfuric acid residual separating-purifying-sorting apparatus | |
CN106669961A (en) | Process for recycling fine coal from middlings | |
CN101213024A (en) | Mineral element separating method and its device | |
CN101693226B (en) | Desliming method of high-talcose type nickel ore in mineral processing | |
CN212263543U (en) | A gravity sorting system | |
CN209379185U (en) | A complete set of spodumene high-density separation equipment | |
CN203018212U (en) | Particle size differentiation flotation column type sorting unit | |
CN204911756U (en) | Hierarchical ore dressing system of water -saving magnetic iron ore | |
CN109847923B (en) | Recovery process of extremely-poor weathered primary ilmenite | |
CN102357396A (en) | Method for separating low-grade lead zinc ores with double-cone heavy medium cyclone | |
CN205887146U (en) | Quartzy tailings deironing device | |
CN105537007B (en) | A kind of mineral floating system | |
CN203484231U (en) | Triple-product cyclone micro bubble flotation column separation device | |
CN1276795C (en) | A kind of equipment for separation and purification of sulfuric acid slag | |
CN209317889U (en) | A kind of fluorine carbon cerium type rare earth weight magnetic tailing recycling production system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Effective date of abandoning: 20040917 |
|
C25 | Abandonment of patent right or utility model to avoid double patenting |