CN201052478Y - Bauxite pole type short flow path separation equipment - Google Patents
Bauxite pole type short flow path separation equipment Download PDFInfo
- Publication number
- CN201052478Y CN201052478Y CNU2007200397670U CN200720039767U CN201052478Y CN 201052478 Y CN201052478 Y CN 201052478Y CN U2007200397670 U CNU2007200397670 U CN U2007200397670U CN 200720039767 U CN200720039767 U CN 200720039767U CN 201052478 Y CN201052478 Y CN 201052478Y
- Authority
- CN
- China
- Prior art keywords
- flotation column
- column
- flotation
- cleaning
- roughing
- 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 - Fee Related
Links
Images
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及铝土矿柱式短流程分选设备,尤其适用于粗、精选集成的铝土矿柱式分选,也可用于其它微细颗粒金属矿或非金属矿的分选。The utility model relates to column-type short-flow sorting equipment for bauxite, which is especially suitable for the column-type sorting of coarse and fine-tuned integrated bauxite, and can also be used for the sorting of other fine particle metal ore or non-metallic ore.
技术背景technical background
我国铝土矿资源丰富,但大部分属于高铝、高硅、嵌布粒度细、容易泥化的一水硬铝石型,铝硅比中等偏低,因此只能使用成本较高的烧结法或混联法。随着生产的发展,高品位铝土矿资源日益减少,氧化铝厂生产能力及经济效益逐渐受到影响。“九五”以来,我国先后开发了一次细磨正浮选、分级浮选、阶段磨矿阶段选别、阶段磨矿-粗细分选等工艺,同时配套开发了各种高效浮选药剂,推动了铝土矿选矿技术的发展。my country is rich in bauxite resources, but most of them belong to the diaspore type with high aluminum, high silicon, fine intercalated particle size, and easy muddying, and the aluminum-silicon ratio is moderately low, so only the sintering method with high cost or hybrid method. With the development of production, high-grade bauxite resources are decreasing day by day, and the production capacity and economic benefits of alumina plants are gradually affected. Since the "Ninth Five-Year Plan", my country has successively developed a process such as fine grinding positive flotation, graded flotation, stage grinding and stage separation, stage grinding-coarse and fine separation, etc. At the same time, various high-efficiency flotation agents have been developed to promote The development of bauxite beneficiation technology.
目前已经工业化应用的铝土矿分选工艺有两种:分级-浮选和阶段磨矿-粗细分选,但两种工艺都是建立在传统浮选机分选的基础上,工艺流程长,投资量大。而对于更适合微细粒物料分选的浮选柱工艺并未见在铝土矿分选中得到应用,有关这方面的报道还是空白。At present, there are two kinds of bauxite separation processes that have been industrially applied: classification-flotation and stage grinding-coarse and fine separation, but both processes are based on traditional flotation machine separation, and the process flow is long. The amount of investment is large. However, the flotation column technology that is more suitable for the separation of fine-grained materials has not been applied in the separation of bauxite, and the report on this aspect is still blank.
用于分选铝土矿的传统浮选机浮选,一般采用一粗一扫两精一精扫作业流程,才能得到合格精矿和尾矿产品,即经过调浆后的浮选入料通过粗选浮选机分选后得到粗选精矿和尾矿;粗选精矿通过两段精选浮选机分选后得到精矿产品,一段精选的底流进入精扫选,精扫选泡沫产品和二段精选底流返回一段精选再选,精扫选尾矿与粗选尾矿合并作为合格尾矿,其流程长,设备多,耗电量大,投资大,维修量大,运行费用高。The flotation of the traditional flotation machine used for sorting bauxite generally adopts the operation process of one rough, one sweep, two fine and one fine sweep, so as to obtain qualified concentrate and tailings products, that is, the flotation feed after slurry adjustment passes through The rougher concentrate and tailings are obtained after the rougher flotation machine is sorted; the rougher concentrate is separated by the two-stage selection flotation machine to obtain the concentrate product, and the underflow of the first stage of selection enters the fine scavenging, and the fine scavenging The foam product and the bottom flow of the second-stage selection return to the first-stage selection and re-election, and the fine-sweeping and roughing tailings are combined as qualified tailings. The process is long, the equipment is large, the power consumption is large, the investment is large, and the amount of maintenance is large. High operating costs.
实用新型内容Utility model content
本实用新型的目的是根据已有技术存在的不足之处,提供一种设备简化,投资少,耗电量小,维修量小,运行费用低的铝土矿柱式短流程分选设备。The purpose of this utility model is to provide a bauxite column-type short-flow sorting equipment with simplified equipment, less investment, less power consumption, less maintenance and lower operating costs based on the shortcomings of the existing technology.
本实用新型所采用的技术方案:它包括矿浆搅拌桶,浮选柱,由电动调节阀、压力传感器和PID仪表构成的液位控制系统,所述浮选柱分为粗选浮选柱和精选浮选柱,粗选浮选柱的入口连接矿浆搅拌桶,粗选浮选柱的泡沫槽出口由管路与精选浮选柱的入料口相连接;精选浮选柱底流口下设有缓冲池,缓冲池与矿浆搅拌桶之间设有中矿泵和连通管。The technical solution adopted by the utility model: it includes a pulp mixing tank, a flotation column, a liquid level control system composed of an electric regulating valve, a pressure sensor and a PID instrument. The flotation column is divided into a rougher flotation column and a finer In the flotation column, the inlet of the rougher flotation column is connected to the pulp mixing tank, and the outlet of the foam tank of the rougher flotation column is connected with the inlet of the selected flotation column by a pipeline; A buffer pool is provided, and a medium ore pump and a connecting pipe are provided between the buffer pool and the slurry mixing tank.
本实用新型的柱式短流程分选设备,采用旋流-静态微泡浮选柱作主分选设备,粗选浮选柱可直接分选出铝土矿尾矿产品,粗选泡沫通过后续浮选柱精选后,直接得到精矿产品,只需一粗一精两段作业,大大提高了精矿品位和回收率。同传统浮选机分选设备相比,柱式短流程分选设备简化,结构紧凑合理,便于维修,投资少,耗电量小,占地面积小,运行费用低,具有广泛的实用性。The column-type short-flow separation equipment of the utility model adopts the cyclone-static micro-bubble flotation column as the main separation equipment, and the roughing flotation column can directly separate the bauxite tailings products, and the roughing foam passes through the subsequent After the flotation column is selected, the concentrate product is directly obtained, and only two operations are required, one rough and one fine, which greatly improves the concentrate grade and recovery rate. Compared with the traditional flotation machine sorting equipment, the column-type short-process sorting equipment is simplified, compact and reasonable in structure, easy to maintain, low in investment, low in power consumption, small in floor space, low in operating costs, and has a wide range of practicability.
附图说明 Description of drawings
附图是本实用新型分选设备系统图。Accompanying drawing is the system diagram of the sorting equipment of the utility model.
图中:矿浆搅拌桶1、粗选浮选柱2、粗选浮选柱底流口3、气泡发生器4、循环泵5、管路6、精选浮选柱7、精选浮选柱底流口8、尾矿管9、缓冲池10、中矿泵11。In the figure: slurry mixing tank 1,
具体实施方式 Detailed ways
下面结合附图中的实施例对本实用新型作进一步的描述:The utility model will be further described below in conjunction with the embodiment in the accompanying drawings:
附图所示,本实用新型的铝土矿柱式短流程分选设备,主要由矿浆搅拌桶1,粗选浮选柱2、精选浮选柱7和液位控制系统构成。两台浮选柱2和7按高差阶梯排列并相连,粗选浮选柱2较精选浮选柱7大,便于粗选浮选柱2上层的泡沫产品自流至精选浮选柱7内。粗选浮选柱2的入口与矿浆搅拌桶1连接,其泡沫槽出口经管路6与精选浮选柱7的入料口相连,经精选浮选柱底流口8下设有缓冲池10,缓冲池10与矿浆搅拌桶1之间设有连通管。As shown in the drawings, the bauxite column-type short-process separation equipment of the present utility model is mainly composed of a pulp mixing tank 1, a
其工作过程:将原矿B和浮选药剂A一起给入到矿浆搅拌桶1内,通过矿浆搅拌桶1内的叶轮进行搅拌,搅拌时间为10~15分钟,搅拌形成的浮选入料质量百分比浓度为30%~35%。浮选入料从矿浆搅拌桶1自流到粗选浮选柱2内,在气泡发生器4和循环泵5的作用下进行粗选,粗选尾矿D从粗选浮选柱底流口3排出,该尾矿为合格的铝土矿尾矿产品。粗选浮选柱2上层泡沫由管道6输送至精选浮选柱7内进行精选,精选尾矿C从精选浮选柱底流口8排出流入中矿缓冲池10;缓冲池10内的精选尾矿C通过中矿泵11将精选尾矿打回矿浆搅拌桶1,与浮选入料综合调浆后再次进行分选;精选浮选柱7的上层泡沫为最终的精矿产品E,该精矿通过精矿管9排出。Its working process: Feed the raw ore B and the flotation agent A together into the pulp mixing tank 1, and stir through the impeller in the pulp mixing tank 1. The stirring time is 10 to 15 minutes, and the mass percentage of the flotation feed material formed by stirring is The concentration is 30% to 35%. The flotation feed material flows from the pulp mixing tank 1 to the
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200397670U CN201052478Y (en) | 2007-06-09 | 2007-06-09 | Bauxite pole type short flow path separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200397670U CN201052478Y (en) | 2007-06-09 | 2007-06-09 | Bauxite pole type short flow path separation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201052478Y true CN201052478Y (en) | 2008-04-30 |
Family
ID=39392147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200397670U Expired - Fee Related CN201052478Y (en) | 2007-06-09 | 2007-06-09 | Bauxite pole type short flow path separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201052478Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657875A (en) * | 2013-12-31 | 2014-03-26 | 中国矿业大学 | Medium-low-grade bauxite machine-column united separation process |
| CN110586340A (en) * | 2019-09-30 | 2019-12-20 | 郑州大学 | Coarse particle mineral hydraulic flotation equipment and method based on orifice plate hydraulic cavitation bubble formation |
| CN112604819A (en) * | 2020-11-27 | 2021-04-06 | 郴州天朗金石矿山设备有限公司 | Efficient energy-saving device for recleaning tailings and low-degree ores |
| CN114011588A (en) * | 2019-06-27 | 2022-02-08 | 北京科技大学 | A multi-process flotation liquid level automatic control training device |
| CN114853005A (en) * | 2022-06-20 | 2022-08-05 | 苏州中材非金属矿工业设计研究院有限公司 | Short-flow graphite purification method adopting machine-column combined separation |
-
2007
- 2007-06-09 CN CNU2007200397670U patent/CN201052478Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657875A (en) * | 2013-12-31 | 2014-03-26 | 中国矿业大学 | Medium-low-grade bauxite machine-column united separation process |
| CN114011588A (en) * | 2019-06-27 | 2022-02-08 | 北京科技大学 | A multi-process flotation liquid level automatic control training device |
| CN110586340A (en) * | 2019-09-30 | 2019-12-20 | 郑州大学 | Coarse particle mineral hydraulic flotation equipment and method based on orifice plate hydraulic cavitation bubble formation |
| CN112604819A (en) * | 2020-11-27 | 2021-04-06 | 郴州天朗金石矿山设备有限公司 | Efficient energy-saving device for recleaning tailings and low-degree ores |
| CN114853005A (en) * | 2022-06-20 | 2022-08-05 | 苏州中材非金属矿工业设计研究院有限公司 | Short-flow graphite purification method adopting machine-column combined separation |
| CN114853005B (en) * | 2022-06-20 | 2024-03-29 | 苏州中材非金属矿工业设计研究院有限公司 | Short-process purification method for graphite by combined separation of machine and column |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101058083A (en) | Bauxite column type short flow-process separating technology and equipment | |
| CN102716814B (en) | Novel flotation column serial connection test system for improving flotation granularity upper limit | |
| CN105127002B (en) | A kind of floatation process for effectively reducing high grey thin mud pollution in cleaned coal | |
| CN102744146B (en) | Ore-dressing method for low-grade bauxite | |
| CN100562370C (en) | Flotation Columns for Mineral Separation | |
| CN101773873B (en) | Slime separation method and equipment | |
| CN102430480A (en) | Regrinding, recleaning and recleaning separation process for coarse clean coal | |
| CN205323969U (en) | From selecting equipment of retrieving low -grade marmatite and tin quarry thing in copper tailing | |
| CN201052478Y (en) | Bauxite pole type short flow path separation equipment | |
| CN100460079C (en) | Column type short process tungsten roughing process and equipment | |
| CN100429001C (en) | Hematite column type short process reverse flotation process and equipment | |
| CN111530646B (en) | Severely oxidized coal flotation system and flotation method | |
| CN204911756U (en) | Hierarchical ore dressing system of water -saving magnetic iron ore | |
| CN107096646B (en) | Method and device for flotation of coarse particle flotation column | |
| CN101347764A (en) | Phosphate Rock Column Separation Process and Equipment | |
| CN207546767U (en) | A kind of device of coarse granule column flotation | |
| CN101693226B (en) | Desliming method of high-talcose type nickel ore in mineral processing | |
| CN202921427U (en) | Flotation recycling gold and sliver device from zinc smelting acid leaching dregs | |
| CN212263543U (en) | A gravity sorting system | |
| CN101786048A (en) | Mineral floatation technique | |
| CN116140049B (en) | Process and device for recycling coarse-grain molybdenum ore particles in molybdenum flotation tailings | |
| CN206701484U (en) | A classification-cyclone-microbubble flotation column and process for reverse flotation of iron ore | |
| CN115814930A (en) | A kind of coal preparation system and separation method | |
| CN223069681U (en) | Improved gold ore floatation process system | |
| CN206763114U (en) | The novel hierarchical flotation column and technique of a kind of iron ore reverse flotation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080430 Termination date: 20160609 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |