CN114602807B - A kind of dry classification and dust removal integrated screening equipment and method for fine granular materials - Google Patents
A kind of dry classification and dust removal integrated screening equipment and method for fine granular materials Download PDFInfo
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B9/00—Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/14—Separating or sorting of material, associated with crushing or disintegrating with more than one separator
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/28—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/42—Drive mechanisms, regulating or controlling devices, or balancing devices, specially adapted for screens
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B15/00—Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area
- B08B15/04—Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area from a small area, e.g. a tool
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Abstract
本发明公开了一种微细粒物料干法分级与除尘一体化筛分设备及方法,属于微细物料筛分技术领域,解决了现有技术中筛分1mm及以下的物料时,颗粒卡堵筛面,筛分环境恶化的问题。本发明的筛分设备包括分级激励装置、负压吸附装置和筛下物料收集装置;分级激励装置包括激振器、筛框和弹性筛面;弹性筛面的筛孔尺寸为1mm;负压吸附装置用于迫使筛上区域的1mm以下物料进入筛下区域;筛下物料收集装置用于收集进入筛下区域的1mm及以下微细粒物料。本发明实现了1mm及以下物料的干法筛分,并避免了筛分过程中粉尘带来的环境污染与物料损失。
The invention discloses an integrated dry classification and dust removal screening equipment and method for fine-grained materials, which belongs to the technical field of fine-grained material screening and solves the problem of particles blocking the screen surface when screening materials of 1 mm and below in the prior art. , screening the problem of environmental degradation. The screening equipment of the present invention includes a classification excitation device, a negative pressure adsorption device and a material collection device under the screen; the classification excitation device includes a vibrator, a screen frame and an elastic screen surface; the mesh size of the elastic screen surface is 1 mm; the negative pressure adsorption device The device is used to force materials below 1mm in the area above the screen to enter the area below the screen; the material collection device under the screen is used to collect fine particles of 1mm and below that enter the area under the screen. The invention realizes dry screening of materials of 1 mm and below, and avoids environmental pollution and material loss caused by dust during the screening process.
Description
技术领域Technical field
本发明涉及微细物料筛分技术领域,尤其涉及一种微细粒物料干法分级与除尘一体化筛分设备及方法。The invention relates to the technical field of fine material screening, and in particular to a screening equipment and method integrating dry classification and dust removal of fine particles.
背景技术Background technique
筛分是将松散的混合物料通过单层或多层筛面的筛孔,按照颗粒大小分成若干不同粒级产品的分级过程。Screening is a grading process in which loose mixed materials are passed through the sieve holes of a single or multi-layer screen surface and divided into several different grades of products according to particle size.
传统干法筛分过程中,筛面容易导致颗粒卡堵;对于粘湿物料而言,粘性细颗粒含量大、外在水分高,极易形成覆盖膜,糊堵筛面筛分过程逐渐恶化,严重影响筛面开孔率与筛分效果。微细粒物料干法筛分过程中,由于粉末物料含量大,在筛分过程中会产生大量的粉尘,造成了环境污染与物料损失。In the traditional dry screening process, the screen surface can easily cause particles to get stuck; for sticky and wet materials, the content of sticky fine particles is large and the external moisture is high, which can easily form a covering film and block the screen surface. The screening process gradually worsens. Seriously affects the screen surface opening rate and screening effect. During the dry screening process of fine-grained materials, due to the large content of powder materials, a large amount of dust will be generated during the screening process, causing environmental pollution and material loss.
发明内容Contents of the invention
鉴于上述的分析,本发明旨在提供一种微细粒物料1mm干法分级与静电除尘一体化设备,用以解决现有以下问题:In view of the above analysis, the present invention aims to provide an integrated equipment for 1mm dry classification and electrostatic precipitating of fine particle materials to solve the following existing problems:
(1)随着筛分的分级粒度下限降低,接近筛孔尺寸颗粒含量增加,尤其粒度范围在1mm及以下的物料,传统筛分方式已难以解决。(1) As the lower limit of screening particle size decreases, the content of particles close to the mesh size increases, especially for materials with a particle size range of 1mm and below, which is difficult to solve with traditional screening methods.
(2)微细粒物料干法筛分过程中,由于粉末物料含量大,在筛分过程中会产生大量的粉尘,造成了环境污染与物料损失。(2) During the dry screening process of fine-grained materials, due to the large content of powder materials, a large amount of dust will be generated during the screening process, causing environmental pollution and material loss.
本发明的目的主要是通过以下技术方案实现的:The purpose of the present invention is mainly achieved through the following technical solutions:
本发明提供了一种微细粒物料干法分级与除尘一体化筛分设备,包括分级激励装置、负压吸附装置和筛下物料收集装置;The invention provides an integrated screening equipment for dry classification and dust removal of fine granular materials, including a classification excitation device, a negative pressure adsorption device and a material collection device under the screen;
分级激励装置包括激振器、筛框和弹性筛面;激振器和弹性筛面均设于筛框上;激振器用于对筛框提供激振力;弹性筛面的筛孔尺寸为1mm;The graded excitation device includes a vibrator, a screen frame and an elastic screen surface; the vibrator and the elastic screen surface are both located on the screen frame; the vibrator is used to provide exciting force to the screen frame; the mesh size of the elastic screen surface is 1mm ;
负压吸附装置与筛框软连接,负压吸附装置设于弹性筛面的下方,负压吸附装置用于使弹性筛面的筛上区域与筛下区域产生压差,迫使筛上区域的1mm以下物料进入筛下区域;The negative pressure adsorption device is softly connected to the screen frame. The negative pressure adsorption device is located below the elastic screen surface. The negative pressure adsorption device is used to create a pressure difference between the upper and lower areas of the elastic screen surface, forcing 1mm of the upper area of the screen to The following materials enter the area under the screen;
筛下物料收集装置设于弹性筛面的下方,用于收集进入筛下区域的1mm及以下微细粒物料。The under-screen material collection device is located under the elastic screen surface and is used to collect fine particles of 1mm and below that enter the under-screen area.
在一种可能的设计中,分级激励装置还包括支架和弹性支撑;支架的一端与固定平台或者地面接触,另一端通过弹性支撑与筛框连接。In one possible design, the graded excitation device also includes a bracket and an elastic support; one end of the bracket is in contact with the fixed platform or the ground, and the other end is connected to the screen frame through the elastic support.
在一种可能的设计中,负压吸附装置包括气流产生单元、气流储存单元、静电除尘单元、吸附物料收集单元和气流输送单元;In one possible design, the negative pressure adsorption device includes an air flow generating unit, an air flow storage unit, an electrostatic precipitator unit, an adsorbed material collection unit and an air flow conveying unit;
气流产生单元、气流储存单元、静电除尘单元、吸附物料收集单元均通过气流输送单元依次连接;且吸附物料收集单元还通过气流输送单元与筛框软连接;气流产生单元产生负压气流,经过气流储存单元、静电除尘单元、吸附物料收集单元后通过气流输送单元进入到弹性筛面的筛下区域。The air flow generation unit, air flow storage unit, electrostatic precipitator unit, and adsorption material collection unit are all connected in sequence through the air flow transport unit; and the adsorption material collection unit is also softly connected to the screen frame through the air flow transport unit; the air flow generation unit generates negative pressure air flow, and passes through the air flow The storage unit, electrostatic precipitator unit and adsorbed material collection unit then enter the under-screen area of the elastic screen surface through the air transport unit.
在一种可能的设计中,吸附物料收集单元包括依次连接的第一收集器和第二收集器;第一收集器设于第二收集器的上方;In a possible design, the adsorbed material collection unit includes a first collector and a second collector connected in sequence; the first collector is located above the second collector;
第一收集器包括中空的第一上圆锥体和第一下圆锥体,第一上圆锥体和第一下圆锥体对接构成封闭空间,封闭空间内设有倾斜的第一滤网;第二收集器包括中空的第二上圆锥体和第二下圆锥体,第二上圆锥体和第二下下圆锥体对接构成封闭空间,封闭空间内设有倾斜的第二滤网。The first collector includes a hollow first upper cone and a first lower cone. The first upper cone and the first lower cone are connected to form a closed space. An inclined first filter is provided in the closed space; the second collector The device includes a hollow second upper cone and a second lower cone. The second upper cone and the second lower cone are connected to form a closed space. An inclined second filter screen is provided in the closed space.
在一种可能的设计中,第一滤网和第二滤网的网孔孔径小于等于0.05mm;In a possible design, the mesh diameter of the first filter screen and the second filter screen is less than or equal to 0.05mm;
以水平面为基准,第一滤网的倾斜角度大于第二滤网的倾斜角度。Based on the horizontal plane, the inclination angle of the first filter screen is greater than the inclination angle of the second filter screen.
在一种可能的设计中,第一收集器的上方设有静电场区域,被负压吸附装置产生的负压气流吸附的微细粒物料先经过静电场区域;In one possible design, an electrostatic field area is provided above the first collector, and the fine particles adsorbed by the negative pressure airflow generated by the negative pressure adsorption device first pass through the electrostatic field area;
静电场区域用于使尘粒带负电,吸附尘粒后将尘粒分离出来。The electrostatic field area is used to make dust particles negatively charged, and then separate the dust particles after adsorption.
在一种可能的设计中,弹性筛面包括多块矩形单元筛面,多块矩形单元筛面平行放置,矩形单元筛面的长边方向与微细粒物料的流动方向垂直;In one possible design, the elastic screen surface includes multiple rectangular unit screen surfaces, the multiple rectangular unit screen surfaces are placed in parallel, and the long side direction of the rectangular unit screen surface is perpendicular to the flow direction of fine granular materials;
沿微细粒物料的入料方向,单元筛面的开孔率逐渐减少。Along the feeding direction of fine-grained materials, the opening rate of the unit screen surface gradually decreases.
在一种可能的设计中,弹性筛面沿入料方向呈倾斜设置,以水平面为基准,弹性筛面的倾斜角度为3-8°。In one possible design, the elastic screen surface is tilted along the feeding direction, and the inclination angle of the elastic screen surface is 3-8° based on the horizontal plane.
在一种可能的设计中,多块单元筛面均采用聚氨酯材料。In one possible design, multiple unit screen surfaces are made of polyurethane material.
在一种可能的设计中,微细粒物料干法分级与除尘一体化筛分设备还包括筛上物料处理单元;In one possible design, the integrated screening equipment for dry classification and dust removal of fine-grained materials also includes an upper-screen material processing unit;
筛上物料处理单元用于处理弹性筛面的筛上物,处理后使其成为1mm及以下的微细粒物。The over-the-sieve material processing unit is used to process the over-the-sieve material on the elastic screen surface and turn it into fine particles of 1 mm and below.
另一方面,本发明还提供了一种微细粒物料干法分级与除尘一体化筛分方法,采用上述的微细粒物料干法分级与除尘一体化筛分设备,该筛分方法包括以下步骤:On the other hand, the present invention also provides an integrated dry classification and dust removal screening method for micro-fine materials, using the above-mentioned integrated dry classification and dust removal screening equipment for micro-fine materials. The screening method includes the following steps:
步骤1、将微细粒物料投入分级激励装置,微细粒物料经过1mm弹性筛的筛面,1mm及以下微细粒物料通过弹性筛进入筛下物料收集装置;筛上物料进入筛上物料处理单元;Step 1. Put the fine-grained materials into the classification excitation device. The fine-grained materials pass through the screen surface of the 1mm elastic screen. The fine-grained materials with 1mm and below pass through the elastic screen and enter the under-sieve material collection device; the above-sieve materials enter the above-sieve material processing unit;
步骤2、经筛上物料处理单元处理后,筛上物料全部形成的1mm及以下微细粒物料。Step 2: After being processed by the material processing unit on the screen, all the fine particles of 1mm and below formed by the materials on the screen will be removed.
与现有技术相比,本发明至少可实现如下有益效果之一:Compared with the prior art, the present invention can achieve at least one of the following beneficial effects:
(1)本发明通过设置负压吸附装置,可以用于增加细粒级物料的透筛量,强化筛分效果,优化筛分环境。通过设置物料收集单元,可以回收细粒级物料,避免物料损失。(1) By setting up a negative pressure adsorption device, the present invention can be used to increase the amount of fine-grained materials passing through the screen, strengthen the screening effect, and optimize the screening environment. By setting up a material collection unit, fine-grained materials can be recycled to avoid material loss.
(2)本发明在第一收集器的上方设置静电场,并在第二收集器的下方设置静电除尘器,输送过程除尘与终端除尘结合的双重静电除尘设计,不仅能够实现高效除尘的同时,并且能够增强筛面尘粒与微细粒矿物的有效分离,避免对环境造成污染。(2) The present invention sets an electrostatic field above the first collector and sets an electrostatic precipitator below the second collector. The dual electrostatic precipitator design that combines dust removal during transportation and terminal dust removal can not only achieve efficient dust removal, but also And it can enhance the effective separation of dust particles and fine minerals on the screen surface to avoid environmental pollution.
(3)本发明提供的微细粒物料的分级与除尘一体化设备,能够实现微细粒矿物与尘粒的有效分离。(3) The integrated equipment for classification and dust removal of fine-grained materials provided by the present invention can achieve effective separation of fine-grained minerals and dust particles.
本发明中,上述各技术方案之间还可以相互组合,以实现更多的优选组合方案。本发明的其他特征和优点将在随后的说明书中阐述,并且,部分优点可从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他优点可通过说明书实施例以及附图中所特别指出的内容中来实现和获得。In the present invention, the above technical solutions can also be combined with each other to achieve more preferred combination solutions. Additional features and advantages of the invention will be set forth in the description which follows, and in part, some advantages will be apparent from the description, or may be learned by practice of the invention. The objectives and other advantages of the invention may be realized and obtained by the embodiments particularly pointed out in the description and drawings.
附图说明Description of drawings
附图仅用于示出具体实施例的目的,而并不认为是对本发明的限制,在整个附图中,相同的参考符号表示相同的部件。The drawings are for the purpose of illustrating specific embodiments only and are not to be construed as limitations of the invention. Throughout the drawings, the same reference characters represent the same components.
图1为本发明的分级激励装置的左视图;Figure 1 is a left view of the hierarchical excitation device of the present invention;
图2为本发明的分级激励装置的主视图;Figure 2 is a front view of the hierarchical excitation device of the present invention;
图3为本发明的分级激励装置与吸附装置的整体结构示意图;Figure 3 is a schematic diagram of the overall structure of the hierarchical excitation device and adsorption device of the present invention;
图4为本发明的筛上物料的处理工艺流程图,其中,+表示筛上物料,-表示筛下物料。Figure 4 is a process flow chart for processing the material above the sieve of the present invention, in which + represents the material above the sieve, and - represents the material below the sieve.
附图标记:Reference signs:
1-分级激励装置;2-弹性筛面;3-风管;4-第一收集器;5-第二收集器;6-第一上圆锥体;7-第一滤网;8-第一下圆锥体;9-第二上圆锥体;10第二滤网;11-第二下圆锥体;12-静电除尘器;13-风室;14-风机;15-激振器;16-筛框;17-弹性支撑;18-支架;19-筛上物料;20-筛下物料收集装置;21-给料方向。1-Grading excitation device; 2-Elastic screen surface; 3-Air duct; 4-First collector; 5-Second collector; 6-First upper cone; 7-First filter; 8-First Lower cone; 9-second upper cone; 10 second filter; 11-second lower cone; 12-electrostatic precipitator; 13-air chamber; 14-fan; 15-vibrator; 16-sieve Frame; 17-elastic support; 18-bracket; 19-material on the screen; 20-material collection device under the screen; 21-feeding direction.
具体实施方式Detailed ways
下面结合附图来具体描述本发明的优选实施例,其中,附图构成本发明的一部分,并与本发明的实施例一起用于阐释本发明的原理,并非用于限定本发明的范围。The preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings. The drawings constitute a part of the present invention and are used together with the embodiments of the present invention to illustrate the principles of the present invention and are not intended to limit the scope of the present invention.
物料分离的方式按照粒度大小主要包括干法分级和湿法分级;其中,干法分级主要包括干法筛分和空气旋流力场分级(气流分级);干法筛分主要是利用筛分设备进行分级,气流分级主要是通过空气旋流力场进行分级,后者处理能力小,且能耗巨大,制约了大规模干法分级的工业应用。因此,干法筛分是解决工业大规模物料干法分级的重要方式。干法筛分存在的问题是现有技术的分级粒度下限只做到3mm或2mm,而无法实现1mm的干法筛分。The methods of material separation mainly include dry classification and wet classification according to particle size; among them, dry classification mainly includes dry screening and air cyclone force field classification (air flow classification); dry screening mainly uses screening equipment For classification, air flow classification is mainly performed through the air cyclone force field. The latter has small processing capacity and huge energy consumption, which restricts the industrial application of large-scale dry classification. Therefore, dry screening is an important way to solve the dry classification of industrial large-scale materials. The problem with dry screening is that the lower limit of the classification particle size of the existing technology is only 3mm or 2mm, and dry screening of 1mm cannot be achieved.
较之前3mm或2mm干法筛分,本发明同时利用负压吸附与静电作用,进行1mm干法筛分。Compared with the previous 3mm or 2mm dry screening, this invention simultaneously utilizes negative pressure adsorption and electrostatic effect to perform 1mm dry screening.
如图1至图4所示,本发明提供了一种微细粒物料干法分级与除尘一体化筛分设备,该设备包括分级激励装置1、负压吸附装置和筛下物料收集装置;分级激励装置1包括激振器15、筛框16和弹性筛面2;激振器15和弹性筛面2均设于筛框16上;激振器15用于对筛框16提供激振力;弹性筛面2的筛孔尺寸为1mm;负压吸附装置与筛框16软连接,负压吸附装置设于弹性筛面2的下方,负压吸附装置用于使弹性筛面2的筛上区域与筛下区域产生压差,迫使筛上区域的1mm以下物料进入筛下区域;筛下物料收集装置20设于弹性筛面2的下方,用于收集进入筛下区域的1mm及以下微细粒物料。As shown in Figures 1 to 4, the present invention provides an integrated screening equipment for dry classification and dust removal of fine-grained materials. The equipment includes a classification excitation device 1, a negative pressure adsorption device and a material collection device under the screen; classification excitation The device 1 includes a vibrator 15, a screen frame 16 and an elastic screen surface 2; the vibrator 15 and the elastic screen surface 2 are both located on the screen frame 16; the vibrator 15 is used to provide exciting force to the screen frame 16; the elasticity The mesh size of the screen surface 2 is 1mm; the negative pressure adsorption device is softly connected to the screen frame 16. The negative pressure adsorption device is located below the elastic screen surface 2. The negative pressure adsorption device is used to connect the upper screen area of the elastic screen surface 2 to the screen frame 16. A pressure difference is generated in the area under the screen, forcing materials below 1 mm in the area above the screen to enter the area under the screen; the under-screen material collection device 20 is located below the elastic screen surface 2 and is used to collect fine particles of 1 mm and below that enter the area under the screen.
具体地,本发明在弹性筛面2的下方设置负压吸附装置,负压吸附装置能够从弹性筛面2下方引入负压气流,使弹性筛面2的筛上区域与筛下区域产生压差,迫使筛上的1mm及以下物料向下透筛;同时,由于物料颗粒的挤压与弹性筛面2的筛孔变形,加速卡堵筛孔颗粒透过筛孔。由于水分的影响,传统筛分过程中1mm的细颗粒易粘附在大颗粒上无法透筛,与现有技术相比,本发明通过负压吸附装置产生的气流力场作用,可以促进微细粒物料中水分的散失,促使微细颗粒物料脱附,进而透筛。Specifically, the present invention provides a negative pressure adsorption device below the elastic screen surface 2. The negative pressure adsorption device can introduce negative pressure airflow from below the elastic screen surface 2 to create a pressure difference between the upper screen area and the lower screen area of the elastic screen surface 2. , forcing the materials 1mm and below on the screen to pass through the screen downward; at the same time, due to the extrusion of the material particles and the deformation of the screen holes of the elastic screen surface 2, the particles blocking the screen holes are accelerated to pass through the screen holes. Due to the influence of moisture, in the traditional screening process, 1mm fine particles tend to adhere to large particles and cannot pass through the sieve. Compared with the existing technology, the present invention can promote the removal of fine particles through the air flow force field generated by the negative pressure adsorption device. The loss of moisture in the material causes the fine particles to desorb and pass through the screen.
与现有技术相比,本发明通过设置分级激励装置1能够对弹性筛面2提供激振力,促进1mm及以下物料通过筛孔。另外,由于本发明的筛面为弹性筛面2,分级激励装置1对筛框16提供激振力时,筛孔受力时会产生微变形,能够促进微细粒物料透过筛面,促进了微细粒物料的筛分。Compared with the existing technology, the present invention can provide excitation force to the elastic screen surface 2 by arranging the graded excitation device 1 to promote materials with a diameter of 1mm and below to pass through the screen holes. In addition, since the screen surface of the present invention is an elastic screen surface 2, when the classification excitation device 1 provides excitation force to the screen frame 16, the screen holes will produce micro-deformation when stressed, which can promote the penetration of fine particles into the screen surface and promote the Screening of fine-grained materials.
本发明的分级激励装置1还包括支架18和弹性支撑17;支架18的一端与固定平台或者地面接触,另一端通过弹性支撑17与筛框16连接。The graded excitation device 1 of the present invention also includes a bracket 18 and an elastic support 17; one end of the bracket 18 is in contact with the fixed platform or the ground, and the other end is connected to the screen frame 16 through the elastic support 17.
具体地,如图1和图2所示,本发明的分级激励装置1还包括支架18,该支架18包括多条支撑腿,例如,四条支撑腿,支撑腿用于支撑筛框16和筛面及其筛分零部件;多个支撑腿的底端与地面或固定平台接触,其顶端与弹性支撑17连接,弹性支撑17与筛框16连接。Specifically, as shown in Figures 1 and 2, the graded excitation device 1 of the present invention also includes a bracket 18. The bracket 18 includes a plurality of support legs, for example, four support legs. The support legs are used to support the screen frame 16 and the screen surface. and its screening components; the bottom ends of the plurality of support legs are in contact with the ground or a fixed platform, and their top ends are connected with elastic supports 17, and the elastic supports 17 are connected with the screen frame 16.
为了进一步保证1mm及以下微细粒矿物能够顺利通过弹性筛面2,本发明的负压吸附装置包括气流产生单元、气流储存单元、静电除尘单元、吸附物料收集单元和气流输送单元;气流产生单元、气流储存单元、静电除尘单元、吸附物料收集单元均通过气流输送单元依次连接;且吸附物料收集单元还通过气流输送单元与筛框16软连接;气流产生单元产生负压气流,经过气流储存单元、静电除尘单元、吸附物料收集单元后通过气流输送单元进入到弹性筛面2的筛下区域。In order to further ensure that fine-grained minerals of 1 mm and below can smoothly pass through the elastic screen surface 2, the negative pressure adsorption device of the present invention includes an air flow generating unit, an air flow storage unit, an electrostatic precipitator unit, an adsorbed material collection unit and an air flow conveying unit; the air flow generating unit, The airflow storage unit, electrostatic precipitator unit, and adsorbed material collection unit are all connected in sequence through the airflow conveying unit; and the adsorbed material collection unit is also softly connected to the screen frame 16 through the airflow conveying unit; the airflow generating unit generates negative pressure airflow, which passes through the airflow storage unit, The electrostatic precipitator unit and the adsorbed material collection unit then enter the under-screen area of the elastic screen surface 2 through the air flow conveying unit.
具体地,本发明的气流产生单元包括风机14,第一静电除尘单元包括除尘器,气流储存单元包括风室13或风包(相当于缓冲装置,具有缓冲作用),气流输送单元包括风管3;负压吸附装置的具体工作过程为:风机14产生负压气流,通过风室13或风包、静电除尘器12、吸附物料收集单元后给入分级激励装置1的弹性筛面2下方,使在弹性筛面2的上方和弹性筛面2的下方之间形成压差,1mm及以下颗粒物料受到负压气流的作用(向下的吸附力),进而促使这部分颗粒透筛并向弹性筛面2的下方运动,成为筛下物。负压吸附装置的吸附过程中,被吸附的微细粒物料的流动方向为:透过弹性筛面,经过风管3进入静电场区域,除尘后分别经过物料吸附单元,经吸附后被收集起来,被排出负压气流。Specifically, the airflow generating unit of the present invention includes a fan 14, the first electrostatic precipitator unit includes a dust collector, the airflow storage unit includes an air chamber 13 or an air bag (equivalent to a buffer device with a buffering effect), and the airflow transport unit includes an air duct 3 The specific working process of the negative pressure adsorption device is: the fan 14 generates negative pressure airflow, which passes through the air chamber 13 or air bag, the electrostatic precipitator 12, and the adsorbed material collection unit and then is fed under the elastic screen surface 2 of the classification excitation device 1, so that A pressure difference is formed between the upper part of the elastic screen surface 2 and the lower part of the elastic screen surface 2. The granular materials 1mm and below are affected by the negative pressure air flow (downward adsorption force), thereby prompting these particles to pass through the screen and move toward the elastic screen. The lower part of surface 2 moves and becomes the object under the sieve. During the adsorption process of the negative pressure adsorption device, the flow direction of the adsorbed fine particles is: through the elastic screen surface, through the air duct 3 and into the electrostatic field area. After dust removal, it passes through the material adsorption unit respectively, and is collected after adsorption. The negative pressure airflow is discharged.
需要强调的是,在负压气流吸附的过程中,势必会吸附到1mm及以下物料,本发明通过设置吸附物料收集单元将这部分物料收集起来,另外,为了避免污染空气,本发明在吸附物料收集单元的下一环节设置静电除尘器12,静电除尘器12用于除去经吸附物料收集单元处理后仍吸附于负压气流中的微细粒物料,进而可以将风机14产生的负压气流排入大气,同时避免造成空气污染。It should be emphasized that during the process of negative pressure airflow adsorption, materials with a diameter of 1 mm or less will inevitably be adsorbed. The present invention collects these materials by setting up an adsorption material collection unit. In addition, in order to avoid contaminating the air, the present invention collects the adsorbed materials The next link of the collection unit is equipped with an electrostatic precipitator 12. The electrostatic precipitator 12 is used to remove fine particles that are still adsorbed in the negative pressure airflow after being processed by the adsorbed material collection unit, and then the negative pressure airflow generated by the fan 14 can be discharged into atmosphere while avoiding air pollution.
为了确保物料的收集效果,尽可能的减少负压气流中的物料,本发明的物料收集单元包括依次连接的第一收集器4和第二收集器5;第一收集器4设于第二收集器5的上方;第一收集器4包括中空的第一上圆锥体6和第一下圆锥体8,第一上圆锥体6和第一下圆锥体8对接构成封闭空间,封闭空间内设有倾斜的第一滤网7;第二收集器5包括中空的第二上圆锥体9和第二下圆锥体11,第二上圆锥体9和第二下下圆锥体对接构成封闭空间,封闭空间内设有倾斜的第二滤网10。In order to ensure the material collection effect and reduce the materials in the negative pressure air flow as much as possible, the material collection unit of the present invention includes a first collector 4 and a second collector 5 connected in sequence; the first collector 4 is located on the second collector Above the container 5; the first collector 4 includes a hollow first upper cone 6 and a first lower cone 8. The first upper cone 6 and the first lower cone 8 are connected to form a closed space, and there are The inclined first filter screen 7; the second collector 5 includes a hollow second upper cone 9 and a second lower cone 11. The second upper cone 9 and the second lower cone are connected to form a closed space. The closed space An inclined second filter screen 10 is provided inside.
具体地,如图2所示,本发明的物料收集单元包括相连接的第一收集器4和第二收集器5,其中,第一收集器4设于第二收集器5的上方,第一收集器4包括均为中空状的第一上圆锥体6和第一下圆锥体8,第一上圆锥体6和第一下圆锥体8对接后形成第一中空腔,在该第一中空腔内倾斜的设置有第一滤网7,在第一滤网7上设有第一刮刀收集器和第一分离口,第一刮刀收集器将第一滤网7上方的物料通过第一分离口分别移出第一上圆锥体6。同样地,第二收集器5包括均为中空状的第二上圆锥体9和第二下圆锥体11,第二上圆锥体9和第二下圆锥体11对接后形成第二中空腔,在该第二中空腔内倾斜的设置有第二滤网10,在第二滤网10上设有第二刮刀收集器和第二分离口,第二刮刀收集器将第二滤网10上方的物料通过第二分离口分别移出第一上圆锥体6。Specifically, as shown in Figure 2, the material collection unit of the present invention includes a connected first collector 4 and a second collector 5, wherein the first collector 4 is located above the second collector 5, and the first collector 4 is disposed above the second collector 5. The collector 4 includes a first upper cone 6 and a first lower cone 8 that are both hollow. The first upper cone 6 and the first lower cone 8 are butted together to form a first hollow cavity. In the first hollow cavity A first filter screen 7 is provided with an inner slope. A first scraper collector and a first separation port are provided on the first filter screen 7. The first scraper collector passes the material above the first filter screen 7 through the first separation port. Remove the first upper cone 6 respectively. Similarly, the second collector 5 includes a second upper cone 9 and a second lower cone 11 that are both hollow. The second upper cone 9 and the second lower cone 11 are butted together to form a second hollow cavity. A second filter screen 10 is provided at an angle in the second hollow cavity. A second scraper collector and a second separation port are provided on the second filter screen 10. The second scraper collector collects the materials above the second filter screen 10. The first upper cones 6 are respectively removed through the second separation opening.
由于被负压气流吸附的物料先经过第一收集器4,物料经第一滤网7被收集走一部分,这样会使负压气流中物料浓度会减少,因此,在设置第一滤网7和第二滤网10时,第一滤网7的倾斜角度大于第二滤网10的倾斜角度。Since the material adsorbed by the negative pressure airflow first passes through the first collector 4, part of the material is collected through the first filter 7, which will reduce the concentration of the material in the negative pressure airflow. Therefore, when setting the first filter 7 and When the second filter screen 10 is used, the inclination angle of the first filter screen 7 is greater than the inclination angle of the second filter screen 10 .
另外,由于负压气流中的物料粒度在1mm及其以下,因此,本发明的第一滤网7和第二滤网10的网孔孔径小于或等于0.05mm,小于或等于0.05mm的物料再利用静电除尘器12进行吸附出去,经第一静除尘器除尘后的负压气流可以直接排进大气中,不会带来环境污染。In addition, since the particle size of materials in the negative pressure airflow is 1 mm and below, the mesh apertures of the first filter screen 7 and the second filter screen 10 of the present invention are less than or equal to 0.05 mm, and materials less than or equal to 0.05 mm are The electrostatic precipitator 12 is used for adsorption, and the negative pressure airflow after dust removal by the first electrostatic precipitator can be directly discharged into the atmosphere without causing environmental pollution.
需要说明的是,上述第一滤网7和第二滤网10均为弹性滤网,第一收集器4和第二收集器5均与动力设备连接,动力设备用于为第一滤网7和第二滤网10提供动力,使其在工作过程中进行振动,进而更高效的将物料过滤和分离出来。It should be noted that the above-mentioned first filter screen 7 and the second filter screen 10 are both elastic filters, and the first collector 4 and the second collector 5 are both connected to power equipment, and the power equipment is used for the first filter screen 7 And the second filter screen 10 provides power to vibrate during the working process, thereby filtering and separating the materials more efficiently.
与现有技术相比,本发明的第一收集器4和第二收集器5采用分别采用上圆锥体和下圆锥体对接形成空腔,能够减少第一收集器4和第二收集器5内部无效空体积,将第一滤网7和第二滤网10倾斜设置方便刮料。Compared with the prior art, the first collector 4 and the second collector 5 of the present invention use upper cones and lower cones to butt together to form a cavity, which can reduce the internal space of the first collector 4 and the second collector 5. To reduce the void volume, the first filter screen 7 and the second filter screen 10 are tilted to facilitate scraping.
需要说明的是,本发明的弹性筛面的筛上区域与筛下区域之间的压差为500Pa-3000Pa。另外,为了保证该压差范围,本发明的第二滤网筛孔小于第一滤网筛孔,第二滤网的筛孔孔径为第一滤网筛孔孔径的65%-99%。It should be noted that the pressure difference between the upper screen area and the lower screen area of the elastic screen surface of the present invention is 500Pa-3000Pa. In addition, in order to ensure this pressure difference range, the mesh openings of the second filter mesh of the present invention are smaller than the mesh openings of the first filter mesh, and the mesh opening diameter of the second filter mesh is 65%-99% of the mesh opening diameter of the first filter mesh.
需要强调的是,本发明在物料收集单元的上一环节即第一收集器4的上方设有静电场区域,被负压气流吸附的微细粒物料先经过静电场区域;静电场区域用于使尘粒带负电,吸附尘粒后将其分离出来。It should be emphasized that the present invention is provided with an electrostatic field area above the first collector 4, which is the previous link of the material collection unit. The fine particles adsorbed by the negative pressure airflow first pass through the electrostatic field area; the electrostatic field area is used to Dust particles are negatively charged and are separated after adsorption.
具体地,本发明在吸附物料收集单元上方中设置静电场的目的是:通过调节静电场强度大小,使尘粒带负电,避免微细粒矿物带电,进而使带电尘粒被收集器壁吸附,减少进入滤网的颗粒量,强化除尘效果的同时,避免滤网堵塞。Specifically, the purpose of setting an electrostatic field above the adsorbed material collection unit in the present invention is to make the dust particles negatively charged by adjusting the intensity of the electrostatic field to prevent fine minerals from being charged, thereby causing the charged dust particles to be adsorbed by the collector wall, reducing The amount of particles entering the filter enhances the dust removal effect while avoiding clogging of the filter.
需要说明的是,调节静电场强度时,其调节的依据是:微细粒矿物与尘粒的表面电荷密度不同,尘粒的表面电荷密度大于微细粒物料的表面电荷密度,受到电场的作用力更强,同时尘粒的质量小于微细粒物料的质量,尘粒受到重力作用更小,导致其主要受到静电力更强,因此使得两者分离。It should be noted that when adjusting the strength of the electrostatic field, the basis for the adjustment is: the surface charge density of fine-grained minerals and dust particles is different. The surface charge density of dust particles is greater than the surface charge density of fine-grained materials, and the force exerted by the electric field is greater. Strong, and at the same time, the mass of dust particles is smaller than the mass of fine particles. The dust particles are less affected by gravity, which causes them to be mainly subject to stronger electrostatic force, thus causing the two to separate.
需要提示的是,1mm及以下微细粒物料中尘粒的清理过程为:一体化筛分设备运行一段时间后,停止给料,同时静电场区域内的电场强度降低,进而使得被吸附的尘粒脱附,实现该部分尘粒的清理。It should be noted that the cleaning process of dust particles in fine particles of 1mm and below is: after the integrated screening equipment has been running for a period of time, the feeding is stopped, and at the same time the electric field intensity in the electrostatic field area is reduced, thereby causing the adsorbed dust particles to Desorption realizes the cleaning of this part of dust particles.
为了提高弹性筛面2的筛分效果,本发明的弹性筛面2包括多块矩形单元筛面,多块矩形单元筛面平行放置,矩形单元筛面的长边方向与微细粒物料的流动方向垂直;沿微细粒物料的入料方向,单元筛面的开孔率逐渐减少。In order to improve the screening effect of the elastic screen surface 2, the elastic screen surface 2 of the present invention includes multiple rectangular unit screen surfaces. The multiple rectangular unit screen surfaces are placed in parallel. The long side direction of the rectangular unit screen surface is consistent with the flow direction of the fine particles. Vertical; along the feeding direction of fine-grained materials, the opening rate of the unit screen surface gradually decreases.
与现有技术相比,本发明的弹性筛面2采用多块矩形单元筛面构成,根据筛分物料的性质,更易更换和调整筛板,从而调整筛孔尺寸。具体地,弹性筛面2的筛孔大小可以根据实际生产需求进行更换,当对筛下细粒级含量占比要去较高时,可以通过更换筛板,减小筛孔尺寸,以适应生产需求;当对筛上粗粒级含量占比要求较高时,可以通过更换筛板,增大筛孔尺寸。Compared with the prior art, the elastic screen surface 2 of the present invention is composed of multiple rectangular unit screen surfaces. According to the properties of the screened materials, it is easier to replace and adjust the screen plate, thereby adjusting the screen hole size. Specifically, the size of the sieve holes of the elastic screen surface 2 can be changed according to actual production needs. When the proportion of fine particles under the screen is to be higher, the sieve plate can be replaced to reduce the size of the sieve holes to adapt to production. demand; when the proportion of coarse particles on the screen is required to be high, the screen hole size can be increased by replacing the screen plate.
需要注意的是,为了提高筛分效果,本发明的弹性筛面2采用聚氨酯材料。与现有技术相比,本发明的弹性筛面2采用聚氨酯,是因为聚氨酯为弹性材料,其能够保证弹性筛面2在筛分时其筛孔能够发生变形,从而避免微细粒物料卡堵筛孔。It should be noted that in order to improve the screening effect, the elastic screen surface 2 of the present invention uses polyurethane material. Compared with the existing technology, the elastic screen surface 2 of the present invention uses polyurethane because polyurethane is an elastic material, which can ensure that the mesh holes of the elastic screen surface 2 can be deformed during screening, thereby preventing fine particles from blocking the screen. hole.
需要指出的是,本发明的弹性筛面2沿入料方向呈倾斜设置,弹性筛面2的倾斜角度为3-8°。将弹性筛面2的倾斜角度控制在3-8°的范围内是因为:弹性筛面2的倾斜角度过小不利于筛分过程中物料向前移动;弹性筛面2的倾斜角度过大时,物料在筛面停留时间短,来不及透筛就成为筛上产品排出。It should be pointed out that the elastic screen surface 2 of the present invention is inclined along the material feeding direction, and the inclination angle of the elastic screen surface 2 is 3-8°. The inclination angle of the elastic screen surface 2 is controlled within the range of 3-8° because: the inclination angle of the elastic screen surface 2 is too small, which is not conducive to the forward movement of materials during the screening process; when the inclination angle of the elastic screen surface 2 is too large, , the material stays on the screen surface for a short time, and it is discharged as the product on the screen before it can pass through the screen.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明通过设置负压吸附装置,可以用于增加细粒级物料的透筛量,强化筛分效果,优化筛分环境。通过设置物料收集单元,可以回收细粒级物料,避免物料损失。(1) By setting up a negative pressure adsorption device, the present invention can be used to increase the amount of fine-grained materials passing through the screen, strengthen the screening effect, and optimize the screening environment. By setting up a material collection unit, fine-grained materials can be recycled to avoid material loss.
(2)本发明在第一收集器4的上方设置静电场,并在第二收集器5的下方设置静电除尘器12,输送过程除尘与终端除尘结合的双重静电除尘设计,不仅能够实现高效除尘的同时,并且能够增强筛面尘粒与微细粒矿物的有效分离,避免对环境造成污染。(2) The present invention sets an electrostatic field above the first collector 4 and sets an electrostatic precipitator 12 below the second collector 5. The dual electrostatic precipitator design that combines dust removal during transportation and terminal dust removal can not only achieve efficient dust removal At the same time, it can enhance the effective separation of dust particles and fine minerals on the screen surface to avoid environmental pollution.
(3)本发明提供的微细粒物料的分级与除尘一体化设备,能够实现微细粒矿物与尘粒的有效分离。(3) The integrated equipment for classification and dust removal of fine-grained materials provided by the present invention can achieve effective separation of fine-grained minerals and dust particles.
需要说明的是,本发明的微细粒物料干法分级与除尘一体化筛分设备还包括筛上物料19处理单元;筛上物料19处理单元用于处理弹性筛面2的筛上物,处理后使其成为1mm及以下的微细粒物。It should be noted that the dry classification and dust removal integrated screening equipment for fine-grained materials of the present invention also includes a processing unit for the over-the-sieve material 19; the over-the-sieve material 19 processing unit is used to process the over-the-sieve material on the elastic screen surface 2. Make it into fine particles of 1mm and below.
另一方面,本发明还提供了一种微细粒物料干法分级与除尘一体化筛分方法,采用上述的微细粒物料干法分级与除尘一体化筛分设备,该筛分方法包括以下步骤:On the other hand, the present invention also provides an integrated dry classification and dust removal screening method for micro-fine materials, using the above-mentioned integrated dry classification and dust removal screening equipment for micro-fine materials. The screening method includes the following steps:
步骤1、将微细粒物料投入分级激励装置1,开启负压吸附装置,微细粒物料经过1mm弹性筛的筛面,在负压吸附装置产生的负压气流的吸附作用下,1mm及以下微细粒物料通过弹性筛进入筛下物料收集装置;筛上物料进入筛上物料处理单元;Step 1. Put the fine-grained materials into the classification excitation device 1, turn on the negative pressure adsorption device, and the fine-grained materials pass through the screen surface of the 1mm elastic screen. Under the adsorption action of the negative pressure airflow generated by the negative pressure adsorption device, the fine particles 1mm and below The material passes through the elastic screen and enters the material collection device under the screen; the material above the screen enters the material processing unit above the screen;
步骤2、经筛上物料处理单元处理后,筛上物料19全部形成的1mm及以下微细粒物料。Step 2: After being processed by the material processing unit on the screen, all the fine particles of 1mm and below formed by the material 19 on the screen are processed.
在上述步骤2中,筛上物料19处理单元的具体处理过程参见下述实施例1。In the above step 2, please refer to the following embodiment 1 for the specific processing process of the screened material 19 processing unit.
实施例1Example 1
本实施例提供了筛上物料处理单元的一种可能的设计。具体地,该筛上物料处理单元包括颚式破碎机,筛上物料19处理前需先经颚式破碎机处理。This embodiment provides a possible design of the above-screen material processing unit. Specifically, the above-screen material processing unit includes a jaw crusher, and the above-screen material 19 needs to be processed by the jaw crusher before being processed.
本发明的筛上物料处理单元还包括第一级筛分机构、第二级筛分机构和第三级筛分机构;第一级筛分机构还与第三级筛分机构直接连接;第一级筛分机构包括第一双层筛分设备,第一双层筛分设备包括第一上层筛和第一下层筛;第二级筛分机构包括第二双层筛分设备,第二双层筛分设备包括第二上层筛和第二下层筛;第三级筛分机构包括单层筛分设备,单层筛分设备包括第三单层筛;第一下层筛、第二下层筛和第三单层筛的筛孔粒径均为1mm。The material processing unit on the screen of the present invention also includes a first-stage screening mechanism, a second-stage screening mechanism and a third-stage screening mechanism; the first-stage screening mechanism is also directly connected to the third-stage screening mechanism; the first-stage screening mechanism is also directly connected to the third-stage screening mechanism. The first-stage screening mechanism includes a first double-layer screening equipment, which includes a first upper screen and a first lower screen; the second-stage screening mechanism includes a second double-layer screening equipment, and the second double-layer screening equipment includes a first upper screen and a first lower screen. The layer screening equipment includes a second upper layer screen and a second lower layer screen; the third level screening mechanism includes a single layer screening equipment, and the single layer screening equipment includes a third single layer screen; the first lower layer screen, the second lower layer screen The mesh size of the third single-layer sieve is 1 mm.
需要说明的是,第一双层筛分设备包括第一上层筛和第一下层筛,第一下层筛的筛孔粒径大小为1mm;第二双层筛分设备包括第二上层筛和第二下层筛,第二下层筛的筛孔粒径大小为1mm;单层筛分设备包括第三单层筛,第三单层筛的筛孔粒径同样为1mm。第一上层筛与第一下层筛、第二上层筛与第二下层筛、第三单层筛的筛面大小、倾斜角度及振动频率均相等。It should be noted that the first double-layer screening equipment includes a first upper layer sieve and a first lower layer sieve. The mesh size of the first lower layer sieve is 1 mm; the second double-layer screening equipment includes a second upper layer sieve. and a second lower sieve, the sieve particle size of the second lower sieve is 1 mm; the single-layer screening equipment includes a third single-layer sieve, and the sieve particle size of the third single-layer sieve is also 1 mm. The screen surface size, inclination angle and vibration frequency of the first upper screen and the first lower screen, the second upper screen and the second lower screen, and the third single-layer screen are all equal.
现有技术中的微细粒矿物干法筛分的粒度界限主要为3mm和2mm,且对于微细粒矿物大多采用湿法筛分。湿法筛分对水的需求量较大,且对于粘土矿物分级易糊堵筛面,恶化筛分环境。另外,传统矿物进行原矿破碎筛分时,多采用单一振动筛分,筛分效率较低;微细粒矿物多次进入破碎磨矿机构,容易出现过粉磨现象,且增加了破碎与磨矿设备的功耗。The particle size limits of dry screening of fine-grained minerals in the prior art are mainly 3mm and 2mm, and wet screening is mostly used for fine-grained minerals. Wet screening requires a large amount of water, and when classifying clay minerals, it is easy to block the screen surface and worsen the screening environment. In addition, when traditional minerals are used for raw ore crushing and screening, a single vibrating screen is often used, and the screening efficiency is low; fine-grained minerals enter the crushing and grinding mechanism multiple times, which is prone to over-grinding, and additional crushing and grinding equipment are required. of power consumption.
与现有技术相比,本发明提供的第一级筛分机构、第二级筛分机构和第三级筛分机构构成了多级筛分机构,多级筛分机构采用第一双层筛分设备、第二双层筛分设备以及第三单层筛分设备的多级组合,能够实现微细粒矿物的1mm多级深度筛分,有效避免微细粒矿物的过粉磨现象。Compared with the existing technology, the first-stage screening mechanism, the second-stage screening mechanism and the third-stage screening mechanism provided by the present invention constitute a multi-stage screening mechanism. The multi-stage screening mechanism adopts the first double-layer screen. The multi-stage combination of sub-equipment, second double-layer screening equipment and third single-layer screening equipment can achieve 1mm multi-stage depth screening of fine-grained minerals, effectively avoiding over-grinding of fine-grained minerals.
为了对第一上层筛的筛上物进行破碎,使第一上层筛的筛上物最后通过第三级筛分机构,本发明的第一级筛分机构还包括破碎机;第一上层筛的筛上物进入破碎机,破碎后产物与第一下层筛的筛上产物混合进入第二级筛分机构,第一下层筛得到的1mm筛下产物进入第三级筛分机构。In order to crush the objects on the first upper screen so that the objects on the first upper screen finally pass through the third-stage screening mechanism, the first-stage screening mechanism of the present invention also includes a crusher; The products above the screen enter the crusher, and the crushed products are mixed with the products above the first lower screen and enter the second-stage screening mechanism. The products under the 1mm sieve obtained from the first lower screen enter the third-stage screening mechanism.
具体地,破碎机与第一上层筛连接,第一上层筛的筛上物进入破碎机进行破碎,得到的破碎后产物与第一下层筛的筛上产物混合并进入第二级筛分机构,而第一下层筛筛分得到的1mm筛下产物则直接进入第三级筛分机构,避免了该部分小于或等于1mm的微细粒矿物进入第二级筛分机构和第三级筛分机构,进而避免出现过粉磨现象,降低了破碎机与磨矿设备的功耗。Specifically, the crusher is connected to the first upper screen, and the objects above the first upper screen enter the crusher for crushing. The obtained crushed products are mixed with the products above the first lower screen and enter the second-stage screening mechanism. , and the products under 1mm screened by the first lower screen directly enter the third-stage screening mechanism, preventing this part of fine-grained minerals less than or equal to 1mm from entering the second-stage screening mechanism and third-stage screening. mechanism, thereby avoiding over-grinding and reducing the power consumption of the crusher and grinding equipment.
为了对第二上层筛的筛上物进行细碎,使第二上层筛的筛上产物形成闭路干法筛分,最终使第二上层筛的筛上物通过第三级筛分机构,本发明的第二级筛分机构还包括圆锥细碎机,第二上层筛的筛上产物进入圆锥细碎机,细碎后产物返回第二上层筛;第二双层筛分设备与圆锥细碎机构成第一闭路干法筛分。In order to finely crush the products on the second upper screen, form a closed-circuit dry screening process on the products on the second upper screen, and finally allow the products on the second upper screen to pass through the third-stage screening mechanism, the invention The second-stage screening mechanism also includes a cone tertiary crusher. The products above the second upper sieve enter the cone tertiary crusher, and the crushed products return to the second upper sieve. The second double-layer screening equipment and the cone tertiary crusher form the first closed-circuit dryer. method of screening.
具体地,本发明的第二级筛分机构还包括圆锥细碎机,圆锥细碎机与入料通道和出料通道均与第二上层筛连接,第二上层筛的筛上产物通过入料通道进入圆锥细碎机,细碎后通过出料通道返回第二上层筛,进行筛分,第二上层筛筛分得到的筛上产物继续进入圆锥细碎机,重复上述过程,而第二上层筛的筛下产物则进入第二下层筛进行1mm筛分,1mm筛分的筛下产物进入第三级筛分机构。Specifically, the second-stage screening mechanism of the present invention also includes a cone crusher. The cone crusher, the inlet channel and the outlet channel are all connected to the second upper screen. The products on the second upper screen enter through the inlet channel. Cone crusher, after fine crushing, returns to the second upper screen through the discharge channel for screening. The products above the screen obtained by the second upper screen continue to enter the cone crusher, and the above process is repeated, while the products under the second upper screen are Then it enters the second lower sieve for 1mm screening, and the 1mm screened products enter the third-level screening mechanism.
与现有技术相比,本发明通过设置圆锥细碎机,使圆锥细碎机与第二双层筛分设备构成第一闭路干法筛分,保证第二上层筛的筛上产物能够被细碎处理,然后返回第二上层筛上,筛分后进入到第三级筛分机构。Compared with the existing technology, the present invention sets up a cone crusher so that the cone crusher and the second double-layer screening equipment form the first closed-circuit dry screening, ensuring that the products on the second upper screen can be finely crushed. Then it returns to the second upper screen, and then enters the third-level screening mechanism after screening.
为了使进入多级干法筛分系统的原矿最终都成为小于或等于1mm的微细粒矿物,本发明的第三级筛分机构还包括磨矿机,磨矿机分别与第二下层筛、第三单层筛连接;第二下层筛的筛上产物进入磨矿机,磨矿后产物与第二下层筛的筛下产物混合,进入第三级筛分机构;第三单层筛进行1mm筛分后,第三单层筛的筛上产物返回磨矿机,筛下产物进入分选作业;第三单层筛分设备与磨矿机构成第二闭路干法筛分。In order to make the raw ore entering the multi-stage dry screening system eventually become fine-grained minerals less than or equal to 1mm, the third-stage screening mechanism of the present invention also includes a grinding machine, which is connected to the second lower screen and the third-level screen respectively. The three single-layer screens are connected; the products above the second lower screen enter the grinding machine, and the ground products are mixed with the products under the second lower screen and enter the third-stage screening mechanism; the third single-layer screen performs a 1mm sieve After separation, the products above the third single-layer screen return to the grinding machine, and the products below the screen enter the sorting operation; the third single-layer screening equipment and the grinding machine form a second closed-circuit dry screening.
与现有技术相比,本发明提供的磨矿机与第三单层筛分设备构成第二闭路干法筛分,第三单层筛的筛上产物进入磨矿机进行磨矿,磨矿后产物返回第三单层筛,第三单层筛进行1mm筛分后,筛下产物为小于或等于1mm的微细粒矿物,该部分微细粒矿物进入到分选作业环节,而筛上物则再次进入磨矿机中;采用本发明的多级干法筛分系统,经过多级筛分后,得到的产物均未粒径小于或等于1mm的微细粒矿物,该系统工艺紧凑,筛分效率高。Compared with the existing technology, the grinding machine provided by the present invention and the third single-layer screening equipment constitute a second closed-circuit dry screening, and the products above the third single-layer screen enter the grinding machine for grinding. The final product returns to the third single-layer sieve. After the third single-layer sieve performs 1mm screening, the products under the sieve are fine-grained minerals less than or equal to 1mm. This part of the fine-grained minerals enters the sorting operation, while the objects on the sieve are Enter the grinding machine again; using the multi-stage dry screening system of the present invention, after multi-stage screening, the obtained products have no fine minerals with a particle size less than or equal to 1 mm. The system has a compact process and high screening efficiency. high.
需要说明的是,第一上层筛和第二上层筛的筛孔粒径采用100mm,50mm,25mm,13mm,6mm或3mm一种;第一上层筛的筛孔粒径大于第二上层筛的筛孔粒径。It should be noted that the sieve particle size of the first upper sieve and the second upper sieve is 100mm, 50mm, 25mm, 13mm, 6mm or 3mm; the sieve particle size of the first upper sieve is larger than that of the second upper sieve. Pore size.
为了保证粒径小于或等于1mm的微细粒物料能够顺利通过粒径为1mm的筛孔,避免堵孔,本发明的第一双层筛分设备和第二双层筛分设备均采用双层弛张筛;单层筛分设备采用单层弛张筛;双层弛张筛和单层弛张筛的筛面均采用弹性筛面2,弹性筛面2分别与动力装置连接。In order to ensure that fine-grained materials with a particle size less than or equal to 1 mm can smoothly pass through the sieve holes with a particle size of 1 mm and avoid clogging, the first double-layer screening equipment and the second double-layer screening equipment of the present invention both adopt double-layer screening equipment. The single-layer screening equipment uses a single-layer relaxation screen; the screen surfaces of the double-layer relaxation screen and the single-layer relaxation screen adopt elastic screen surface 2, and the elastic screen surface 2 is connected to the power device respectively.
与现有技术相比,本发明的双层弛张筛和单层弛张筛的筛面均与动力装置连接,动力装置用于对各个弛张筛提供动力,使其筛孔变形,筛上的小于或等于1mm的末煤能够顺利通过弹性筛的筛面。Compared with the prior art, the screen surfaces of the double-layer relaxation screen and the single-layer relaxation screen of the present invention are connected to a power device. The power device is used to provide power to each relaxation screen to deform its mesh holes. The coal dust less than or equal to 1mm can pass through the screen surface of the elastic screen smoothly.
需要强调的是,本发明的双层弛张筛和单层弛张筛的筛面均呈倾斜设置,弹性筛面2的倾斜角度为3-8°,将弹性筛面2的倾斜角度控制在3-8°的范围内是因为:弹性筛面2的倾斜角度过小不利于筛分过程中物料向前移动;弹性筛面2的倾斜角度过大时,物料在筛面停留时间短,来不及透筛就成为筛上产品排出。It should be emphasized that the screen surfaces of the double-layer relaxation screen and the single-layer relaxation screen of the present invention are all inclined, and the inclination angle of the elastic screen surface 2 is 3-8°. The inclination angle of the elastic screen surface 2 is controlled at The reason for the range of 3-8° is that: the inclination angle of the elastic screen surface 2 is too small, which is not conducive to the forward movement of the material during the screening process; when the inclination angle of the elastic screen surface 2 is too large, the material stays on the screen surface for a short time and is too late. After passing through the sieve, it becomes the product on the sieve and is discharged.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。The above are only preferred specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto. Any person familiar with the technical field can easily think of changes or modifications within the technical scope disclosed in the present invention. All substitutions are within the scope of the present invention.
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| CN111186839A (en) * | 2020-02-27 | 2020-05-22 | 中国科学院化学研究所 | Reaction system and method for preparing nano-pore carbon material by using ternary low-temperature molten salt |
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| CN202725512U (en) * | 2012-08-01 | 2013-02-13 | 安徽理工大学 | Full-grain high-efficiency dry coal preparation system for power coal separation |
| CN106362950A (en) * | 2016-12-11 | 2017-02-01 | 华北理工大学 | Rotational flow negative pressure sieve |
| CN107537764A (en) * | 2017-09-27 | 2018-01-05 | 中国矿业大学 | A kind of Coupled Rigid-flexible elastic rod vibratory sieve |
| CN111186839A (en) * | 2020-02-27 | 2020-05-22 | 中国科学院化学研究所 | Reaction system and method for preparing nano-pore carbon material by using ternary low-temperature molten salt |
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