CN113182070B - Novel dry type wind-magnetic combined magnetic separator - Google Patents
Novel dry type wind-magnetic combined magnetic separator Download PDFInfo
- Publication number
- CN113182070B CN113182070B CN202110520795.9A CN202110520795A CN113182070B CN 113182070 B CN113182070 B CN 113182070B CN 202110520795 A CN202110520795 A CN 202110520795A CN 113182070 B CN113182070 B CN 113182070B
- Authority
- CN
- China
- Prior art keywords
- magnetic
- sorting
- hopper
- particle collection
- collection system
- 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.)
- Active
Links
Images
Classifications
-
- 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
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
-
- 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
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/01—Selective separation of solid materials carried by, or dispersed in, gas currents using gravity
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
本发明公开了一种新型干式风磁联合磁选机,包括分选腔,所述分选腔的一侧设有用于吸附磁性颗粒的磁辊组件,所述分选腔内靠近磁辊组件的位置设有用于破坏磁团聚的导流板组件;所述分选腔的一端连接鼓风机,分选腔的另一端分别连接磁性颗粒收集系统和非磁性颗粒收集系统;所述鼓风机的一侧设置入料斗,入料斗通过入料口与分选腔连通,入料斗的上方设置磁性颗粒收集系统。本发明通过进风口进风,带动通过入料口进入分选腔内的原料形成气固两相流,通过磁辊、导流板的作用,有效破坏磁团聚,使物料充分暴露在风力、重力、磁力的作用中,对细粒级矿物进行有效分选,提升了磁选效率。
The invention discloses a novel dry-type combined air-magnetic separator, comprising a sorting cavity, one side of the sorting cavity is provided with a magnetic roller assembly for adsorbing magnetic particles, and the interior of the sorting cavity is close to the magnetic roller assembly A deflector assembly for destroying magnetic agglomeration is provided at the position of the separator; one end of the sorting chamber is connected to the blower, and the other end of the sorting chamber is respectively connected to the magnetic particle collection system and the non-magnetic particle collection system; one side of the blower is provided with The feeding hopper is connected with the sorting cavity through the feeding port, and a magnetic particle collection system is set above the feeding hopper. In the invention, the air enters through the air inlet to drive the raw materials entering the separation chamber through the material inlet to form a gas-solid two-phase flow. , Under the action of magnetic force, the fine-grained minerals are effectively separated, which improves the magnetic separation efficiency.
Description
技术领域technical field
本发明涉及一种磁选设备,尤其涉及一种新型干式风磁联合磁选机。The invention relates to a magnetic separator, in particular to a novel dry-type wind-magnetic combined magnetic separator.
背景技术Background technique
磁性物质,特别是强磁性细粒级矿物,在被磁化后存在磁偶极子力,导致磁性颗粒相互吸引而团聚,磁性颗粒与非磁性颗粒难以被有效区分。现有的磁选技术通常采用干式磁选机或湿式磁选机进行分选,干式磁选机要求被分选的物质干燥,颗粒之间可以自由移动、成独立的自由状态,因此在面对磁性物质团聚时会影响磁选效果,甚至会造成不可分选的后果;湿式磁选机要使用液体作为稀释剂提高分选效率,因此不能大面积使用,特别是在干旱地区应用受限,且分选的颗粒还需要脱水干燥,导致湿式磁选机在寒冷缺水地区运行困难。Magnetic substances, especially ferromagnetic fine-grained minerals, have magnetic dipole forces after being magnetized, which causes magnetic particles to attract each other and agglomerate, and it is difficult to effectively distinguish magnetic particles from non-magnetic particles. The existing magnetic separation technology usually uses a dry magnetic separator or a wet magnetic separator for separation. The dry magnetic separator requires the material to be separated to be dry, and the particles can move freely and form an independent free state. In the face of the agglomeration of magnetic substances, it will affect the magnetic separation effect, and even cause the consequences of non-separation; the wet magnetic separator uses liquid as a diluent to improve the separation efficiency, so it cannot be used in a large area, especially in arid areas. In addition, the sorted particles also need to be dehydrated and dried, which makes it difficult for the wet magnetic separator to operate in cold and water-deficient areas.
发明内容SUMMARY OF THE INVENTION
发明目的:本发明的目的在于提供一种在干式的条件下可以破坏磁团聚以解决细粒级矿物选别问题的新型干式风磁联合磁选机。Purpose of the invention: The purpose of the present invention is to provide a new type of dry air-magnetic combined magnetic separator that can destroy magnetic agglomeration under dry conditions to solve the problem of fine-grained mineral separation.
技术方案:本发明的一种新型干式风磁联合磁选机,包括分选腔,所述分选腔的一侧设有用于吸附磁性颗粒的磁辊组件,所述分选腔内靠近磁辊组件的位置设有用于破坏磁团聚的导流板组件;所述分选腔的一端连接鼓风机,分选腔的另一端分别连接磁性颗粒收集系统和非磁性颗粒收集系统;所述鼓风机的一侧设置入料斗,入料斗通过入料口与分选腔连通,入料斗的上方设置磁性颗粒收集系统。Technical solution: A new type of dry wind-magnetic combined magnetic separator of the present invention includes a separation chamber, one side of the separation chamber is provided with a magnetic roller assembly for adsorbing magnetic particles, and the separation chamber is close to the magnetic The position of the roller assembly is provided with a deflector assembly for destroying magnetic agglomeration; one end of the sorting chamber is connected to the blower, and the other end of the sorting chamber is respectively connected to the magnetic particle collection system and the non-magnetic particle collection system; one end of the blower is connected. The feeding hopper is set on the side, the feeding hopper is connected with the sorting cavity through the feeding port, and the magnetic particle collecting system is set above the feeding hopper.
进一步的,所述磁辊组件包括电机和两组形状一致的磁辊,两组磁辊上下平行设置在分选腔的一侧,所述电机带动两组磁辊进行同向同速转动;每组磁辊包括对称设置的磁性段和非磁性段,当其中一组磁辊的磁性段靠近分选腔时,另一组磁辊的磁性段远离分选腔。由于两组磁辊的设置方向完全相反,且每一个单独的磁辊具有一半有磁性的工作区域,且两磁辊的工作区域相反,因此在同向同速运转的情况下,可以保证两磁辊中在同一时间至少有一个磁辊处于工作区域,从而对磁性颗粒粒子进行吸附。Further, the magnet roller assembly includes a motor and two sets of magnet rollers with the same shape, the two sets of magnet rollers are arranged in parallel on one side of the sorting cavity, and the motor drives the two sets of magnet rollers to rotate in the same direction and speed; The set of magnetic rollers includes symmetrically arranged magnetic segments and non-magnetic segments, and when the magnetic segments of one set of magnet rollers are close to the sorting cavity, the magnetic segments of the other set of magnet rolls are far away from the sorting cavity. Because the setting directions of the two sets of magnetic rollers are completely opposite, and each individual magnetic roller has half of the magnetic working area, and the working areas of the two magnetic rollers are opposite, so in the case of running in the same direction and the same speed, the two magnetic rollers can be guaranteed. At least one magnetic roller in the rollers is in the working area at the same time, so as to attract the magnetic particles.
进一步的,所述的磁辊与分选腔的侧壁间隙为3~5mm,优选为3mm,位于上侧的磁辊的磁场强度大于位于下侧的磁辊的磁场强度。所述磁辊在分选腔中心的磁场强度达到0.8T-1.2T,其中,位于上侧的磁辊的磁场强度大于位于下侧的磁辊的磁场强度,磁场的差异可以更好的捕捉磁场颗粒,提升磁选效率,优选的,位于上方的磁辊在分选腔外壳的圆心及磁辊圆心的连线与分选腔中心的交点上的磁场强度达到1.2T,位于下方的磁辊在分选腔外壳的圆心及磁辊圆心的连线与分选腔中心的交点上的磁场强度达到1.0T。Further, the gap between the magnetic roller and the side wall of the sorting cavity is 3-5 mm, preferably 3 mm, and the magnetic field intensity of the magnetic roller located on the upper side is greater than that of the magnetic roller located on the lower side. The magnetic field strength of the magnetic roller in the center of the sorting cavity reaches 0.8T-1.2T, wherein the magnetic field strength of the magnetic roller located on the upper side is greater than that of the magnetic roller located on the lower side, and the difference of the magnetic field can better capture the magnetic field Particles, improve the magnetic separation efficiency, preferably, the magnetic field strength of the upper magnetic roller at the intersection of the center of the separation chamber shell and the line connecting the magnetic roller center and the center of the separation chamber reaches 1.2T, and the magnetic roller at the lower The magnetic field intensity at the intersection of the center of the separation chamber shell and the center of the magnetic roller and the center of the separation chamber reaches 1.0T.
进一步的,所述导流板组件由若干等长的导流板组成,导流板均匀分布在分选腔的内壁之间,相邻的导流板之间形成用于分散颗粒的通道。导流板一方面起到导流作用,另一方面也是为了使得物料在导流板中间不断碰撞,破坏磁团聚,且也延长了物料暴露在分选腔内的时间。Further, the baffle assembly is composed of several equal-length baffles, the baffles are evenly distributed between the inner walls of the sorting cavity, and channels for dispersing particles are formed between adjacent baffles. On the one hand, the deflector plays a guiding role, and on the other hand, it is also to make the material continuously collide in the middle of the deflector, destroy the magnetic agglomeration, and also prolong the time that the material is exposed in the sorting chamber.
进一步的,所述磁性颗粒收集系统包括第一旋风分离器和磁性颗粒集料斗,所述第一旋风分离器的进料口与分选腔的一端连接,第一旋风分离器的出料口正对磁性颗粒集料斗的进料端。其中,磁性颗粒集料斗的底部与入料斗的上端面之间呈40~50°设置,优选为45°,磁性颗粒集料斗的一侧设有用于将磁性颗粒返回入料斗的挡板,挡板可以通过卡扣与合页结构进行设置,实现可拆卸的效果,挡板拆除后便于物料的连续多次选别,可以保证将筛选的颗粒返回至分选腔内进行重复筛选,提高磁性颗粒的纯度。Further, the magnetic particle collection system includes a first cyclone separator and a magnetic particle collection hopper, the feed port of the first cyclone separator is connected to one end of the sorting cavity, and the discharge port of the first cyclone separator is directly On the feed end of the magnetic particle collection hopper. Wherein, the distance between the bottom of the magnetic particle collecting hopper and the upper end face of the feeding hopper is 40° to 50°, preferably 45°, and one side of the magnetic particle collecting hopper is provided with a baffle for returning the magnetic particles into the hopper. It can be set through the buckle and hinge structure to achieve the effect of detachment. After the baffle is removed, it is convenient for the continuous and multiple sorting of materials, which can ensure that the screened particles are returned to the sorting chamber for repeated screening, and the magnetic particles are improved. purity.
进一步的,所述非磁性颗粒收集系统包括第二旋分分离器和非磁性颗粒集料斗,所述第二旋风分离器的进料口与分选腔的一端连接,第二旋风分离器的出料口正对非磁性颗粒集料斗的进料端。Further, the non-magnetic particle collection system includes a second cyclone separator and a non-magnetic particle collection hopper, the feeding port of the second cyclone separator is connected to one end of the sorting cavity, and the outlet of the second cyclone separator is The material port is facing the feeding end of the non-magnetic particle collection hopper.
进一步的,所述分选腔底部设有向上凸起的粗料排料口,所述粗料排料口设置在入料斗与导流板组件之间,粗料排料口的下方设有粗料集料斗。保证风力无法带动的大颗粒物料滑落后进行储存放置。Further, the bottom of the sorting cavity is provided with an upwardly protruding coarse material discharge port, the coarse material discharge port is arranged between the hopper and the deflector assembly, and a coarse material discharge port is provided below the coarse material discharge port. Material collection hopper. Ensure that the large particles that cannot be driven by the wind will be stored and placed after sliding.
进一步的,还包括用于吸收风尘的袋式除尘器,所述袋式除尘器的进风口分别与磁性颗粒收集系统的第一旋风分离器和非磁性颗粒收集系统的第二旋风分离器连接。可以将旋风分离器处理后的风尘杂质进行收集。Further, it also includes a bag filter for absorbing wind dust, the air inlet of the bag filter is respectively connected with the first cyclone separator of the magnetic particle collection system and the second cyclone separator of the non-magnetic particle collection system. The dust impurities treated by the cyclone can be collected.
进一步的,所述入料斗内的入料粒径为5~11μm;所述分选腔内管壁粗糙度为3.2~5.0μm。入料粒度大小保证了选别效果,粗糙度则可以保证尽量减小分选过程中的能力损耗。Further, the particle size of the feeding material in the feeding hopper is 5-11 μm; the roughness of the tube wall in the sorting cavity is 3.2-5.0 μm. The size of the incoming material ensures the sorting effect, and the roughness can ensure that the capacity loss in the sorting process is minimized.
本发明的工作原理:原料在风力的作用下进入分选腔,粗颗粒在重力作用下,下滑进入粗料集料斗;而细颗粒经过第一处导流板发生一定碰撞,破坏颗粒的团聚,在风力引导下,颗粒进入磁辊工作区,其中磁性颗粒在磁力作用下被吸附在管壁上,非磁性颗粒则在风力作用下继续向上;在第一个磁辊转至非工作区时,磁性颗粒由管壁脱落,在风力作用下向上,此时第二个磁辊恰转至工作区,磁性颗粒在磁力作用下进入磁性颗粒集料斗,而非磁性颗粒则不受磁力影响下进入非磁性颗粒集料斗。The working principle of the invention is as follows: the raw materials enter the sorting chamber under the action of the wind force, and the coarse particles slide down into the coarse material collection hopper under the action of gravity; while the fine particles collide with the first deflector to destroy the agglomeration of the particles. Under the guidance of the wind, the particles enter the working area of the magnetic roller, where the magnetic particles are adsorbed on the pipe wall under the action of the magnetic force, and the non-magnetic particles continue to move upward under the action of the wind; when the first magnetic roller turns to the non-working area, The magnetic particles fall off the pipe wall and move upward under the action of the wind. At this time, the second magnetic roller just turns to the working area, and the magnetic particles enter the magnetic particle collection hopper under the action of the magnetic force, while the non-magnetic particles enter the non-magnetic particle under the influence of the magnetic force. Magnetic particle collection hopper.
有益效果:本发明和现有技术相比,具有如下显著优点:(1)本发明通过进风口进风,带动通过入料口进入分选腔内的原料形成气固两相流,通过磁辊、导流板的作用,有效破坏磁团聚,使物料充分暴露在风力、重力、磁力的作用中,对细粒级矿物进行有效分选,提升了磁选效率;(2)本发明在磁性产品集料斗处设有可拆卸挡板,磁性产品可连续多次进入分选腔内,优化选别效果,解决了一次磁选效果不佳,多次磁选步骤繁琐的问题。Beneficial effects: Compared with the prior art, the present invention has the following significant advantages: (1) The present invention enters the air through the air inlet to drive the raw materials entering the sorting cavity through the feeding port to form a gas-solid two-phase flow, and passes through the magnetic roller. , The role of the deflector effectively destroys the magnetic agglomeration, so that the material is fully exposed to the action of wind, gravity and magnetic force, and the fine-grained minerals are effectively sorted, and the magnetic separation efficiency is improved; (2) The present invention is used in magnetic products. There is a detachable baffle plate at the collecting hopper, and the magnetic products can enter the separation chamber for many times in a row to optimize the separation effect and solve the problems of poor magnetic separation effect once and cumbersome magnetic separation steps for multiple times.
附图说明Description of drawings
图1为本发明装置结构示意图;1 is a schematic diagram of the structure of the device of the present invention;
图2为本发明磁性颗粒受力示意图;Fig. 2 is the schematic diagram of the force of the magnetic particle of the present invention;
图3为本发明磁辊位置示意图;3 is a schematic diagram of the position of the magnetic roller of the present invention;
图4为本发明导流板位置示意图;4 is a schematic diagram of the position of the deflector of the present invention;
图5为本发明磁辊结构示意图。FIG. 5 is a schematic diagram of the structure of the magnetic roller of the present invention.
具体实施方式Detailed ways
下面结合附图和实施例对本发明作进一步说明。The present invention will be further described below with reference to the accompanying drawings and embodiments.
如图1所示的一种新型干式风磁联合磁选机,包括分选腔1,分选腔1呈弧状,内部为方形管道,尺寸为80mm*125mm,分选腔管壁粗糙度要求大于3.2μm;分选腔1的一端连接鼓风机4,鼓风机4正对方向为进风方向,入口风速大于0.11m/s,入料的临界料气比为0.45,在鼓风机4前方有入料斗7,入料斗7通过入料口8与分选腔1连通,入料口8前方设有一向上凸起缺口,为粗料排料口11,粗料排料口11下方为粗料集料斗12,保证风力无法带动的大颗粒物料滑落后放置。分选腔1的一侧设有用于吸附磁性颗粒的磁辊组件2,分选腔1内靠近磁辊组件2的位置设有用于破坏磁团聚的导流板组件3,分选腔1的另一端分别连接磁性颗粒收集系统5和非磁性颗粒收集系统6。As shown in Figure 1, a new type of dry air-magnetic combined magnetic separator includes a
参见图3和图5,磁辊组件2包括电机21和两组形状一致的磁辊22,两组磁辊22上下平行设置在分选腔1的一侧,为了保证转动的均匀性,两磁辊圆心处在与弧形分选腔1的壳体圆心相连,与水平方向上下各呈30°夹角的连线上,且与分选腔1外部距离为3mm,两组磁辊22由电机11通过皮带轮带动作同向同速运动,每组磁辊22包括对称设置的磁性段221和非磁性段222,共同组成圆柱体结构,使得每个磁辊具有一半有磁性的工作区域,两组磁辊22的磁性段设置方向相反,当其中一组磁辊22的磁性段221靠近分选腔1时,另一组磁辊22的磁性段221远离分选腔1,工作时保证两磁辊同一时间最少一磁辊处于工作区域,保证磁性颗粒至少受其中一个磁辊的磁场影响,实现充分捕捉分选腔中的磁性颗粒。其中,位于上方的磁辊的磁场强度略大于位于下方的磁辊的磁场强度,以便更好的捕捉可能经碰撞出现的微小磁性颗粒。上方的磁辊在分选腔中心的磁场强度为1.2T,下方的磁辊在分选腔中心的磁场强度为1.0T,两个磁辊配合可以更好的捕捉磁团聚被破坏后出现的细小磁性颗粒。3 and 5 , the magnet roller assembly 2 includes a
参见图4,导流板组件3设置两组,由若干等长的导流板31组成,两组导流板组件3分别设于腔体中两磁辊水平高度的下方,每组导流板31均匀分布在分选腔1的内壁之间,等间隔布置,导流板31的长度与分选腔的管壁等长,相邻的导流板31之间形成用于分散颗粒的通道32。导流板组件使得物料在导流板中间不断碰撞,破坏磁团聚,且也延长了物料暴露在分选腔的时间,导流板还起到引导风力方向和引导非磁性颗粒运动方向的作用,参见图2分选腔内原料颗粒的受力作用示意图,非磁性颗粒在风力及惯性作用下可继续向上进入左侧的非磁性颗粒收集系统6,而磁性颗粒则在磁力作用下发生偏转,进入右侧的磁性颗粒收集系统5,且由于磁力的作用使得磁性颗粒也可以尽量沿靠近磁辊一侧的内壁移动,减少了进入左侧非磁性颗粒收集系统6的可能。Referring to FIG. 4 , there are two groups of
参见图1,磁性颗粒收集系统5包括第一旋风分离器51和磁性颗粒集料斗52,第一旋风分离器51的进料口与分选腔1的一端连接,第一旋风分离器51的出料口正对磁性颗粒集料斗52的进料端;磁性颗粒集料斗52设置在入料斗7的正上方,磁性颗粒集料斗52底部为45°倾斜设置,一侧设有可拆卸的挡板521,收集的磁性颗粒可在拆除挡板后,在重力作用下滑入入料斗7中再次分选,提高选别精度。非磁性颗粒收集系统6包括第二旋分分离器61和非磁性颗粒集料斗62,第二旋风分离器61的进料口与分选腔1的一端连接,第二旋风分离器61的出料口正对非磁性颗粒集料斗62的进料端。第一旋风分离器51和第二旋风分离器61的出风口连接有袋式除尘器9,袋式除尘器9将产生的风尘进行收集。Referring to FIG. 1 , the magnetic
本发明的干式风磁联合磁选机的工作方式为:工作时首先启动风机4,磁辊组件3及第一旋风分离器51和第二旋风分离器61。将物料置于入料斗7,物料由入料口8进入分选腔1内部,在风力带动下形成气固两相流向上进入弧形的分选腔1,粗料在重力作用下滑落,由凸起的粗料排料口11进入粗料集料斗12;气固两相流在导流板31内碰撞,有效破坏细小颗粒的团聚,使其充分暴露在下方的磁辊的选别中,磁性颗粒此时被磁力吸引吸附在管壁上,而非磁性颗粒则由导流板31引导后,在风力作用下垂直向上进入非磁性颗粒收集系统6,磁性颗粒在下方的磁辊转至非磁性区域后脱落后亦向上经过导流板进入二次分选区,在上方磁辊的磁力和风力的作用下,磁性颗粒得到充分暴露,被磁力吸引,脱离风力作用,从向上的气流中脱离出来,吸附在管壁上,待上方的磁辊转至非磁性区域后,此时的磁性颗粒被风力带动进入磁性颗粒收集系统5;当需要提高产品纯度时,拆除挡板521将收集的磁性产品重复返回分选腔1内,优化选别效果。The working mode of the dry air-magnetic combined magnetic separator of the present invention is as follows: when working, the fan 4 , the
使用平均粒径D50为10.3μm的钢渣及平均粒径D50为5.31μm的镍渣,在入口风力为0.11m/s,料气比为0.45的情况下,分别进行了12组实验,验证了合理设置两磁辊磁场强度对选别效果的影响,具体参见下表1。Using steel slag with an average particle size D50 of 10.3 μm and nickel slag with an average particle size D50 of 5.31 μm, 12 sets of experiments were carried out under the condition that the inlet air force was 0.11 m/s and the material-to-gas ratio was 0.45, and the reasonableness was verified. Set the influence of the magnetic field strength of the two magnetic rollers on the sorting effect, see Table 1 for details.
表1Table 1
由表1可知,随着磁场强度的上升,不论是对钢渣还是镍渣,磁选机的磁选效率均得到了有效提高,在磁辊的强度达到0.8-1.0T的情况下,磁选的效率达到峰值,在75%-80%之间。It can be seen from Table 1 that with the increase of the magnetic field strength, the magnetic separation efficiency of the magnetic separator has been effectively improved whether it is for steel slag or nickel slag. When the strength of the magnetic roller reaches 0.8-1.0T, the magnetic separation efficiency Efficiency peaks between 75%-80%.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110520795.9A CN113182070B (en) | 2021-05-13 | 2021-05-13 | Novel dry type wind-magnetic combined magnetic separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110520795.9A CN113182070B (en) | 2021-05-13 | 2021-05-13 | Novel dry type wind-magnetic combined magnetic separator |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113182070A CN113182070A (en) | 2021-07-30 |
CN113182070B true CN113182070B (en) | 2022-09-30 |
Family
ID=76981388
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110520795.9A Active CN113182070B (en) | 2021-05-13 | 2021-05-13 | Novel dry type wind-magnetic combined magnetic separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113182070B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114602649B (en) * | 2022-03-15 | 2024-03-26 | 鞍钢集团北京研究院有限公司 | Magnetic separation and method based on wind-gravity-magnetic composite force field |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2077631A (en) * | 1980-06-05 | 1981-12-23 | Tongeren U K Ltd Van | Third stage separator system for fluidised catalytic cracking unit in oil refining, and method of operating same |
JP3128527U (en) * | 2006-09-29 | 2007-01-18 | 駿富達科技股▲ふん▼有限公司 | Magnetic fine particle adsorption roller |
EP2289628B1 (en) * | 2009-08-27 | 2014-06-18 | Lux Magnet | Magnetic separator with eddy current, with optimised trajectory and interaction zone of the particles |
CN204018012U (en) * | 2014-08-15 | 2014-12-17 | 张珂 | A kind of dry type wind magnetic separator |
CN204351007U (en) * | 2014-12-05 | 2015-05-27 | 甘肃正阳食品有限公司 | A kind of potato full-powder classification conveying device |
CN204503270U (en) * | 2015-03-31 | 2015-07-29 | 河北纳诺新材料科技有限公司 | A kind of papermaking Producing Titanium Dioxide airslide disintegrating mill |
CN107309174A (en) * | 2017-08-25 | 2017-11-03 | 长沙深湘通用机器有限公司 | Sorting unit |
CN107971223B (en) * | 2017-11-30 | 2023-09-12 | 河南小威环境科技有限公司 | Particle wind power separator, copper-aluminum separation treatment system and method for lithium battery |
CN107803340A (en) * | 2017-12-08 | 2018-03-16 | 承德天宝矿业集团有限公司 | The method and system of phosphorus composition is extracted from iron ore tailings |
CN212227515U (en) * | 2020-03-17 | 2020-12-25 | 济源市京华工程陶瓷材料有限公司 | A secondary drying and classifying device for ceramic granulated powder |
-
2021
- 2021-05-13 CN CN202110520795.9A patent/CN113182070B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN113182070A (en) | 2021-07-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113182070B (en) | Novel dry type wind-magnetic combined magnetic separator | |
CN106669888A (en) | Efficient roller pressing grinding station and technique thereof | |
CN101362036A (en) | Gas-solid separation method and device using pipe sedimentation | |
CN114602649B (en) | Magnetic separation and method based on wind-gravity-magnetic composite force field | |
CN117358382A (en) | Fine-granularity abrasive air flow crushing device and method with adjustable particle shape | |
JP3807741B1 (en) | Reversing dust removing device with a large number of current plates | |
CN217411512U (en) | Dry grinding and dry separation system for iron-containing slag powder of steel slag | |
CN102728461B (en) | Micro powder fine powder dry-type magnet separator | |
CN110339941B (en) | A turbulent flat magnetic separator | |
CN110976288A (en) | Energy-saving environment-friendly efficient powder concentrator | |
CN110877299A (en) | A thorough piece-rate system that is used for abrasive material and non-magnetic impurity of foundry goods shot-blast | |
CN201659025U (en) | Novel iron ore concentrates concentrating and magnetic separating machine | |
CN203235383U (en) | Horizontal electrostatic precipitator integrating gravity and cyclone dust removal | |
CN114713377B (en) | A rotating triboelectric separation device and separation method of flexible cluster rods with airflow coordination | |
CN211587521U (en) | Energy-saving environment-friendly efficient powder concentrator | |
CN203875012U (en) | Degglomerator thick-fine powder air flow separation device | |
CN209735145U (en) | Inertia dust remover | |
CN112791827B (en) | Automatic ore dressing equipment for low-grade barium ore | |
CN103263815A (en) | Horizontal electric dust collector with integrated gravity cyclone dust collection function | |
CN219539711U (en) | Flue gas treatment device of steel smelting furnace | |
CN218222823U (en) | Collection device and high-confidentiality crushing equipment | |
CN221537303U (en) | Gravity grain and coarse separator | |
CN205392995U (en) | Perpendicular flow pattern gravity -type air classifier | |
CN222076804U (en) | A secondary separation device for metal materials | |
CN205701111U (en) | A kind of cyclone separator with plate |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20231116 Address after: 014200 Chepuqu Village, Jinshan Town, Guyang County, Baotou City, Inner Mongolia Autonomous Region Patentee after: Baotou Yihong Mining Co.,Ltd. Address before: 2081, building a, 88 Jianghai West Road, Liangxi District, Wuxi City, Jiangsu Province, 214000 Patentee before: Wuxi Xiangyuan Information Technology Co.,Ltd. Effective date of registration: 20231116 Address after: 2081, building a, 88 Jianghai West Road, Liangxi District, Wuxi City, Jiangsu Province, 214000 Patentee after: Wuxi Xiangyuan Information Technology Co.,Ltd. Address before: 224051 Jianjun road 211, Ting Hu District, Yancheng City, Jiangsu Patentee before: YANCHENG INSTITUTE OF TECHNOLOGY |
|
TR01 | Transfer of patent right |