WO1995032057A1 - Dispositif de criblage fin de type cyclone - Google Patents

Dispositif de criblage fin de type cyclone Download PDF

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Publication number
WO1995032057A1
WO1995032057A1 PCT/CN1995/000044 CN9500044W WO9532057A1 WO 1995032057 A1 WO1995032057 A1 WO 1995032057A1 CN 9500044 W CN9500044 W CN 9500044W WO 9532057 A1 WO9532057 A1 WO 9532057A1
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WO
WIPO (PCT)
Prior art keywords
screen
sieve
cylinder
fine
flange
Prior art date
Application number
PCT/CN1995/000044
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English (en)
French (fr)
Inventor
Zhigang Fang
Fenggang Song
Original Assignee
Beijing General Research Institute Of Mining And Metallurgy
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beijing General Research Institute Of Mining And Metallurgy filed Critical Beijing General Research Institute Of Mining And Metallurgy
Priority to CA002167053A priority Critical patent/CA2167053A1/en
Priority to US08/581,544 priority patent/US5630514A/en
Priority to BR9505500A priority patent/BR9505500A/pt
Priority to AU24438/95A priority patent/AU684025B2/en
Priority to GB9601129A priority patent/GB2294892B/en
Publication of WO1995032057A1 publication Critical patent/WO1995032057A1/zh

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Classifications

    • 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
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08—Vortex chamber constructions
    • B04C5/10—Vortex chamber constructions with perforated walls

Definitions

  • the Ming refers to the machinery and equipment for the production of sandy gasified aluminum. It is a kind of fine cyclone with a cage structure, which is used for the classification of aluminum hydroxide.
  • the aluchemical aluminum plant usually adopts the Bayer process.
  • the radon gas produced is a fine-grained material.
  • the range of argon-gasified aluminum particles produced by the decomposition tank is wide, and three products of sandy ammonia gaseous aluminum, coarse crystal seeds and fine crystal seeds need to be classified, and coarse-grained sand radon. 5 (+ 44 ⁇ ⁇ grain grade content is greater than 90%), sent to the next sintering process to fire the aluminum alloy, the medium and fine grain coarse seeds and fine crystal seeds are returned to the three-stage and one-stage decomposition tanks, and grown again .
  • the classification methods currently used at home and abroad mostly use two-stage gravity sedimentation tanks or two-stage hydrocyclone ⁇ .
  • the inventor has developed a cyclone fine classification device in 1987. It is a cylindrical screen equipped with a plastic material in the hydrocyclone housing.] The combination of the hydrocyclone and the arc sieving two sorting equipment, and the application of two classification principles of gravity centrifugation and fine particle sieving, to achieve the purpose of improving the classification efficiency.
  • the equipment consists of an overflow cap, an overflow pipe, a feed body, a multi-section cylinder, a cylindrical screen, a flange, a lower body, a cone, an underflow port, a pressure gauge and other components.
  • the upper part is a small cylinder (composed of a feed body and an overflow cap, which is where the slurry is fed in and overflowed); the outer layer in the middle is a multi-section cylinder, the inner layer is a cylindrical mesh, and the diameter of the screen is equivalent to
  • the diameter of the upper cylinder, the diameter of the multi-section cylinder is 1.3 times the diameter of the upper cylinder, and the lower part is provided with a sieve under the sieve and a top-down sieve product which is at right angles to the multi-section cylinder. It penetrates into the lower body of the sieve and consists of a partially exposed hollow inverted cone.
  • the cylinder screen is made of nylon 1010 'raw material through injection molding, and pressed into a rectangular screen (475. 65 X 150mm), the screen holes are stripe, and there are 0.15, 0.3 and 0.
  • the sieve bar has a wedge-shaped section.
  • the rectangular screen is made into a cylindrical screen by secondary molding.
  • the swirling flow has been applied in production, with many advantages, but there are also some disadvantages. That is, the structure of the cylinder net installed in the equipment is unreasonable. Under high-speed swirling, pressure shock and nearly 60'C working conditions Easy to deform or even fall off, frequent replacement. Due to the length and width of the rectangular screen
  • the purpose of the present invention is to find a reasonable sieve for fixing the tangerine to improve the difficulty of sieve loading and unloading, reduce the deformation and fall of the sieve, improve the equipment operation rate, and achieve the purpose of improving the classification effect.
  • the sieve cage type swirl fine screen of the present invention comprises an overflow cap, an overflow pipe, a feed pipe, a cone, an underflow port, a pressure gauge, and:
  • a There is an integral cylinder with an upper stop connected by one end connected to the lower flange of the feed body and the other end connected to the upper flange of the lower screen body;
  • a cylindrical screen is installed between the upper end of the whole cylinder and the upper end of the lower sieve inner ring with a cylindrical screen between each flange and three flanges.
  • the screw is connected to a cage frame with different number of nodes in height to form a cage screen (ie, a screen cage);
  • the cylindrical screen is made by adding 15-30% glass fiber in nylon 1010, and it is best to add 22.3% glass fiber.
  • the cylindrical screen can also use polyformaldehyde, and the diameter of the screen cage is 150-900mm. 450mm diameter is the best.
  • Figure 2 is a structural diagram of the sieves of the present invention
  • the sieve cage type swirling fine sieve of the present invention is composed of an overflow cap 1, an overflow pipe 2, a feed body 3, and an integral cylinder.
  • the body 4, the sieve 5, the lower sieve 6, the cone 7, the underflow port 8, the pressure gauge 9 and other main components are composed of each other as shown in FIG. 1 to form a whole. That is, the lower body 6 is used as the base body, and the lower flange of the lower screen body 6 and the upper flange of the cone 7 are fixed by bolts.
  • the whole cylinder 4 is placed on the outer ring of the base body from top to bottom, and the flanges of the two are used for the flanges.
  • Bolt connection and fixation Place the screen cage 5 in the integral cylinder 4; the upper end is positioned with the upper stop of the integral cylinder 4; the lower end is positioned with the upper stop of the inner ring of the lower screen 6;
  • the upper flange of the monolithic cylinder 4 is fixedly connected by bolts, and presses the screen cage 5 to fix it; the upper flange of the feed body 3 and the lower flange of the overflow cap 1 are bolted and fixed
  • the overflow pipe 2 is provided; the underflow port 8 is fixed on the lower flange of the cone 7 by bolts.
  • the screen cage 5 is composed of the upper flange 10, the middle flange 11, the lower flange 12, the ® cylinder screen 13, and the screw 14 connected to each other, that is, the screw 14 is connected to the upper method.
  • the flange 11 and the lower flange 12 are used to fix the cylindrical screen 13.
  • the advantages of this structure are: the flanges 10, 11, and 12 are supported by the screw 14 so that the cylindrical screen 13 is not subject to pressure deformation in the height direction and does not fall off due to loose assembly; secondly, the flange plate is no longer needed
  • the multi-section cylinder is fixed, but the sieve cage 5 is fixed.
  • the upper flange 10 and the lower flange 12 of the cage are installed at the upper stop of the integral cylinder 4 and the upper stop of the lower sieve inner ring. ; Then, several sections of cylindrical screen are assembled into a sieve cage 5 to make the original multi-section cylindrical body into a single-piece whole cylindrical body 4. In this way, it is simple and convenient to change the screen of the cylinder from screen to screen 5 in the past.
  • the diameter of the screen cage is generally 150-900mm, and the optimal diameter is 450mm, which can be determined according to the size of the slurry processing capacity. ⁇
  • the screen mesh in the screen cage 5 of the present invention is greatly improved in material and structure.
  • the connecting mesh of the sieve is five, the thickness of the sieve is 6.5mm, the width is 3.05mm, and the connecting rings at both ends are five, making it more rigid than the original sieve;
  • the mesh uses 22.3% glass fiber added to the nylon 1010 raw material to make a reinforced nylon screen, which increases the heat distortion temperature and meets the production requirements of slurry at nearly 60 ° C. Abrasion resistance.
  • the screen can also be made of polyformamidine, with a temperature resistance of 85. C or more.
  • the under-screen body 6 has a horseshoe shape, and the under-screen outlet pipe on the under-screen body 6 is inclined 45 degrees downward from the horizontal.
  • the working process of the sieve cage type swirling fine sieve of the present invention is that the decomposition tank is transported to the feeding port on the feed body 3 of the equipment with a certain pressure ⁇ argon gasified aluminum slurry, and enters the feeding in an approximately involute direction.
  • the slurry moves in a circular motion along the wall of the cylinder.
  • the centrifugal force of the coarse and medium particles is relatively large. They collide with the cage-shaped screen 5 and the medium particles pass through the screen.
  • the outlet pipe is discharged, and the coarse particles that cannot pass through the screen are rotated into the cone 7 along the inner cone wall of the lower sieve body 6, and then discharged through the underflow port 8.
  • the fine particles have a small centrifugal force, which is near the central vortex and is affected by the central vortex upward. Movement, discharged by the overflow pipe.
  • the sieve cage type cyclone fine sieve is a wet-type fine-granular classification device, which can be used for radon gasification aluminum classification in the Bayer process sandy gasification process, coarse slime recovery, fine slime classification, and can also be applied. It is used for tilling and concentrating fine-grained materials in other industries.
  • This equipment is used for sandy gasification, and can meet the requirements of the two-stage decomposition process of agglomeration of fine particles and cohesive growth of coarse particles. Small and alternate technical difficulties make the product's physical properties stable, and the coarse-grained products separated have less than 44 ⁇ in particle size and high solid content; medium-sized products return to the decomposition tank as seed crystals, and have strong activation capacity; fine-grained grades The product has a low solid content.
  • This equipment has the advantages of large processing capacity, high classification efficiency, small equipment size, simplified process, low investment, low power consumption, long life of screens and screens, and easy replacement.
  • the size of the sieve cage-type swirling fine screen of the present invention is divided by the diameter of the cylindrical screen 5.
  • the two layers are docked.
  • the equipment assembled by it is a cpl50mm cyclone fine screen. Length of three rectangular screens With 4 layers of butt joints, a sieve cage 5 with a diameter X and a height of q; 450mm X 600mm is formed, and a cp450mm sieve cage type swirl fine screen is assembled with it.
  • Feeder 3 of this equipment has an inner diameter of cp450mm, a height of 370mm, a wall thickness of 12mm, an inner diameter of cylinder 4 of cp585mm, a height of 640mm, and a wall thickness of 8mm.
  • the diameter of the slurry outlet pipe pl50mm on the lower body 6, the upper mouth of the inverted cone 7 The diameter is cp270mm, and the lower diameter is p80min. Its parts are mainly made of wear-resistant cast iron.
  • the p450mm sieve cage type cyclone fine sieve is used to divide the alumina produced by a domestic alumina widely.
  • the feeding pressure is 0.06-0.07MPa
  • the feeding solid content is about 400g / L.
  • the fineness is less than about 20%
  • the slurry processing capacity of each equipment is about 200mVh
  • the underflow coarse grained product is less than 1/2 than the feed, and the solid content is about doubled. result.

Landscapes

  • Cyclones (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Combined Means For Separation Of Solids (AREA)

Description

锭流细筛
技术领域
明涉及砂状氣化铝生产的机械设备， 是一种 ^网为笼型结构 的旋流细 ，連用于氢氣化铝分级。
背景技术
氡化铝厂通常采用拜尔法生产工艺， 产出的氲氣化 吕是一种细颗 粒物料。 在生产过程中，由分解槽产出的氬氣化铝粒级范围较宽，需分 级出砂状氨氣化铝、 粗晶种和細晶种三种产品，粗粒级的砂状氳氣化 5 ( + 44μΐΏ粒级含量大于 90% ) ,送下一烧结工序烧成氡化铝，中、 细 粒级的粗晶种和细晶种分別返回到三段和一段分解槽，重新长大。为了 分鈒出上述三种产品，目前国内外采用的分级方法，多半是用二段重力 沉降槽或两级水力旋流 ^， 由于上述两种方法均存在着分级效果差， 占地面积大，工艺复杂，投資高，粍电多等缺点，本发明人曾在 1987年 研制了一种旋流细 ^分级设备， 它是在水力旋流器壳体中安装塑料材 质的圆筒筛 ·Ρ] , 使水力旋流^与弧形筛两种分鈒设备结合为一体， 同 时应用重力离心与细粒筛分两种分级原理， 达到提高分级效率的目 的。 该设备由溢流帽、溢流管、给料体、多节筒体、圆筒筛网、法兰盘、^ 下体、圆锥体、底流口、压力表等部件构成。 上部为小圆柱体（由給料体 和溢流帽組成，是料浆给入和溢流徘出处）；中部的外层为多节筒体，内 层为圆筒 网，筛网的直径相当于上部圓柱体直径， 多节筒体直径为 上部圆柱体直径的 1. 3倍，下部为设有一个与多节筒体成直角的^下 中颗粒产品徘出 ψ的 筛 下体和一个由上而下穿入筛下体且有部分露 出的空心倒圆锥体組成。 圆筒筛网采用尼龙 1010'原料通过注塑成形， 压制成矩形筛网（475. 65 X 150mm)，筛孔成条形，有 0. 15 , 0. 3和 0.
45mm三种，筛条呈楔形断面。 矩形筛冋通过二次成型制成圓筒筛网。 该旋流細 已在生产中应用， 优点很多，但也存在着一些不足之处，即 圆筒网安装在设备中的结构不合理， 在高速旋流、压力冲击和近 60'C 工作条件下易于变形甚 至脱落， 更换頻繁。 由于矩形筛网的长宽
― 1 ―
ISA/CN 更 正 页 蚬格只有一种， 而不同规格（ 不同直径和不同高度）的旋流细筛，均通 过筛网纵、 横向对接来实现。在高度方向上的对接，采用几节^网就对 应几节筒体并由法兰连接两者的结构。这种结构，筛网更换时需一节一 节地拆卸筒体与法兰，安装维修困难，影响正常生产。
发明内容
.本发明的目的在于寻我一种合理的筛网固定结枸， 以改善筛网装 卸难的问题， 減少筛网变形与脱落，提高设备运转率，达到提高分级效 果的目的。
本发明的筛笼型旋流细筛， 包括溢流帽、溢流管、给料^、圆锥体、 底流口、压力表，以及：
a : 设有由一端与给料体下法兰连接，另一端与筛下体上法兰连接 的具有上止口的整体筒体；
b :在整体筒体内部的上止口和筛下体内环上止口处定位的带有上 法兰、中法兰、下法兰和每层法兰之间装有圆筒筛网并用三根螺杆连接 为在高度上不同节数的笼型框架，形成笼型筛网（即筛笼）；
c : 4 整个空心倒圆锥体分为两段，上段空心倒圆锥体和一个由水 平向下倾斜 45度出口管的底部为马蹄形的空心例圆锥环构成筛下 体。 ·
圆筒筛网是采用在尼龙 1010内加入 15— 30% 的玻璃纤维， 以加 入 22. 3%玻璃纤维为最佳， 圆筒筛网也可采用聚甲醛，筛笼的直径为 150— 900mm，现以直径 450mm为最佳。
由于采用上述技术方案， 改善了圆筒^网的装卸、变形与脱落问 题，克服了倒圆锥体和筛下体之间的难密封问题，提高了 备的运转 率，设备体积小，投資少，耗电省，大大提高了氳氣化 吕细粒物料的分级 效果。
附图概述
图 1.为本发明结构示意图
图 2.为本发明的茏型筛网结构图
图 3.为本发明的矩形筛网结构示意图
本发明的最佳实施方式
本发明筛笼型旋流细筛是由溢流帽 1、溢流管 2、给料体 3、整体筒 体 4、筛茏 5、筛下体 6、圆锥体 7、底流口 8、压力表 9等主要部件组成， 如图 1所示相互连接构成整体。即以 ^下体 6为基体，筛下体 6的下法 兰和圆锥体 7的上法兰用螺栓联接固定， 整体筒体 4由上而下放在基 体的外圆环上， 两者的法兰用螺栓联接固定；将筛笼 5放在整体筒休 4 中， 上端用整体筒体 4的上止口定位，下端用筛下体 6的内环上止口 定位； 给料体 3的下法兰与整体筒体 4的上法兰用螺栓固定联接， 并 压住筛笼 5使其固定；给料体 3的上法兰与溢流帽 1的下法兰两者之 间用螺栓联接，并固定了溢流管 2 ;底流口 8由螺栓固定在圆锥体 7的 下法兰上。筛笼 5如图 2所示，是由上法兰 10、中法兰 11、下法兰 12、® 筒筛网 13、螺杆 14相互连接构成 ，即由螺杆 14连接上法¾ 10、中法 兰 11和下法兰 12来固定圆筒筛网 13。这种结构的优点是： 由螺杆 14 支撑法兰 10、11、12使圆筒筛网 13在高度方向既不受压变形，也不由 于装配松动产生脱落；其次是法兰盘不再需用多节筒体加以固定， 而 只是筛笼 5的固定方式，采用以 ^笼的上法兰 10和下法兰 12安装在 整体筒体 4的上止口和筛下体内环上止口处定位； 再就是数节圆筒筛 网組装为一个筛笼 5 ,使原来的多节筒体变为单节的整体筒体 4。这样 由过去一节一地更换圆筒筛网变成更换筛笼 5，简单方便。 筛笼的直径 一般为 150— 900mm，现最佳直径为 450mm，可根据料浆处理量的大小 逸定。 ·
本发明筛笼 5中的筛网，在材质与结构上作了较大的改进。如图 3 所示：筛网的连接筋为 5条，筛条的厚度为 6. 5mm，宽度为 3. 05mm，其 两端的连接环各为 5个，使其比原筛网刚度增加；材质逸择上： 网采 用在尼龙 1010原料中加入 22. 3% 的玻璃纤维， 制成了增强尼龙筛 网， 提高了热变形温度，满足了料浆为近 60°C 的生产要求'，同时增加 了耐磨性能。 此外筛网还可以用聚甲窿为原料，耐温可达 85。C以上。
为有利于筛下产品的排放，如图 1所示，筛下体 6为马蹄形，筛下 体 6上的筛下出口管由水平向下倾斜 45度。
本发明筛笼型旋流细筛的工作过程是由分解槽以一定的压力 ^氬 氣化铝料浆输送到该设备给料体 3上的给料口，以近似渐开线方向进 入给料体 3内，料浆沿圓筒筒壁作圆周运动，在惯性力作用下，粗、中颗 粒的离心力较大， 碰撞笼型筛网 5，中颗粒通过筛网，由筛下体 6外环 出口管排出，不能通过筛网的粗颗粒物料沿着筛下体 6内锥壁旋入圓 锥体 7，再由底流口 8排出，细颗粒离心力较小，在中心旋涡附近，受中 心旋涡影响向上运动，由溢流管排出。
本发明筛笼型旋流细筛是一种湿式细粒分级设备， 可用于拜尔法 砂状氣化 吕生产中的氳氣化铝分级， 粗煤泥回收，细煤泥分级，还可应 用于其它行业细粒物料的分鈒、浓缩等作业。该设备用于砂状氣化 吕生 产，能满足细粒附聚、粗粒粘结长大的二段分解工艺要求，可解决氳氣 化 吕粒度周期粗化。 细小交替出现的技术难关，使产品物理性质稳定， 分^出的粗粒产品小于 44μηι的粒级含量少，固含高；中粒级产品返回 分解槽作晶种，活化能力强；细粒级产品固含低。 该设备具有处理能力 大，分级效率高，设备体积小，工艺簡化、投資少，耗电省，筛.网寿命长， 更换方便等优点。
实施例：
本发明筛笼型旋流细筛的规格大小是以圆筒筛网 5的直径的大 小来划分的。一块矩形筛网长 L= 475. 65mm，围成的圆 cp 150mm，高 H= 150mm , 两层对接，由它組装的设备规格为 cpl50mm旋流细筛。 三 块矩形筛网的长度
Figure imgf000006_0001
， 用其 4层对 接， 便形成直径 X高为 q;450mm X 600mm 的筛笼 5， 以其装配出 cp450mm 筛 笼型旋流细筛。 该设备的给料体 3 内径为 cp450mm， 高 370mm , 壁厚 12mm，筒体 4内径为 cp585mm，高 640mm，壁厚 8mm， ^ 下体 6上的料浆出口管直径 pl50mm，倒圆锥体 7上口直径 cp270mm， 下口直径 p80min， 其部件主要采用耐磨铸铁制造而成。 采用 p450mm 筛笼型旋流细筛对囯内某氧化铝广生产的氳氡化铝进行分鈒，当给料 压力为 0. 06 - 0. 07MPa , 给料固含 400g/L左右，给料细度小于 44μπι 粒级含量 20%左右时，取得每台设备料浆处理能力为 200mVh左右， 底流粗粒鈒产品小于 44μπι粒级含量比给料减少 1/2以上， 固含约提 高一倍的结果。
对 国 外 某 氣化铝厂生产的氨氣化铝进行分鈒， 当给料压力为 0. 09MPa , 给料固含 476— 467g/L，给料细度小于 44μπι粒级含量为 8. 7 %— 6. 2 %时，取得每台设备料浆处理能力为 200m3/h左右，底流粗粒 级产品小于 44μπι粒级含量为 4. 9%— 1. 2 % ,固含为 802— 922g/L，溢 流固含 70— 78g/L的效果

Claims

权 利 要 求
1. 薛笼型旋流细 ， 包括溢流帽、溢流管、给料体、圆锥体、底流 口、压力表，其特征在于：
a : 设有由一端与给料体下法兰连接，另一端与筛下体上法兰连接 的具有上止口的整体筒体；
b :在整体筒体内部的上止口和筛下体内环上止口处定位的带有上 法兰、中法兰、下法兰和每层法兰之间装有圆筒筛网并用三根螺杆连接 为在高度上不同节数的笼型框架，形成笼型筛网； -
C : 将整个空心倒圆锥体分为两段，上段空心倒圆锥体和一个由水 平向下倾斜 45度出口管的底部为马蹄形的空心倒圆锥环构成筛下体。
2. 根据权利要求 1所述的筛笼型旋流细筛，其特征在于圆筒^网是 采用在尼龙 1010内加入 15— 30% 的玻璃纤维， 以加入 22. 3 %玻璃 纤维为最佳。 '
3. 根据权利要求 1所述的筛笼型旋流细^，其特征在于圆筒^网也 可采用聚甲醛。
4. 根据权利要求 1所述的筛笼型旋流细筛，其特征在于圆筒筛网的 直径为 150— 900mm，现以直径 450mm为最佳。
PCT/CN1995/000044 1994-05-20 1995-05-19 Dispositif de criblage fin de type cyclone WO1995032057A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
CA002167053A CA2167053A1 (en) 1994-05-20 1995-05-19 Cage type cyclone fine screen device
US08/581,544 US5630514A (en) 1994-05-20 1995-05-19 Cage type cyclone fine screen device
BR9505500A BR9505500A (pt) 1994-05-20 1995-05-19 Dispositivo de tela fina de ciclone do tipo de grade
AU24438/95A AU684025B2 (en) 1994-05-20 1995-05-19 Cyclone-type fine screen device
GB9601129A GB2294892B (en) 1994-05-20 1995-05-19 Cyclone-type fine screen device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN94211268.7 1994-05-20
CN94211268U CN2203190Y (zh) 1994-05-20 1994-05-20 一种筛笼型旋流细筛

Publications (1)

Publication Number Publication Date
WO1995032057A1 true WO1995032057A1 (fr) 1995-11-30

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US (1) US5630514A (zh)
CN (1) CN2203190Y (zh)
AU (1) AU684025B2 (zh)
BR (1) BR9505500A (zh)
CA (1) CA2167053A1 (zh)
GB (1) GB2294892B (zh)
WO (1) WO1995032057A1 (zh)

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CN102441529A (zh) * 2010-10-12 2012-05-09 株式会社川田 微粉去除装置
CN105396706A (zh) * 2015-02-13 2016-03-16 杨林 一种水力单体末煤粗煤泥11种粒级精煤产品旋流器
CN114618775A (zh) * 2022-03-10 2022-06-14 中材淄博重型机械有限公司 一种节能环保无动力复合式选粉机
CN117414958A (zh) * 2023-12-18 2024-01-19 河南省远洋粉体科技股份有限公司 一种铝粉旋风分级装置

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EP1281424A1 (fr) * 2001-07-30 2003-02-05 Jean-Denis Rochat Procédé de séparation d'un fluide
CN104785448B (zh) * 2015-04-21 2016-06-01 吉首大学 花生气力输送分选装置
CN106079150A (zh) * 2016-06-30 2016-11-09 重庆浩立塑胶有限公司 送料选料装置
CN110420751A (zh) * 2019-07-11 2019-11-08 中国恩菲工程技术有限公司 用于分级氢氧化铝的装置
CN111569537B (zh) * 2020-05-12 2021-12-03 宁波锦心节能环保科技有限公司 一种旋风除尘方法

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US4279743A (en) * 1979-11-15 1981-07-21 University Of Utah Air-sparged hydrocyclone and method
US4986900A (en) * 1989-04-04 1991-01-22 A. Ahlstrom Corporation Sectional screen cylinder

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102441529A (zh) * 2010-10-12 2012-05-09 株式会社川田 微粉去除装置
CN102441529B (zh) * 2010-10-12 2016-09-28 株式会社川田 微粉去除装置
CN105396706A (zh) * 2015-02-13 2016-03-16 杨林 一种水力单体末煤粗煤泥11种粒级精煤产品旋流器
CN114618775A (zh) * 2022-03-10 2022-06-14 中材淄博重型机械有限公司 一种节能环保无动力复合式选粉机
CN117414958A (zh) * 2023-12-18 2024-01-19 河南省远洋粉体科技股份有限公司 一种铝粉旋风分级装置
CN117414958B (zh) * 2023-12-18 2024-03-08 河南省远洋粉体科技股份有限公司 一种铝粉旋风分级装置

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AU2443895A (en) 1995-12-18
GB2294892B (en) 1998-05-20
BR9505500A (pt) 1997-08-12
CA2167053A1 (en) 1995-11-30
CN2203190Y (zh) 1995-07-12
GB9601129D0 (en) 1996-03-20
GB2294892A (en) 1996-05-15
US5630514A (en) 1997-05-20
AU684025B2 (en) 1997-11-27

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