CN113806882B - Determination method of multichannel partition plate of hydrocyclone feeder - Google Patents
Determination method of multichannel partition plate of hydrocyclone feeder Download PDFInfo
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Abstract
Description
技术领域Technical field
本发明属于水力旋流器设计技术领域,具体涉及一种水力旋流器进料器多通道分隔板的确定方法。The invention belongs to the technical field of hydrocyclone design, and specifically relates to a method for determining a multi-channel partition plate of a hydrocyclone feeder.
背景技术Background technique
水力旋流器由于结构简单,无运转部件,占地面积小,加之操作简单,是广泛应用于化工、矿物分选、环保、石油工程和生物工程等工业上的物料分级和分离的主要设备之一。水力旋流器的分级原理是利用离心沉降原理实现物料按其沉降速度不同而分成不同的粒度级别产品,即物料在一定压力下由旋流器入口进入旋流器后产生强旋转运动,在离心力的作用下粗而重的颗粒向外运动进入外旋流由沉砂口排出;在流体曳力和向心浮力作用下,细而轻的颗粒向内迁移进入内旋流由溢流口排出,从而完成颗粒的分级与分离。Due to its simple structure, no moving parts, small footprint, and simple operation, hydrocyclone is one of the main equipment widely used for material classification and separation in industries such as chemical industry, mineral sorting, environmental protection, petroleum engineering, and bioengineering. one. The classification principle of the hydrocyclone is to use the centrifugal sedimentation principle to separate the materials into products of different particle size levels according to their different sedimentation speeds. That is, the materials enter the cyclone from the cyclone inlet under a certain pressure and generate strong rotational motion. Under the centrifugal force Under the action of fluid drag and centripetal buoyancy, the coarse and heavy particles move outward into the external swirling flow and are discharged from the sand sinking port; under the action of fluid drag and centripetal buoyancy, the fine and light particles migrate inward into the inner swirling flow and are discharged from the overflow port. This completes the classification and separation of particles.
进料器是物料进入水力旋流器的首要通道,研究结果表明,进料器结构对旋流器分离过程的影响主要有3点:1、旋流器的工作能耗;2、旋流器的物理磨损;3、旋流器的流场稳定性。可以说进料器结构的优劣是决定水力旋流器的寿命、流场分布及分离性能的关键因素之一。当前工业中广泛应用的进料器为单入口单通道形式,其优点是简单易加工、现场配置方便,其缺点是能耗高、磨损大、给料不均匀导致流场稳定差;研究中被广泛认可的进料器形式为对称入口形式,如双入口、四入口水力旋流器,其优点是能有效解决单入口旋流器存在的问题,但缺点是各个入口对给料均衡性要求极高,这给对称入口水力旋流器的实际应用带来了困难。在进料器设计方法上,单入口单通道形式进料器通常采用切线法、渐开线法或阿基米德螺线法三种方法,对称入口形式进料器则是将单入口进行圆对称设计。当前水力旋流器进料器设计方法都存在着一些问题,如切线法虽然加工简单,但旋流器分级性能差;阿基米德螺线法虽然加工复杂一些,也仍然存在给料分布均匀性差的问题,但旋流器分级性能好一些;而渐开线法介于二者之间。因此,有必要开发一种更好的水力旋流器进料器的设计方法,既能避免单入口单通道和对称入口进料器存在的问题,又能弥补当前进料器设计方法的不足。The feeder is the primary channel for materials to enter the hydrocyclone. Research results show that the feeder structure mainly affects the cyclone separation process in three points: 1. The working energy consumption of the cyclone; 2. The cyclone Physical wear; 3. Flow field stability of the cyclone. It can be said that the quality of the feeder structure is one of the key factors that determines the life, flow field distribution and separation performance of the hydrocyclone. The feeder currently widely used in industry is a single-inlet single-channel form. Its advantages are simple and easy processing and convenient on-site configuration. Its disadvantages are high energy consumption, large wear, and uneven feeding, resulting in poor flow field stability. In the study, it was found that The widely recognized feeder form is the symmetrical inlet form, such as double-inlet and four-inlet hydrocyclones. The advantage is that it can effectively solve the problems of single-inlet cyclones, but the disadvantage is that each inlet requires extremely balanced feeding. High, which brings difficulties to the practical application of symmetrical inlet hydrocyclones. In terms of feeder design methods, single-inlet single-channel feeders usually adopt three methods: tangent method, involute method or Archimedean spiral method. Symmetrical inlet-type feeders use a single inlet in a circular shape. Symmetrical design. There are some problems in the current hydrocyclone feeder design methods. For example, although the tangent method is simple to process, the classification performance of the cyclone is poor; although the Archimedean spiral method is more complicated to process, it still has uniform distribution of the feed. There is a problem of poor performance, but the classification performance of the cyclone is better; while the involute method is somewhere in between. Therefore, it is necessary to develop a better design method for hydrocyclone feeders that can not only avoid the problems of single-inlet single-channel and symmetrical-inlet feeders, but also make up for the shortcomings of current feeder design methods.
发明内容Contents of the invention
针对旋流器进料器结构和设计方法存在的不足,本发明的目的在于提供一种水力旋流器进料器多通道分隔板的确定方法,提高旋流器给料口处给料的均衡性,从而显著提高旋流器内流场稳定,提高水力旋流器分离精度。In view of the shortcomings in the structure and design method of the cyclone feeder, the purpose of the present invention is to provide a method for determining the multi-channel partition plate of the hydrocyclone feeder to improve the efficiency of feeding at the cyclone feed port. Balance, thus significantly improving the stability of the flow field in the cyclone and improving the separation accuracy of the hydrocyclone.
本发明的目的是通过下述技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
本发明的一种水力旋流器进料器多通道分隔板的确定方法,包括进料器的中空圆柱和连通在中空圆柱中部周侧的进料体,在所述的中空圆柱上下端均设有法兰,所述的进料体具有矩形横截面,矩形横截面的边壁由通道分隔板构成;其特征在于,所述的多通道分隔板的设计方法包括以下步骤:A method for determining a multi-channel partition plate of a hydrocyclone feeder of the present invention includes a hollow cylinder of the feeder and a feed body connected to the peripheral side of the middle part of the hollow cylinder. The upper and lower ends of the hollow cylinder are evenly spaced. A flange is provided, the feed body has a rectangular cross-section, and the side walls of the rectangular cross-section are composed of channel partition plates; it is characterized in that the design method of the multi-channel partition plate includes the following steps:
步骤1、确定相关参数Step 1. Determine relevant parameters
确定中空圆柱半径R、进料体的入口宽度w、进料体的延伸长度Li、进料体的通道数n和进料体的包角θ;Determine the radius R of the hollow cylinder, the entrance width w of the feed body, the extension length L i of the feed body, the number of channels n of the feed body, and the wrapping angle θ of the feed body;
步骤2、建立xoy直角坐标系Step 2. Establish xoy rectangular coordinate system
以中空圆柱横截面的圆心作为原点o,以原点o与进料体与中空圆柱的相切点P0的连线为X轴,以原点o与进料体延伸方向为Y轴,建立xoy直角坐标系;Taking the center of the cross section of the hollow cylinder as the origin o, taking the line connecting the origin o and the tangent point P 0 of the feed body and the hollow cylinder as the X axis, taking the origin o and the extension direction of the feed body as the Y axis, establish the xoy right angle Coordinate System;
步骤3、确定通道等分点位置Step 3. Determine the position of the channel bisection point
设定各通道宽度相同,均为则在xoy直角坐标系中,以进料体与中空圆柱的相切点P0为基点,在X轴上每隔b距离确定一个等分点,等分点坐标为 Set the width of each channel to be the same, which is Then in the xoy rectangular coordinate system, taking the tangent point P 0 of the feed body and the hollow cylinder as the base point, determine an equal dividing point every b distance on the X axis, and the equal dividing point coordinates are
步骤4、建立通道分隔板Step 4. Create channel dividers
分别以各通道等分点P2i-1为起点,逆时针设置,按照具有渐缩特性的阿基米德螺旋线驱动方程建立对应的各通道分隔板,并与中空圆柱相切于P2i;Taking the bisection point P 2i-1 of each channel as the starting point, set it counterclockwise, establish the corresponding channel separation plate according to the Archimedean spiral driving equation with tapering characteristics, and tangent to the hollow cylinder at P 2i ;
步骤5、以进料体与中空圆柱的相切点P0和通道等分点P2n-1为起点,沿Y轴负方向取长度为L建立直线段外通道,并将外通道端点封闭;Step 5. Taking the tangent point P 0 between the feed body and the hollow cylinder and the channel bisection point P 2n-1 as the starting point, take the length L along the negative direction of the Y-axis to establish a straight-line segment outer channel, and seal the end points of the outer channel;
步骤6、以通道等分点P2i-1(1≤i≤n-1)为起点,于外通道内沿Y轴负方向取长度为a设置直线段通道分隔板。Step 6. Taking the channel bisecting point P 2i-1 (1≤i≤n-1) as the starting point, set a straight-line channel partition plate with a length a along the negative direction of the Y-axis in the outer channel.
在步骤4中,所述的阿基米德螺旋线的驱动方程为:In step 4, the driving equation of the Archimedean spiral is:
与现有技术相比,本发明的优点是:Compared with the prior art, the advantages of the present invention are:
1)本发明的水力旋流器进料器多通道分隔板的确定方法,以单入口螺旋线进料体为基础,可以根据实际情况设定通道数量和包角等参数,因此可用于所有尺寸和类型的水力旋流器。1) The method for determining the multi-channel partition plate of the hydrocyclone feeder of the present invention is based on the single-inlet spiral feed body. Parameters such as the number of channels and wrapping angle can be set according to the actual situation, so it can be used for all Sizes and types of hydrocyclones.
2)本发明的水力旋流器进料器多通道分隔板的确定方法,其通道分隔板构成曲线为具有渐缩特性的阿基米德螺旋线,并且与圆柱体完全相切,因此有助于旋流的形成同时又满足均匀光滑、无凸起、无台阶的要求。2) The method for determining the multi-channel partition plate of the hydrocyclone feeder of the present invention. The channel partition plate constitutes an Archimedean spiral with tapering characteristics and is completely tangent to the cylinder. Therefore, It contributes to the formation of swirling flow while meeting the requirements of uniform smoothness, no bulges, and no steps.
3)本发明的水力旋流器进料器多通道分隔板的确定方法,其通道分隔板构成曲线具有相似性,各个通道的宽度恒定且一致,均为因此有助于提高流场的对称性,进一步提高水力旋流器分离精度。3) The method for determining the multi-channel partition plate of the hydrocyclone feeder of the present invention, the channel partition plate composition curves are similar, the width of each channel is constant and consistent, and they are all Therefore, it helps to improve the symmetry of the flow field and further improve the separation accuracy of the hydrocyclone.
4)本发明的水力旋流器进料器多通道分隔板的确定方法,其进料通道入口在外形上依旧为单入口,便于实际应用中的配置,更适应生产现场实际需要。4) In the method for determining the multi-channel partition plate of the hydrocyclone feeder of the present invention, the entrance of the feed channel is still a single entrance in appearance, which facilitates configuration in practical applications and is more suitable for the actual needs of the production site.
附图说明Description of drawings
图1为本发明水力旋流器进料器结构及计算用图。Figure 1 is a diagram showing the structure and calculation of the hydrocyclone feeder of the present invention.
图2为六种不同旋流器进料通道剖视俯视示意图。Figure 2 is a schematic cross-sectional top view of six different cyclone feed channels.
图3为与图2对应的旋流器垂直剖面矿浆流线图。Figure 3 is a vertical section slurry streamline diagram of the cyclone corresponding to Figure 2.
图4为与图2对应的旋流器不同进料通道沉砂分配率曲线。Figure 4 is the sand settling distribution rate curve of different feed channels of the cyclone corresponding to Figure 2.
具体实施方式Detailed ways
以下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 in conjunction with the accompanying drawings and examples.
如图1-图4所示,本发明的一种水力旋流器进料器多通道分隔板的确定方法,包括进料器的中空圆柱1和连通在中空圆柱1中部周侧的进料体,在所述的中空圆柱上下端均设有法兰,所述的进料体具有矩形横截面,矩形横截面的边壁由通道分隔板3构成;其特征在于,所述的多通道分隔板3的设计方法包括以下步骤:As shown in Figures 1 to 4, a method for determining a multi-channel partition plate of a hydrocyclone feeder of the present invention includes a hollow cylinder 1 of the feeder and a feed material connected to the central peripheral side of the hollow cylinder 1 body, flanges are provided at the upper and lower ends of the hollow cylinder, the feed body has a rectangular cross-section, and the side walls of the rectangular cross-section are composed of channel partition plates 3; it is characterized in that the multi-channel The design method of partition 3 includes the following steps:
步骤1、确定相关参数Step 1. Determine relevant parameters
确定中空圆柱1(与水力旋流器的柱段半径相同)半径R,确定进料体的入口宽度W,确定通道数量n=3,确定包角θ=2π。Determine the radius R of the hollow cylinder 1 (same as the column radius of the hydrocyclone), determine the inlet width W of the feed body, determine the number of channels n = 3, and determine the wrap angle θ = 2π.
步骤2、建立xoy直角坐标系Step 2. Establish xoy rectangular coordinate system
以中空圆柱横截面的圆心O(0,0)作为原点,以原点o与进料体与中空圆柱的相切点P0的连线为X轴,以原点o与进料体延伸方向为Y轴,建立xoy直角坐标系。Take the center O(0,0) of the hollow cylinder cross section as the origin, take the line connecting the origin o and the tangent point P 0 of the feed body and the hollow cylinder as the X axis, take the origin o and the extension direction of the feed body as Y axis to establish the xoy rectangular coordinate system.
步骤3、确定通道等分点位置Step 3. Determine the position of the channel bisection point
设定各通道宽度相同,均为在xoy直角坐标系中,以进料体与中空圆柱1的相切点P0(R,0)为基点,则沿X轴正方向每隔b距离确定等分点P1、P3、P5,其中P1为第一通道等分点,P3为第二通道等分点,P5为第三通道等分点;在xoy直角坐标系中,坐标分别为:P5(R+W,0)。Set the width of each channel to be the same, which is In the xoy rectangular coordinate system, taking the tangent point P 0 (R, 0) between the feed body and the hollow cylinder 1 as the base point, then determine the equal division points P 1 , P 3 , P every b distance along the positive direction of the X axis 5 , where P 1 is the bisection point of the first channel, P 3 is the bisection point of the second channel, and P 5 is the bisection point of the third channel; in the xoy rectangular coordinate system, the coordinates are: P 5 (R+W,0).
步骤4、建立通道分隔板Step 4. Create channel dividers
分别以各通道等分点P2i-1为起点,逆时针设置,按照具有渐缩特性的阿基米德螺旋线驱动方程建立对应的各通道分隔板3,并与中空圆柱1相切于P2i,具体如下:Taking the bisecting point P 2i-1 of each channel as the starting point, set it counterclockwise, and establish the corresponding dividing plate 3 of each channel according to the Archimedean spiral driving equation with tapering characteristics, and tangent to the hollow cylinder 1 at P 2i , the details are as follows:
如图1所示,根据xoy直角坐标系,P1为第一通道等分点,L1为第一通道分隔板3,P2为第一通道分隔板3与中空圆柱1的相切点。以第一通道等分点P1为起点,按照阿基米德螺旋线制备第一通道分隔板3,第一通道分隔板3末端与中空圆柱1相切于P2点。As shown in Figure 1, according to the xoy rectangular coordinate system, P 1 is the first channel bisecting point, L 1 is the first channel dividing plate 3, and P 2 is the tangent between the first channel dividing plate 3 and the hollow cylinder 1 point. Taking the first channel bisecting point P 1 as the starting point, the first channel dividing plate 3 is prepared according to the Archimedean spiral. The end of the first channel dividing plate 3 is tangent to the hollow cylinder 1 at point P 2 .
涉及第一通道分隔板3的阿基米德螺旋线驱动方程为:The Archimedean spiral driving equation involving the first channel divider plate 3 is:
如图1所示,P3为第二通道等分点,L2为第二通道分隔板3,P4为第二通道分隔板3与中空圆柱1相切点。以第二通道等分点P3为起点,按照阿基米德螺旋线制备第二通道分隔板3,第二通道分隔板3末端与中空圆柱1相切于P4点。As shown in Figure 1, P 3 is the second channel bisecting point, L 2 is the second channel dividing plate 3, and P 4 is the tangent point between the second channel dividing plate 3 and the hollow cylinder 1. Taking the second channel bisecting point P 3 as the starting point, prepare the second channel dividing plate 3 according to the Archimedean spiral. The end of the second channel dividing plate 3 is tangent to the hollow cylinder 1 at point P 4 .
涉及第二通道分隔板3的阿基米德螺旋线驱动方程为:The Archimedean spiral driving equation involving the second channel divider plate 3 is:
如图1所示,P5为第三通道等分点,L3为第三通道分隔板3,P6为第三通道分隔板3与中空圆柱1的相切点。以第三通道等分点P5为起点,按照阿基米德螺旋线建立第三通道分隔板3,第三通道分隔板3末端与中空圆柱1相切于P6。As shown in Figure 1, P 5 is the third channel bisecting point, L 3 is the third channel dividing plate 3, and P 6 is the tangent point between the third channel dividing plate 3 and the hollow cylinder 1. Taking the third channel bisecting point P 5 as the starting point, the third channel dividing plate 3 is established according to the Archimedean spiral. The end of the third channel dividing plate 3 is tangent to the hollow cylinder 1 at P 6 .
涉及第三通道分隔板3的阿基米德螺旋线驱动方程为:The Archimedean spiral driving equation involving the third channel divider plate 3 is:
步骤5、以进料体与中空圆柱1的相切点P0和通道等分点P2n-1为起点,沿Y轴负方向取长度为L建立直线段外通道2,并将外通道2端点封闭。Step 5. Taking the tangent point P 0 between the feed body and the hollow cylinder 1 and the channel bisection point P 2n-1 as the starting point, take the length L along the negative direction of the Y-axis to establish a straight-line segment outer channel 2, and connect the outer channel 2 Endpoint closed.
步骤6、以通道等分点P2i-1(1≤i≤n-1)为起点,于外通道2内沿Y轴负方向取长度为a设置直线段通道分隔板3。Step 6. Taking the channel bisecting point P 2i-1 (1≤i≤n-1) as the starting point, set a straight-line channel partition 3 with a length a along the negative direction of the Y-axis in the outer channel 2.
实施例1Example 1
本实施例采用中空圆柱1(与水力旋流器的柱段半径相同)半径R为75mm,进料体的入口宽度,亦即外通道宽度W为30mm,外通道2长度L为100mm,通道数量n为1,通道包角θ为2π。In this embodiment, the radius R of the hollow cylinder 1 (the same as the column radius of the hydrocyclone) is 75mm, the inlet width of the feed body, that is, the width W of the outer channel is 30mm, the length L of the outer channel 2 is 100mm, and the number of channels n is 1, and the channel wrap angle θ is 2π.
实施例1采用数值模拟方法,用于考察不同通道个数进料体对水力旋流器分离效果的影响。Embodiment 1 adopts a numerical simulation method to examine the impact of feed bodies with different channel numbers on the separation effect of a hydrocyclone.
实施例2Example 2
本实施例与实施例1不同之处在于通道数量n为2,通道分隔板3长度a为35mm。The difference between this embodiment and Embodiment 1 is that the number of channels n is 2, and the length a of the channel dividing plate 3 is 35 mm.
实施例2也是采用数值模拟方法,用于考察不同通道个数进料体对水力旋流器分离效果的影响。Example 2 also uses a numerical simulation method to examine the impact of feed bodies with different channel numbers on the separation effect of the hydrocyclone.
实施例3Example 3
本实施例与实施例2不同之处在于通道数量n为3。The difference between this embodiment and Embodiment 2 is that the number n of channels is 3.
实施例3也是采用数值模拟方法,用于考察不同通道个数进料体对水力旋流器分离效果的影响。Embodiment 3 also uses a numerical simulation method to examine the impact of feed bodies with different channel numbers on the separation effect of the hydrocyclone.
实施例4Example 4
本实施例与实施例2不同之处在于通道数量n为4。The difference between this embodiment and Embodiment 2 is that the number n of channels is 4.
实施例4也是采用数值模拟方法,用于考察不同通道个数进料体对水力旋流器分离效果的影响。Embodiment 4 also uses a numerical simulation method to examine the impact of feed bodies with different channel numbers on the separation effect of the hydrocyclone.
由图2、图3可知按照本发明设计方法所设计的进料通道与传统进料通道相比,可显著提高旋流器内流场稳定,能充分发挥水力旋流器的性能,进一步提高分离精度。由图4可知,本发明的进料通道其分离效果与双入口进料通道分离效果相当,在同等工况下,分离粒度由传统进料通道的22μm降至20μm左右,分级可能偏差(Ep=(d75-d25)/2)则由传统进料通道的7.6μm降至5μm左右。也就是说,本发明的进料通道的水力旋流器,在相同工况下,分级粒度和精度都明显提升。另外,本发明的进料通道在外形上依旧为单入口,便于实际应用中的配置,更适应生产现场实际需要。It can be seen from Figures 2 and 3 that the feed channel designed according to the design method of the present invention can significantly improve the stability of the flow field in the cyclone, fully utilize the performance of the hydrocyclone, and further improve the separation compared with the traditional feed channel. Accuracy. As can be seen from Figure 4, the separation effect of the feed channel of the present invention is equivalent to that of the double-inlet feed channel. Under the same working conditions, the separation particle size is reduced from 22 μm in the traditional feed channel to about 20 μm, and the classification may deviate (E p =(d 75 -d 25 )/2) is reduced from 7.6μm of the traditional feed channel to about 5μm. That is to say, under the same working conditions, the hydrocyclone of the feed channel of the present invention can significantly improve the classification particle size and accuracy. In addition, the feed channel of the present invention still has a single entrance in appearance, which facilitates configuration in practical applications and is more suitable for actual needs at the production site.
以上所述仅是本发明的优选实施方式,应当指出对于本技术领域的普通技术人员,在不脱离本发明构思的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围内。The above are only preferred embodiments of the present invention. It should be pointed out that those skilled in the art can make several improvements and modifications without departing from the concept of the present invention. These improvements and modifications should also be regarded as within the protection scope of the present invention.
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Citations (3)
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US4652363A (en) * | 1984-11-01 | 1987-03-24 | Miller Francis G | Dual feed hydrocyclone and method of separating aqueous slurry |
CN106493004A (en) * | 2016-11-28 | 2017-03-15 | 鞍钢集团矿业有限公司 | A kind of hydrocyclone and its entrance structure determination method for parameter |
CN112791864A (en) * | 2021-01-26 | 2021-05-14 | 沈阳建筑大学 | A hydrocyclone and a design method for the inlet curve of the volute |
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Publication number | Priority date | Publication date | Assignee | Title |
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US4652363A (en) * | 1984-11-01 | 1987-03-24 | Miller Francis G | Dual feed hydrocyclone and method of separating aqueous slurry |
CN106493004A (en) * | 2016-11-28 | 2017-03-15 | 鞍钢集团矿业有限公司 | A kind of hydrocyclone and its entrance structure determination method for parameter |
CN112791864A (en) * | 2021-01-26 | 2021-05-14 | 沈阳建筑大学 | A hydrocyclone and a design method for the inlet curve of the volute |
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