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CN106269313B - A kind of cyclone separator that guide vane is installed in central tube - Google Patents

A kind of cyclone separator that guide vane is installed in central tube Download PDF

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CN106269313B
CN106269313B CN201610635338.3A CN201610635338A CN106269313B CN 106269313 B CN106269313 B CN 106269313B CN 201610635338 A CN201610635338 A CN 201610635338A CN 106269313 B CN106269313 B CN 106269313B
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guide vane
angle
central cylinder
cyclone separator
central tube
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CN106269313A (en
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谭磊
刘明
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Tsinghua University
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Tsinghua University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/103Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/107Cores; Devices for inducing an air-core in hydrocyclones

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Abstract

本发明涉及一种在中心筒内装设导流叶片的旋风分离器,属于旋风分离器技术领域。该旋风分离器的中心筒内装设导流叶片,在中心筒内部沿周向均匀布置导流叶片。导流叶片的轮毂布置在中心筒内管的外壁上,轮缘布置在中心筒的内壁上。导流叶片由正交试验得到最优水平,并将中心筒向远离分离器切向入口的方向偏置。通过导流叶片及中心筒偏置的结构,旋风分离器内流场使气流在流入中心筒之前汇集成一股向上的主流,主流中气流速度以竖直向上的轴向速度为主。本发明的旋风分离器内流场内部涡核漩涡强度减小,外部漩涡强度增大,有利于固体颗粒的分离,提高了分离效率;在中心筒内装设导流叶片的旋风分离器结构简单,适用于任何类型的切流式旋风分离器。

The invention relates to a cyclone separator equipped with guide blades in a central cylinder, and belongs to the technical field of cyclone separators. The central cylinder of the cyclone separator is equipped with guide blades, and the guide vanes are uniformly arranged along the circumferential direction inside the central cylinder. The hub of the guide vane is arranged on the outer wall of the inner tube of the central cylinder, and the rim is arranged on the inner wall of the central cylinder. The guide vanes are optimally leveled by orthogonal tests and bias the central cylinder away from the tangential inlet of the separator. Through the offset structure of the guide vanes and the central cylinder, the flow field in the cyclone separator makes the airflow converge into an upward mainstream before flowing into the central cylinder, and the velocity of the airflow in the mainstream is dominated by the vertical upward axial velocity. In the cyclone separator of the present invention, the intensity of the inner vortex core vortex in the flow field is reduced, and the intensity of the outer vortex is increased, which is beneficial to the separation of solid particles and improves the separation efficiency; the structure of the cyclone separator equipped with guide vanes in the central cylinder is simple, Suitable for any type of cross-flow cyclone separator.

Description

一种在中心筒内装设导流叶片的旋风分离器A cyclone separator with guide vanes installed in the central cylinder

技术领域technical field

本发明涉及一种在中心筒内装设导流叶片的旋风分离器,属于旋风分离器技术领域。The invention relates to a cyclone separator equipped with guide blades in a central cylinder, and belongs to the technical field of cyclone separators.

背景技术Background technique

旋风分离器是一种通过离心力的作用从含有杂质的气体中分离出固体颗粒或液滴的静止机械设备。它结构简单、没有运动部件,在实际应用中分离效率高且压降适中,可以广泛应用于高温高压以及颗粒浓度高的场合,在催化裂化工艺、发电及加工制造业、涡轮进气等方面均发挥着重要的作用。A cyclone separator is a static mechanical device that separates solid particles or liquid droplets from a gas containing impurities by the action of centrifugal force. It has a simple structure, no moving parts, high separation efficiency and moderate pressure drop in practical applications, and can be widely used in high temperature, high pressure and high particle concentration occasions. play an important role.

最基本的旋风分离器,是一种通过离心力的作用从含有杂质的气体中分离出固体颗粒或液滴的静止机械设备。气流从旋风分离器的进气口进入分离器内部,该进气口一般沿切向布置。进入分离器内,气流便开始向下做旋转运动,在气流旋转的过程中,颗粒由于受到离心力的作用而向分离器器壁运动,被甩向器壁的颗粒也就从气体中分离了出来。这些被分离器出来的颗粒最终将从下部的排尘口被排出。而气体将在分离器底部附近从外侧的向下旋转转变为内侧的向上旋转,并从中心筒也就是排气管被排出。The most basic cyclone separator is a static mechanical device that separates solid particles or liquid droplets from a gas containing impurities by the action of centrifugal force. The airflow enters the interior of the cyclone separator from the air inlet, which is generally arranged tangentially. When entering the separator, the airflow begins to rotate downwards. During the rotation of the airflow, the particles are moved to the separator wall due to the action of centrifugal force, and the particles thrown to the wall are also separated from the gas. . The particles from the separator will eventually be discharged from the lower dust outlet. The gas will change from a downward rotation on the outside to an upward rotation on the inside near the bottom of the separator, and is discharged from the central cylinder, which is the exhaust pipe.

传统的旋风分离器由于存在结构设计上的不足,导致其分离性能较差。这些不足包括,分离器顶部因二次流形成的“上灰环”、中心筒下端附近的“短路流”及排尘口附近的“粉尘返混”。为了改进这些结构使得分离器效率能够明显提高,国内外研究者从旋风分离器的进气口、排气口和排尘口等结构出发进行了大量的改进研究,设计了多种不同类型的高效低阻的旋风分离器结构。Traditional cyclone separators have poor separation performance due to structural design deficiencies. These deficiencies include the "upper ash ring" formed by the secondary flow at the top of the separator, the "short-circuit flow" near the lower end of the central cylinder, and the "dust back-mixing" near the dust outlet. In order to improve these structures so that the efficiency of the separator can be significantly improved, researchers at home and abroad have carried out a lot of improvement research on the structure of the air inlet, exhaust port and dust outlet of the cyclone separator, and designed a variety of different types of high-efficiency cyclone separators. Low resistance cyclone separator structure.

发明内容Contents of the invention

本发明的目的是提出一种在中心筒内装设导流叶片的旋风分离器,以有效改善分离器内部流场,提高旋风分离器对固体颗粒的分离效率。The purpose of the present invention is to propose a cyclone separator with guide vanes installed in the central cylinder, so as to effectively improve the internal flow field of the separator and improve the separation efficiency of the cyclone separator for solid particles.

本发明提出的在中心筒内装设导流叶片的旋风分离器,包括筒体、中心筒、中心筒内管、导流叶片和导流罩;所述的筒体的上部为圆筒形,筒体的下部为圆锥形,圆筒形筒体的一侧设有旋风分离器进口,圆筒形筒体的顶部设有排气口,圆锥形筒体的下部为排尘口;所述的中心筒偏心安装在圆筒形筒体段,中心筒与圆筒形筒体的偏心距e为2%D0~6%D0,D0为圆筒形筒体的直径,偏离方向为垂直于气流入口并远离入口;所述的中心筒内管同心安装在中心筒内,中心筒内管下端布置圆锥形的导流罩,导流罩锥顶开设一个小的圆孔;所述的导流叶片的轮毂安装在中心筒内管上,导流叶片的轮缘布置在中心筒的内壁上,导流叶片的四边分别为导流叶片进口边、导流叶片出口边、导流叶片轮缘和导流叶片轮毂,导流叶片轮毂固定在中心筒内管的表面;导流叶片的结构由导流叶片轮毂与导流叶片轮缘各自的进口、中点、出口三处的导流叶片切线与圆周方向的夹角即叶片安放角βi,1、βi,0、βm,1、βm,0、βo,1、βo,0确定,其中,导流叶片轮毂的进口轮廓线与圆周方向的夹角为βi,1,导流叶片轮缘进口轮廓线与圆周方向的夹角为βi,0,导流叶片轮毂中点轮廓线与圆周方向的夹角为βm,1,导流叶片轮缘中点轮廓线与圆周方向的夹角βm,0,导流叶片轮毂出口轮廓线与圆周方向的夹角为βo,1,导流叶片轮缘出口轮廓线与圆周方向的夹角βo,0,则有βi,1为55°~64°,βi,1i,0为15°~24°,βo,1、βo,0均为90°,导流叶片轮毂中点的角度βm,1和导流叶片轮缘中点的角度βm,0分别按照各自进出口角度之和按比例系数k确定,比例系数k为0.3~0.6,即βm,1=k(βi,1o,1),βm,0=k(βi,0o,0),以导流叶片轮毂的进口、中点、出口三处的角度确定一条抛物线作为导流叶片轮毂的型线,以导流叶片轮缘的进口、中点、出口三处的角度确定一条抛物线作为导流叶片轮缘的型线。The cyclone separator with guide vanes installed in the central cylinder proposed by the present invention includes a cylinder body, a central cylinder, an inner tube of the central cylinder, guide vanes and a flow deflector; the upper part of the cylinder is cylindrical, and the cylinder The lower part of the body is conical, one side of the cylindrical body is provided with a cyclone separator inlet, the top of the cylindrical body is provided with an exhaust port, and the lower part of the conical body is a dust discharge port; the center The cylinder is eccentrically installed on the cylindrical cylinder section, the eccentric distance e between the central cylinder and the cylindrical cylinder is 2% D 0 ~ 6% D 0 , D 0 is the diameter of the cylindrical cylinder, and the deviation direction is perpendicular to The air flow inlet is far away from the inlet; the inner tube of the central tube is installed concentrically in the central tube, and the lower end of the inner tube of the central tube is arranged with a conical shroud, and a small circular hole is opened on the cone top of the shroud; The hub of the blade is installed on the inner tube of the central cylinder, and the rim of the guide vane is arranged on the inner wall of the central cylinder. The four sides of the guide vane are the inlet side of the guide vane, the outlet side of the guide vane, the rim of the guide vane and the Guide vane hub, the guide vane hub is fixed on the surface of the inner tube of the central cylinder; the structure of the guide vane is composed of the guide vane tangent line and The included angle in the circumferential direction is determined by the blade placement angle β i,1 , β i,0 , β m,1 , β m,0 , β o,1 , β o,0, among which, the inlet contour of the guide vane hub The included angle with the circumferential direction is β i,1 , the included angle between the guide vane rim inlet contour line and the circumferential direction is β i,0 , the included angle between the guide vane hub midpoint contour line and the circumferential direction is β m, 1 . The angle between the midpoint contour line of the guide vane rim and the circumferential direction is β m,0 , the angle between the guide vane hub outlet contour line and the circumferential direction is β o,1 , and the angle between the guide vane hub outlet contour line and the circumferential direction is β o,1 . For the angle β o,0 in the circumferential direction, β i,1 is 55°~64°, β i,1i,0 is 15°~24°, β o,1 and β o,0 are both 90°, the angle β m,1 of the center point of the hub of the guide vane and the angle β m,0 of the center point of the rim of the guide vane are respectively determined according to the sum of the respective inlet and outlet angles and proportional coefficient k, and the proportional coefficient k is 0.3 to 0.6 , that is, β m,1 =k(β i,1o,1 ), β m,0 =k(β i,0o,0 ), taking the inlet, midpoint, and outlet of the guide vane hub Three angles determine a parabola as the profile line of the guide vane hub, and a parabola is determined as the profile line of the guide vane hub by the angles of the inlet, midpoint, and outlet of the guide vane rim.

上述旋风分离器中的导流叶片的数目,可以为4~10。The number of guide vanes in the cyclone separator can be 4-10.

本发明提出的在中心筒内装设导流叶片的旋风分离器,其优点是,在旋风分离器的中心筒内部沿周向均匀布置导流叶片,导流叶片的叶片安放角变化规律由正交试验得到最优水平,并且将中心筒向远离分离器切向入口的方向偏置。导流叶片的轮毂布置在中心筒内管的外壁上,轮缘布置在中心筒的内壁上。中心筒内管下端布置圆锥形的导流罩,导流罩锥顶开设一个小的圆孔。通过导流叶片及中心筒偏置对于旋风分离器内流场的改善,使得气流在流入中心筒之前已经汇集成一股向上的主流,该主流中气流速度以竖直向上的轴向速度为主。这种对流场的改善使得旋风分离器流场内部涡核漩涡强度减小,外部漩涡强度增大,有利于固体颗粒的分离,提高了分离效率;同时,由于加装导流叶片带来的排气段压力损失增长较小,对旋风分离器总体压降的影响较小。本发明的在中心筒内装设导流叶片的旋风分离器结构简单,易于加工和制造,适用于任何类型的切流式旋风分离器。本发明旋风分离器结构简单,提高分离效率效果显著。The cyclone separator with guide vanes installed in the central cylinder proposed by the present invention has the advantage that the guide vanes are uniformly arranged along the circumferential direction inside the central cylinder of the cyclone separator, and the change law of the vane placement angle of the guide vanes is determined by the orthogonal Trials yielded optimum levels and the central cylinder was biased away from the tangential inlet of the separator. The hub of the guide vane is arranged on the outer wall of the inner tube of the central cylinder, and the rim is arranged on the inner wall of the central cylinder. A conical shroud is arranged at the lower end of the inner tube of the central cylinder, and a small circular hole is opened on the conical top of the shroud. Through the improvement of the flow field in the cyclone separator through the deflection of the guide vanes and the central cylinder, the airflow has converged into an upward main flow before flowing into the central cylinder, and the air velocity in the main flow is dominated by the vertical upward axial velocity. This improvement of the flow field reduces the vortex intensity of the inner vortex core in the flow field of the cyclone separator, and increases the intensity of the outer vortex, which is beneficial to the separation of solid particles and improves the separation efficiency; at the same time, due to the addition of guide vanes The increase in pressure loss in the exhaust section is small, and the impact on the overall pressure drop of the cyclone separator is small. The cyclone separator with guide vanes installed in the central cylinder of the present invention has a simple structure, is easy to process and manufacture, and is suitable for any type of cutting flow cyclone separator. The cyclone separator of the present invention has simple structure and remarkable effect of improving separation efficiency.

附图说明Description of drawings

图1是本发明提出的在中心筒内装设导流叶片的旋风分离器的结构示意图。Fig. 1 is a schematic structural view of a cyclone separator provided with guide vanes in a central cylinder proposed by the present invention.

图2是图1所示的旋风分离器中的中心筒内导流叶片的结构示意图。Fig. 2 is a schematic structural view of guide vanes in the central cylinder in the cyclone separator shown in Fig. 1 .

图1和图2中,1是旋风分离器进口,2是中心筒,3是圆筒形筒体,4是圆锥形筒体,5是排尘口,6是排气口,7是导流叶片,8是导流罩,9是中心筒内管,10是导流叶片进口边,11是导流叶片出口边,12是导流叶片轮缘,13是导流叶片轮毂。In Figure 1 and Figure 2, 1 is the cyclone separator inlet, 2 is the central cylinder, 3 is a cylindrical cylinder, 4 is a conical cylinder, 5 is a dust outlet, 6 is an exhaust outlet, and 7 is a guide Blade, 8 is the guide cover, 9 is the inner tube of the central cylinder, 10 is the inlet edge of the guide vane, 11 is the outlet edge of the guide vane, 12 is the rim of the guide vane, and 13 is the hub of the guide vane.

具体实施方式Detailed ways

本发明提出的在中心筒内装设导流叶片的旋风分离器,其结构如图1所示,包括筒体、中心筒2、中心筒内管9、导流叶片7和导流罩8。筒体的上部为圆筒形,筒体的下部为圆锥形,圆筒形筒体3的一侧设有旋风分离器进口1,圆筒形筒体3的顶部设有排气口6,圆锥形筒体4的下部为排尘口5。中心筒2偏心安装在圆筒形筒体段,中心筒2与圆筒形筒体3的偏心距e为2%D0~6%D0,D0为圆筒形筒体的直径,偏离方向为垂直于气流入口并远离入口。中心筒内管9同心安装在中心筒2内,中心筒内管9下端布置圆锥形的导流罩8,导流罩锥顶开设一个小的圆孔。导流叶片7的轮毂13安装在中心筒内管9上,导流叶片的轮缘12布置在中心筒2的内壁上,导流叶片7的四边分别为导流叶片进口边10、导流叶片出口边11、导流叶片轮缘12和导流叶片轮毂13,导流叶片轮毂13固定在中心筒内管9的表面;导流叶片的结构由导流叶片轮毂与导流叶片轮缘各自的进口、中点、出口三处的导流叶片切线与圆周方向的夹角即叶片安放角βi,1、βi,0、βm,1、βm,0、βo,1、βo,0确定,如图2所示,其中,导流叶片轮毂的进口轮廓线与圆周方向的夹角为βi,1,导流叶片轮缘进口轮廓线与圆周方向的夹角为βi,0,导流叶片轮毂中点轮廓线与圆周方向的夹角为βm,1,导流叶片轮缘中点轮廓线与圆周方向的夹角βm,0,导流叶片轮毂出口轮廓线与圆周方向的夹角为βo,1,导流叶片轮缘出口轮廓线与圆周方向的夹角βo,0,则有βi,1为55°~64°,βi,1i,0为15°~24°,βo,1、βo,0均为90°,导流叶片轮毂中点的角度βm,1和导流叶片轮缘中点的角度βm,0分别按照各自进出口角度之和按比例系数k确定,比例系数k为0.3~0.6,即βm,1=k(βi,1o,1),βm,0=k(βi,0o,0),以导流叶片轮毂的进口、中点、出口三处的角度确定一条抛物线作为导流叶片轮毂的型线,以导流叶片轮缘的进口、中点、出口三处的角度确定一条抛物线作为导流叶片轮缘的型线。The cyclone separator with guide vanes installed in the central cylinder proposed by the present invention has a structure as shown in FIG. The upper part of the cylinder is cylindrical, and the lower part of the cylinder is conical. One side of the cylindrical cylinder 3 is provided with a cyclone separator inlet 1, and the top of the cylindrical cylinder 3 is provided with an exhaust port 6. The cone The bottom of the cylindrical body 4 is a dust outlet 5. The central cylinder 2 is eccentrically installed on the cylindrical cylinder section, the eccentric distance e between the central cylinder 2 and the cylindrical cylinder 3 is 2% D 0 ~ 6% D 0 , D 0 is the diameter of the cylindrical cylinder, and the deviation The direction is perpendicular to the airflow inlet and away from the inlet. The inner pipe 9 of the central cylinder is concentrically installed in the central cylinder 2, and the lower end of the inner pipe 9 of the central cylinder is arranged with a conical shroud 8, and a small circular hole is opened at the conical top of the shroud. The hub 13 of the guide vane 7 is installed on the inner tube 9 of the central cylinder, the rim 12 of the guide vane is arranged on the inner wall of the central cylinder 2, and the four sides of the guide vane 7 are respectively the guide vane inlet edge 10, the guide vane Outlet edge 11, guide vane wheel rim 12 and guide vane hub 13, guide vane hub 13 is fixed on the surface of center tube inner tube 9; The angle between the tangent line of the guide vane at the inlet, midpoint and outlet and the circumferential direction is the blade placement angle β i,1 , β i,0 , β m,1 , β m,0 , β o,1 , β o ,0 is determined, as shown in Figure 2, where the angle between the inlet contour line of the guide vane hub and the circumferential direction is β i,1 , and the angle between the inlet contour line of the guide vane rim and the circumferential direction is β i, 0 , the included angle between the guide vane hub midpoint contour line and the circumferential direction is β m,1 , the included angle between the guide vane hub midpoint contour line and the circumferential direction β m,0 , the guide vane hub outlet contour line and The included angle in the circumferential direction is β o,1 , and the included angle β o,0 between the outlet contour line of the guide vane rim and the circumferential direction, then β i,1 is 55°~64°, β i,1i ,0 is 15°~24°, β o,1 and β o,0 are both 90°, the angle β m,1 of the midpoint of the guide vane hub and the angle β m,0 of the midpoint of the guide vane rim are respectively According to the sum of the respective entrance and exit angles, it is determined by the proportional coefficient k, and the proportional coefficient k is 0.3~0.6, that is, β m,1 =k(β i,1o,1 ), β m,0 =k(β i, 0o,0 ), a parabola is determined by the angles of the inlet, midpoint and outlet of the guide vane hub as the shape line of the guide vane hub, and the inlet, midpoint and outlet of the guide vane rim The angle at determines a parabola as the profile of the guide vane rim.

上述旋风分离器中的导流叶片的数目,可以为4~10。The number of guide vanes in the cyclone separator can be 4-10.

以下结合附图,详细介绍本发明旋风分离器的工作原理和工作过程:Below in conjunction with accompanying drawing, introduce in detail the operating principle and working process of cyclone separator of the present invention:

携带固体颗粒的含尘气体从旋风分离器进口1沿切向进入,绕中心筒2旋转,固体颗粒由于受到离心力的作用被甩向圆筒形筒体3的内壁,最终落入排尘口5,分离后的气体在排尘口5附近由外部的向下旋转转变为内部的向上旋转,并流入中心筒2,经由导流叶片7最终从排气口6排出。The dust-laden gas carrying solid particles enters tangentially from the cyclone separator inlet 1 and rotates around the central cylinder 2. The solid particles are thrown to the inner wall of the cylindrical cylinder 3 due to centrifugal force, and finally fall into the dust outlet 5 , the separated gas changes from external downward rotation to internal upward rotation near the dust discharge port 5, and flows into the central cylinder 2, and is finally discharged from the exhaust port 6 through the guide vanes 7.

如图1所示,导流叶片7在中心筒2内部沿圆周方向均匀布置,其轮毂位于中心筒内管9的外壁上,其轮缘位于中心筒2的内壁上,中心筒内管9下端布置圆锥形的导流罩8,导流罩8锥顶开设一个小的圆孔。As shown in Figure 1, the guide vanes 7 are evenly arranged in the circumferential direction inside the central cylinder 2, and its hub is located on the outer wall of the central cylinder inner tube 9, its rim is located on the inner wall of the central cylinder 2, and the lower end of the central cylinder inner tube 9 A conical shroud 8 is arranged, and a small circular hole is opened on the conical top of the shroud 8 .

如图1和图2所示,以所述旋风分离器的筒体直径D0为参考,中心筒轴线与旋风分离器筒体轴线的偏心距离e为2%D0~6%D0,偏离方向为垂直于气流切向入口并远离入口。导导流叶片的结构由导流叶片轮毂与导流叶片轮缘各自的进口、中点、出口三处的导流叶片切线与圆周方向的夹角即叶片安放角βi,1、βi,0、βm,1、βm,0、βo,1、βo,0确定。其中,导流叶片轮毂的进口轮廓线与圆周方向的夹角为βi,1,导流叶片轮缘进口轮廓线与圆周方向的夹角为βi,0,导流叶片轮毂中点轮廓线与圆周方向的夹角为βm,1,导流叶片轮缘中点轮廓线与圆周方向的夹角βm,0,导流叶片轮毂出口轮廓线与圆周方向的夹角为βo,1,导流叶片轮缘出口轮廓线与圆周方向的夹角βo,0,则有βi,1为55°~64°,βi,1i,0为15°~24°,βo,1、βo,0均为90°。轮毂与轮缘中点的角度βm,1、βm,0按照各自进出口角度之和的一定比例确定,比例系数k为0.3~0.6,即βm,1=k(βi,1o,1),βm,0=k(βi,0o,0)。以轮毂的进口、中点、出口三处的角度确定一条抛物线作为轮毂叶片型线,以轮缘的进口、中点、出口三处的角度确定一条抛物线作为轮缘叶片型线。As shown in Figures 1 and 2, taking the cylinder diameter D 0 of the cyclone separator as a reference, the eccentric distance e between the axis of the central cylinder and the cylinder axis of the cyclone separator is 2% D 0 to 6% D 0 , which deviates from The direction is perpendicular to the airflow tangential to the inlet and away from the inlet. The structure of the guide vane consists of the angle between the guide vane tangent and the circumferential direction at the inlet, midpoint, and outlet of the guide vane hub and the guide vane rim, namely, the blade placement angle β i,1 , β i, 0 , β m,1 , β m,0 , β o,1 , β o,0 are determined. Among them, the angle between the inlet contour line of the guide vane hub and the circumferential direction is β i,1 , the angle between the inlet contour line of the guide vane hub and the circumferential direction is β i,0 , and the midpoint contour line of the guide vane hub The included angle with the circumferential direction is β m,1 , the included angle β m,0 between the midpoint contour line of the guide vane rim and the circumferential direction, and the included angle β o,1 between the guide vane hub outlet contour line and the circumferential direction , the angle β o,0 between the outlet contour line of the guide vane rim and the circumferential direction, then β i,1 is 55°~64°, β i,1i,0 is 15°~24°, β o,1 and β o,0 are both 90°. The angles β m,1 and β m,0 between the hub and the midpoint of the rim are determined according to a certain ratio of the sum of the respective inlet and outlet angles, and the proportional coefficient k is 0.3 to 0.6, that is, β m,1 = k(β i,1 + β o,1 ), β m,0 =k(β i,0o,0 ). A parabola is determined at the angles of the entrance, midpoint, and exit of the hub as the profile line of the hub blade, and a parabola is determined at the angles of the entrance, midpoint, and exit of the rim as the profile line of the rim blade.

在本发明的一个实施例中,中心筒上的导流叶片的数目为6,导流叶片7的结构由导流叶片轮毂与导流叶片轮缘各自的进口、中点、出口三处的导流叶片切线与圆周方向的夹角即叶片安放角βi,1、βi,0、βm,1、βm,0、βo,1、βo,0确定,角度大小依次为58°、37°、74°、63.5°、90°、90°。In one embodiment of the present invention, the number of guide vanes on the central cylinder is 6, and the structure of the guide vanes 7 is guided by the respective inlets, midpoints, and outlets of the guide vane hub and the guide vane rim. The angle between the tangent line of the flow blade and the circumferential direction, that is, the blade placement angle β i,1 , β i,0 , β m,1 , β m,0 , β o,1 , β o,0 is determined, and the angles are 58° in turn , 37°, 74°, 63.5°, 90°, 90°.

Claims (2)

1. a kind of cyclone separator that guide vane is installed in central tube, which is characterized in that including cylinder, central tube, center Cylinder inner tube, guide vane and kuppe;The top of the cylinder is cylindrical shape, and the lower part of cylinder is conical, cylindrical shape cylinder The side of body is equipped with cyclone inlet, and the top of cylindrical drum is equipped with exhaust outlet, and the lower part of divergent-cone wall is dust discharge Mouthful;The central tube is eccentrically mounted at cylindrical drum section, and the eccentric distance e of central tube and cylindrical drum is 2%D0~6% D0, D0For the diameter of cylindrical drum, offset direction is perpendicular to air flow inlet and far from entrance;The central tube inner tube is same It feels at ease in central tube, the kuppe of central tube inner tube lower end arrangement cone, the kuppe vertex of a cone opens up a small circular hole; The wheel hub of the guide vane is mounted in central tube inner tube, and the wheel rim of guide vane is arranged on the inner wall of central tube, is led Flow blade four when being respectively guide vane inlet side, guide vane exit, guide vane wheel rim and guide vane wheel hub, lead Stream blade wheel hub is fixed on the surface of central tube inner tube;The structure of guide vane is each by guide vane wheel hub and guide vane wheel rim From import, midpoint, outlet three at guide vane tangent line and circumferencial direction angle, that is, blade angle βi,1、βi,0、βm,1、 βm,0、βo,1、βo,0It determines, wherein, the import contour line of guide vane wheel hub and the angle of circumferencial direction are βi,1, guide vane wheel The angle of edge import contour line and circumferencial direction is βi,0, the angle of guide vane wheel hub midpoint contour line and circumferencial direction is βm,1, the angle β of guide vane wheel rim midpoint contour line and circumferencial directionm,0, guide vane wheel hub outlet profile line and circumference side To angle be βo,1, the angle β of guide vane wheel rim outlet profile line and circumferencial directiono,0, then have βi,1It is 55 °~64 °, βi,1i,0It is 15 °~24 °, βo,1、βo,0It is 90 °, the angle beta at guide vane wheel hub midpointm,1With guide vane wheel rim midpoint Angle betam,0According to the sum of respective inlet and outlet angle, coefficient k determines in proportion respectively, and proportionality coefficient k is 0.3~0.6, i.e. βm,1 =k (βi,1o,1), βm,0=k (βi,0o,0), with the angle-determining one at the import of guide vane wheel hub, midpoint, outlet three Molded line of the parabola as guide vane wheel hub, with the angle-determining one at the import of guide vane wheel rim, midpoint, outlet three Molded line of the parabola as guide vane wheel rim.
2. cyclone separator as described in claim 1, it is characterised in that the number of the guide vane is 4~10.
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* Cited by examiner, † Cited by third party
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DE202018103655U1 (en) * 2017-07-03 2018-07-26 Outotec (Finland) Oy Cyclone with vanes
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CN109351491A (en) * 2018-10-30 2019-02-19 湖南天际智慧材料科技有限公司 A kind of turbine separates and collects the device of nanometer powder and is made from it powder manufacturing apparatus
CN109078765A (en) * 2018-11-09 2018-12-25 青岛特利尔环保股份有限公司 A kind of cyclone separator
CN112238003B (en) * 2019-07-19 2022-08-12 中国石油化工股份有限公司 Gas-solid separation device and coupling separation method
CN114932018B (en) * 2022-05-06 2024-11-05 北京凯盛建材工程有限公司 Cyclone dust removal device
CN118022506B (en) * 2024-04-11 2024-06-11 中国石油天然气第八建设有限公司 Steam-water separation device

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85104117A (en) * 1985-05-28 1986-12-10 格鲁德比勒公司 Separator using centrifugal force
SU1655580A1 (en) * 1989-06-14 1991-06-15 Семибратовский Филиал Научно-Исследовательского Института По Санитарной И Промышленной Очистке Газов Cyclone
CN201454710U (en) * 2009-06-30 2010-05-12 北京三川世纪技术有限公司 Guide vane type cyclone and combined filter separator
CN201552068U (en) * 2009-12-02 2010-08-18 镇江飞利达电站设备有限公司 Straw ash negative-pressure recovery device of biomass power generation plant
CN201776193U (en) * 2010-05-31 2011-03-30 中国石油大学(华东) Guide vane type tornadotron with stepped slit of dust exhaust structure
CN201791602U (en) * 2010-08-20 2011-04-13 冯和平 Cyclone dust collector
CN102615005A (en) * 2012-03-29 2012-08-01 中国石油大学(北京) Cyclone separator with damping reduction device
CN102671778A (en) * 2012-05-30 2012-09-19 郭丰亮 Cyclone dust collector with spiral air inlet pipe
CN104646195A (en) * 2015-02-11 2015-05-27 天津腾达集团有限公司 Cyclone dust collector
CN204448317U (en) * 2015-02-11 2015-07-08 相鹏 Multifunction efficient cyclone separator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1003157C2 (en) * 1996-05-17 1997-11-18 Romico Hold A V V Rotary particle separator with high separation rate.

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85104117A (en) * 1985-05-28 1986-12-10 格鲁德比勒公司 Separator using centrifugal force
SU1655580A1 (en) * 1989-06-14 1991-06-15 Семибратовский Филиал Научно-Исследовательского Института По Санитарной И Промышленной Очистке Газов Cyclone
CN201454710U (en) * 2009-06-30 2010-05-12 北京三川世纪技术有限公司 Guide vane type cyclone and combined filter separator
CN201552068U (en) * 2009-12-02 2010-08-18 镇江飞利达电站设备有限公司 Straw ash negative-pressure recovery device of biomass power generation plant
CN201776193U (en) * 2010-05-31 2011-03-30 中国石油大学(华东) Guide vane type tornadotron with stepped slit of dust exhaust structure
CN201791602U (en) * 2010-08-20 2011-04-13 冯和平 Cyclone dust collector
CN102615005A (en) * 2012-03-29 2012-08-01 中国石油大学(北京) Cyclone separator with damping reduction device
CN102671778A (en) * 2012-05-30 2012-09-19 郭丰亮 Cyclone dust collector with spiral air inlet pipe
CN104646195A (en) * 2015-02-11 2015-05-27 天津腾达集团有限公司 Cyclone dust collector
CN204448317U (en) * 2015-02-11 2015-07-08 相鹏 Multifunction efficient cyclone separator

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