CN202506603U - Variable-cross section bending torsion movable blade rotary coal powder separator - Google Patents
Variable-cross section bending torsion movable blade rotary coal powder separator Download PDFInfo
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Abstract
Description
技术领域 technical field
本实用新型涉及煤粉分离器领域,特别涉及一种变截面弯扭动叶的旋转煤粉分离器。 The utility model relates to the field of coal powder separators, in particular to a rotary coal powder separator with variable section curved and twisted blades. the
背景技术 Background technique
目前,为了适应煤种、负荷变化以及低NOX燃烧器运行的需要,一般制粉系统的中速磨大多配静动叶组合式旋转煤粉分离器。旋转煤粉分离器是制粉系统的重要组成部分,其运行性能直接影响制粉系统及整个机组的安全经济运行。现有的静动叶组合式旋转煤粉分离器由于导向静叶及转子动叶型式的固定性,需要通过改变静、动叶安装的组合方式及转子动叶的转速来提高分离器的运行性能,不仅会使旋转煤粉分离器的安装变得复杂繁琐,而且无形中增加了电动机的能耗;现有的静动叶组合式旋转煤粉分离器不能在低能耗下达到较高的分离效率,其分离效率的增加必定会引起其能耗的增大。对于新型弯扭动叶式旋转煤粉分离器的最新研究未考虑转子动叶片的实际厚度,而且没有对其结构进行优化设计,因而研究低能耗下具有较高分离效率的旋转煤粉分离器的最优结构成为研究的热题。 At present, in order to meet the needs of coal types, load changes and low NO X burner operation, the medium-speed mills of general pulverization systems are mostly equipped with static and moving blade combined rotary coal separators. The rotary pulverized coal separator is an important part of the pulverizing system, and its operating performance directly affects the safe and economical operation of the pulverizing system and the entire unit. Due to the fixity of the guide vane and the rotor vane type of the existing static and movable vane combined rotary coal separator, it is necessary to improve the operation performance of the separator by changing the combination of the static and movable vane installation and the rotating speed of the rotor vane , which will not only make the installation of the rotary pulverized coal separator complicated and cumbersome, but also increase the energy consumption of the motor virtually; the existing static and moving blade combined rotary pulverized coal separator cannot achieve high separation efficiency under low energy consumption , the increase of its separation efficiency will definitely lead to the increase of its energy consumption. The latest research on the new curved and twisted blade type rotary coal powder separator does not consider the actual thickness of the rotor moving blade, and does not optimize its structure, so the research on the rotary coal powder separator with higher separation efficiency under low energy consumption The optimal structure has become a hot topic of research.
发明内容 Contents of the invention
本实用新型为了解决现有旋转煤粉分离器不能在低能耗下达到较高的分离效率以及弯扭动叶式旋转煤粉分离器最优结构的不确定性等问题,提供了一种考虑转子动叶实际厚度、对转子动叶进汽侧入口段及出汽侧出口段截面进行渐变设计的一种新型旋转煤粉分离器,并对其结构进行了优化设计。 In order to solve the problems that the existing rotary pulverized coal separator cannot achieve higher separation efficiency under low energy consumption and the uncertainty of the optimal structure of the rotary pulverized coal separator with curved and twisted blades, the utility model provides a The actual thickness of the moving blade, a new type of rotary pulverized coal separator with gradual design of the cross-section of the inlet section of the steam inlet side and the outlet section of the steam outlet side of the rotor moving blade, and an optimized design of its structure. the
解决上述问题所采用的技术方案如下: The technical solution adopted to solve the above problems is as follows:
该旋转煤粉分离器由分离器壳体、导向静叶、动叶框架、转子动叶、落煤管、 锥形挡板和回粉管组成,导向静叶为传统直叶片,均匀分布在回粉管顶部的外圈且固定在分离器壳体上;转子动叶为变截面弯扭叶片,均匀分布在内圈的动叶框架上;落煤管位于分离器壳体的中心;锥形挡板设置在转子动叶的下部,且与转子动叶的下部底边匹配对接。 The rotary pulverized coal separator is composed of a separator shell, guide vane, moving vane frame, rotor vane, coal drop pipe, conical baffle and powder return pipe. The guide vane is a traditional straight blade, evenly distributed in the return The outer ring on the top of the powder pipe is fixed on the separator shell; the rotor blades are curved and twisted blades with variable cross-section, which are evenly distributed on the blade frame of the inner ring; the coal falling pipe is located in the center of the separator shell; The plate is arranged at the lower part of the rotor blade, and is mated and docked with the bottom edge of the lower part of the rotor blade. the
所述转子动叶的进汽侧变截面段的四个弧AG、AH、CK、CL,出汽侧变截面段的四个弧BI、BJ、DM、DN,各自的曲率半径不等。 The four arcs AG, AH, CK, and CL of the variable section on the steam inlet side of the rotor blade, and the four arcs BI, BJ, DM, and DN on the variable section on the steam outlet side have different radii of curvature. the
所述转子动叶中进行弯曲后的弧AB与弧CD的曲率半径不等。 The curvature radii of the curved arc AB and arc CD in the rotor blade are not equal. the
所述转子动叶的内测出汽边的上部顶角B和外侧进汽边的下部底角C均向转子动叶的中心扭转,减小了煤粉气流进入时的阻挡损失和流出时的涡流损失,大大降低了阻力损失,有助于分离器分离电耗的降低。 The upper top angle B of the internal steam outlet side of the rotor blade and the lower bottom angle C of the outer steam inlet side are both twisted towards the center of the rotor blade, which reduces the blocking loss when the pulverized coal airflow enters and the airflow when it flows out. The eddy current loss greatly reduces the resistance loss, which helps to reduce the separation power consumption of the separator. the
所述转子动叶的弯度为15°,扭转角度为25° The rotor blades have a camber of 15° and a torsion angle of 25°
所述转子动叶的进汽边AC和出汽边BD均为直线。 Both the steam inlet side AC and the steam outlet side BD of the rotor blade are straight lines. the
所述导向静叶的水平安装角γ∈[0,45°];转子动叶的水平安装角α∈[0,45°],垂直安装角β∈[0,45°]。 The horizontal installation angle γ∈[0,45°] of the guide vane; the horizontal installation angle α∈[0,45°] and the vertical installation angle β∈[0,45°] of the rotor blade. the
所述转子动叶的水平安装角度为10°。 The horizontal installation angle of the rotor blades is 10°. the
本实用新型的有益效果为: The beneficial effects of the utility model are:
本实用新型对旋转煤粉分离器的转子动叶考虑了实际厚度,并对其进汽侧入口段及出汽侧出口段的截面进行了渐变设计,在更低的电动机转速下能使旋转煤粉分离器的出口煤粉较细,分离性能较高,阻力损失较低,从而提高了制粉系统、锅炉及整个机组的安全性和经济性,对电厂的节能降耗有重要作用;其弯扭转子动叶片最佳结构的确定,为旋转煤粉分离器的设计及制造提供了新方法。 The utility model considers the actual thickness of the rotor blade of the rotary coal powder separator, and gradually changes the section of the inlet section of the steam inlet side and the outlet section of the steam outlet side, so that the rotating coal can be rotated at a lower motor speed. The pulverized coal at the outlet of the powder separator is finer, the separation performance is higher, and the resistance loss is lower, thereby improving the safety and economy of the pulverization system, the boiler and the entire unit, and playing an important role in the energy saving and consumption reduction of the power plant; its bend The determination of the optimal structure of the twisted rotor blade provides a new method for the design and manufacture of the rotary pulverized coal separator. the
附图说明 Description of drawings
图1是本实用新型的整体结构示意图; Fig. 1 is the overall structural representation of the utility model;
图2是转子动叶的结构示意图; Figure 2 is a schematic structural view of the rotor blade;
图3是转子动叶变截面弯扭后型线部分的俯视图; Figure 3 is a top view of the section of the rotor blade after bending and twisting;
图4是导向静叶和转子动叶中间横截面的剖面图; Figure 4 is a sectional view of the middle cross section of the guide vane and the rotor vane;
图5是图4中Y处的局部放大及导向静叶和转子动叶的水平安装角γ和α的安装示意图; Fig. 5 is a partial enlargement of Y in Fig. 4 and a schematic diagram of the installation of the horizontal installation angles γ and α of the guide vane and the rotor vane;
图6是转子动叶的垂直安装角β的安装示意图。 Fig. 6 is a schematic diagram of installation of the vertical installation angle β of rotor blades. the
图中标号: Labels in the figure:
1-分离器壳体;2-导向静叶;3-动叶框架;4-转子动叶;5-落煤管6-锥形挡板;7-回粉管。 1-separator shell; 2-guide vane; 3-moving blade frame; 4-rotor moving blade; 5-coal drop pipe 6-conical baffle; 7-powder return pipe. the
OO′是旋转轴中心线; OO' is the centerline of the axis of rotation;
h是转子动叶的长度; h is the length of the rotor blade;
d是转子动叶弯扭前的宽度; d is the width of the rotor blade before bending;
δ是转子动叶的厚度; δ is the thickness of the rotor blade;
A、B、C、D是转子动叶的四个顶点; A, B, C, D are the four vertices of the rotor blade;
AC是转子动叶的进汽边; AC is the steam inlet side of the rotor blade;
BD是转子动叶的出汽边; BD is the steam outlet side of the rotor blade;
弧AG、AH、CK、CL是转子动叶进汽侧变截面段的四个弧; The arcs AG, AH, CK, and CL are the four arcs of the variable section section on the inlet steam side of the rotor blade;
弧BI、BJ、DM、DN是转子动叶出汽侧变截面段的四个弧; Arcs BI, BJ, DM, and DN are four arcs of the variable section section on the outlet steam side of the rotor blade;
γ是导向静叶的水平安装角; γ is the horizontal installation angle of the guide vane;
α是转子动叶的水平安装角; α is the horizontal installation angle of the rotor blade;
β是转子动叶的垂直安装角。 β is the vertical installation angle of rotor blades. the
具体实施方式 Detailed ways
本实用新型提供了一种变截面弯扭动叶的旋转煤粉分离器,下面结合附图和 具体实施方式对本实用新型做进一步说明。 The utility model provides a rotary pulverized coal separator with variable cross-section curved and twisted blades. The utility model will be further described below in conjunction with the accompanying drawings and specific embodiments. the
如图1所示,本实施方式由分离器壳体1、导向静叶2、动叶框架3、转子动叶4、落煤管5、锥形挡板6和回粉管7组成。导向静叶2为传统直叶片,均匀分布在回粉管7顶部的外圈且固定在分离器壳体1上;转子动叶4为变截面的弯扭叶片,均匀分布在内圈的动叶框架3上;落煤管5位于分离器壳体1的中心位置;锥形挡板6设置在转子动叶4的下部,且与转子动叶4的下部底边匹配对接。
As shown in FIG. 1 , this embodiment consists of a
如图2和图3所示,本实施方式所述的旋转煤粉分离器的转子动叶4为考虑叶片实际厚度,且对叶片进汽侧入口段及出汽侧出口段的截面进行渐变设计的弯扭叶片,转子动叶4由传统直叶向其变截面的弯扭叶片转化的具体实施过程如下:
As shown in Fig. 2 and Fig. 3, the
1)厚度:选定一个长方体直叶片,其长为h,宽为d,高(叶片的厚度)为δ; 1) Thickness: select a cuboid straight blade whose length is h, width is d, and height (thickness of the blade) is δ;
2)变截面:选取长方体直叶片的四条厚度边的中点,记为A、B、C、D;在长方体直叶片的四条宽度边上依次选取G、I,H、J,K、M,F、N八个点,依次连接AG、AH、CK、CL、BI、BJ、DM、DN;做弧AG、AH、CK、CL、BI、BJ、DM、DN,其曲率半径分别为R1~R8,且各曲率半径Rx取值不等(其中x为自然数∈[1,8]);连接AC、BD,则面AHJBDNLC、面AGIBDMKC、面AGIBJH和面CKMDNL组成变截面四面体; 2) Variable cross-section: select the midpoint of the four thickness sides of the straight cuboid blade, denoted as A, B, C, D; select G, I, H, J, K, M in turn on the four width sides of the cuboid straight blade, Eight points F and N are sequentially connected to AG, AH, CK, CL, BI, BJ, DM, DN; make arcs AG, AH, CK, CL, BI, BJ, DM, DN, and their curvature radii are R 1 ~R 8 , and the values of each curvature radius R x are different (where x is a natural number ∈ [1, 8]); connecting AC and BD, the face AHJBDNLC, the face AGIBDMKC, the face AGIBJH and the face CKMDNL form a variable cross-section tetrahedron;
3)弯曲:始终保持AC,BD两边为直线,将变截面四面体直叶片进行纵向弧形弯曲,弧AB的曲率半径为R9,弧CD的曲率半径为R10,且R9与R10取值不等; 3) Bending: Always keep AC and BD as straight lines, and bend the straight blade of variable cross-section tetrahedron in a longitudinal arc. The radius of curvature of arc AB is R 9 , the radius of curvature of arc CD is R 10 , and R 9 and R 10 The values are not equal;
4)扭转:首先保持变截面弯曲叶片上的A、C、D三个顶点的位置不变,且维持BD边始终为直线,使内测出汽边的上部顶角B向转子动叶4的中心发生扭转;在出汽边上部顶角B扭转完成的基础上,保持变截面弯扭叶片上的A、B、 D三个顶点的位置不变,且维持AC边始终为直线,使外侧进汽边的下部底角C向转子动叶4的中心发生扭转。
4) Torsion: First, keep the positions of the three vertices A, C, and D on the curved blade with variable cross-section unchanged, and keep the side BD always as a straight line, so that the upper vertex B of the internally measured steam outlet side is directed toward the
导向静叶2的水平安装角γ∈[0,45°];转子动叶4的水平安装角α∈[0,45°],垂直安装角β∈[0,45°];转子动叶4弯度的取值范围为[0,45°];转子动叶4扭转角度的取值范围为[0,45°]。
The horizontal installation angle γ∈[0,45°] of the
导向静叶2的水平安装角γ的定义:结合图5,γ为中间横截面剖面图中导向静叶2的叶宽PQ与导向静叶2的内侧出汽边的端点P与旋转轴中心线OO′的投影点O的连线OP的夹角(锐角)。
The definition of the horizontal installation angle γ of the guide vane 2: combined with Fig. 5, γ is the vane width PQ of the
转子动叶4的垂直安装角β的定义:结合图6,取面AGIBJH的中心点E点、面CKMDNL的中心点F点,连接两中心点EF,则EF所在直线与旋转轴中心线OO′的夹角(锐角)即为转子动叶4的垂直安装角β。
The definition of the vertical installation angle β of the rotor rotor blade 4: combined with Figure 6, take the center point E of the surface AGIBJH and the center point F of the surface CKMDNL, and connect the two center points EF, then the line where EF is located and the centerline of the rotation axis OO′ The included angle (acute angle) is the vertical installation angle β of
转子动叶4的水平安装角α的定义:结合图5,在转子动叶4的垂直安装角β确定的基础上,作一个平面通过EF的中点且垂直于旋转轴中心线OO′,所作平面与旋转轴中心线OO′交点的投影点为点O,与转子动叶4的AC、BD两边交点的投影点分别为点A′、B′,则直线OB′与直线B′A′的夹角(锐角)即为转子动叶4的水平安装角α。
The definition of the horizontal installation angle α of the rotor blade 4: combined with Fig. 5, on the basis of the determination of the vertical installation angle β of the
转子动叶4弯度的定义:结合图2,转子动叶(4)弯曲后(即虚线叶片)的进汽边和出汽边与起始变截面直叶片进汽边和出汽边的夹角。 The definition of the camber of the rotor blade 4: combined with Figure 2, the angle between the steam inlet side and the steam outlet side of the curved rotor blade (4) (that is, the dotted line blade) and the initial variable cross-section straight blade’s steam inlet side and steam outlet side . the
转子动叶4扭转角度的定义:结合图2,转子动叶(4)的内测出汽边的上部顶角B和外侧进汽边的下部底角C向转子动叶(4)的中心扭转的角度。 The definition of the torsion angle of the rotor blade 4: combined with Figure 2, the upper top angle B of the inner steam outlet side of the rotor blade (4) and the lower bottom angle C of the outer steam inlet side are twisted towards the center of the rotor blade (4) Angle. the
通过理论分析与模拟试验可知,本实用新型对旋转煤粉分离器的转子动叶4不仅考虑了实际厚度、而且对其进汽侧入口段及出汽侧出口段的截面进行了渐变设计,在系统通风量不变的条件下,分离器弯扭转子动叶最佳结构为弯度为15°, 扭转角度为25°,水平安装角度为10°,与传统直叶式旋转煤粉分离器相比,其流场分布比较均匀,主要体现在速度分布和压力分布的均匀程度上;分离器的转子转速相对降低22%;出口的煤粉细度降低18.7%;综合分离效率提高1.43%;内部两相场的通风阻力降低了194Pa。本实用新型对旋转煤粉分离器转子动叶4考虑实际厚度、对其进汽侧入口段及出汽侧出口段的截面进行渐变设计,在更低的电动机转速下可使旋转煤粉分离器的出口煤粉较细,分离性能较高,阻力损失较低,因而提高了制粉系统、锅炉及整个机组的安全经济性,对电厂的节能降耗有重要作用;旋转煤粉分离器的弯扭转子动叶片最佳结构的确定,为分离器的设计及制造提供了新方法和理论依据。
Through theoretical analysis and simulation tests, it can be seen that the utility model not only considers the actual thickness of the
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104759412A (en) * | 2015-04-21 | 2015-07-08 | 黑龙江迪科电站技术有限公司 | Adjustable dynamic rotary separator for coal mill |
CN105583155A (en) * | 2016-03-23 | 2016-05-18 | 君联益能(北京)科技有限公司 | Double-regulation flow distribution type efficient separator |
-
2011
- 2011-12-27 CN CN2011205552113U patent/CN202506603U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104759412A (en) * | 2015-04-21 | 2015-07-08 | 黑龙江迪科电站技术有限公司 | Adjustable dynamic rotary separator for coal mill |
CN105583155A (en) * | 2016-03-23 | 2016-05-18 | 君联益能(北京)科技有限公司 | Double-regulation flow distribution type efficient separator |
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