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CN109230549B - A composite pneumatic conveying swirl elbow - Google Patents

A composite pneumatic conveying swirl elbow Download PDF

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CN109230549B
CN109230549B CN201811182731.7A CN201811182731A CN109230549B CN 109230549 B CN109230549 B CN 109230549B CN 201811182731 A CN201811182731 A CN 201811182731A CN 109230549 B CN109230549 B CN 109230549B
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swirl
pipe
inlet
gas
straight pipe
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CN109230549A (en
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李建平
周锋
杨道龙
田世伟
田超
李雨泽
罗江南
周后宇
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China University of Mining and Technology CUMT
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/52Adaptations of pipes or tubes
    • B65G53/523Wear protection
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/52Adaptations of pipes or tubes
    • B65G53/521Adaptations of pipes or tubes means for preventing the accumulation or for removal of deposits

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Air Transport Of Granular Materials (AREA)

Abstract

一种复合型气力输送旋流弯管,包括用于输送流体的管体,所述管体包括入口直管部、弯管部及出口直管部三部分。所述的入口直管部包括入口直管段、气固混合入口、旋流气体入口、旋流气体混合室和旋流生成孔;所述的弯管部包括弯管段、一级旋流生成管和二级旋流生成管;所述的出口直管部包括出口直管段和开在其端部的气固混合出口。本发明能够产生充足的旋流气体,实现旋流输送,有效减少颗粒与管壁之间的碰撞和摩擦,提高物料输送质量,有效延长弯管使用寿命,同时降低局部压力损失,提高气力输送系统的工作效率。

Figure 201811182731

A composite pneumatic conveying swirl elbow comprises a pipe body for conveying fluid, the pipe body comprises three parts: an inlet straight pipe part, a curved pipe part and an outlet straight pipe part. The inlet straight pipe part includes an inlet straight pipe section, a gas-solid mixing inlet, a swirl gas inlet, a swirl gas mixing chamber and a swirl generation hole; the elbow part includes an elbow section, a first-level swirl generation pipe and a secondary swirl generating tube; the outlet straight pipe part includes an outlet straight pipe section and a gas-solid mixing outlet opened at its end. The invention can generate sufficient swirling gas, realize swirling conveying, effectively reduce the collision and friction between particles and the pipe wall, improve the quality of material conveying, effectively prolong the service life of the elbow, reduce the local pressure loss, and improve the pneumatic conveying system. work efficiency.

Figure 201811182731

Description

一种复合型气力输送旋流弯管A composite pneumatic conveying swirl elbow

技术领域technical field

本发明涉及一种煤炭颗粒气力输送管道,尤其是一种复合型气力输送旋流弯管。The invention relates to a coal particle pneumatic conveying pipeline, in particular to a composite pneumatic conveying swirl elbow.

背景技术Background technique

煤炭是我国的基础能源和重要原料,煤炭工业关系着国家经济命脉。随着国民经济的迅速发展,我国对煤炭的需求量日益增加。煤炭运输环节在煤炭开采成本中占有很大比例,现有井下输送设备配套设施复杂,安全事故频发。气力输送是利用一定压力和速度的气流输送颗粒物料的运输技术,已广泛应用于石油、化工及食品加工等领域,清洁、绿色、循环利用率高。Coal is my country's basic energy source and an important raw material, and the coal industry is related to the lifeline of the national economy. With the rapid development of the national economy, my country's demand for coal is increasing. Coal transportation accounts for a large proportion of coal mining costs. The existing underground transportation equipment and supporting facilities are complex, and safety accidents occur frequently. Pneumatic conveying is a transportation technology that uses air flow with a certain pressure and speed to transport granular materials. It has been widely used in petroleum, chemical and food processing fields. It is clean, green and has high recycling rate.

然而目前煤炭气力输送过程中仍不可避免的会发生管道磨损问题,导致输送能效较低,煤炭粉尘大量溢出污染环境,尤其以弯管最为明显。另外,气力输送系统中的压力损失包含沿程压力损失和局部压力损失,在弯管处主要表现为局部压力损失,颗粒流流速大小和流动方向随弯管急剧改变,产生速度梯度,导致流场内部形成湍流,从而加剧颗粒之间的碰撞和破碎。However, at present, the problem of pipeline wear is still inevitable in the process of coal pneumatic transportation, resulting in low transportation energy efficiency and a large amount of coal dust overflowing to pollute the environment, especially the elbow is the most obvious. In addition, the pressure loss in the pneumatic conveying system includes the pressure loss along the way and the local pressure loss, which is mainly manifested as the local pressure loss at the elbow. Turbulence is formed inside, which intensifies the collision and fragmentation between particles.

发明内容SUMMARY OF THE INVENTION

为了克服现有技术的上述不足,本发明提供一种煤炭颗粒气力输送管道,能够产生充足的旋流气体,实现持续性旋流输送,可有效减少颗粒与管壁之间的碰撞和摩擦,提高物料输送质量,有效延长弯管使用寿命,同时降低局部压力损失,提高气力输送系统的工作效率。In order to overcome the above-mentioned deficiencies of the prior art, the present invention provides a coal particle pneumatic conveying pipeline, which can generate sufficient swirling gas, realize continuous swirling conveying, effectively reduce the collision and friction between the particles and the pipe wall, and improve the The quality of material conveying can effectively prolong the service life of the elbow, reduce the local pressure loss, and improve the working efficiency of the pneumatic conveying system.

本发明解决其技术问题采用的技术方案是:包括用于输送流体的管体,所述的管体包括依次相连的入口直管部、弯管部及出口直管部,所述的入口直管部包括入口直管段、气固混合入口、旋流气体入口、旋流气体混合室和旋流生成孔,气固混合入口位于入口直管段的端口,入口直管段的外周形成有一个旋流气体混合室,旋流气体混合室上开设有旋流气体入口,旋流气体混合室与入口直管段之间沿周向均匀分布偶数个旋流生成孔,且每个旋流生成孔与入口直管段切向和轴向所成的夹角均相同;所述的弯管部包括弯管段、一级旋流生成管和二级旋流生成管,一级旋流生成管和二级旋流生成管的数量相等,且二者数量的总和与旋流生成孔的一致,一级旋流生成管和二级旋流生成管平行相间铸造于弯管部段外壁四周,与入口直管段的旋流生成孔交错分布;各个旋流生成管内外径尺寸均相同,每个旋流生成管的一端都连通至旋流气体混合室,另一端通过旋流生成孔连通到弯管部段内部,旋流生成孔与弯管段切向和轴向所成的夹角均相同;一级旋流生成管末端位于弯管段的1/3处,二级旋流生成管末端位于弯管段的2/3处;所述的出口直管部包括出口直管段和开在其端部的气固混合出口。The technical solution adopted by the present invention to solve the technical problem is: comprising a pipe body for conveying fluid, the pipe body comprises an inlet straight pipe part, a curved pipe part and an outlet straight pipe part which are connected in sequence, and the inlet straight pipe part is connected in sequence. The gas-solid mixing inlet includes an inlet straight pipe section, a gas-solid mixing inlet, a swirl gas inlet, a swirl gas mixing chamber and a swirl generating hole. The gas-solid mixing inlet is located at the port of the inlet straight pipe section, and a swirl gas mixture is formed on the outer circumference of the inlet straight pipe section. The swirl gas mixing chamber is provided with a swirl gas inlet, and an even number of swirl generation holes are evenly distributed along the circumferential direction between the swirl gas mixing chamber and the inlet straight pipe section, and each swirl generation hole is tangential to the inlet straight pipe section. The angle formed by the direction and the axial direction is the same; the elbow section includes a elbow section, a first-stage swirl generation pipe and a second-level swirl generation pipe, and a first-level swirl generation pipe and a second-level swirl generation pipe The numbers are equal, and the sum of the two numbers is consistent with that of the swirl generation holes. The primary swirl generation pipe and the secondary swirl generation pipe are cast in parallel and alternately around the outer wall of the elbow section, and the swirl generation of the inlet straight pipe section The holes are staggered; the inner and outer diameters of each swirl generating pipe are the same, one end of each swirl generating pipe is connected to the swirl gas mixing chamber, and the other end is connected to the inside of the elbow section through the swirl generating hole, and the swirl generating The tangential and axial angles formed by the hole and the elbow section are the same; the end of the primary swirl generation pipe is located at 1/3 of the elbow section, and the end of the secondary cyclone generation pipe is located at 2/3 of the elbow section The outlet straight pipe section includes an outlet straight pipe section and a gas-solid mixing outlet opened at its end.

相比现有技术,本发明的一种煤炭颗粒气力输送管道,结构紧凑体积小,节约安装空间,一级旋流生成管和二级旋流生成管长度比翅型旋流辅管长度短,降低了旋流气体沿程压力损失;通过入口直管部的旋流生成孔使输送颗粒起旋,一级旋流生成管和二级旋流生成管不断为管路补充旋流气体,避免因旋流流量不足而重新恢复成纯轴流输送,从而减少颗粒与管壁之间的碰撞和摩擦,提高物料输送质量,有效延长弯管使用寿命,同时降低局部压力损失,提高气力输送系统的工作效率,具有较强的创新性和广泛的实用性。Compared with the prior art, the coal particle pneumatic conveying pipeline of the present invention has a compact structure and small volume, saves installation space, and the lengths of the primary swirl generation pipe and the secondary swirl generation pipe are shorter than that of the fin type swirl auxiliary pipe. The pressure loss of the swirl gas along the way is reduced; the swirl generation hole in the inlet straight pipe part makes the conveyed particles swirl, and the first-level swirl generation pipe and the second-level swirl generation pipe continuously supplement the swirl gas to the pipeline to avoid the The swirl flow is insufficient and the pure axial flow is restored, thereby reducing the collision and friction between the particles and the pipe wall, improving the quality of material conveying, effectively prolonging the service life of the elbow, reducing the local pressure loss, and improving the work of the pneumatic conveying system. Efficiency, strong innovation and wide practicability.

附图说明Description of drawings

下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

图1是本发明一个实施例的结构示意图。FIG. 1 is a schematic structural diagram of an embodiment of the present invention.

图中,1、管体,2、入口直管段,3、弯管段,4、出口直管段,5、气固混合入口,6、旋流气体入口,7、旋流气体混合室,8、旋流生成孔,9、一级旋流生成管,10、二级旋流生成管,11、气固混合出口。In the figure, 1. Pipe body, 2. Inlet straight pipe section, 3. Elbow pipe section, 4. Outlet straight pipe section, 5. Gas-solid mixing inlet, 6. Swirl gas inlet, 7. Swirl gas mixing chamber, 8. Swirl generation hole, 9, first-level swirl generation pipe, 10, second-level swirl generation pipe, 11, gas-solid mixing outlet.

具体实施方式Detailed ways

为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明的保护范围。In order to make the purposes, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments These are some embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

图1示出了本发明一个较佳的实施例的结构示意图,图中的一种复合型气力输送旋流弯管,包括用于输送流体的管体1,所述管体1包括入口直管部、弯管部及出口直管部三部分。FIG. 1 shows a schematic structural diagram of a preferred embodiment of the present invention. In the figure, a composite pneumatic conveying swirl elbow includes a pipe body 1 for conveying fluid, and the pipe body 1 includes an inlet straight pipe It consists of three parts: the pipe part, the elbow part and the outlet straight pipe part.

所述的入口直管部包括入口直管段2、气固混合入口5、旋流气体入口6、旋流气体混合室7和六个旋流生成孔8,气固混合入口5位于入口直管段2的端口,入口直管段2的外周形成有一个旋流气体混合室7,旋流气体混合室7上开设有旋流气体入口6,旋流气体混合室7与入口直管段2之间沿周向均匀分布六个旋流生成孔8,且每个旋流生成孔8与入口直管段2切向和轴向所成的夹角均相同,气体从旋流入口6进入旋流混合室7后,一部分气流通过六个旋流孔8生成旋流气流,使颗粒流在直管部开始起旋。旋流气体及轴流气体均由空压机加压后先输送至储气罐内进行稳压,再分别进入管道内,物料从前一段管道输送到该管体1时,颗粒流并非直接进入弯管部,而是首先进入该管体1的直管部,气流流经前段直管时为轴流流场,经过旋流生成孔8后,轴向气流在旋流气流的扰动混合下产生旋流流场,系统内颗粒开始起旋,以“旋浮”状态在中心流场中向前输送,并在管壁周围形成一层气流缓冲区,减少颗粒与管壁之间的碰撞和摩擦,降低系统能耗。The inlet straight pipe portion includes an inlet straight pipe section 2, a gas-solid mixing inlet 5, a swirl gas inlet 6, a swirl gas mixing chamber 7 and six swirl generating holes 8, and the gas-solid mixing inlet 5 is located in the inlet straight pipe section 2. A swirling gas mixing chamber 7 is formed on the outer periphery of the inlet straight pipe section 2, and a swirling gas inlet 6 is opened on the swirling gas mixing chamber 7. Six swirl flow generation holes 8 are evenly distributed, and each swirl flow generation hole 8 has the same angle formed by the tangential and axial directions of the inlet straight pipe section 2. After the gas enters the swirl flow mixing chamber 7 from the swirl flow inlet 6, A part of the airflow passes through the six swirl holes 8 to generate a swirl airflow, so that the particle flow starts to swirl at the straight pipe portion. Both the swirl gas and the axial flow gas are pressurized by the air compressor and then transported to the gas storage tank for pressure stabilization, and then enter the pipeline respectively. When the material is transported from the previous pipeline to the pipe body 1, the particle flow does not directly enter the bend. The pipe part first enters the straight pipe part of the pipe body 1. When the airflow flows through the straight pipe in the front section, it is an axial flow field. In the flow field, the particles in the system begin to swirl, and are transported forward in the central flow field in a "floating" state, and a layer of airflow buffer zone is formed around the pipe wall to reduce the collision and friction between the particles and the pipe wall. Reduce system power consumption.

作为本实施例的优选设计是,所述旋流气体入口6与阀门相连,通过阀门控制旋流气体总流量,从而根据颗粒的种类、颗粒流的速度和压力调节旋流流量占比。As a preferred design of this embodiment, the swirl gas inlet 6 is connected to a valve, and the total flow of swirl gas is controlled by the valve, so as to adjust the proportion of swirl flow according to the type of particles, the speed and pressure of particle flow.

所述的弯管部包括弯管段3、三个一级旋流生成管9和三个二级旋流生成管10,一级旋流生成管9和二级旋流生成管10平行相间铸造于弯管部段外壁四周,与入口直管段2的六个旋流生成孔8交错分布,旋流气体入口6避免正对任意一个旋流生成孔8,否则大部分气体会通过该孔直接进入到输送管道内部,导致颗粒流具有较大的不稳定性;各个旋流生成管内外径尺寸均相同,每个旋流生成管的一端都连通至旋流气体混合室7,另一端通过旋流生成孔8连通到弯管部段内部,旋流生成孔8与弯管段3切向和轴向所成的夹角均相同;一级旋流生成管9末端位于弯管段3的1/3处,二级旋流生成管10末端位于弯管段3的2/3处。气流从旋流入口6进入旋流混合室7后,没有进入旋流孔8的气流分别进入一级旋流生成管9和二级旋流生成管10,在弯管部为颗粒流补充旋流流量,保证输送物料时颗粒不断起旋。The elbow section includes elbow sections 3, three primary swirl generation tubes 9 and three secondary swirl generation tubes 10. The primary swirl generation tubes 9 and the secondary swirl generation tubes 10 are cast in parallel and alternately. Around the outer wall of the elbow section, it is staggered with the six swirl generating holes 8 of the inlet straight pipe section 2. The swirl gas inlet 6 avoids facing any swirl generating hole 8, otherwise most of the gas will directly enter through this hole. To the inside of the conveying pipeline, the particle flow has greater instability; the inner and outer diameters of each swirl generation pipe are the same, and one end of each swirl generation pipe is connected to the swirl gas mixing chamber 7, and the other end passes through the swirl flow. The generation hole 8 is connected to the inside of the elbow section, and the angle formed by the swirl generation hole 8 and the elbow section 3 in the tangential and axial directions are the same; 3, the end of the secondary swirl generating pipe 10 is located at 2/3 of the elbow section 3. After the airflow enters the swirl mixing chamber 7 from the swirl inlet 6, the airflow that does not enter the swirl hole 8 enters the primary swirl generation pipe 9 and the secondary swirl generation pipe 10 respectively, and supplements the swirl flow for the particle flow at the elbow. The flow rate ensures that the particles continue to spin when the material is conveyed.

所述的出口直管部包括出口直管段4和开在其端部的气固混合出口11。颗粒流从弯管部进入到出口直管部后,逐渐恢复成纯轴流输送,通过气固混合出口11进入到下一级输送管道。The outlet straight pipe portion includes an outlet straight pipe section 4 and a gas-solid mixing outlet 11 opened at its end. After the particle flow enters the straight pipe portion of the outlet from the elbow portion, it gradually returns to pure axial flow transportation, and enters the next-stage transportation pipeline through the gas-solid mixing outlet 11 .

旋流气体入口6、一级旋流生成管9和二级旋流生成管10的具体数量不局限于本实施例中的取值,还可以依据弯管强度、管径及耐磨性等实际条件进行增减。The specific numbers of the swirl gas inlet 6, the first-stage swirl generation pipe 9 and the second-stage swirl generation pipe 10 are not limited to the values in this embodiment, and can also be determined according to actual conditions such as elbow strength, pipe diameter, and wear resistance. conditions are increased or decreased.

以上所述,仅是本发明的较佳实施例,并非对本发明做任何形式上的限制,凡是依据本发明的技术实质,对以上实施例所做出任何简单修改和同等变化,均落入本发明的保护范围之内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention in any form. Any simple modifications and equivalent changes made to the above embodiments according to the technical essence of the present invention shall fall into the scope of the present invention. within the scope of protection of the invention.

Claims (3)

1.一种煤炭颗粒气力输送管道,包括用于输送流体的管体(1),所述的管体(1)包括依次相连的入口直管部、弯管部及出口直管部,其特征是:1. A coal particle pneumatic conveying pipeline, comprising a pipe body (1) for conveying fluid, and the pipe body (1) comprises an inlet straight pipe portion, a curved pipe portion and an outlet straight pipe portion that are connected in sequence, and it is characterized in that: Yes: 所述的入口直管部包括入口直管段(2)、气固混合入口(5)、旋流气体入口(6)、旋流气体混合室(7)和旋流生成孔(8),气固混合入口(5)位于入口直管段(2)的端口,入口直管段(2)的外周形成有一个旋流气体混合室(7),旋流气体混合室(7)上开设有旋流气体入口(6),旋流气体混合室(7)与入口直管段(2)之间沿周向均匀分布偶数个旋流生成孔(8),且每个旋流生成孔(8)与入口直管段(2)切向和轴向所成的夹角均相同;The inlet straight pipe portion comprises an inlet straight pipe section (2), a gas-solid mixing inlet (5), a swirl gas inlet (6), a swirl gas mixing chamber (7) and a swirl generating hole (8), and the gas-solid The mixing inlet (5) is located at the port of the inlet straight pipe section (2), a swirling gas mixing chamber (7) is formed on the outer periphery of the inlet straight pipe section (2), and a swirling gas inlet is opened on the swirling gas mixing chamber (7). (6), between the swirl gas mixing chamber (7) and the inlet straight pipe section (2), an even number of swirl flow generation holes (8) are evenly distributed along the circumferential direction, and each swirl flow generation hole (8) is connected to the inlet straight pipe section. (2) The angles formed by the tangential and axial directions are the same; 所述的弯管部包括弯管段(3)、一级旋流生成管(9)和二级旋流生成管(10),一级旋流生成管(9)和二级旋流生成管(10)的数量相等,且二者数量的总和与旋流生成孔(8)的一致,一级旋流生成管(9)和二级旋流生成管(10)平行相间铸造于弯管部段外壁四周,与入口直管段(2)上的旋流生成孔(8)交错分布;各个旋流生成管内外径尺寸均相同,每个旋流生成管的一端都连通至旋流气体混合室(7),另一端通过旋流生成孔(8)连通到弯管部段内部,旋流生成孔(8)与弯管段(3)切向和轴向所成的夹角均相同;一级旋流生成管(9)末端位于弯管段(3)的1/3处,二级旋流生成管(10)末端位于弯管段(3)的2/3处;The elbow section includes a elbow section (3), a primary swirl generation pipe (9), a secondary swirl generation pipe (10), a primary swirl generation pipe (9) and a secondary swirl generation pipe The number of (10) is equal, and the sum of the two numbers is consistent with that of the swirl flow generation hole (8). Around the outer wall of the section, the swirl generating holes (8) on the inlet straight pipe section (2) are alternately distributed; the inner and outer diameters of each swirl generating pipe are the same, and one end of each swirl generating pipe is connected to the swirl gas mixing chamber. (7), the other end is connected to the inside of the elbow section through the swirl flow generation hole (8), and the angle formed by the swirl flow generation hole (8) and the elbow section (3) in the tangential and axial directions are the same; one The end of the primary swirl generation pipe (9) is located at 1/3 of the elbow section (3), and the end of the secondary cyclone generation pipe (10) is located at 2/3 of the elbow section (3); 所述的出口直管部包括出口直管段(4)和开在其端部的气固混合出口(11)。The outlet straight pipe portion includes an outlet straight pipe section (4) and a gas-solid mixing outlet (11) opened at the end thereof. 2.根据权利要求1所述的一种煤炭颗粒气力输送管道,其特征是:所述旋流生成孔(8)的数量为六个,一级旋流生成管(9)和二级旋流生成管(10)均为三个。2. A coal particle pneumatic conveying pipeline according to claim 1, characterized in that: the number of the swirl flow generating holes (8) is six, the first-level swirl flow generating pipe (9) and the second-level swirl flow There are three generating tubes (10). 3.根据权利要求1或2所述的一种煤炭颗粒气力输送管道,其特征是:所述的旋流气体入口(6)与阀门相连,通过阀门控制旋流气体总流量。3. A coal particle pneumatic conveying pipeline according to claim 1 or 2, characterized in that: the swirling gas inlet (6) is connected to a valve, and the total flow of swirling gas is controlled by the valve.
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CN113307037B (en) * 2021-04-17 2022-11-15 华北水利水电大学 Dilute phase pneumatic conveying cyclone antifriction elbow
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