CN202935945U - Positive and negative pressure combined dense phase powder material pneumatic conveying device - Google Patents

Positive and negative pressure combined dense phase powder material pneumatic conveying device Download PDF

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CN202935945U
CN202935945U CN 201220617348 CN201220617348U CN202935945U CN 202935945 U CN202935945 U CN 202935945U CN 201220617348 CN201220617348 CN 201220617348 CN 201220617348 U CN201220617348 U CN 201220617348U CN 202935945 U CN202935945 U CN 202935945U
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negative pressure
powder
bin
receiving bin
conveying
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王昕�
杨文娟
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Qinhuangdao Yanda Yuanda Mechanical & Electrical Technology Co ltd
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Qinhuangdao Yanshan University Yuanda Mechanical & Electrical Technology Co ltd
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Abstract

The positive and negative pressure combined dense phase powder material pneumatic conveying equipment has positive pressure conveying and sending bin and negative pressure conveying and receiving bin, the sending bin and the receiving bin are coaxially connected via middle powder feeding butterfly valve, the lower end of the sending bin is equipped with powder outlet pipeline, the powder outlet pipeline is equipped with several powder outlet two-way valves, the upper portion of the sending bin is equipped with material level sensor, pressure sensor and air inlet valve, the upper end of the receiving bin is connected with air filtering bin, a partition board is placed between the receiving bin and the air filtering bin, on the partition board a bag-type air filter is mounted, the back-blowing pipe of the filter is connected with air storage tank by means of control valve, the above-mentioned filtering bin is equipped with vacuum generator, the receiving bin is equipped with material level sensor and feed inlet, the feed inlet is connected with powder inlet pipeline, and the powder inlet pipeline is equipped with several powder inlet. The utility model discloses can realize that the powder material is by the transport of multipoint to multipoint, have simple structure, small, area is few, characteristics that conveying efficiency is high.

Description

正负压组合式密相粉体物料气力输送装置Positive and negative pressure combined dense phase powder material pneumatic conveying device

技术领域 technical field

本实用新型涉及粉体物料密相气力输送设备,具体涉及一种正负压组合式密相粉体物料气力输送装置。  The utility model relates to dense phase pneumatic conveying equipment for powder materials, in particular to a positive and negative pressure combined dense phase powder material pneumatic conveying device. the

背景技术 Background technique

气力输送技术按输送单位质量物料与所消耗的气体质量之比可分为密相气力输送和稀相气力输送两种。由于密相气力输送效率高,节能效果明显,同时具有对物料颗粒破坏小、固气分离容易等明显优势,近几年来得到了广泛应用。密相气力输送操作可采用正压气力输送实现,也可采用负压气力输送实现。当需要实现由多个始发点向多个目标点密相输送操作时,需要将正负压密相输送设备组合起来使用。现有技术的正负压密相输送组合设备,存在结构复杂、占地面积大、输送效率低的问题。  Pneumatic conveying technology can be divided into dense phase pneumatic conveying and dilute phase pneumatic conveying according to the ratio of conveying unit mass material to gas mass consumed. Due to the high efficiency of dense-phase pneumatic conveying, obvious energy-saving effect, and obvious advantages such as small damage to material particles and easy solid-gas separation, it has been widely used in recent years. Dense-phase pneumatic conveying operation can be realized by positive pressure pneumatic conveying or negative pressure pneumatic conveying. When it is necessary to realize the dense-phase conveying operation from multiple starting points to multiple target points, it is necessary to combine positive and negative pressure dense-phase conveying equipment. The positive and negative pressure dense-phase conveying combined equipment in the prior art has the problems of complex structure, large floor area and low conveying efficiency. the

发明内容 Contents of the invention

本实用新型的目的在于针对上述问题,提供一种结构简单、占地面积少、输送效率高,能够实现粉体物料由多点到多点输送操作的正负压组合式密相粉体物料气力输送装置。  The purpose of this utility model is to solve the above problems, to provide a positive and negative pressure combined dense-phase powder material air pump with simple structure, small floor space, high conveying efficiency, and the ability to realize the powder material from multi-point to multi-point conveying operation. delivery device. the

实现上述目的的技术方案是:一种正负压组合式密相粉体物料气力输送装置,它具有一个置于下方的正压输送发送仓和一个置于上方的负压输送接受仓,所述的正压输送发送仓和负压输送接受仓为下部设有圆锥斗体的圆筒形仓体,所述的正压输送发送仓和负压输送接受仓经置于中间的一进粉蝶阀相连接同轴线设置,所述正压输送发送仓的下端连接一装配管道阀的出粉管道,所述正压输送发送仓的上部装配有发送仓料位传感器、压力传感器和压缩空气进气阀,所述负压输送接受仓的上端连接一空气过滤器,所述负压输送接受仓与所述空气过滤仓之间设置一固定隔板,置于所述负压输送接受仓内的袋式空气过滤器与所述固定隔板上的过滤器安装口相连接,由所述过滤器安装口引出的过滤器反吹管通过一两位两通控制阀与一压缩空气储气罐相连接,在所述空气过滤仓的上面装配有真空发生器,所述的负压输送接受仓装配有接受仓料位传感器和进料口,该进料口连接一进粉管道,所述的进粉管道装配有多个进粉承压双路阀,所述的出粉管道装配有多个出粉承压双路阀。  The technical solution to achieve the above purpose is: a positive and negative pressure combined dense-phase powder material pneumatic conveying device, which has a positive pressure conveying sending bin placed below and a negative pressure conveying receiving bin placed above, the The positive pressure conveying sending chamber and the negative pressure conveying receiving chamber are cylindrical chambers with conical buckets at the bottom. It is connected with the coaxial line, the lower end of the positive pressure conveying and sending chamber is connected with a powder outlet pipeline equipped with a pipeline valve, and the upper part of the positive pressure conveying and sending chamber is equipped with a sending chamber material level sensor, a pressure sensor and a compressed air inlet valve , the upper end of the negative pressure delivery receiving bin is connected to an air filter, a fixed partition is set between the negative pressure delivery receiving bin and the air filter bin, and the bag-type The air filter is connected to the filter installation port on the fixed partition, and the filter blowback pipe drawn from the filter installation port is connected to a compressed air storage tank through a two-position two-way control valve. The air filter bin is equipped with a vacuum generator above, and the negative pressure delivery receiving bin is equipped with a receiving bin material level sensor and a feeding port, and the feeding port is connected to a powder feeding pipeline, and the powder feeding pipeline is assembled There are multiple powder inlet pressure-bearing two-way valves, and the powder outlet pipeline is equipped with multiple powder outlet pressure-bearing two-way valves. the

本实用新型的技术方案还包括:所述的袋式空气过滤器设置多个。  The technical solution of the present invention also includes: multiple bag-type air filters are provided. the

本实用新型正负压组合式密相粉体物料气力输送装置,能够实现粉体物料由多点到多点输送操作,并且具有结构简单、体积小、占地面积少、输送效率高的特点。  The positive and negative pressure combined dense-phase powder material pneumatic conveying device of the utility model can realize the conveying operation of the powder material from multiple points to multiple points, and has the characteristics of simple structure, small volume, less floor space and high conveying efficiency. the

附图说明 Description of drawings

图1是本正负压组合式密相粉体物料气力输送装置的结构示意图。  Figure 1 is a schematic structural view of the positive and negative pressure combined dense phase powder material pneumatic conveying device. the

具体实施方式 Detailed ways

结合附图对本实用新型的具体实施方式进行说明。  The specific embodiment of the utility model will be described in conjunction with the accompanying drawings. the

如附图,本正负压组合式密相粉体物料气力输送装置具有一个置于下方的正压输送发送仓2和一个置于上方的负压输送接受仓7,其正压输送发送仓2和负压输送接受仓7为下部设有圆锥斗体的圆筒形仓体,两仓体下部圆锥斗体的锥角在30°至60°之间。正压输送发送仓2的圆筒仓体部分的直径与高度之比在1:0.8至1:1.8之间,该正压输送发送仓2的上端设置成半球面体,在该半球面体上的中心位置安装一承压进粉蝶阀3,该承压进粉蝶阀3将正压输送发送仓2和负压输送接受仓7同轴线竖置连接在一起。在正压输送发送仓2的上部装配有发送仓料位传感器4、压力传感器5和压缩空气进气阀6。正压输送发送仓2的下端连接一装配管道阀1的出粉管道17,出粉管道17装配有多个出粉承压双路阀20。负压输送接受仓7的上端连接一空气过滤仓8,负压输送接受仓7与空气过滤仓8两者之间通过法兰连接。在负压输送接受仓7与空气过滤仓8之间设置一固定隔板9,该固定隔板9将负压输送接受仓7与空气过滤仓8两仓隔开。固定隔板9上开有圆孔,其圆孔内装有袋式空气过滤器14,在该过滤器开口的上方装有压缩空气反吹气管13,反吹气管13与两位两通控制阀11相连,两位两通阀11安装在压缩空气储气罐12上,该压缩空气储气罐12位于空气过滤仓8的外部并与其固定连接。如附图实施例,本实用新型可在固定隔板9上开设多个圆孔,并在每一圆孔内分别安装一袋式空气过滤器14,各袋式空气过滤器14分别装配压缩空气反吹气管13及两位两通控制阀11,而构成多袋式空气过滤器结构。在负压输送接受仓7的圆筒体上,靠近袋式空气过滤器14的下端设有一料位传感器15和一进料口16,进料口16连接一进粉管道18,该进粉管道18装配有多个进粉承压双路阀19。  As shown in the attached figure, this positive and negative pressure combined dense-phase powder material pneumatic conveying device has a positive pressure conveying and sending chamber 2 placed below and a negative pressure conveying receiving chamber 7 placed above, and its positive pressure conveying and sending chamber 2 And the negative pressure conveying accepting bin 7 is the cylindrical bin body that the bottom is provided with conical bucket body, and the taper angle of the conical bucket body at the bottom of the two bin bodies is between 30° and 60°. The ratio of the diameter to the height of the cylinder body part of the positive pressure conveying chamber 2 is between 1:0.8 and 1:1.8, and the upper end of the positive pressure conveying chamber 2 is arranged as a hemispherical body, and the center of the hemispherical body A pressure-bearing powder-feeding butterfly valve 3 is installed at the position, and the pressure-bearing powder-feeding butterfly valve 3 vertically connects the positive-pressure conveying sending chamber 2 and the negative-pressure conveying receiving chamber 7 with coaxial lines. The upper part of the positive pressure delivery sending bin 2 is equipped with a sending bin material level sensor 4 , a pressure sensor 5 and a compressed air inlet valve 6 . The lower end of the positive pressure conveying and sending chamber 2 is connected to a powder outlet pipeline 17 equipped with a pipeline valve 1 , and the powder outlet pipeline 17 is equipped with a plurality of powder outlet pressure-bearing two-way valves 20 . The upper end of the negative pressure delivery receiving bin 7 is connected with an air filter bin 8, and the negative pressure delivery receiving bin 7 and the air filter bin 8 are connected by a flange. A fixed partition 9 is set between the negative pressure conveying and receiving chamber 7 and the air filter chamber 8, and the fixed partition 9 separates the negative pressure conveying and accepting chamber 7 from the air filtering chamber 8. There is a round hole on the fixed partition 9, and a bag-type air filter 14 is installed in the round hole, and a compressed air back-blowing air pipe 13 is installed above the filter opening, and the back-blowing air pipe 13 and the two-position two-way control valve 11 Connected, the two-position two-way valve 11 is installed on the compressed air storage tank 12, and the compressed air storage tank 12 is located outside the air filter chamber 8 and is fixedly connected with it. As shown in the accompanying drawings, the utility model can provide a plurality of round holes on the fixed partition 9, and install a bag-type air filter 14 in each round hole, and each bag-type air filter 14 is equipped with compressed air respectively. The blowback air pipe 13 and the two-position two-way control valve 11 form a multi-bag air filter structure. On the cylindrical body of the negative pressure conveying and receiving bin 7, a material level sensor 15 and a feed inlet 16 are arranged near the lower end of the bag-type air filter 14, and the feed inlet 16 is connected with a powder inlet pipeline 18, and the powder inlet pipeline 18 is equipped with a plurality of powder-feeding pressure-bearing two-way valves 19. the

本实用新型的工作原理说明如下:  The working principle of the utility model is described as follows:

当需要将粉体物料由a、b、c点中的某一点输送到d、e、f中的某一点时,位于该点处的承压双路阀19和20打开,仅使该点与输送管路相通。然后启动正负压组合式密相粉体物料气力输送装置,该装置启动后,先关闭管道阀1并打开进粉蝶阀3,使正压输送发送仓2的出粉管道关闭、而与负压输送接受仓7连通。启动真空发生器10,使负压输送接受仓7和正压输送发送仓2同时产生负压。与进粉管道18相通点处的粉体物料在该负压和气粉混合阀(图中未表示)的共同作用下,通过管道18被输送到负压输送接受仓7中,然后,粉体物料在重力的作用下,经过进粉蝶阀3落入到正压输送发送仓2中。和粉体物料一同进入负压输送接受仓7中的空气经过袋式空气过滤器14,由真空发生器10抽走,该部分空气夹带的粉尘被袋式空气过滤器14过滤掉。袋式空气过滤器14工作一段时间以后,它的过滤微孔会发生部分堵塞现象,使过滤效率下降,为此,在每个袋式空气过滤器开口的上方都装有一个压缩空气反吹气管13,该反吹气管间隔一定时间循环对各过滤器进行单独反吹,清除掉沾附在袋式空气过滤器14表面上的粉尘,以保证过滤器的效率。当正压输送发送仓2内的粉体物料的高度达到发送仓料位传感器4所在的位置附近时,发送仓料位传感器4发出信号,进粉蝶阀3关闭,负压输送系统继续工作。进粉蝶阀3关闭后,压缩空气进气阀6打开,给正压输送发送仓2充入洁净的压缩空气,当正压输送发送仓2内的压力达到设定值时,正压输送发送仓2内的粉体和压缩空气已经比较充分地混合了,此时打开管道阀1,正压输送发送仓2内的有压粉体物料就会沿着出粉管道17进入到指定的输送点处。当然,在出粉管道17上还需要象一般的正压输送系统那样设置一些补气阀,同时也可以在正压输送发送仓2的下端设置一些物料输送状态控制阀,以实现对粉体物料的输送状态进行控制。当正压输送发送仓2内的粉体物料全部输送完后,正压输送发送仓2内的压力逐渐恢复到常压状态,此时,关闭管道阀1,然后打开进粉蝶阀3,正压输送发送仓2内的空气透过负压输送接受仓7内的粉体物料进入到负压输送接受仓7的上部,然后,经过袋式空气滤器14过滤后,再由真空发生器10抽走。当正压输送发送仓2内的压力与负压输送接受仓7内的压力接近时,负压输送接受仓7内的粉体物料在重力的作用下落入到正压输送发送仓2内,当正压输送发送仓2内的料位高度再次达到其料位传感器4附近时,该料位传感器发出信号,正压输送发送仓2再次执行正压输送操作。这种连续的负压输送操作与间歇的正压输送操作组合,实现了由多点到多点的粉体物料输送操作 。一般来讲,粉体正压输送的速度要比负压输送速度高得多,正压输送所用的时间很短,同时负压输送接受仓7的接受仓料位传感器15以下的容积设计得足够大,在进粉蝶阀3关闭后,正压输送发送仓2进行正压输送操作这段时间内,进入到负压输送接受仓7内的粉体物料达不到接受仓料位传感器15所在的位置,负压输送系统是连续工作的。但当正压输送系统出现问题时,正压操作的时间可能过常,使得负压输送接受仓7内的粉体物料达到接受仓料位传感器15所在的位置,此时,接受仓料位传感器15发出信号,负压输送系统停止操作,以免进入到负压输送接受仓7内的粉体物料过多,损坏负压输送系统,这也是接受仓料位传感器15的作用所在。 When it is necessary to transport the powder material from a certain point in points a, b, and c to a certain point in d, e, and f, the pressure-bearing two-way valves 19 and 20 at this point are opened, and only this point is connected with the The delivery pipelines are connected. Then start the positive and negative pressure combined dense-phase powder material pneumatic conveying device. After the device is started, first close the pipeline valve 1 and open the powder inlet butterfly valve 3, so that the powder outlet pipeline of the positive pressure conveying and sending bin 2 is closed, and it is connected with the negative pressure. The conveying and receiving bin 7 is connected. Start the vacuum generator 10, so that the negative pressure delivery receiving bin 7 and the positive pressure delivery sending bin 2 generate negative pressure at the same time. Under the joint action of the negative pressure and the gas-powder mixing valve (not shown in the figure), the powder material at the point communicating with the powder inlet pipeline 18 is transported to the negative pressure conveying and receiving bin 7 through the pipeline 18, and then the powder material Under the action of gravity, it falls into the positive pressure conveying and sending bin 2 through the powder inlet butterfly valve 3 . The air that enters the negative pressure conveying and receiving bin 7 together with the powder material passes through the bag type air filter 14 and is sucked away by the vacuum generator 10 , and the dust entrained in this part of the air is filtered out by the bag type air filter 14 . After the bag-type air filter 14 works for a period of time, its filter micropores will be partially blocked, which will reduce the filtration efficiency. For this reason, a compressed air back-blowing air pipe is installed above the opening of each bag-type air filter. 13. The back-blowing air pipe circulates and back-flushes each filter separately at intervals of a certain period of time to remove the dust adhering to the surface of the bag-type air filter 14, so as to ensure the efficiency of the filter. When the height of the powder material in the positive pressure conveying sending bin 2 reaches near the position of the sending bin material level sensor 4, the sending bin material level sensor 4 sends out a signal, the powder inlet butterfly valve 3 is closed, and the negative pressure conveying system continues to work. After the powder inlet butterfly valve 3 is closed, the compressed air intake valve 6 is opened to fill the positive pressure conveying chamber 2 with clean compressed air. When the pressure in the positive pressure conveying chamber 2 reaches the set value, the positive pressure conveying chamber 2 The powder and compressed air in 2 have been fully mixed. At this time, the pipeline valve 1 is opened, and the pressurized powder material in the delivery chamber 2 will enter the designated delivery point along the powder outlet pipeline 17. . Of course, it is necessary to set some air supply valves on the powder outlet pipeline 17 like a general positive pressure conveying system, and at the same time, some material conveying state control valves can be set at the lower end of the positive pressure conveying and sending bin 2 to realize the control of powder materials. The delivery status is controlled. After all the powder materials in the positive pressure conveying and sending chamber 2 have been conveyed, the pressure in the positive pressure conveying and sending chamber 2 gradually returns to the normal pressure state. The air in the conveying and sending chamber 2 enters the upper part of the negative pressure conveying and receiving chamber 7 through the negative pressure conveying and receiving chamber 7, and then, after being filtered by the bag-type air filter 14, it is sucked away by the vacuum generator 10 . When the pressure in the positive pressure conveying sending chamber 2 is close to the pressure in the negative pressure conveying receiving chamber 7, the powder material in the negative pressure conveying receiving chamber 7 falls into the positive pressure conveying sending chamber 2 under the action of gravity, when When the material level height in the positive pressure conveying sending chamber 2 reaches the vicinity of its material level sensor 4 again, the material level sensor sends out a signal, and the positive pressure conveying sending chamber 2 performs the positive pressure conveying operation again. This combination of continuous negative pressure conveying operation and intermittent positive pressure conveying operation realizes the multi-point to multi-point powder material conveying operation. Generally speaking, the speed of positive pressure conveying of powder is much higher than that of negative pressure conveying, and the time used for positive pressure conveying is very short. At the same time, the volume below the receiving bin material level sensor 15 of negative pressure conveying receiving bin 7 is designed to be sufficient Large, after the powder inlet butterfly valve 3 is closed, the powder material entering the negative pressure conveying receiving chamber 7 cannot reach the position where the receiving chamber material level sensor 15 is located during the period of time when the positive pressure conveying and sending chamber 2 is performing positive pressure conveying operation. position, the negative pressure delivery system works continuously. But when there is a problem with the positive pressure conveying system, the time of positive pressure operation may be too normal, so that the powder material in the negative pressure conveying receiving bin 7 reaches the position where the receiving bin material level sensor 15 is located. At this time, the receiving bin material level sensor 15 sends a signal, and the negative pressure conveying system stops operating, so as to avoid excessive powder materials entering the negative pressure conveying receiving bin 7 and damaging the negative pressure conveying system, which is also the function of the receiving bin material level sensor 15.

Claims (2)

1. the close phase powder material of positive negative pressure combined type Pneumatic conveyer, it is characterized in that: it has a malleation that is placed in the below and carries sending warehouse (2) and a negative pressure transportation receiving bin (7) that is placed in the top, described malleation carries sending warehouse (2) and negative pressure transportation receiving bin (7) to be provided with the cylindrical shape warehouse of circular cone bucket body for the bottom, described malleation carries sending warehouse (2) and negative pressure transportation receiving bin (7) to advance white butterfly valve (3) and be connected and be coaxially set through being placed in one of centre, described malleation carries the lower end of sending warehouse (2) to connect the powder delivery pipeline (17) of an assembling pipeline valve (1), described malleation carries the top of sending warehouse (2) to be equipped with sending warehouse level sensor (4), pressure sensor (5) and compressed air inlet valve (6), the upper end of described negative pressure transportation receiving bin (7) connects an air filtration storehouse (8), between described negative pressure transportation receiving bin (7) and air filtration storehouse (8), a stationary barrier (9) is set, the pocket type air filter (14) that is placed in negative pressure transportation receiving bin (7) is connected with filter installing port on described stationary barrier (9), the filter anti-blowpipe (13) of being drawn by the filter installing port is connected with a compressed air reservoir (12) by a 2/2-way control cock (11), be equipped with vacuum generator (10) on described air filtration storehouse (8), described negative pressure transportation receiving bin (7) is equipped with receiving bin level sensor (15) and inlet point (16), this inlet point (16) connects a powder inlet pipe road (18), described powder inlet pipe road (18) is equipped with a plurality of powder pressure-bearing two-way valves (19) that advance, described powder delivery pipeline (17) is equipped with a plurality of powder delivery pressure-bearing two-way valves (20).
2. the close phase powder material of positive negative pressure combined type according to claim 1 Pneumatic conveyer, it is characterized in that: described pocket type air filter (14) arranges a plurality of.
CN 201220617348 2012-11-21 2012-11-21 Positive and negative pressure combined dense phase powder material pneumatic conveying device Expired - Lifetime CN202935945U (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102923484A (en) * 2012-11-21 2013-02-13 秦皇岛燕大源达机电科技有限公司 Positive and negative pressure combined type dense phase powder material pneumatic conveying device
CN104176503A (en) * 2013-05-22 2014-12-03 欧才权 Gap-discharging continuous vacuum feeding machine
CN104210852A (en) * 2013-05-30 2014-12-17 欧才权 Clearance arrangement type continuous vacuum feeding machine
CN110171715A (en) * 2019-05-09 2019-08-27 西安拓普电气有限责任公司 Feeding system
CN114229480A (en) * 2021-12-28 2022-03-25 安徽艾普克斯智能科技有限公司 Cement material conveying bin pump

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102923484A (en) * 2012-11-21 2013-02-13 秦皇岛燕大源达机电科技有限公司 Positive and negative pressure combined type dense phase powder material pneumatic conveying device
CN104176503A (en) * 2013-05-22 2014-12-03 欧才权 Gap-discharging continuous vacuum feeding machine
CN104176503B (en) * 2013-05-22 2016-06-29 欧才权 Platoon type continuous vacuum feeder
CN104210852A (en) * 2013-05-30 2014-12-17 欧才权 Clearance arrangement type continuous vacuum feeding machine
CN104210852B (en) * 2013-05-30 2016-12-28 欧才权 Between row's type continuous vacuum feeder
CN110171715A (en) * 2019-05-09 2019-08-27 西安拓普电气有限责任公司 Feeding system
CN114229480A (en) * 2021-12-28 2022-03-25 安徽艾普克斯智能科技有限公司 Cement material conveying bin pump
CN114229480B (en) * 2021-12-28 2022-07-08 安徽艾普克斯智能科技有限公司 Cement material conveying bin pump

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