CN110652893A - Microbubble generating device and bubble segmentation component - Google Patents
Microbubble generating device and bubble segmentation component Download PDFInfo
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
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- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2373—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media for obtaining fine bubbles, i.e. bubbles with a size below 100 µm
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
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Abstract
本申请提供一种微气泡发生装置,同时还提供一种用于产生微气泡的气泡分割元件。所述微气泡发生装置包括:气液混合器、气泡生成器以及气泡过滤器;所述气液混合器设置有进气口和进液口,用于气体与液体混合,其输出端输出气液混合物;所述气泡生成器与所述气液混合器连接,具有进水口和出水口,所述进水口于所述气液混合器的输出端连接;所述气泡生成器内部设置有气泡分割元件,所述气泡分割元件至少包含两层气泡刺破层,所述气泡刺破层包括朝向所述进水口方向的尖端,且相邻层的尖端相互错开;所述气泡过滤器一端连接所述气泡生成器的出水口,其内部设置过滤层,其另一端为微气泡发生装置的微气泡水出水口。
The present application provides a microbubble generating device, and also provides a bubble dividing element for generating microbubbles. The micro-bubble generating device includes: a gas-liquid mixer, a bubble generator and a bubble filter; the gas-liquid mixer is provided with an air inlet and a liquid inlet for mixing gas and liquid, and its output end outputs gas and liquid mixture; the bubble generator is connected to the gas-liquid mixer, and has a water inlet and a water outlet, and the water inlet is connected to the output end of the gas-liquid mixer; the bubble generator is provided with a bubble dividing element , the bubble dividing element includes at least two layers of bubble piercing layers, the bubble piercing layers include tips facing the direction of the water inlet, and the tips of adjacent layers are staggered from each other; one end of the bubble filter is connected to the bubbles The water outlet of the generator is provided with a filter layer inside, and the other end is the microbubble water outlet of the microbubble generating device.
Description
技术领域technical field
本发明涉及微纳米技术领域,具体涉及一种微气泡发生装置。本申请同时涉及一种用于产生微气泡的气泡分割元件。The invention relates to the field of micro-nano technology, in particular to a micro-bubble generating device. The application also relates to a bubble dividing element for generating microbubbles.
背景技术Background technique
微气泡是气泡发生时产生直径在五十微米以下的微小气泡,,微气泡发生之后,气泡自己收缩,在这个过程因气泡变小所以上升速度变缓慢,因而其融化效率高,另外,微气泡还具有比表面积大,气含量高、表面带电荷等特点。Microbubbles are tiny bubbles with a diameter of less than 50 microns that are generated when bubbles occur. After the occurrence of microbubbles, the bubbles shrink by themselves. During this process, the rising speed of the bubbles becomes slower, so the melting efficiency is high. In addition, the microbubbles are It also has the characteristics of large specific surface area, high gas content and surface charge.
在工业上,微气泡在固液界面减阻方面显示出重要的作用。将同样的纳米气泡布满液体传输管道的内壁,将可以减少液体传输过程固液界面的摩擦,从而节省能量和成本。同时,微气泡可以被用于日常生活中。因为许多人造产品和自然资源是物质混合形成的,一些情况下我们希望这些物质保持混合,还有些情况我们需要分开它们。这时,我们就可以利用微气泡使油性物质和水融合稳定的时间更长,可以使从油砂中分离出油更加经济和有效率。In industry, microbubbles play an important role in drag reduction at the solid-liquid interface. Filling the same nanobubbles all over the inner wall of the liquid transfer pipeline will reduce the friction of the solid-liquid interface during the liquid transfer process, thereby saving energy and cost. Meanwhile, microbubbles can be used in daily life. Because many man-made products and natural resources are formed by mixing substances, in some cases we want these substances to remain mixed, and in other cases we need to separate them. At this time, we can use microbubbles to stabilize oily substances and water for a longer time, which can make oil separation from oil sands more economical and efficient.
目前,微气泡发生主要分为以下几种:At present, the occurrence of microbubbles is mainly divided into the following categories:
(1)典型的压力溶解式微气泡发生装置:使气液混合物在加压罐中加至一定压力后,气体以饱和浓度溶解与液体中,通过使用减压阀突然降低压力,此时饱和在液相中的气体析出,从而产生微气泡;(1) Typical pressure-dissolving micro-bubble generating device: after the gas-liquid mixture is added to a certain pressure in a pressurized tank, the gas is dissolved in the liquid at a saturated concentration, and the pressure is suddenly reduced by using a pressure reducing valve. The gas in the phase is separated out, resulting in the generation of microbubbles;
(2)超声波产生微气泡的方式:超声波产生微气泡主要是利用了超声空化现象,高频率的声波以纵波的形式在液体中传播,当声强超过液体静压值,将会破坏液体介质的完整性,导致液体中出现空穴,当空穴形成时,一般处于真空状态,溶解在水中的气体会迅速进入空穴形成微气泡;(2) Ultrasonic generation of microbubbles: Ultrasonic generation of microbubbles mainly utilizes the phenomenon of ultrasonic cavitation. High-frequency sound waves propagate in the liquid in the form of longitudinal waves. When the sound intensity exceeds the liquid static pressure value, the liquid medium will be destroyed. The integrity of the liquid leads to the appearance of cavities in the liquid. When the cavities are formed, they are generally in a vacuum state, and the gas dissolved in the water will quickly enter the cavities to form micro-bubbles;
(3)微孔成泡技术:微孔成泡技术是利用某些介质(如冶金粉末、陶瓷或塑料)作材料,再掺以适量的粘合剂,在高温下烧结而成的微多孔结构,当压缩气体经过微孔介质时,被微孔切割成微纳米气泡。(3) Microporous foaming technology: Microporous foaming technology is a microporous structure formed by sintering certain media (such as metallurgical powder, ceramics or plastics) as materials, mixed with an appropriate amount of binder, and sintered at high temperature. , when the compressed gas passes through the microporous medium, it is cut into micro-nano bubbles by the micropores.
然而,上述现有的产生微气泡的装置及方法均存在一些问题,使用上述装置(1)产生的微气泡的分布和尺寸由压力罐中的压力直接决定,其变量单一,在一定条件下,无法产生符合生产要求的微气泡。上述方式(2)以及(3)均存在制造难度大、气泡尺寸离散、能耗高的缺点。因此,有必要对微气泡发生装置进行优化设计,以提高微气泡发生效果,使其更具备工业实用性。However, the above-mentioned existing devices and methods for generating microbubbles all have some problems. The distribution and size of the microbubbles generated by using the above-mentioned device (1) are directly determined by the pressure in the pressure tank, and the variables are single. Under certain conditions, Microbubbles that meet production requirements cannot be generated. The above methods (2) and (3) both have the disadvantages of high manufacturing difficulty, discrete bubble size and high energy consumption. Therefore, it is necessary to optimize the design of the micro-bubble generating device to improve the effect of micro-bubble generation and make it more industrially practical.
发明内容SUMMARY OF THE INVENTION
本申请提供一种微气泡发生装置。本申请同时提供一种用于产生微气泡的气泡分割元件。The present application provides a micro-bubble generating device. The present application also provides a bubble dividing element for generating microbubbles.
本申请提供的微气泡发生装置,包括:The microbubble generating device provided in this application includes:
气液混合器、气泡生成器;Gas-liquid mixer, bubble generator;
所述气液混合器设置有进气口和进液口,用于气体与液体混合,其输出端输出气液混合物;The gas-liquid mixer is provided with an air inlet and a liquid inlet for mixing gas and liquid, and the output end outputs the gas-liquid mixture;
所述气泡生成器与所述气液混合器连接,具有进口和出口,所述进口与所述气液混合器的输出端连接;所述气泡生成器内部设置有气泡分割元件,所述气泡分割元件至少包含两层气泡刺破层,所述气泡刺破层包括朝向所述进水口方向的尖端,且相邻气泡刺破层的尖端相互错开;经过所述气泡分割元件的气液混合物通过所述出口流出。The bubble generator is connected to the gas-liquid mixer, and has an inlet and an outlet, and the inlet is connected to the output end of the gas-liquid mixer; the bubble generator is provided with a bubble dividing element, and the bubble divides The element comprises at least two layers of bubble piercing layers, the bubble piercing layers include tips facing the direction of the water inlet, and the tips of adjacent bubble piercing layers are staggered from each other; the gas-liquid mixture passing through the bubble dividing element passes through the outflow from the outlet.
优选的,所述微气泡发生装置,包括气泡过滤器,所述气泡过滤器一端连接所述气泡生成器的出口,其内部设置过滤层,通过气泡过滤器的气液混合物从所述气泡过滤器的另一端输出。Preferably, the micro-bubble generating device includes a bubble filter, one end of the bubble filter is connected to the outlet of the bubble generator, and a filter layer is arranged inside the bubble filter, and the gas-liquid mixture passing through the bubble filter is removed from the bubble filter. output at the other end.
优选的,所述相邻气泡刺破层的尖端相互错开,具体采用如下结构:位于下游位置的气泡刺破层的尖端朝向上游气泡刺破层的出泡口。Preferably, the tips of the adjacent bubble-piercing layers are staggered from each other, and the specific structure is as follows: the tip of the bubble-piercing layer located in the downstream position faces the bubble outlet of the upstream bubble-piercing layer.
优选的,所述气泡生成器内部设置有气泡分割元件,包括:所述气泡发生器内部设置有至少两个气泡分割元件,所述气泡分割元件将所述气泡发生器内部至少分割为三层。Preferably, the inside of the bubble generator is provided with a bubble dividing element, including: at least two bubble dividing elements are provided inside the bubble generator, and the bubble dividing element divides the inside of the bubble generator into at least three layers.
优选的,所述气泡生成器内部设置有两个气泡分割元件,包括:每个所述气泡分割元件的目不相同,所述各个气泡分割元件的目随着所在液流的位置不同而不同,并且位于下游的比位于上游的目大。Preferably, the bubble generator is provided with two bubble dividing elements, including: the purpose of each of the bubble dividing elements is different, and the purpose of each bubble dividing element is different according to the position of the liquid flow, And the ones located downstream are larger than the ones located upstream.
优选的,位于最下游的所述气泡分割元件的目大于300。Preferably, the mesh of the bubble dividing element located most downstream is greater than 300.
优选的,所述气泡发生器采用压力罐。Preferably, the bubble generator adopts a pressure tank.
优选的,所述压力罐内部设置用于安装所述气泡分割元件的环形凹槽,所述环形凹槽的数量与所述气泡分割元件的数量一致。Preferably, an annular groove is provided inside the pressure tank for installing the air bubble dividing element, and the number of the annular groove is consistent with the number of the air bubble dividing element.
优选的,所述压力罐采用隔膜式压力罐。Preferably, the pressure tank adopts a diaphragm type pressure tank.
优选的,所述气泡生成器为管道。Preferably, the bubble generator is a pipe.
优选的,所述管道为螺旋管道。Preferably, the pipeline is a spiral pipeline.
优选的,所述气泡分割元件逐层设置于以所述螺旋管道中心轴线为中心的纵向切面中。Preferably, the bubble dividing elements are arranged layer by layer in a longitudinal section centered on the central axis of the helical pipe.
优选的,所述气泡分割元件至少包含两层气泡刺破层,每层气泡刺破层的尖端朝向同一侧,且相邻气泡刺破层的尖端相互错开。Preferably, the bubble dividing element comprises at least two layers of bubble piercing layers, the tips of each layer of bubble piercing layers face the same side, and the tips of adjacent bubble piercing layers are staggered from each other.
优选的,所述相邻气泡刺破层的尖端相互错开,具体采用如下结构:位于下游位置的气泡刺破层的尖端朝向上游气泡刺破层的出泡口。Preferably, the tips of the adjacent bubble-piercing layers are staggered from each other, and the specific structure is as follows: the tip of the bubble-piercing layer located in the downstream position faces the bubble outlet of the upstream bubble-piercing layer.
优选的,所述气泡分割元件的目大于300。Preferably, the mesh of the bubble dividing element is greater than 300.
与现有技术相比,本申请具有以下优点:Compared with the prior art, the present application has the following advantages:
本申请提供了一种用于产生微气泡的微气泡发生装置,包括:气液混合器、气泡生成器;The application provides a microbubble generating device for generating microbubbles, including: a gas-liquid mixer and a bubble generator;
所述气液混合器设置有进气口和进液口,用于气体与液体混合,其输出端输出气液混合物;所述气泡生成器与所述气液混合器连接,具有进口和出口,所述进口与所述气液混合器的输出端连接;所述气泡生成器内部设置有气泡分割元件,所述气泡分割元件至少包含两层气泡刺破层,所述气泡刺破层包括朝向所述进口方向的尖端,且相邻气泡刺破层的尖端相互错开;经过所述气泡分割元件的气液混合物通过所述出口流出。本方案摒弃了传统的使用压力溶解式微气泡发生装置以及微泡成孔技术,利用所述由气泡刺破层构成的气泡分割元件直接对气液混合物中的气泡进行处理,同时,在构建所述气泡分割元件的同时,考虑气泡的可流动性与形状不规则等特性,充分利用气泡刺破层在物理上结构,使所述气液混合物流过多层气泡分割元件后可以形成包含微气泡的液体,这一结构设置不仅能耗低,而且产出的微气泡大小统一,同时大大提高了微气泡的产出效率。The gas-liquid mixer is provided with an air inlet and a liquid inlet for mixing gas and liquid, and its output end outputs a gas-liquid mixture; the bubble generator is connected to the gas-liquid mixer and has an inlet and an outlet, The inlet is connected to the output end of the gas-liquid mixer; the bubble generator is provided with a bubble dividing element, and the bubble dividing element comprises at least two layers of bubble piercing layers, the The tips in the direction of the inlet, and the tips of the adjacent bubble piercing layers are staggered from each other; the gas-liquid mixture passing through the bubble dividing element flows out through the outlet. This solution abandons the traditional pressure-dissolving micro-bubble generating device and micro-bubble pore-forming technology, and uses the bubble dividing element composed of the bubble piercing layer to directly process the bubbles in the gas-liquid mixture. At the same time as the bubble dividing element, considering the characteristics of the flowability and irregular shape of the bubbles, the physical structure of the bubble piercing layer is fully utilized, so that the gas-liquid mixture can flow through the multi-layer bubble dividing element to form a bubble containing microbubbles. Liquid, this structure setting not only has low energy consumption, but also produces uniform size of microbubbles, and at the same time greatly improves the production efficiency of microbubbles.
附图说明Description of drawings
图1是本申请第一实施例提供的微气泡发生装置的结构示意图;1 is a schematic structural diagram of a microbubble generating device provided in a first embodiment of the present application;
图2是本申请第一实施例提供的气泡发生器的结构示意图;2 is a schematic structural diagram of a bubble generator provided by the first embodiment of the present application;
图3是本申请第一实施例提供的气泡分割元件的部分结构示意图。FIG. 3 is a partial structural schematic diagram of the bubble dividing element provided by the first embodiment of the present application.
具体实施方式Detailed ways
在下面的描述中阐述了很多具体细节以便充分理解本申请。但是本申请能够以很多不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本申请内涵的情况下做类似的推广,因此本申请不受下面公开的具体实施例的限制。In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present application. However, the present application can be implemented in many other ways different from those described herein, and those skilled in the art can make similar promotions without departing from the connotation of the present application. Therefore, the present application is not limited by the specific embodiments disclosed below.
本申请第一实施例提供一种微气泡发生装置,请参看图1,其为本申请第一实施例的示意图,在该微气泡发生装置中,包括:气液混合器101、气泡生成器102以及气泡过滤器103。The first embodiment of the present application provides a micro-bubble generating device. Please refer to FIG. 1 , which is a schematic diagram of the first embodiment of the present application. The micro-bubble generating device includes: a gas-
所述气液混合器101设置有进气口1011和进液口1012,用于气体与液体混合,其输出端输出气液混合物,并通过所述气泡发生器的进口1021进入所述气泡发生器102,所述气液混合物在所述气泡发生器中形成微气泡,通过所述气泡发生器的出口1022进入所述气泡过滤器103,气泡过滤器将所述直径较大的微气泡过滤,最后输出符合要求的微气泡。所述气液混合器是微气泡发生装置产生微气泡的基础,所述气液混合器内可以适当的增加压力,以使所述气体与液体充分混合,即,使所述气体在所述气液混合器中以气泡形式存在与所述液体中。The gas-
如图2所示,其为本申请第一实施例中所述的气泡生成器的结构示意图,所述气泡生成器具有进口1021和出口1022,分别用于接收来自气液混合器的气液混合物,以及将经过处理的气液混合物流出。此外,所述气泡生成器内部还设置有气泡分割元件104。As shown in FIG. 2, which is a schematic structural diagram of the bubble generator described in the first embodiment of the application, the bubble generator has an
在气液混合物中,气体多以大气泡的形式存在,而本申请提供的微气泡发生装置的目的正是将这些大气泡制成符合要求的微气泡,从而通过微气泡满足人们的日常需求以及工业上的需要,因此,本申请在气泡生成器102设置有气泡分割元件104,所述气液混合物流经所述气泡分割元件104,在所述气泡分割元件104的作用下,将所述大气泡分割成符合要求的微气泡。In the gas-liquid mixture, gas mostly exists in the form of large bubbles, and the purpose of the microbubble generating device provided in this application is to make these large bubbles into microbubbles that meet the requirements, so as to meet people's daily needs and Therefore, the
下面我们结合气泡发生器对本申请所述的气泡分割元件104进行详细说明。Hereinafter, we will describe the bubble dividing element 104 described in this application in detail in conjunction with the bubble generator.
如图2所示,所述气泡分割元件104设置于所述气泡发生器内部,所述气泡分割元件至少包含两层气泡刺破层1041,所述气泡刺破层1041包括朝向所述进水口方向的尖端,且相邻气泡刺破层的尖端相互错开。As shown in FIG. 2 , the bubble dividing element 104 is disposed inside the bubble generator, and the bubble dividing element includes at least two layers of
由此可见,所述气泡分割元件104是由所述气泡刺破层1041构成的,另外,由于气泡分割元件104的作用是分割气液混合物中的大气泡,因此,所述气泡分割元件必然存在进泡口1042与出泡口1043,所述进泡口1042与出泡口1043的结构类似于筛网的结构,并且所述进泡口1042进入的气泡并不是未经处理的气泡,而是已经被所述气泡分割元件104最下层尖端分割的相对大气泡直径较小的气泡。It can be seen that the bubble dividing element 104 is composed of the
另外,由于气泡在液体中是不规则且可流动的,因此,为避免直径较大的气泡在流动过程中也能通过进泡口而不被分割的问题,本实施例在一个气泡分割元件中采用多层气泡刺破层,其目的是将所述气液混合物中的气泡多次分割,防止直径较大的气泡直接从所述出泡口流出。In addition, since the bubbles are irregular and flowable in the liquid, in order to avoid the problem that the bubbles with larger diameters can pass through the bubble inlet without being divided during the flow process, in this embodiment, a bubble dividing element is used. The multi-layer bubble piercing layer is used for the purpose of dividing the bubbles in the gas-liquid mixture multiple times to prevent the bubbles with larger diameters from directly flowing out of the bubble outlet.
如图3所示,其为本申请第一实施例中所述的气泡分割元件104的部分结构示意图,由于气泡分割元件由气泡刺破层构造,因此,所述气泡分割元件的进泡口1042和出泡口1043分别对应位于所述所述气泡分割元件最上游的气泡刺破层的进泡口以及最下游气泡刺破层的出泡口,所述气泡刺破层1041构造气泡分割元件104时,需要将位于下游的气泡刺破层的尖端对准上游刺破层的出泡口。在气液混合物流动的过程中,如果直径较大的气泡进入下层气泡刺破层的出泡口,也会被上层气泡刺破层的尖端切割。As shown in FIG. 3 , which is a partial structural schematic diagram of the bubble dividing element 104 described in the first embodiment of the application, since the bubble dividing element is constructed of a bubble piercing layer, the
也就是说,当气液混合物从上游流动到所述气泡分割元件时,所述气液混合物中的大气泡首先接触所述气泡分割元件104位于最上游的气泡刺破层的尖端,并被尖端戳破,使大气泡分裂成若干直径较小的气泡,之后,从分别从所述最上游的气泡刺破层的各个出泡口流出,由于位于下游的气泡刺破层的尖端正对所述最上游的气泡刺破层的出泡口,因此,当流出所述最上游气泡刺破层的出泡口的气泡不符合气泡分割元件允许通过的直径时,所述气泡随着气液混合物的流动方向继续接触所述位于下游的气泡刺破层的尖端,气泡被继续分解,通过两层或者多层的气泡刺破层,最终从位于最下游的气泡刺破层1041出泡口流出时,气泡已经基本上全部是符合微气泡尺寸要求的气泡;当然,在上述过程中不排除被分割为小气泡的气泡又结合为大气泡。另外,上述气泡分割过程需要和气液混合物在一定的压力下较快速的从上游流动向下游。需要说明的是,所述气泡分割元件的结构并不仅仅局限于由具备尖端的所述气泡刺破层逐层搭建构成,凡是可以分割气泡的元件,或者在外力作用下,通过某一元件能够令所述气泡在移动方向上,按照一定的规律分裂的元件均可以称为气泡分割元件均不偏离本申请的核心,另外,所述气泡分割元件也可以为一个整体。例如:所述气泡分割元件可以由至少两层筛网搭建构成,所述上层筛网的非网孔部分对应到下层筛网的网孔部分。这些属于对本实施例中所述气泡分割元件结构的简单变换,不偏离本申请的核心,都在本申请的保护范围之内。That is to say, when the gas-liquid mixture flows from the upstream to the bubble dividing element, the large bubbles in the gas-liquid mixture first contact the tip of the bubble piercing layer located at the most upstream of the bubble dividing element 104, and are pushed by the tip. Puncture the large bubbles to split into several smaller diameter bubbles, and then flow out from the respective bubble outlets of the most upstream bubble piercing layer, because the tip of the downstream bubble piercing layer is facing the The bubble outlet of the most upstream bubble piercing layer, therefore, when the bubbles flowing out of the bubble outlet of the most upstream bubble piercing layer do not conform to the diameter allowed by the bubble dividing element, the bubbles will follow the gas-liquid mixture. When the flow direction continues to contact the tip of the downstream bubble piercing layer, the bubbles continue to decompose, pass through two or more layers of bubble piercing layers, and finally flow out from the bubble outlet of the most downstream
此外,微气泡是气泡发生时产生直径在50微米(μm)以下的微小气泡。因此,若想实现微气泡的发生,所述气泡刺破层至少为300目,所述气泡刺破层尖端的面积也应远远小于50微米(μm),以防止所述尖端无法刺破气泡的问题。另外,如果直接采用符合微气泡发生条件的气泡刺破层构建所述气泡分割层,直径较大的气泡直接接触所述气泡分割层的一面受力均匀,将会导致所述气泡分割元件无法刺破所述直径较大的气泡,而无法达到预期的效果,甚至还会堵塞气泡分割元件。In addition, microbubbles are microbubbles having a diameter of 50 micrometers (μm) or less that are generated when bubbles are generated. Therefore, in order to realize the generation of micro-bubbles, the bubble piercing layer should be at least 300 meshes, and the area of the tip of the bubble piercing layer should also be much smaller than 50 micrometers (μm) to prevent the tip from being unable to pierce the bubbles The problem. In addition, if the bubble piercing layer that meets the conditions for micro-bubble generation is directly used to construct the bubble segmenting layer, the bubbles with larger diameters directly contact the bubble segmenting layer and receive uniform force, which will cause the bubble segmenting element to fail to pierce the bubble segment. If the bubbles with larger diameters are broken, the expected effect cannot be achieved, and the bubble dividing element will even be blocked.
因此,所述气泡生成器中设置有至少两个气泡分割元件,所述气泡分割元件将所述气泡发生器内部至少分割为三层。每个所述气泡分割元件的目不相同,所述各个气泡分割元件的目随着所在液流的位置不同而不同,并且位于下游的比位于上游的目大。Therefore, the bubble generator is provided with at least two bubble dividing elements, and the bubble dividing elements divide the inside of the bubble generator into at least three layers. The meshes of each of the bubble dividing elements are different, and the meshes of the respective bubble dividing elements are different according to the position of the liquid flow, and the meshes located downstream are larger than the meshes located upstream.
这里所说的目是一种计量单位,指的是每英寸筛网的孔眼数目,由于气泡分割元件是由气泡刺破层构成,因此,本申请中的目具体指的是每英寸气泡刺破层出泡口的数量,例如:50目就是指每英寸上的孔眼数是50个,500目就是指每英寸上的孔眼数是500个,数目越高,孔眼越多。另外,除了表示筛网的孔眼外,它同时用于表示能够通过筛网的粒子的粒径,目数越高,粒径越小。我国使用的是美国标准,美国泰勒标准筛的筛目尺寸对照表,请参看如下表格:The purpose here is a unit of measurement, which refers to the number of holes per inch of the screen. Since the bubble dividing element is composed of a bubble piercing layer, the purpose in this application specifically refers to the bubble piercing per inch. The number of layer bubble openings, for example: 50 mesh means that the number of holes per inch is 50, 500 mesh means that the number of holes per inch is 500, the higher the number, the more holes. In addition, in addition to indicating the holes of the screen, it is also used to indicate the particle size of the particles that can pass through the screen. The higher the mesh number, the smaller the particle size. my country uses the American standard, and the mesh size comparison table of the American Taylor standard sieve, please refer to the following table:
另外,本实施例中上游和下游的概念是相对于液流方向提出的。由于本申请所述的气泡生成器具有进口和出口,也就是说,在气泡生成器内,凡是具有流体性质的物体,在本申请所述的气泡生成器内的运动规律均为从所述进口流向所述出口,因此,我们用上游和下游来表示各个气泡分割元件的位置关系,以此使读者可以更加清楚明白本申请所述各个气泡分割元件在所述气泡生成器中的位置关系。In addition, the concepts of upstream and downstream in this embodiment are presented with respect to the direction of liquid flow. Since the bubble generator described in this application has an inlet and an outlet, that is to say, in the bubble generator, all objects with fluid properties in the bubble generator described in this application have the law of motion from the inlet. Flow to the outlet, therefore, we use upstream and downstream to represent the positional relationship of each bubble dividing element, so that readers can more clearly understand the positional relationship of each bubble dividing element in the bubble generator.
为了使读者可以更清楚的理解本实施例所述的微气泡发生装置的工作原理,下面我们结合图1、图2和图3详细说明该装置微气泡的发生过程。In order to enable readers to understand the working principle of the microbubble generating device described in this embodiment more clearly, the following describes the generating process of the microbubble in the device in detail with reference to FIG. 1 , FIG. 2 and FIG. 3 .
用水代表通过进液口1012进入所述气液混合器101中的液体,用空气代表通过进气口1011进入所述气液混合器101中的气体,所述空气进入所述气液混合器101后,以气泡的形式融合与水中,形成气液混合物。此时,所述气泡直径偏大,并不满足微气泡的直径要求。当所述气泡在水中结构稳定之后,即,形成气液混合物之后。所述气液混合物通过管道由所述气泡生成器102的进口1021进入所述气泡生成器102,此时,所述气液混合物按照从所述气泡生成器的进口1021向所述出口1022流动的运动规律流动。Water represents the liquid entering the gas-
由于所述气泡生气器102中设置有多层气泡分割元件,由空气和水构成的气液混合物在所述气泡生成器流动时,必然会逐层通过气泡分割元件,因此,所述气液混合物通过气泡分割元件的过程中直径大于所述气泡分割元件筛网直径的气泡必然会被所述气泡分割元件分割,形成直径较小的气泡,另外,由于微气泡发生的过程中整个装置内的水和空气是不断运动的,即使所述气液混合物中的气泡经一次分割后仍不能通过所述气泡分割元件,也会被不断流动的气液混合物继续带向所述气泡分割元件,直至能够通过所述气泡分割元的筛网。此外,由于所述气泡生成器中每层气泡分割元件的目顺着气液混合物流动方向逐个变小,所述气液混合物每通过一个气泡分割元件,其气泡直径也会变的越来越小,直至所述气泡的直径满足微气泡的直径。Since the
由于气泡之间会通过互相碰撞结合,而设置在最下游的气泡分割元与所述气泡生成器出口之间并没有其它装置阻止这一结合过程,因此,由所述气泡生成器生成的微气泡水中,必然会存在直径较大的气泡。当所述微气泡水由所述气泡生成器涌出后,还需要通过气泡过滤器,将由于气泡之间相互碰撞结合的直径较大的气泡过滤,从而得到纯净的微气泡水。Since the bubbles will be combined by mutual collision, and there is no other device between the most downstream bubble dividing element and the outlet of the bubble generator to prevent this combination process, therefore, the microbubbles generated by the bubble generator In water, there are bound to be bubbles with larger diameters. After the microbubble water is gushed out from the bubble generator, it needs to pass through a bubble filter to filter the bubbles with larger diameters due to the collision between the bubbles, so as to obtain pure microbubble water.
需要说明的是,本实施例中所述的气体与液体并不限于空气与水,在实际应用中可以根据需要选择不同的气体与液体,例如:选择油与惰性气体结合,也可以由本实施例提供的微气泡发生装置产生溶于油中的微气泡。It should be noted that the gases and liquids described in this embodiment are not limited to air and water. In practical applications, different gases and liquids can be selected according to needs. For example, oil and inert gas are selected to be combined. The provided microbubble generating device generates microbubbles dissolved in oil.
优选的,所述气泡发生器采用压力罐。本实施例中所述气泡生成器采用压力罐的主要目的,一是使所述气液混合物中的气泡充分融入液体中以减小所述气泡分割元件的工作压力;二是在工业上一般需要大流量的包含微气泡的液体,而压力罐往往设置有减压阀,当所述气泡生成器完成将气液混合物转化成微气泡的过程之后,只需打开减压阀,包含微气泡的液体就会快速从所述微气泡发生装置中涌出,以满足工业需求。此外,为了在所述压力罐中设置所述气泡分割元件,所述压力罐内部设置用于安装所述气泡分割元件的环形凹槽,所述环形凹槽的数量与所述气泡分割元件的数量一致。Preferably, the bubble generator adopts a pressure tank. The main purpose of using a pressure tank for the bubble generator in this embodiment is to fully integrate the bubbles in the gas-liquid mixture into the liquid to reduce the working pressure of the bubble dividing element; Large flow of liquid containing micro-bubbles, and pressure tanks are often provided with a pressure reducing valve. After the bubble generator completes the process of converting the gas-liquid mixture into micro-bubbles, it is only necessary to open the pressure-reducing valve, and the liquid containing micro-bubbles It will quickly pour out of the microbubble generating device to meet industrial needs. In addition, in order to provide the air bubble dividing element in the pressure tank, an annular groove for installing the air bubble dividing element is provided inside the pressure tank, and the number of the annular groove is the same as the number of the air bubble dividing element. Consistent.
另外,由于所述气泡分割元件被设置与所述压力罐内,因而,在考虑压力罐时,应优选罐体内部允许逐层设置所述气泡分割元件且罐体内部空间较大的压力罐,因此,本实施例在选择压力罐时,选择了隔膜式压力罐。In addition, since the bubble dividing element is arranged in the pressure tank, when considering the pressure tank, it should be preferred that the bubble dividing element can be installed layer by layer inside the tank body and the inner space of the tank body is large. Therefore, when selecting a pressure tank in this embodiment, a diaphragm type pressure tank is selected.
需要说明的是,上述气泡生成器罐体的选择只是本装置的一种优选的实施方式,在其他实施方式中可以采用不同的罐体结构,例如:压力罐可以根据实际情况采用气囊式压力罐。这些属于对本装置结构的简单变换,不偏离本申请的核心,都在本申请的保护范围之内。It should be noted that the above selection of the tank body of the bubble generator is only a preferred embodiment of the device. In other embodiments, different tank body structures can be used. For example, the pressure tank can be a bladder type pressure tank according to the actual situation. . These are simple changes to the structure of the device, do not deviate from the core of the present application, and are all within the protection scope of the present application.
另外,气泡生成器还可以为管道,为了在管道内设置更多的气泡分割元件,且节约空间,可以将所述管道设置为螺旋管道。另外,所述气泡分割元件逐层设置于以所述螺旋管道中心轴线为中心的纵向切面中。In addition, the bubble generator can also be a pipe. In order to arrange more bubble dividing elements in the pipe and save space, the pipe can be set as a spiral pipe. In addition, the bubble dividing elements are arranged layer by layer in a longitudinal section centered on the central axis of the helical pipe.
由此可见,经过所述气泡分割元件的气液混合物已经具备了微气泡的性质,但由于所述气泡分割元件并没有布满所述气泡生成器,因此,在所述气泡生成器出口以及距离其最近的一个气泡分割元件之间,必然会存在微气泡互相碰撞而导致微气泡相互融合的情况,因此,在所述微气泡发生装置设计的过程中,应当考虑将这些已融合的且不符合微气泡标准的气泡进行过滤,因此,本申请所述的第一实施例中还包含一气泡过滤器103。It can be seen that the gas-liquid mixture passing through the bubble dividing element already has the properties of micro-bubbles, but because the bubble dividing element is not covered with the bubble generator, therefore, at the outlet of the bubble generator and the distance Between the nearest bubble dividing element, there will inevitably be microbubbles colliding with each other and causing microbubbles to fuse with each other. Therefore, in the process of designing the microbubble generating device, it should be considered that these fused and non-conforming The micro-bubble standard bubbles are filtered. Therefore, the first embodiment described in this application further includes a
所述气泡过滤器103一端连接所述气泡生成器102的出口,其内部设置过滤层,通过气泡过滤器的气液混合物从所述气泡过滤器的另一端输出;气泡过滤器103的过滤尺寸,能够只允许符合微气泡定义的气泡经过,直径较大的气泡能够被挡住,直到分裂为微气泡,才能流出。One end of the
综上所述,本实施例提供的用于微气泡发生装置结构巧妙,摒弃了传统的使用压力溶解式微气泡发生装置以及微泡成孔技术,利用所述由气泡刺破层构成的气泡分割元件直接对气液混合物中的气泡进行处理,同时,在构建所述气泡分割元件的过程中,考虑气泡的可流动性与形状不规则等特性,充分利用气泡刺破层在物理上结构,使所述气液混合物流过多层气泡分割元件后可以形成包含微气泡的液体,这一结构设置不仅能耗低,而且产出的微气泡大小统一,同时大大提高了微气泡的产出效率。To sum up, the structure of the micro-bubble generating device provided in this embodiment is ingenious, and the traditional pressure-dissolving micro-bubble generating device and the micro-bubble pore-forming technology are abandoned, and the bubble dividing element composed of the bubble piercing layer is used. The bubbles in the gas-liquid mixture are directly processed, and at the same time, in the process of constructing the bubble dividing element, the flowability and irregular shape of the bubbles are considered, and the physical structure of the bubble piercing layer is fully utilized, so that the After the gas-liquid mixture flows through the multi-layer bubble dividing element, a liquid containing micro-bubbles can be formed. This structural arrangement not only has low energy consumption, but also produces a uniform size of micro-bubbles, and at the same time greatly improves the production efficiency of micro-bubbles.
在上述的实施例中,提供了一种微气泡发生装置,与之相应的,本申请还提供一种用于产生微气泡的气泡分割元件。由于装置实施例基本相似与产生微气泡的气泡分割元件实施例,所以描述得比较简单,相关之处参见系统实施例的部分说明即可。下述描述的设备实施例仅仅是示意性的。In the above-mentioned embodiments, a micro-bubble generating device is provided, and correspondingly, the present application also provides a bubble dividing element for generating micro-bubbles. Since the embodiment of the device is basically similar to the embodiment of the bubble dividing element for generating micro-bubbles, the description is relatively simple, and reference may be made to part of the description of the system embodiment for related parts. The device embodiments described below are merely illustrative.
本实施例为一种用于产生微气泡的气泡分割元件,包括:所述气泡分割元件至少包含两层气泡刺破层,每层气泡刺破层的尖端朝向同一侧,且相邻气泡刺破层的尖端相互错开。This embodiment is a bubble dividing element for generating microbubbles, including: the bubble dividing element includes at least two layers of bubble piercing layers, the tips of each layer of bubble piercing layers face the same side, and adjacent bubbles pierce The tips of the layers are staggered from each other.
所述相邻气泡刺破层的尖端相互错开,具体采用如下结构:位于下游位置的气泡刺破层的尖端朝向上游气泡刺破层的出泡口。所述气泡分割元件的目大于300。The tips of the adjacent bubble-piercing layers are staggered from each other, and the specific structure is as follows: the tip of the bubble-piercing layer located at the downstream position faces the bubble outlet of the upstream bubble-piercing layer. The mesh of the bubble dividing element is greater than 300.
本申请虽然以较佳实施例公开如上,但其并不是用来限定本申请,任何本领域技术人员在不脱离本申请的精神和范围内,都可以做出可能的变动和修改,因此本申请的保护范围应当以本申请权利要求所界定的范围为准。Although the present application is disclosed above with preferred embodiments, it is not intended to limit the present application. Any person skilled in the art can make possible changes and modifications without departing from the spirit and scope of the present application. Therefore, the present application The scope of protection shall be subject to the scope defined by the claims of this application.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111803983A (en) * | 2020-07-22 | 2020-10-23 | 湖北大江环保科技股份有限公司 | Oxygen pressure leaching flash evaporation exhaust control structure and control method thereof |
| CN114126749A (en) * | 2020-03-27 | 2022-03-01 | 真共生株式会社 | Rotary mixer, bubble shear filter, ultrafine bubble generation device, and method for producing ultrafine bubble fluid |
| CN115125105A (en) * | 2022-07-07 | 2022-09-30 | 百仑生物科技(江苏)有限公司 | Disposable bioreactor |
| CN115317960A (en) * | 2022-07-29 | 2022-11-11 | 中国计量大学 | A method for precise segmentation of bubbles and free release of sub-bubbles |
| CN115572682A (en) * | 2022-11-11 | 2023-01-06 | 中国科学院深圳先进技术研究院 | Double-layer brain slice incubation groove and patch clamp system |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2522173Y (en) * | 2002-01-25 | 2002-11-27 | 古继海 | Interference-type efficient floatation tower |
| JP2007000848A (en) * | 2005-06-27 | 2007-01-11 | Matsushita Electric Works Ltd | Method for generating fine bubble |
| JP2011177693A (en) * | 2010-03-04 | 2011-09-15 | Nyk Kk | Gas-liquid mixing apparatus |
| CN202129034U (en) * | 2011-04-29 | 2012-02-01 | 中国石油化工股份有限公司 | Gas-liquid mixer |
| CN102441332A (en) * | 2011-10-10 | 2012-05-09 | 浙江省海洋开发研究院 | Static mixer for pipeline |
| CN102917780A (en) * | 2010-03-22 | 2013-02-06 | 苏舍化学技术有限公司 | Mixing or dispersing element and process for static mixing or dispersing |
| CN102985172A (en) * | 2010-07-15 | 2013-03-20 | 韩国机械研究院 | Micro bubble generation device based on rotating unit |
| CN108704499A (en) * | 2018-08-02 | 2018-10-26 | 上海久田汽车零部件制造有限公司 | Microbubble generator |
| DE102017115645A1 (en) * | 2017-07-12 | 2019-01-17 | Washtec Holding Gmbh | Foam generating device for a vehicle treatment device |
| CN209302560U (en) * | 2018-12-06 | 2019-08-27 | 上海中兴科源环保科技有限公司 | Shear and bubble water generator |
| CN211659736U (en) * | 2019-09-17 | 2020-10-13 | 李常德 | Microbubble generating device and bubble segmentation component |
-
2019
- 2019-09-17 CN CN201910875283.7A patent/CN110652893A/en not_active Withdrawn
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2522173Y (en) * | 2002-01-25 | 2002-11-27 | 古继海 | Interference-type efficient floatation tower |
| JP2007000848A (en) * | 2005-06-27 | 2007-01-11 | Matsushita Electric Works Ltd | Method for generating fine bubble |
| JP2011177693A (en) * | 2010-03-04 | 2011-09-15 | Nyk Kk | Gas-liquid mixing apparatus |
| CN102917780A (en) * | 2010-03-22 | 2013-02-06 | 苏舍化学技术有限公司 | Mixing or dispersing element and process for static mixing or dispersing |
| CN102985172A (en) * | 2010-07-15 | 2013-03-20 | 韩国机械研究院 | Micro bubble generation device based on rotating unit |
| CN202129034U (en) * | 2011-04-29 | 2012-02-01 | 中国石油化工股份有限公司 | Gas-liquid mixer |
| CN102441332A (en) * | 2011-10-10 | 2012-05-09 | 浙江省海洋开发研究院 | Static mixer for pipeline |
| DE102017115645A1 (en) * | 2017-07-12 | 2019-01-17 | Washtec Holding Gmbh | Foam generating device for a vehicle treatment device |
| CN108704499A (en) * | 2018-08-02 | 2018-10-26 | 上海久田汽车零部件制造有限公司 | Microbubble generator |
| CN209302560U (en) * | 2018-12-06 | 2019-08-27 | 上海中兴科源环保科技有限公司 | Shear and bubble water generator |
| CN211659736U (en) * | 2019-09-17 | 2020-10-13 | 李常德 | Microbubble generating device and bubble segmentation component |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114126749A (en) * | 2020-03-27 | 2022-03-01 | 真共生株式会社 | Rotary mixer, bubble shear filter, ultrafine bubble generation device, and method for producing ultrafine bubble fluid |
| EP3967391A4 (en) * | 2020-03-27 | 2022-12-28 | Shinbiosis Corporation | ROTARY MIXER, BUBBLE SHEAR FILTER, ULTRAFINE BUBBLES GENERATING DEVICE AND ULTRAFINE BUBBLES FLUID PRODUCTION METHOD |
| CN114126749B (en) * | 2020-03-27 | 2024-11-08 | 真共生株式会社 | Rotating mixer, bubble shear filter, ultrafine bubble generating device and method for producing ultrafine bubble fluid |
| CN111803983A (en) * | 2020-07-22 | 2020-10-23 | 湖北大江环保科技股份有限公司 | Oxygen pressure leaching flash evaporation exhaust control structure and control method thereof |
| CN111803983B (en) * | 2020-07-22 | 2020-12-29 | 湖北大江环保科技股份有限公司 | Oxygen pressure leaching flash evaporation exhaust control structure and control method thereof |
| CN115125105A (en) * | 2022-07-07 | 2022-09-30 | 百仑生物科技(江苏)有限公司 | Disposable bioreactor |
| CN115125105B (en) * | 2022-07-07 | 2023-12-19 | 百仑生物科技(江苏)有限公司 | Disposable bioreactor |
| CN115317960A (en) * | 2022-07-29 | 2022-11-11 | 中国计量大学 | A method for precise segmentation of bubbles and free release of sub-bubbles |
| CN115317960B (en) * | 2022-07-29 | 2024-01-26 | 中国计量大学 | Method for precisely dividing bubbles and freely releasing sub-bubbles |
| CN115572682A (en) * | 2022-11-11 | 2023-01-06 | 中国科学院深圳先进技术研究院 | Double-layer brain slice incubation groove and patch clamp system |
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