CN102351281A - Fine-pitch multilayer pulse electric field flow treatment chamber - Google Patents
Fine-pitch multilayer pulse electric field flow treatment chamber Download PDFInfo
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Abstract
本发明涉及了一种微间距多层脉冲电场流动处理室,它包括由多块金属平板电极和绝缘薄层组成的多个并联层状处理室腔室,绝缘薄层设于两金属平板电极之间,绝缘薄层需要特殊剪裁,使两金属平板电极中间形成流线型处理腔体,绝缘薄层厚度即电极距离,金属平板电极错开放置,两端分别由金属螺杆连接,起固定和导通作用,这样只需两末端的金属板与脉冲电源两极连接,采用多层微间距平板电极,可以减小脉冲电源制作成本,即不需要高压就可达到较高的场强,而且,电场分布均匀,减小了边缘效应,便于液体流通;该装置体积小,有利于脉冲电场处理技术进入民用领域。
The invention relates to a micro-pitch multi-layer pulsed electric field flow processing chamber, which includes a plurality of parallel layered processing chambers composed of a plurality of metal plate electrodes and insulating thin layers, and the insulating thin layer is arranged between the two metal plate electrodes The insulating thin layer needs to be specially tailored to form a streamlined processing chamber between the two metal flat electrodes. The thickness of the insulating thin layer is the electrode distance. The metal flat electrodes are staggered and placed, and the two ends are connected by metal screws to fix and conduct. In this way, only the metal plates at both ends need to be connected to the poles of the pulse power supply, and the use of multi-layer micro-pitch flat plate electrodes can reduce the production cost of the pulse power supply, that is, high field strength can be achieved without high voltage, and the electric field is evenly distributed and reduced. The edge effect is reduced and liquid circulation is facilitated; the device is small in size, which is conducive to the pulse electric field treatment technology entering the civilian field.
Description
技术领域 technical field
本发明涉及一种民用水净化的灭菌装置,特别涉及一种微间距多层适用于中等电压的脉冲电场流动处理室。 The invention relates to a sterilizing device for purifying civil water, in particular to a pulse electric field flow treatment chamber with multiple layers of micro-pitch and suitable for medium voltage.
背景技术 Background technique
脉冲电场技术具有处理温度低,杀菌时间短,耗能低,无化学副产物等优点,因而得到广泛关注。目前的脉冲电场处理室较大,往往需要采用高压脉冲电场来形成足可杀灭细菌的电场。绝大部分这类装置仍处于实验室研究阶段,未在工业及民用领域广泛使用。由于在电极形状等因素的影响,处理室内存在电场分布不均匀的问题,使两电极之间各个局部的电场强度相差甚远,导致电场强度过高的局部可能产生电弧放电;或者电场强度过低的局部可能达不到名义电场强度的处理效果。又由于对脉冲电场处理系统的研究基本上是基于较大容量处理室,所以需要高压脉冲发生器。例如,专利号为200410011305的中国发明专利公开了一种高压脉冲电场处理装置,专利号为200710008437的中国发明专利公开了一种可用于连续式高压脉冲电场设备的脉冲电场处理室。这类装置体积大,成本高,制作难度较大,稳定性不好。微间隙处理室则可使用低电压脉冲发生器实现同样的灭菌效果,但是单个微间隙处理室处理量少,平板电极直角边缘有边缘效应,易产生电火花。 Pulsed electric field technology has the advantages of low treatment temperature, short sterilization time, low energy consumption, and no chemical by-products, so it has attracted widespread attention. The current pulsed electric field treatment chamber is relatively large, and a high-voltage pulsed electric field is often required to form an electric field sufficient to kill bacteria. Most of these devices are still in the stage of laboratory research and have not been widely used in industrial and civilian fields. Due to the influence of factors such as electrode shape, there is a problem of uneven electric field distribution in the treatment chamber, which makes the electric field strength of each part between the two electrodes very different, resulting in the possibility of arc discharge in the part where the electric field strength is too high; or the electric field strength is too low The treatment effect of the nominal electric field strength may not be achieved locally. And because the research on the pulsed electric field processing system is basically based on a large-capacity processing chamber, a high-voltage pulse generator is required. For example, Chinese Invention Patent No. 200410011305 discloses a high-voltage pulsed electric field treatment device, and Chinese Invention Patent No. 200710008437 discloses a pulsed electric field treatment chamber that can be used in continuous high-voltage pulsed electric field equipment. This type of device is bulky, high in cost, difficult to manufacture, and poor in stability. The micro-gap treatment chamber can use a low-voltage pulse generator to achieve the same sterilization effect, but the processing capacity of a single micro-gap treatment chamber is small, and the right-angled edge of the flat electrode has an edge effect, which is easy to generate electric sparks.
因此,急需一种结构简单、成本低、使用范围广的能有效处理物料的脉冲电场杀菌设备。 Therefore, there is an urgent need for a pulsed electric field sterilization equipment with simple structure, low cost and wide application range that can effectively process materials.
发明内容 Contents of the invention
有鉴于此,为了解决上述问题,本发明提出一种结构简单、成本低、能有效的处理物料的脉冲电场杀菌设备,通过级联多个电极不但可以扩大处理室容量,还可以在低电压条件下获得高电场,解决了脉冲电场杀菌必须采用高压脉冲电源设备的问题,降低了脉冲电源设备的成本。处理腔室设计成流线型可以减少平板电极直角边缘的边缘效应,并且便于物料流通。采用错置的平板电极使电场分布均匀,便于更有效的处理物料。 In view of this, in order to solve the above problems, the present invention proposes a pulsed electric field sterilization equipment with simple structure, low cost, and effective treatment of materials. By cascading multiple electrodes, not only can the capacity of the treatment chamber be expanded, but also can be used under low voltage conditions. High electric field can be obtained under the condition of pulse electric field, which solves the problem that high-voltage pulse power supply equipment must be used for pulse electric field sterilization, and reduces the cost of pulse power supply equipment. The processing chamber is designed to be streamlined to reduce the edge effect of the right-angled edge of the flat electrode and facilitate material circulation. Displaced plate electrodes are used to make the electric field evenly distributed, which facilitates more effective material processing.
本发明提供的一种微间距多层脉冲电场流动处理室,包括至少一个正电极、至少一个负电极、至少两片绝缘薄层和绝缘盒体;所述正电极与负电极为板状电极且相对固定放置,所述两片绝缘层分别设置于正负电极的相对面上,所述两片绝缘层相对面之间形成处理腔室,所述正电极和负电极分别与脉冲电源的两极连接,所述正电极和负电极之间电场的电力线方向与处理腔室物料流动方向垂直,所述正负电极密封在绝缘盒体中。 A micro-pitch multilayer pulsed electric field flow processing chamber provided by the present invention includes at least one positive electrode, at least one negative electrode, at least two insulating thin layers and an insulating box; the positive electrode and the negative electrode are plate electrodes and are opposite to each other fixedly placed, the two insulating layers are respectively arranged on the opposite surfaces of the positive and negative electrodes, a processing chamber is formed between the opposite surfaces of the two insulating layers, the positive electrode and the negative electrode are respectively connected to the two poles of the pulse power supply, The electric force line direction of the electric field between the positive electrode and the negative electrode is perpendicular to the material flow direction in the processing chamber, and the positive and negative electrodes are sealed in an insulating box.
进一步,所述绝缘薄层包括第一绝缘薄层和第二绝缘薄层,所述第一绝缘薄层和第二绝缘薄层的中部凹陷,所述第一绝缘薄层和第二绝缘薄层之间形成两端窄中间宽的流线型处理腔室; Further, the insulating thin layer includes a first insulating thin layer and a second insulating thin layer, the middle of the first insulating thin layer and the second insulating thin layer is recessed, and the first insulating thin layer and the second insulating thin layer A streamlined processing chamber with narrow ends and a wide middle is formed between them;
进一步,所述第一绝缘薄层的宽度大于第二绝缘薄层与第一绝缘薄层相对应位置的宽度; Further, the width of the first insulating thin layer is larger than the width of the corresponding position of the second insulating thin layer and the first insulating thin layer;
进一步,所述正电极上下端通过第一金属螺杆固定,所述负电极上下端通过第二金属螺杆固定; Further, the upper and lower ends of the positive electrode are fixed by a first metal screw, and the upper and lower ends of the negative electrode are fixed by a second metal screw;
进一步,所述正负电极分别设置有第一接线槽和第二接线槽,所述绝缘盒体侧面设置有第一接线口和第二接线口,所述第一接线口与第一接线槽相连,所述第二接线口与第二接线槽相连; Further, the positive and negative electrodes are respectively provided with a first wiring slot and a second wiring slot, and the side of the insulating box is provided with a first wiring opening and a second wiring opening, and the first wiring opening is connected to the first wiring slot , the second wiring port is connected to the second wiring slot;
进一步,所述绝缘盒体上设置有入口和出口。所述入口和出口与处理腔室相连通,所述绝缘盒体开设有入口的侧面设置有与处理室宽度匹配的凹槽,所述入口位于凹槽部位的中央。所述绝缘盒体开设有出口的侧面设置有与处理室宽度匹配的凹槽,所述出口位于凹槽部位的中央; Further, the insulating box is provided with an inlet and an outlet. The inlet and the outlet communicate with the processing chamber, and the side of the insulating box with the inlet is provided with a groove matching the width of the processing chamber, and the inlet is located in the center of the groove. The side of the insulating box with the outlet is provided with a groove matching the width of the processing chamber, and the outlet is located in the center of the groove;
进一步,所述正负电极为金属平板电极。所述正负电极还设置有亲水涂层,所述亲水涂层厚度为0至5 微米; Further, the positive and negative electrodes are flat metal electrodes. The positive and negative electrodes are also provided with a hydrophilic coating, and the thickness of the hydrophilic coating is 0 to 5 microns;
进一步,所述金属平板电极采用不锈钢材质制作; Further, the metal plate electrode is made of stainless steel;
进一步,所述的绝缘薄层采用聚四氟乙烯材质制作; Further, the insulating thin layer is made of polytetrafluoroethylene;
进一步,所述正负电极包括12片金属平板,所述金属平板沿螺杆方向平行可重叠。 Further, the positive and negative electrodes include 12 metal flat plates, and the metal flat plates are parallel and overlapable along the direction of the screw.
本发明的优点在于:采用级联多电极不但可以扩大处理室容量,还可以在低压条件下就可获得高电场,解决了脉冲电场杀菌必须采用高压脉冲电源设备的问题,降低了脉冲电源设备的成本,这样能耗相对较低,可以进一步提高能量利用率,装置小;处理腔室设计成流线型可以减少平板电极直角边缘的边缘效应,并且便于物料流通;采用错置的平板电极,电场分布均匀,便于更有效的处理物料;电极采用金属螺杆固定,只需在两端连接外部电源即可实现所有对应正负电极导通;同时,采用螺杆固定,便于对电极进行拆卸、清洗和更换。因此,本发明大大减小了脉冲电源电压,成本减小,安全性提高,有利于脉冲电场技术进入民用领域。 The advantage of the present invention is that: the use of cascaded multi-electrodes can not only expand the capacity of the treatment chamber, but also obtain a high electric field under low voltage conditions, which solves the problem that high-voltage pulse power supply equipment must be used for pulse electric field sterilization, and reduces the cost of pulse power supply equipment. Cost, so that the energy consumption is relatively low, which can further improve the energy utilization rate, and the device is small; the processing chamber is designed to be streamlined, which can reduce the edge effect of the right-angled edge of the flat electrode and facilitate material circulation; the misplaced flat electrode is used, and the electric field is evenly distributed , to facilitate more effective material processing; the electrodes are fixed by metal screws, and all corresponding positive and negative electrodes can be realized by connecting external power at both ends; at the same time, fixed by screws, it is easy to disassemble, clean and replace the electrodes. Therefore, the present invention greatly reduces the pulse power supply voltage, reduces the cost, improves the safety, and facilitates the pulse electric field technology to enter the civilian field.
本发明的其它优点、目标和特征在某种程度上将在随后的说明书中进行阐述,并且在某种程度上,基于对下文的考察研究对本领域技术人员而言将是显而易见的,或者可以从本发明的实践中得到教导。本发明的目标和其它优点可以通过下面的说明书,权利要求书,以及附图中所特别指出的结构来实现和获得。 Other advantages, objects and features of the present invention will be set forth in the following description to some extent, and to some extent, will be obvious to those skilled in the art based on the investigation and research below, or can be obtained from It is taught in the practice of the present invention. The objectives and other advantages of the invention may be realized and attained by the structure particularly pointed out in the written description and claims hereof as well as the appended drawings.
附图说明 Description of drawings
为了使本发明的目的、技术方案和优点更加清楚,下面将结合附图对本发明作进一步的详细描述,其中: In order to make the purpose, technical solutions and advantages of the present invention clearer, the present invention will be described in further detail below in conjunction with the accompanying drawings, wherein:
图1是本发明去顶端盖的处理室示意图; Fig. 1 is the schematic diagram of the processing chamber of the present invention without end cap;
图2是本发明电极结构示意图; Fig. 2 is a schematic diagram of the electrode structure of the present invention;
图3是本发明密封盒示意图; Fig. 3 is a schematic diagram of the sealing box of the present invention;
图4是本发明单处理单元内部示意图; Fig. 4 is an internal schematic diagram of a single processing unit of the present invention;
图5是本发明密封盒顶部示意图; Fig. 5 is a schematic diagram of the top of the sealing box of the present invention;
图6是入口宽2 cm,出口宽2 cm通道的速度轮廓线(入口速度为0.01 m/s); Figure 6 is the velocity profile of a channel with a width of 2 cm at the entrance and a channel with a width of 2 cm at the exit (the entrance velocity is 0.01 m/s);
图7是入口宽2 cm,出口宽2 cm通道的出口处速度分布图(入口速度为0.01 m/s); Figure 7 is the velocity distribution diagram at the exit of the channel with an entrance width of 2 cm and an exit width of 2 cm (the entrance velocity is 0.01 m/s);
图8是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.01 m/s); Figure 8 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 4 cm (entrance velocity is 0.01 m/s);
图9是入口宽2 cm,出口宽4 cm通道的出口处速度分布图(入口速度为0.01 m/s); Figure 9 is the distribution of velocity at the exit of a channel with an entrance width of 2 cm and an exit width of 4 cm (entrance velocity is 0.01 m/s);
图10是入口宽2 cm,出口宽6 cm通道的速度轮廓线(入口速度为0.01 m/s); Figure 10 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 6 cm (entrance velocity is 0.01 m/s);
图11是图7入口宽2 cm,出口宽6 cm通道的出口处速度分布图(入口速度为0.01 m/s); Figure 11 is the velocity distribution diagram at the exit of the channel with an entrance width of 2 cm and an exit width of 6 cm in Figure 7 (the entrance velocity is 0.01 m/s);
图12是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.001 m/s); Figure 12 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 4 cm (entrance velocity is 0.001 m/s);
图13是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.02 m/s)。 Figure 13 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 4 cm (entrance velocity is 0.02 m/s).
具体实施方式 Detailed ways
以下将结合附图,对本发明的优选实施例进行详细的描述;应当理解,优选实施例仅为了说明本发明,而不是为了限制本发明的保护范围。 The preferred embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings; it should be understood that the preferred embodiments are only for illustrating the present invention, rather than limiting the protection scope of the present invention.
图1是本发明去顶端盖的处理室示意图;本发明提供的实施例采用6片正电极和6片负电极,图2是本发明电极结构示意图;图3是本发明密封盒示意图;图4是本发明的单处理单元内部示意图。如图所示:本发明提供的一种微间距多层脉冲电场流动处理室,包括至少一个正电极1、至少一个负电极2、至少两片绝缘薄层13和绝缘盒体12;所述正电极1与负电极2为板状电极且相对固定放置,所述两片绝缘层13分别设置于正负电极的相对面上,所述两片绝缘层13相对面之间形成处理腔室3,所述正电极1和负电极2分别与脉冲电源的两极连接,所述正电极1和负电极2之间电场的电力线方向与处理腔室3物料流动方向垂直,所述正负电极密封在绝缘盒体12中;实际放置时,盒子是平放的,即待处理液可以从左边进,右边出。
Fig. 1 is the schematic diagram of the treatment chamber of the present invention without the end cap; the embodiment provided by the present invention adopts 6 positive electrodes and 6 negative electrodes, and Fig. 2 is a schematic diagram of the electrode structure of the present invention; Fig. 3 is a schematic diagram of the sealed box of the present invention; Fig. 4 It is the internal schematic diagram of the single processing unit of the present invention. As shown in the figure: a micro-pitch multi-layer pulsed electric field flow treatment chamber provided by the present invention includes at least one
作为上述实施例的进一步改进,所述绝缘薄层13包括第一绝缘薄层131和第二绝缘薄层132,所述第一绝缘薄层131和第二绝缘薄层132的中部凹陷,所述第一绝缘薄层131和第二绝缘薄层132之间形成上窄下宽的流线型处理腔室。
As a further improvement of the above-mentioned embodiment, the insulating
作为上述实施例的进一步改进,所述第一绝缘薄层131的厚度大于第二绝缘薄层132与第一绝缘薄层131相对应位置的厚度。
As a further improvement of the above embodiment, the thickness of the first insulating
作为上述实施例的进一步改进,所述正电极上下端通过第一金属螺杆4固定,所述负电极上下端通过第二金属螺杆5固定。
As a further improvement of the above embodiment, the upper and lower ends of the positive electrode are fixed by the
作为上述实施例的进一步改进,所述正负电极分别设置有第一接线槽6和第二接线槽7,第二接线槽7在另一侧电极处位置与第一接线槽6位置相对应,所述绝缘盒体12侧面设置有第一接线口8和第二接线口9,第二接线口在第一接线口8对侧与8位置相对应,所述第一接线口8与第一接线槽6相连,所述第二接线口9与第二接线槽7相连,绝缘盒体12内部的正负电极上的第一接线槽6、第二接线槽7分别与外部的第一接线口8和第二接线口9位置对应、连接,再与脉冲电源设备实现连接。
As a further improvement of the above embodiment, the positive and negative electrodes are respectively provided with a
作为上述实施例的进一步改进,所述绝缘盒体12上设置有入口10和出口11,所述入口10和出口11与处理腔室3相连通,所有正负电极固定好,放置在密封盒体12内部空间中,共同构成可用于连续处理的处理室;所述绝缘盒体开设有入口的侧面设置有与处理室3宽度匹配的凹槽14,密封盒出口内侧凹槽在密封盒入口内侧凹槽14对侧与14位置相对应,所述入口位于凹槽部位的中央,所述绝缘盒体开设有出口的侧面设置有与处理室3宽度匹配的凹槽,所述出口位于凹槽部位的中央。
As a further improvement of the above embodiment, the
作为上述实施例的进一步改进,所述正负电极为金属平板电极;所述正负电极还设置有亲水涂层,所述亲水涂层厚度为0至5 微米。 As a further improvement of the above embodiment, the positive and negative electrodes are flat metal electrodes; the positive and negative electrodes are also provided with a hydrophilic coating, and the thickness of the hydrophilic coating is 0 to 5 microns.
作为上述实施例的进一步改进,所述金属平板电极采用不锈钢材质制作。 As a further improvement of the above embodiment, the flat metal electrode is made of stainless steel.
作为上述实施例的进一步改进,所述的绝缘薄层采用聚四氟乙烯材质制作。 As a further improvement of the above embodiment, the insulating thin layer is made of polytetrafluoroethylene.
作为上述实施例的进一步改进,所述正负电极包括12片金属平板,所述金属平板沿螺杆方向平行可重叠,第一金属螺杆4包括两根金属螺杆分别固定于正电极上下端,第二金属螺杆5包括两根金属螺杆分别固定于负电极上下端,总共四个螺杆实现同极性的固定、导通。
As a further improvement of the above embodiment, the positive and negative electrodes include 12 metal flat plates, and the metal flat plates can be overlapped in parallel along the screw direction. The
每对正负电极之间由绝缘薄片隔开,形成处理腔室,在两端电极开有接线槽6、7,方便与脉冲电场设备两极相连。所述电极个数可以根据实际需要增加或者减少,产生不同数量处理腔室,实现不同的单次处理量。所述绝缘薄片厚度也可适当调整,如200 微米,300 微米或者更大的厚度,而且也可以不用绝缘薄片,而是直接在金属电极2两侧加工几百微米厚度的绝缘材料。所述电极用金属螺杆固定、导通,便于对电极进行拆卸、清洗和更换。
Each pair of positive and negative electrodes is separated by an insulating sheet to form a processing chamber, and the electrodes at both ends are provided with
绝缘薄层13的形状如图4中的阴影部分,中间形成上窄下宽的流线型处理腔室3,为了与错置开的电极对应,左右绝缘层宽度并不对称。
The shape of the insulating
金属平板正负电极1、2材料为不锈钢或者可选择更耐腐蚀的金属电极。所述绝缘薄层13或者绝缘涂层13材料为聚四氟乙烯。所述密封盒12也可采用聚四氟乙烯制作。
The metal plate positive and
下面详细描述使用单个处理室的工作过程: The working process using a single chamber is described in detail below:
放在绝缘盒体中的处理室横着放置的,即带处理液从左侧进入,右侧流出,实际使用时可以将多个处理室串联起来使用,进一步提高灭菌效果。 The treatment chamber placed in the insulating box is placed horizontally, that is, the treatment liquid enters from the left side and flows out from the right side. In actual use, multiple treatment chambers can be connected in series to further improve the sterilization effect.
使用单层静态处理室(即一个正电极、一个负电极组成),电场强度为20 kV/cm,脉冲个数50个,脉冲宽度为50 微米,脉冲间隔400 ms时,大肠杆菌有3.22个数量级下降,实际用于流动处理时,脉冲频率要高得多,更有利于杀菌。 When using a single-layer static treatment chamber (that is, one positive electrode and one negative electrode), the electric field strength is 20 kV/cm, the number of pulses is 50, the pulse width is 50 microns, and the pulse interval is 400 ms, E. coli has 3.22 orders of magnitude When it is actually used for flow treatment, the pulse frequency is much higher, which is more conducive to sterilization.
电极大小可以根据实际需要进行调整,本实例取电极宽10 cm,长15 cm,实际处理室的宽度可以适当调节,但最好满足入口窄出口宽;电极个数为12片,电极距离200 微米,电极厚度1 mm,密封盒大小可以根据所用电极数量进行调节,即内部大小为刚好容纳多层电极,其两端凹槽深5 mm。 The size of the electrode can be adjusted according to actual needs. In this example, the electrode width is 10 cm and the length is 15 cm. The width of the actual processing chamber can be adjusted appropriately, but it is best to meet the narrow entrance and exit width; the number of electrodes is 12, and the electrode distance is 200 microns , The electrode thickness is 1 mm, and the size of the sealed box can be adjusted according to the number of electrodes used, that is, the internal size is just enough to accommodate multi-layer electrodes, and the grooves at both ends are 5 mm deep.
图6是入口宽2 cm,出口宽2 cm通道的速度轮廓线(入口速度为0.01 m/s);图7是入口宽2 cm,出口宽2 cm通道的出口处速度分布图(入口速度为0.01 m/s);图8是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.01 m/s);图9是入口宽2 cm,出口宽4 cm通道的出口处速度分布图(入口速度为0.01 m/s);图10是入口宽2 cm,出口宽6 cm通道的速度轮廓线(入口速度为0.01m/s);图11是入口宽2 cm,出口宽6 cm通道的出口处速度分布图(入口速度为0.01 m/s);图12是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.001 m/s);图13是入口宽2 cm,出口宽4 cm通道的速度轮廓线(入口速度为0.02 m/s)。从这些图可以看出,当入口出口宽度一致时,整个处理通道中速度分布相对来说更不均匀;当然,并非出口宽度越大越好,宽度过大时,两侧速度过低,液体积存在处理通道中可能导致液体温升过大。所以综合考虑,本实例选择的是入口宽2 cm,出口宽4 cm,中间最宽为7 cm的处理通道。 Fig. 6 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 2 cm (the entrance velocity is 0.01 m/s); Fig. 7 is a velocity profile at the exit of a channel with an entrance width of 2 cm and an exit width of 2 cm (the entrance velocity is 0.01 m/s); Figure 8 is the velocity profile of a channel with an entrance width of 2 cm and an exit width of 4 cm (the entrance velocity is 0.01 m/s); Figure 9 is the velocity at the exit of a channel with an entrance width of 2 cm and an exit width of 4 cm Distribution map (inlet velocity is 0.01 m/s); Figure 10 is the velocity profile of the channel with an entrance width of 2 cm and an exit width of 6 cm (inlet velocity is 0.01m/s); Figure 11 is a channel with an entrance width of 2 cm and an exit width of 6 cm The velocity profile at the exit of the cm channel (inlet velocity is 0.01 m/s); Figure 12 is the velocity profile of the channel with an entrance width of 2 cm and an exit width of 4 cm (inlet velocity is 0.001 m/s); Figure 13 is the entrance width Velocity profile of a 2 cm channel with a 4 cm exit width (entrance velocity is 0.02 m/s). It can be seen from these figures that when the width of the inlet and outlet is the same, the velocity distribution in the entire processing channel is relatively more uneven; of course, the larger the width of the outlet, the better. Excessive temperature rise of the liquid may result in the process channel. Therefore, after comprehensive consideration, this example chooses a processing channel with an entrance width of 2 cm, an exit width of 4 cm, and a width of 7 cm in the middle.
作为一个适用于连续流的处理室,需要对其流速进行控制,尤其是本发明是微间隙通道,既要保证处理液在通道中受到足够脉冲个数,同时要保证单位时间足够的处理量,还要降低液体流通时产生气泡的可能性,更需要合适的流速。从图8、12、13可以看出,当入口速度达到0.02 m/s时,通道内流速分布开始变得极不规则,容易有气泡产生,入口速度越低,整个通道流速分布越均匀。综合因素考虑,可以选择入口速度在0.001 m/s到0.01 m/s之间。 As a treatment chamber suitable for continuous flow, it is necessary to control its flow rate, especially the micro-gap channel of the present invention. It is necessary to ensure that the treatment liquid receives a sufficient number of pulses in the channel, and at the same time ensure a sufficient processing volume per unit time. It is also necessary to reduce the possibility of air bubbles when the liquid is circulated, and an appropriate flow rate is required. It can be seen from Figures 8, 12, and 13 that when the inlet velocity reaches 0.02 m/s, the flow velocity distribution in the channel becomes extremely irregular, and bubbles are likely to be generated. The lower the inlet velocity, the more uniform the flow velocity distribution in the entire channel. Considering all factors, the inlet velocity can be selected between 0.001 m/s and 0.01 m/s.
以上所述仅为本发明的优选实施例,并不用于限制本发明,显然,本领域的技术人员可以对本发明进行各种改动和变型而不脱离本发明的精神和范围。这样,倘若本发明的这些修改和变型属于本发明权利要求及其等同技术的范围之内,则本发明也意图包含这些改动和变型在内。 The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Obviously, those skilled in the art can make various changes and modifications to the present invention without departing from the spirit and scope of the present invention. Thus, if these modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalent technologies, the present invention also intends to include these modifications and variations.
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CN108110621A (en) * | 2017-12-15 | 2018-06-01 | 浙江工商大学 | The board-like high electric field elementary cell and reactor of a kind of anti-surface leakage |
CN114988538A (en) * | 2022-07-14 | 2022-09-02 | 广西大学 | Circulating water sterilization system based on pulse electric field treatment technology |
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