CN116158557A - Nebulizers and Vaping Devices - Google Patents
Nebulizers and Vaping Devices Download PDFInfo
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- CN116158557A CN116158557A CN202111405682.0A CN202111405682A CN116158557A CN 116158557 A CN116158557 A CN 116158557A CN 202111405682 A CN202111405682 A CN 202111405682A CN 116158557 A CN116158557 A CN 116158557A
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- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24F—SMOKERS' REQUISITES; MATCH BOXES; SIMULATED SMOKING DEVICES
- A24F40/00—Electrically operated smoking devices; Component parts thereof; Manufacture thereof; Maintenance or testing thereof; Charging means specially adapted therefor
- A24F40/40—Constructional details, e.g. connection of cartridges and battery parts
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- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24F—SMOKERS' REQUISITES; MATCH BOXES; SIMULATED SMOKING DEVICES
- A24F40/00—Electrically operated smoking devices; Component parts thereof; Manufacture thereof; Maintenance or testing thereof; Charging means specially adapted therefor
- A24F40/40—Constructional details, e.g. connection of cartridges and battery parts
- A24F40/48—Fluid transfer means, e.g. pumps
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Abstract
本发明公开了一种雾化器和电子雾化装置。该雾化器包括壳体、安装座和雾化芯;壳体具有出气通道;安装座的内部具有雾化腔;雾化芯设于雾化腔中;雾化芯具有雾化面,雾化面面向安装座的出气孔,出气通道连通于安装座的出气孔;其中,安装座上开设有进气孔,进气孔用于与外界大气以及雾化腔连通,以使外界大气能通过进气孔流入雾化腔,雾化面与进气孔之间的相隔一定距离h。本申请的雾化器和电子雾化装置能降低流出出气口的气溶胶的温度,提升用户的使用体验。
The invention discloses an atomizer and an electronic atomization device. The atomizer includes a housing, an installation seat and an atomizing core; the housing has an air outlet channel; the interior of the installation seat has an atomization cavity; the atomization core is arranged in the atomization cavity; the atomization core has an atomization surface, and the atomization The surface faces the air outlet of the mounting base, and the air outlet channel is connected to the air outlet of the mounting base; wherein, the mounting base is provided with an air inlet, which is used to communicate with the outside atmosphere and the atomization chamber, so that the outside atmosphere can pass through the air outlet. The air hole flows into the atomization chamber, and the atomization surface and the air inlet hole are separated by a certain distance h. The atomizer and electronic atomization device of the present application can reduce the temperature of the aerosol flowing out of the air outlet, and improve the user experience.
Description
技术领域technical field
本发明涉及电子雾化装置技术领域,尤其涉及一种雾化器和电子雾化装置。The invention relates to the technical field of electronic atomization devices, in particular to an atomizer and an electronic atomization device.
背景技术Background technique
电子雾化装置是一种能将气溶胶产生基质雾化成气溶胶的装置,被广泛应用于日常生活中。电子雾化装置中的雾化芯具有雾化面,雾化面上设置有发热层,发热层通电后能对雾化面附近的气溶胶产生基质进行加热,以使气溶胶产生基质加热雾化生成气溶胶,气溶胶经由出气口流出电子雾化装置供用户使用。An electronic atomization device is a device that can atomize an aerosol-generating substrate into an aerosol, and is widely used in daily life. The atomizing core in the electronic atomization device has an atomizing surface, and a heating layer is arranged on the atomizing surface. After the heating layer is energized, it can heat the aerosol generating substrate near the atomizing surface, so that the aerosol generating substrate is heated and atomized An aerosol is generated, and the aerosol flows out of the electronic atomization device through the air outlet for use by the user.
通常,雾化芯的雾化面朝下设置,即朝向电子雾化装置的进气口设置。为了增加流出电子雾化装置的气雾量,雾化芯的雾化面也可以朝上设置,即朝向出气口设置,由此可以大大缩短出气口与雾化面之间的距离,提高流出电子雾化装置的气雾量。然而,雾化面朝上设置会使从出气口流出的气溶胶的温度增大,用户的使用体验变差。Usually, the atomizing surface of the atomizing core is set downward, that is, it is set towards the air inlet of the electronic atomizing device. In order to increase the amount of aerosol flowing out of the electronic atomization device, the atomizing surface of the atomizing core can also be set up, that is, facing the air outlet, so that the distance between the air outlet and the atomizing surface can be greatly shortened, and the flow of electrons can be improved. The amount of aerosol in the nebulizer. However, setting the atomizing side upward will increase the temperature of the aerosol flowing out from the air outlet, and the user experience will be deteriorated.
发明内容Contents of the invention
本发明提供的雾化器和电子雾化装置,解决雾化面朝上设置时流出出气口的气溶胶的温度较高、用户的使用体验较差的问题。The atomizer and the electronic atomization device provided by the present invention solve the problems of high temperature of the aerosol flowing out of the air outlet and poor user experience when the atomization surface is set upward.
为了解决上述技术问题,本申请提供的第一个技术方案为:提供一种雾化器,该雾化器包括壳体、安装座和雾化芯;壳体具有出气通道;安装座的内部具有雾化腔;雾化芯设于雾化腔中;雾化芯具有雾化面,雾化面面向安装座的出气孔,出气通道连通于安装座的出气孔;其中,安装座上开设有进气孔,进气孔用于与外界大气以及雾化腔连通,以使外界大气能通过进气孔流入雾化腔,雾化面与进气孔之间相隔一定距离h。In order to solve the above technical problems, the first technical solution provided by this application is: provide an atomizer, the atomizer includes a housing, an installation base and an atomizing core; the housing has an air outlet channel; the inside of the installation base has The atomization chamber; the atomization core is set in the atomization chamber; the atomization core has an atomization surface, the atomization surface faces the air outlet hole of the mounting seat, and the air outlet channel is connected to the air outlet hole of the mounting seat; wherein, the mounting seat is provided with an inlet The air hole, the air intake hole is used to communicate with the outside atmosphere and the atomization chamber, so that the outside air can flow into the atomization chamber through the air inlet hole, and there is a certain distance h between the atomization surface and the air inlet hole.
其中,h的范围为0mm<h≤0.7mm。Wherein, the range of h is 0mm<h≤0.7mm.
其中,h的范围为0.2mm≤h≤0.5mm。Wherein, the range of h is 0.2mm≤h≤0.5mm.
其中,壳体中具有安装腔;安装座设于安装腔中;安装座具有相互连接的顶壁和侧壁,顶壁和侧壁围设形成雾化腔;安装座的侧壁与安装腔的侧壁配合形成导气通道;雾化芯靠近顶壁的一侧具有雾化面;其中,安装座的侧壁开设有进气孔,以导气通道与雾化腔连通。Wherein, there is an installation cavity in the shell; the installation seat is arranged in the installation cavity; the installation seat has a top wall and a side wall connected to each other, and the top wall and the side wall are surrounded to form an atomization chamber; the side wall of the installation seat and the installation cavity The side walls cooperate to form an air guiding channel; the side of the atomizing core close to the top wall has an atomizing surface; wherein, the side wall of the mounting seat is provided with an air inlet to communicate with the atomizing chamber through the air guiding channel.
其中,壳体中具有储液腔,储液腔用于存储气溶胶产生基质;安装座中具有导液通道,导液通道与储液腔连通,导液通道用于将储液腔中的气溶胶产生基质导流至雾化芯的侧壁和/或雾化芯远离出气孔的一面。Wherein, there is a liquid storage chamber in the housing, and the liquid storage chamber is used to store the aerosol generating matrix; there is a liquid guide channel in the mounting seat, and the liquid guide channel is connected with the liquid storage chamber, and the liquid guide channel is used to transfer the gas in the liquid storage chamber The sol generating matrix is guided to the side wall of the atomization core and/or the side of the atomization core away from the air outlet.
其中,安装座包括安装顶盖和安装底座;安装顶盖套设在安装底座上;Wherein, the installation seat includes an installation top cover and an installation base; the installation top cover is sleeved on the installation base;
安装顶盖的侧壁的外表面设有导气槽,安装腔的侧壁与导气槽的底壁配合形成导气通道,导气槽靠近安装顶盖的顶壁的一侧设有进气孔;安装底座具有进气口,导气通道远离进气孔的一端与进气口连通。The outer surface of the side wall where the top cover is installed is provided with an air guiding groove, the side wall of the installation cavity cooperates with the bottom wall of the air guiding groove to form an air guiding channel, and the side of the air guiding groove close to the top wall where the top cover is installed is provided with an air inlet hole; the installation base has an air inlet, and the end of the air guide channel away from the air inlet is connected with the air inlet.
其中,进气孔的宽度等于导气槽的宽度。Wherein, the width of the air inlet hole is equal to the width of the air guide groove.
其中,导气槽的一端为封闭端,靠近安装顶盖的顶壁设置,导气槽的另一端为敞口端,延伸至安装顶盖的底面。Wherein, one end of the air guide groove is a closed end, which is arranged close to the top wall of the installation top cover, and the other end of the air guide groove is an open end, which extends to the bottom surface of the installation top cover.
其中,安装底座包括底部和支撑部,安装顶盖套设于支撑部上并与底部抵接,雾化芯设于支撑部靠近安装顶盖的顶壁的一侧。Wherein, the installation base includes a bottom and a support part, the installation top cover is sleeved on the support part and abuts against the bottom, and the atomizing core is arranged on a side of the support part close to the top wall of the installation top cover.
其中,导气槽的数量为两个,分别设置于安装顶盖相对的两个侧壁的外表面上;底部背离支撑部的一面具有第一凹槽作为进气口,第一凹槽靠近两个导气槽的两端具有两个第一开孔,两个第一开孔分别与两个导气槽靠近底部的一端连通。Wherein, there are two air guide grooves, which are respectively arranged on the outer surfaces of the two opposite side walls of the installation top cover; the side of the bottom away from the support part has a first groove as an air inlet, and the first groove is close to the two sides. There are two first openings at both ends of each air guiding groove, and the two first openings communicate with the ends of the two air guiding grooves near the bottom respectively.
其中,雾化芯包括基体、发热层和两个电极,基体设于支撑部靠近安装顶盖的顶壁的一侧,基体靠近顶壁的表面为雾化面,发热层和两个电极设于雾化面上,两个电极分别连接发热层的相对的两端。Wherein, the atomizing core includes a base body, a heating layer and two electrodes, the base body is set on the side of the support part close to the top wall where the top cover is installed, the surface of the base body close to the top wall is the atomizing surface, the heating layer and the two electrodes are set on the On the atomizing surface, two electrodes are respectively connected to opposite ends of the heating layer.
其中,雾化器还包括两个电极连接件,每个电极连接件的一端与一个电极电连接,另一端设置于安装底座的底部背离支撑部的表面。Wherein, the atomizer further includes two electrode connectors, one end of each electrode connector is electrically connected to an electrode, and the other end is arranged on the surface of the bottom of the installation base away from the supporting part.
其中,底部背离支撑部的表面具有第二凹槽,第二凹槽靠近壳体的一侧具有第二开孔;每个电极连接件的另一端穿过第二开孔设置于第二凹槽内。Wherein, the surface of the bottom away from the support part has a second groove, and the side of the second groove close to the housing has a second opening; the other end of each electrode connector is arranged in the second groove through the second opening Inside.
为了解决上述技术问题,本申请提供的第二个技术方案为:提供一种电子雾化装置,包括电池组件和雾化器,电池组件用于为雾化器供电,其中,雾化器为上述任一项所涉及的雾化器。In order to solve the above technical problems, the second technical solution provided by this application is: provide an electronic atomization device, including a battery assembly and an atomizer, the battery assembly is used to power the atomizer, wherein the atomizer is the above-mentioned Any of the nebulizers involved.
本发明提供的雾化器和电子雾化装置,该雾化器通过在安装座上开设进气孔,将外界大气与雾化腔连通,以使外界大气能通过进气孔流入雾化腔中,并携带雾化腔中生成的气溶胶流出雾化器供用户使用。同时,流入雾化腔中的冷空气会和雾化面生成的热的气溶胶进行热对流,通过使雾化芯的雾化面与进气孔之间具有一定距离h,能增大雾化面附近的涡流区域,减少冷空气与热的气溶胶之间的热对流,从而使冷空气与气溶胶混合后的气流温度降低,流出雾化器的出气口的气溶胶的温度减小,提升了用户的使用体验。In the atomizer and electronic atomization device provided by the present invention, the atomizer connects the outside atmosphere with the atomization chamber by opening an air inlet hole on the mounting base, so that the outside air can flow into the atomization chamber through the air inlet hole , and carry the aerosol generated in the atomization chamber out of the atomizer for the user to use. At the same time, the cold air flowing into the atomization chamber will conduct thermal convection with the hot aerosol generated on the atomization surface, and the atomization can be increased by making a certain distance h between the atomization surface of the atomization core and the air inlet hole. The vortex area near the surface reduces the thermal convection between the cold air and the hot aerosol, so that the temperature of the airflow after the mixing of the cold air and the aerosol is reduced, and the temperature of the aerosol flowing out of the air outlet of the nebulizer is reduced, increasing the temperature of the aerosol. user experience.
附图说明Description of drawings
为了更清楚地说明本申请实施例中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本申请的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其它的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings that need to be used in the description of the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some embodiments of the present application. For those skilled in the art, other drawings can also be obtained based on these drawings without creative effort.
图1为本申请提供的电子雾化装置的一种功能模块框图;Fig. 1 is a block diagram of a functional module of the electronic atomization device provided by the present application;
图2为本申请提供的雾化器第一实施例的一种立体结构示意图;Fig. 2 is a schematic diagram of a three-dimensional structure of the first embodiment of the atomizer provided by the present application;
图3为图2的雾化器的爆炸结构示意图;Fig. 3 is a schematic diagram of the explosion structure of the atomizer in Fig. 2;
图4为图2的雾化器沿A-A向的剖视图;Fig. 4 is a cross-sectional view of the atomizer in Fig. 2 along the direction A-A;
图5为图3中安装顶盖的一个角度的立体结构示意图;Fig. 5 is a three-dimensional structural schematic diagram of an angle of installing the top cover in Fig. 3;
图6为图3中安装顶盖的另一个角度的立体结构示意图;Fig. 6 is a three-dimensional structural schematic diagram of another angle of installing the top cover in Fig. 3;
图7为图3中雾化芯的一种立体结构示意图;Fig. 7 is a schematic diagram of a three-dimensional structure of the atomization core in Fig. 3;
图8为图3中安装座和雾化芯装配后的一种剖视图;Fig. 8 is a cross-sectional view of the assembly seat and atomizing core in Fig. 3;
图9为图2的雾化器沿B-B向的局部剖视图;Fig. 9 is a partial sectional view of the atomizer in Fig. 2 along the B-B direction;
图10为图3中安装座和雾化芯装配后的另一种剖视图;Fig. 10 is another cross-sectional view of the assembled seat and atomizing core in Fig. 3;
图11为图2的雾化器内气体的局部流速图;Fig. 11 is a local flow velocity diagram of the gas in the atomizer of Fig. 2;
图12为图2的雾化器内局部温度分布图;Figure 12 is a diagram of the local temperature distribution in the atomizer of Figure 2;
图13为本申请提供的间距-出气口的气溶胶的温度的曲线图;Fig. 13 is the curve diagram of the temperature of the aerosol of spacing-air outlet provided by the present application;
图14为本申请提供的间距-出气口的气溶胶量的曲线图;Fig. 14 is the curve diagram of the aerosol amount of the spacing-air outlet provided by the present application;
图15为本申请提供的间距-出气口的气溶胶量以及温度的柱状图;Fig. 15 is a histogram of spacing-aerosol amount and temperature at the air outlet provided by the present application;
图16为图3中安装顶盖、雾化芯、第二密封件、第三密封件以及安装底座的一种爆炸结构示意图;Fig. 16 is a schematic diagram of an exploded structure of installing the top cover, the atomizing core, the second seal, the third seal and the installation base in Fig. 3;
图17为图3中安装座与端盖的爆炸结构示意图;Fig. 17 is a schematic diagram of the exploded structure of the mounting seat and the end cover in Fig. 3;
图18为图3中安装顶盖、雾化芯、第二密封件、第三密封件以及安装底座的另一种爆炸结构示意图;Fig. 18 is a schematic diagram of another explosion structure in which the top cover, the atomizing core, the second seal, the third seal and the installation base are installed in Fig. 3;
图19为本申请提供的雾化器第二实施例的局部结构示意图;Fig. 19 is a partial structural schematic diagram of the second embodiment of the atomizer provided by the present application;
图20为第一实验件的结构示意图;Fig. 20 is the structural representation of the first experimental piece;
图21为第二实验件的结构示意图;Fig. 21 is the structural representation of the second experimental piece;
图22为第一实验件出口处的气流温度分布图;Fig. 22 is the airflow temperature distribution diagram at the outlet of the first experimental piece;
图23为第二实验件出口处的气流温度分布图;Fig. 23 is the air flow temperature distribution diagram at the outlet of the second experimental piece;
图24为不同边界层形态对应的局部表面换热系数的变化规律示意图;Figure 24 is a schematic diagram of the change law of the local surface heat transfer coefficient corresponding to different boundary layer forms;
图25为图19的出气通道内的气流的流动路径示意图;Fig. 25 is a schematic diagram of the flow path of the airflow in the outlet channel of Fig. 19;
图26为现有的雾化器中出气通道内速度场分布图;Fig. 26 is a distribution diagram of the velocity field in the outlet channel of the existing atomizer;
图27为本申请提供的雾化器第二实施例中出气通道内速度场分布图;Fig. 27 is a distribution diagram of the velocity field in the air outlet channel in the second embodiment of the atomizer provided by the present application;
图28为图19中凸起的截面为正方形的结构示意图;Fig. 28 is a schematic diagram of the structure in which the raised section in Fig. 19 is a square;
图29为另一实施方式中凸起的截面为圆形的结构示意图;Fig. 29 is a structural schematic diagram of a protrusion with a circular cross-section in another embodiment;
图30为计算得到的不同出气通道长度的吸阻随凸起高度的变化规律图;Fig. 30 is a chart showing the variation law of the suction resistance with the height of the protrusion calculated for different outlet channel lengths;
图31为不同凸起高度对应的出气口的温度分布图;Figure 31 is a temperature distribution diagram of the air outlet corresponding to different protrusion heights;
图32为凸起的截面为正方形的流场计算示意图;Fig. 32 is a schematic diagram for calculation of a flow field with a raised cross-section being a square;
图33为正方形截面凸起的不同高度的换热系数变化规律图;Fig. 33 is a graph showing the variation law of the heat transfer coefficient of different heights of square cross-section bulges;
图34为正方向截面凸起不同的P/H值对应的速度场分布图;Fig. 34 is the distribution diagram of the velocity field corresponding to different P/H values of the bulge in the positive direction section;
图35为换热系数随正方向截面凸起不同的P/H值的变化规律图;Fig. 35 is a graph showing the change law of the heat transfer coefficient with different P/H values of the cross-sectional protrusions in the positive direction;
图36为凸起的截面为圆形的流场计算示意图;Fig. 36 is a schematic diagram for calculation of a flow field with a convex cross-section being circular;
图37为圆形截面凸起的不同高度的换热系数变化规律图;Fig. 37 is a graph showing the variation law of heat transfer coefficients of different heights of circular cross-section bulges;
图38为圆形截面凸起不同的P/H值对应的速度场分布图;Fig. 38 is a distribution diagram of the velocity field corresponding to different P/H values of circular cross-section bulges;
图39为换热系数随圆形截面凸起不同的P/H值的变化规律图;Fig. 39 is a graph showing the variation law of the heat transfer coefficient with different P/H values of circular cross-section protrusions;
图40为本申请提供的雾化器第三实施例的局部结构示意图;Fig. 40 is a partial structural schematic diagram of the third embodiment of the atomizer provided by the present application;
图41为现有的雾化器局部结构示意图;Fig. 41 is a schematic diagram of a partial structure of an existing atomizer;
图42为图41提供的雾化器的出气口的气溶胶温度分布云图;Fig. 42 is a cloud diagram of the aerosol temperature distribution at the air outlet of the atomizer provided in Fig. 41;
图43为图40提供的雾化器的出气口的气溶胶温度分布云图;Figure 43 is a cloud diagram of the aerosol temperature distribution at the air outlet of the atomizer provided in Figure 40;
图44为图40提供的雾化器的出气通道靠近出气口一端的几面流速矢量分布图;Figure 44 is a flow velocity vector distribution diagram on several surfaces of the air outlet channel of the atomizer provided in Figure 40 near the air outlet;
图45为出气口气溶胶最高温度与间隔距离d之间的关系曲线图;Figure 45 is a graph of the relationship between the maximum temperature of the aerosol at the air outlet and the separation distance d;
图46为出气口中心位置A的气溶胶温度与间隔距离d之间的关系曲线图。Fig. 46 is a graph showing the relationship between the aerosol temperature at the center position A of the air outlet and the separation distance d.
具体实施方式Detailed ways
下面将结合本申请实施例中的附图,对本申请实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅是本申请的一部分实施例,而不是全部的实施例。基于本申请中的实施例,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,都属于本申请保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present application with reference to the accompanying drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, not all of them. Based on the embodiments in this application, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of this application.
以下描述中,为了说明而不是为了限定,提出了诸如特定系统结构、接口、技术之类的具体细节,以便透彻理解本申请。In the following description, for purposes of illustration rather than limitation, specific details, such as specific system architectures, interfaces, and techniques, are set forth in order to provide a thorough understanding of the present application.
本申请中的术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”、“第三”的特征可以明示或者隐含地包括至少一个所述特征。本申请的描述中,“多个”的含义是至少两个,例如两个,三个等,除非另有明确具体的限定。本申请实施例中所有方向性指示(诸如上、下、左、右、前、后……)仅用于解释在某一特定姿态(如附图所示)下各部件之间的相对位置关系、运动情况等,如果所述特定姿态发生改变时,则所述方向性指示也相应地随之改变。本申请实施例中的术语“包括”和“具有”以及它们任何变形,意图在于覆盖不排他的包含。例如包含了一系列步骤或单元的过程、方法、系统、产品或设备没有限定于已列出的步骤或单元,而是可选地还包括没有列出的步骤或单元,或可选地还包括对于这些过程、方法、产品或设备固有的其它步骤或组件。The terms "first", "second", and "third" in this application are used for descriptive purposes only, and cannot be understood as indicating or implying relative importance or implicitly specifying the quantity of indicated technical features. Thus, features defined as "first", "second" and "third" may explicitly or implicitly include at least one of said features. In the description of the present application, "plurality" means at least two, such as two, three, etc., unless otherwise specifically defined. All directional indications (such as up, down, left, right, front, back...) in the embodiments of the present application are only used to explain the relative positional relationship between the various components in a certain posture (as shown in the drawings) , sports conditions, etc., if the specific posture changes, the directional indication also changes accordingly. The terms "comprising" and "having" and any variations thereof in the embodiments of the present application are intended to cover non-exclusive inclusion. For example, a process, method, system, product or device comprising a series of steps or units is not limited to the listed steps or units, but optionally also includes unlisted steps or units, or optionally further includes For other steps or components inherent in those processes, methods, products, or devices.
在本文中提及“实施例”意味着,结合实施例描述的特定特征、结构或特性可以包含在本申请的至少一个实施例中。在说明书中的各个位置出现所述短语并不一定均是指相同的实施例,也不是与其它实施例互斥的独立的或备选的实施例。本领域技术人员显式地和隐式地理解的是,本文所描述的实施例可以与其它实施例相结合。Reference herein to an "embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment can be included in at least one embodiment of the present application. The appearances of a phrase in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. It is understood explicitly and implicitly by those skilled in the art that the embodiments described herein can be combined with other embodiments.
下面结合附图和实施例对本申请进行详细的说明。The application will be described in detail below in conjunction with the accompanying drawings and embodiments.
请参阅图1,图1是本申请提供的电子雾化装置的一种功能模块示意图。在本实施例中,提供一种电子雾化装置。该电子雾化装置可用于气溶胶产生基质的雾化。电子雾化装置包括相互电连接的雾化器11和电池组件12。Please refer to FIG. 1 . FIG. 1 is a schematic diagram of a functional module of the electronic atomization device provided in this application. In this embodiment, an electronic atomization device is provided. The electronic atomization device can be used for atomization of aerosol-generating substrates. The electronic atomization device includes an
其中,雾化器11用于存储气溶胶产生基质并雾化气溶胶产生基质以形成可供用户吸食的气溶胶。该雾化器11具体可用于不同的领域,比如,医疗、美容、休闲吸食等;在一具体实施例中,该雾化器11可用于电子气溶胶化装置,用于雾化待雾化基质并产生气溶胶,以供抽吸者抽吸,以下实施例均以此为例;当然,在其他实施例中,该雾化器11也可应用于喷发胶设备,以雾化用于头发定型的喷发胶;或者应用于治疗上下呼吸系统疾病的设备,以雾化医用药品。Wherein, the
雾化器11的具体结构与功能可参见以下任一实施例所涉及的雾化器11的具体结构与功能,且可实现相同或相似的技术效果,在此不再赘述。For the specific structure and function of the
电池组件12包括电池(图未示)和控制器(图未示)。电池用于为雾化器11供电,以使得雾化器11能够雾化气溶胶产生基质形成气溶胶;控制器用于控制雾化器11工作。电池组件12还包括电池支架气流传感器等其他元件。The battery pack 12 includes a battery (not shown) and a controller (not shown). The battery is used to supply power to the
雾化器11与电池组件12可以是一体设置,也可以是可拆卸连接,可以根据具体需要进行设计。The
请参阅图2、图3和图4,图2是本实施例提供的雾化器第一实施例的一种立体结构示意图,图3为图2的雾化器的爆炸结构示意图,图4为图2的雾化器沿A-A向的剖视图。Please refer to Fig. 2, Fig. 3 and Fig. 4, Fig. 2 is a schematic three-dimensional structural diagram of the first embodiment of the atomizer provided in this embodiment, Fig. 3 is a schematic diagram of the exploded structure of the atomizer in Fig. 2, and Fig. 4 is The sectional view of the atomizer along the A-A direction in Fig. 2 .
本实施例中,提供一种雾化器11,该雾化器11包括壳体111、安装座112、雾化芯113和端盖114。In this embodiment, an
其中,壳体111内形成有储液腔1111、出气通道1112和安装腔1113,储液腔1111和出气通道1112分别与安装腔1113连通。Wherein, a
储液腔1111用于储存气溶胶产生基质,壳体111可以由铝、不锈钢等金属制成,也可以由塑料制成,只需能储存气溶胶产生基质,且不与气溶胶产生基质反应即可。储液腔1111的形状、大小和位置不限,可以根据需要进行设计。本实施例中,储液腔1111与出气通道1112并排设置在安装腔1113的同一侧,且储液腔1111环绕出气通道1112设置。The
安装座112设置于安装腔1113中。安装座112内具有雾化腔1123,雾化芯113设置于雾化腔1123中。具体地,在本实施例中,安装座112进一步包括安装顶盖1121和安装底座1122,安装顶盖1121套设在安装底座1122靠近储液腔1111的一侧。请参考图5和图6,图5为图3中安装顶盖的一个角度的立体结构示意图,图6为图3中安装顶盖的另一个角度的立体结构示意图。其中,安装顶盖1121包括相互连接的顶壁1121a和侧壁1121b,安装顶盖1121的侧壁1121b可以是环形侧壁,设于安装顶盖1121的顶壁1121a远离储液腔1111的一侧。安装顶盖1121的顶壁1121a和侧壁1121b可以一体成型。安装顶盖1121的顶壁1121a和安装顶盖1121的侧壁1121b围设形成雾化腔1123。在其他实施例中,还可以是安装顶盖1121和安装底座1122配合形成雾化腔1123,安装座112形成雾化腔1123的方式不限于本申请提到的方式。The
请参阅图3和图4,安装顶盖1121的顶壁1121a上具有出气孔1121c,出气孔1121c的一端与雾化腔1123连通,出气孔1121c的另一端与出气通道1112连通,以使雾化腔1123与出气通道1112连通。雾化芯113雾化后的气溶胶与冷空气混合后流入出气通道1112。进一步地,出气通道1112远离安装腔1113的一端具有出气口1112a,即,出气通道1112的一端的端口为出气口1112a,出气通道1112通过出气口1112a与外界大气连通,以使出气通道1112中的气溶胶能流出雾化器11提供给用户使用。Referring to Fig. 3 and Fig. 4, there is an
请参考图7,图7为图3中雾化芯的一种立体结构示意图;Please refer to Figure 7, Figure 7 is a schematic diagram of a three-dimensional structure of the atomization core in Figure 3;
其中,雾化芯113包括基体1133、发热层1134和两个电极1135。基体1133靠近储液腔1111的一侧具有雾化面1131,即,雾化芯113具有雾化面;发热层1134和两个电极1135设于雾化面1131上。基体1133可以储存和导流气溶胶产生基质。基体1133的材料可以是多孔材料,例如多孔陶瓷,多孔陶瓷可以利用毛细作用力将气溶胶产生基质导引至发热层1134上,发热层1134能对其加热雾化形成气溶胶。发热层1134可以是发热丝、发热网、发热膜、发热线路等,可以根据需要进行选择。两个电极1135设于发热层1134的两端,两个电极1135可以通过连接件与电池组件12电连接,以使两个电极1135通电后,两个电极1135之间的发热层1134通电加热气溶胶产生基质。Wherein, the
在本实施方式中,雾化芯113的雾化面面向安装座112的出气孔1121c,即,雾化面朝上设置。In this embodiment, the atomizing surface of the
请参考图3和图4,雾化器11还包括第一密封件115、第二密封件116和第三密封件117。第一密封件115设于安装顶盖1121靠近储液腔1111的一端,以实现安装顶盖1121与壳体111之间的密封。第二密封件116套设于雾化芯113上,以实现雾化芯113与安装顶盖1121之间的密封。第三密封件117设于安装底座1122与雾化芯113之间,以实现雾化芯113与安装底座1122之间的密封,以及安装顶盖1121与安装底座1122之间的密封。第一密封件115、第二密封件116和第三密封件117的材质可以为任何具有一定柔性且可以耐一定温度的密封材料。本实施例中,第一密封件115、第二密封件116和第三密封件117的材质为硅胶。第一密封件115、第二密封件116和第三密封件117的形状和大小不限,可以根据需要进行设计。Please refer to FIG. 3 and FIG. 4 , the
请参阅图5和图8,图8为图3中安装座和雾化芯装配后的一种剖视图。Please refer to Fig. 5 and Fig. 8, Fig. 8 is a cross-sectional view of the mounting base and the atomizing core in Fig. 3 after assembly.
其中,安装顶盖1121的顶壁1121a上还设有下液孔1121d,下液孔1121d的一端与储液腔1111连通,下液孔1121d的另一端与雾化腔1123连通,以使储液腔1111中的气溶胶产生基质能通过下液孔1121d流至雾化腔1123中。下液孔1121d的数量可以为一个或多个,本实施例中,下液孔1121d的数量为两个,且对称设置于出气孔1121c的相对两侧。Wherein, the
在本实施例中,安装座112中具有导液通道1124。具体地,可以是安装顶盖1121中形成导液通道1124,例如可以是安装顶盖1121的侧壁1121b形成导液通道1124,或者,第二密封件116以及第三密封件117与安装顶盖1121的侧壁1121b配合形成导液通道1124,导液通道1124与下液孔1121d连通,以使导液通道1124与储液腔1111连通。导液通道1124可以将储液腔1111中的气溶胶产生基质导流至雾化芯113的侧壁和/或雾化芯113远离出气孔1121c的一面。在本实施例中,导液通道1124将气溶胶产生基质导流至雾化芯113远离出气孔1121c的一面。具体地,第三密封件117靠近雾化芯113的一端设有导液槽1171,导液槽1171与导液通道1124连通。导液槽1171能将导液通道1124中的气溶胶产生基质导流至雾化芯113远离安装顶盖1121的顶壁1121a的一面,以使雾化芯113能加热雾化气溶胶产生基质产生气溶胶。在其他实施例中,也可以是第二密封件116上设置有导液槽1171,以将导液通道1124中的气溶胶产生基质导流至雾化芯113的侧壁。通过设置导液通道1124和导液槽1171,能使储液腔1111中的气溶胶产生基质能流至雾化芯113的侧面或与雾化面1131相对的一面,以使雾化芯113能吸收气溶胶产生基质并将气溶胶产生基质导流至雾化面1131,以加热形成气溶胶。In this embodiment, the mounting
请参阅图9,图9为图2的雾化器沿B-B向的局部剖视图,图9中的箭头表示雾化器11中的气流路径。Please refer to FIG. 9 . FIG. 9 is a partial cross-sectional view of the atomizer in FIG. 2 along the direction B-B. The arrows in FIG. 9 indicate the airflow path in the
在一种实施例中,安装座112的侧壁1121b与安装腔1113的侧壁1113a配合形成导气通道1125。导气通道1125的一端与雾化器11的进气口1122a连通,以使外界大气能通过雾化器11的进气口1122a进入导气通道1125中;导气通道1125的另一端与雾化腔1123连通,以使导气通道1125中的气流能进入雾化腔1123中。In one embodiment, the
进一步地,安装座112开设有进气孔1125a,可以是安装顶盖1121的侧壁1121b上开设有进气孔1125a,进气孔1125a的一端与导气通道1125连接,另一端与雾化腔1123连通,以使导气通道1125中的气流通过进气孔1125a进入雾化腔1123中。进气孔1125a可以设于雾化面1131朝向出气孔1121c的一侧,例如,进气孔1125a可以设置于雾化面1131与出气孔1121c之间,以使进入雾化腔1123中的气流能携带雾化芯113的雾化面1131产生的气溶胶,经由出气孔1121c流至出气通道1112,最终从出气口1112a流出雾化器11供用户使用。Further, the mounting
具体地,请参考图5和图10,图10为图3中安装座和雾化芯装配后的另一种剖视图。Specifically, please refer to FIG. 5 and FIG. 10 , FIG. 10 is another cross-sectional view of the assembly seat and atomizing core in FIG. 3 .
本实施例中,安装顶盖1121的侧壁1121b的外表面设有导气槽1121e,安装腔1113的侧壁1113a与导气槽1121e的底壁配合形成导气通道1125,导气通道1125靠近安装顶盖1121的顶壁1121a的一侧设有进气孔1125a。在其他实施例中,也可以是安装腔1113的侧壁1113a设置导气槽1121e,安装座112的侧壁1121b与导气槽1121e的底壁配合形成导气通道1125。导气通道1125的形成方式不限于上述提到的方式。In this embodiment, the outer surface of the
在一种实施例中,请参考图5和图6,导气槽1121e的一端为封闭端,靠近安装顶盖1121的顶壁1121a设置;导气槽1121e的另一端为敞口端,延伸至安装顶盖1121的底面1121f。导气槽1121e的形状可以是如本实施例的长方形,也可以是其他的形状。导气槽1121e的数量可以为一个或多个。本实施例中,导气槽1121e的数量为两个,分别设置于安装顶盖1121相对的两个侧壁1121b的外表面上。两个导气槽1121e分别与安装腔1113的侧壁1113a形成两个导气通道1125,两个导气通道1125均与雾化器11的出气口1112a连通。两个导气槽1121e中的每个导气槽1121e靠近安装顶盖1121的顶壁1121a的一端设有进气孔1125a。从出气口1112a进入雾化器11的气流经由两个导气通道1125流至雾化腔1123中。In one embodiment, please refer to FIG. 5 and FIG. 6 , one end of the
本实施例中,导气槽1121e靠近安装顶盖1121的顶壁1121a一端的底面1121g向安装顶盖1121的内部倾斜,同时,进气口1122a设置于导气槽1121e靠近安装顶盖1121的顶壁1121a的端部。导气槽1121e靠近安装顶盖1121的顶壁1121a一端的深度增大,且越靠近安装顶盖1121的顶壁1121a,导气槽1121e的深度越大,以使导气通道1125的气流更容易从导气通道1125导流至出气孔1121c中。在其他实施例中,还可以是导气槽1121e的全部底面1121g向安装顶盖1121的内部倾斜。In this embodiment, the
进气孔1125a的宽度可以小于导气槽1121e的宽度,也可以等于导气槽1121e的宽度。本实施例中,进气孔1125a的宽度等于导气槽1121e的宽度。进气孔1125a的宽度越宽,进气孔1125a能通过的气流量越大,有利于增大从出气口1112a流出的气溶胶量。The width of the
如图10所示,进气孔1125a与雾化芯113的雾化面1131之间具有间距。具体的,雾化面1131与进气孔1125a靠近雾化面1131的底面1125b之间具有间距,且间距的距离为h。As shown in FIG. 10 , there is a distance between the
请参考图11,图11为图2的雾化器内气体的局部流速图,具体的,为图11中所示的为雾化腔1123处的局部流速图。雾化面1131产生的气溶胶会在雾化面1131附近形成涡流区域,其中,涡流区域为虚线框围设的区域。从导气通道1125流入雾化腔1123中的冷空气会和雾化面1131生成的热的气溶胶进行热对流。Please refer to FIG. 11 . FIG. 11 is a partial flow velocity diagram of the gas in the atomizer in FIG. 2 , specifically, the partial flow velocity diagram at the
从图11可以看出,当h=0时,即进气孔1125a与雾化芯113的雾化面1131之间不具有间距时,雾化面1131附近的涡流区域较小,冷空气与热的气溶胶之间的热对流较大,冷空气与气溶胶混合后的气流温度较高,流出雾化器11的出气口1112a的气溶胶的温度较高,导致用户的使用体验较差。It can be seen from Fig. 11 that when h=0, that is, when there is no distance between the
从图11还可以看出,当h>0时,即进气孔1125a与雾化芯113的雾化面1131之间具有间距时,相比于h=0的结构,雾化面1131附近的涡流区域增大,且h的值越大,即间距越大,雾化面1131附近的涡流区域越大。因此,通过在进气孔1125a与雾化芯113的雾化面1131之间设置间距,雾化面1131附近的涡流区域的增大减少了冷空气与热的气溶胶之间的热对流,从而使冷空气与气溶胶混合后的气流温度降低,流出雾化器11的出气口1112a的气溶胶的温度减小,提升了用户的使用体验。It can also be seen from Fig. 11 that when h>0, that is, when there is a distance between the
进一步请参考图12,图12为图2的雾化器内局部温度分布图,具体的,为图12中所示的为雾化腔1123处的局部温度图。从图12可以看出,当h=0时,涡流区域较小,与冷空气对流的气溶胶的温度较高,使得冷空气与气溶胶混合后的气流温度较高,流出雾化器11的出气口1112a的气溶胶的温度较高,导致用户的使用体验较差。当h>0时,雾化面1131附近的涡流区域增大,相比于h=0时,与冷空气对流的气溶胶的温度有所降低,且h的值越大,涡流区域越大,与冷空气对流的气溶胶的温度越低。因此,通过在进气孔1125a与雾化芯113的雾化面1131之间设置间距,能使冷空气与气溶胶混合后的气流温度降低,流出雾化器11的出气口1112a的气溶胶的温度减小,从而提升了用户的使用体验。Further please refer to FIG. 12 . FIG. 12 is a diagram of the local temperature distribution in the atomizer of FIG. 2 , specifically, the diagram of the local temperature at the
具体的,h的值不能过大,当h的值过大时,气溶胶的涡流区域过大,与冷空气对流的气溶胶过少,会使得流出雾化器11的出气口1112a的气溶胶量过小。Specifically, the value of h cannot be too large. When the value of h is too large, the vortex area of the aerosol is too large, and the aerosol convective with the cold air is too little, which will make the aerosol flow out of the
在本实施例中,实验所采用的雾化器11参数如下:出气通道1112的直径是2.5mm,长度29.4mm,雾化芯113上的S型发热层1134的温度初始温度250°,雾化量是3s/9mg,电池组件12对雾化芯113的输入功率是6.5W。当然,我们也可以采用其他具有不同参数的雾化器11,但是仍可以通过实验结果绘制具有相似数学关系的间距-出气口的气溶胶的烟雾量的曲线图。In this embodiment, the parameters of the
可以参考表1、图13以及图14,表1为h分别为0mm、0.1mm、0.2mm、0.3mm、0.4mm、0.5mm、0.6mm、0.7mm时,流出雾化器11的出气口1112a的气溶胶的温度和气溶胶量的实验结果;图13为根据表1的实验结果绘制的间距-出气口1112a的气溶胶的温度曲线图,图14为根据表1的实验结果绘制的间距-出气口的气溶胶量的曲线图。You can refer to Table 1, Figure 13 and Figure 14. Table 1 shows when h is 0mm, 0.1mm, 0.2mm, 0.3mm, 0.4mm, 0.5mm, 0.6mm, and 0.7mm respectively, the
表1Table 1
从实验结果可以看出,当h=0时,流出雾化器11的出气口1112a的气溶胶量较大,但雾化器11的出气口1112a的气溶胶的温度较高,导致用户的体验较差。当h>0时,流出雾化器11的出气口1112a的气溶胶的温度降低,且h越大,流出雾化器11的出气口1112a的气溶胶的温度明显降低,但流出雾化器11的出气口1112a的气溶胶量随着h的增大呈降低的趋势。当h=0.7时,流出雾化器11的出气口1112a的气溶胶量降低至7.19mg/puff。It can be seen from the experimental results that when h=0, the amount of aerosol flowing out of the
因此,可以设置雾化面1131与进气孔1125a之间相隔一定距离h,例如,针对以上实验的所用的雾化器,对应h的范围为0mm<h≤0.7mm。h的值可以为0.1mm、0.2mm、0.3mm、0.4mm、0.5mm、0.6mm、0.7mm等。优选地,0.2mm≤h≤0.5mm。通过设置雾化面1131与进气孔1125a之间的距离h以使得出气口1112a的气溶胶的温度降低,能使雾化面1131与进气孔1125a靠近雾化面1131的底面1125b之间的间距设置在合适的范围,使得流出雾化器11的出气口1112a的气溶胶的温度减小的同时,保证流出雾化器11的出气口1112a的气溶胶的烟雾量不会过少,有利于提升用户的使用体验。Therefore, a certain distance h can be set between the
在本实施例中,发明人还尝试通过增加出气通道1112的长度来降低出气口1112a的气溶胶的温度,实验表明:出气通道1112的长度在29.4mm时,发现出气口1112a的气溶胶的温度是93.16°;出气通道1112的长度增长13mm,达到42.4mm时,出气口1112a的气溶胶的温度是87°。虽然温度降低了6.17°,但出气通道1112的长度增长超过50%,这是产品设计所不可接受的,因此,通过设置雾化面1131与进气孔1125a之间相隔一定距离h的技术方案具有明显的性能和效果提高。可以参考图15,图15为h分别为0mm和0.4mm时,流出雾化器11的出气口1112a的气溶胶的温度和气溶胶量的实验结果的柱状图。从图15中可以看出,h=0mm时,出气口1112a的气溶胶温度为102.7℃,出气口1112a的气溶胶量为7.54mg/puff;h=0.4mm时,出气口1112a的气溶胶温度为86.4℃,出气口1112a的气溶胶量为7.33mg/puff;h=0.4mm时,流出雾化器11的出气口1112a的气溶胶的温度大大减小,且流出雾化器11的出气口1112a的气溶胶量不会过小。In this embodiment, the inventor also tried to reduce the temperature of the aerosol at the
在一种实施例中,如图16所示,图16为图3中安装顶盖、雾化芯、第二密封件、第三密封件以及安装底座的一种爆炸结构示意图。In one embodiment, as shown in FIG. 16 , FIG. 16 is a schematic diagram of an exploded structure of installing the top cover, the atomizing core, the second seal, the third seal and the installation base in FIG. 3 .
其中,安装底座1122包括底部1122b和支撑部1122c,安装顶盖1121套设于支撑部1122c上并与底部1122b抵接,支撑部1122c设于雾化腔1123中,雾化芯113设于支撑部1122c靠近安装顶盖1121的顶壁的一侧。通过调整支撑部1122c的高度,可以调节雾化芯113的位置,进而调节进气孔1125a与雾化芯113的雾化面1131之间距离h的大小。Wherein, the
在一种实施例中,如图2和图17所示,图17为图3中安装座与端盖的爆炸结构示意图。In one embodiment, as shown in FIG. 2 and FIG. 17 , FIG. 17 is a schematic diagram of the exploded structure of the mounting seat and the end cover in FIG. 3 .
其中,端盖114封盖壳体111远离出气口1112a的一端,例如,端盖114可以套设在壳体111远离出气口1112a的一端,壳体111和端盖114可拆卸连接。Wherein, the
进一步地,安装底座1122背离安装顶盖1121的一侧具有进气口1122a,端盖114上设有通孔1141,通孔1141与外接大气连通,且进气口1122a与通孔1141连通,以使外界大气能进入进气口1122a。Further, the side of the
本实施例中,安装底座1122的底部1122b背离支撑部1122c的一面具有第一凹槽1122d,第一凹槽1122d作为进气孔1125a与通孔1141连通。第一凹槽1122d靠近导气槽1121e的一端具有贯穿安装底座1122的底部1122b的第一开孔1122e。第一开孔1122e可以为通孔或位于底部1122b边缘的缺口。第一开孔1122e将第一凹槽1122d与导气槽1121e靠近底部1122b的一端连通,以使气流能从第一凹槽1122d流入导气槽1121e中。In this embodiment, the bottom 1122b of the mounting
第一开孔1122e的数量可以与导气槽1121e的数量相同。本实施例中,第一开孔1122e的数量为两个,两个第一开孔1122e与两个导气槽1121e相对设置,两个第一开孔1122e分别将第一凹槽1122d与两个导气槽1121e连通。The number of the
在一种实施例中,如图17和图18所示,图18为图3中安装顶盖、雾化芯、第二密封件、第三密封件以及安装底座的另一种爆炸结构示意图。In one embodiment, as shown in FIG. 17 and FIG. 18 , FIG. 18 is a schematic diagram of another exploded structure for installing the top cover, the atomizing core, the second seal, the third seal and the installation base in FIG. 3 .
其中,雾化器11还包括两个电极连接件118,每个电极连接件118的一端与一个电极1135电连接;另一端设置于安装底座1122的底部1122b背离支撑部1122c的表面,且通过端盖114的通孔1141暴露,以使电极连接件118能与电池组件12电连接,从而电池组件12能为雾化芯113供电。在一个实施例中,两个电极连接件118分别设置于所述雾化芯113的两侧,且分别对应电极1135位置设置。即,两个电极连接件118中心旋转对称设置。Wherein, the
进一步地,底部1122b背离支撑部1122c的表面设有两个第二凹槽1122f,分别用于容置两个电极连接件118远离雾化芯113的一端。具体的,第二凹槽1122f靠近壳体111的一侧具有第二开孔1122g,第二开孔1122g可以是底部1122b边缘设置的缺口,每个电极连接件118远离雾化芯113的一端穿过相应的第二开孔1122g设置于相应的第二凹槽1122f中。电极连接件118的设置方式不限于本申请提供的方式,也可以是其他的设置方式,只要能将雾化芯113的两个电极1135与电池组件12电连接即可。Further, two
请参考图19,图19为本申请提供的雾化器第二实施例的局部结构示意图。Please refer to FIG. 19 . FIG. 19 is a partial structural schematic view of the second embodiment of the atomizer provided by the present application.
在雾化器11第二实施例中,雾化器11的结构与雾化器11第一实施例的结构基本相同,不同之处在于:雾化器11包括降温结构119,降温结构119设置于出气通道1112内。其中,降温结构119被配置为降低流经出气通道1112的气溶胶的温度。In the second embodiment of the
通过在出气通道1112内设置降温结构119,以对出气通道1112壁面附近的气溶胶的流动状态进行干涉,使得出气通道1112的壁面的换热系数增大,进而使得流出雾化器11的出气口1112a的气溶胶的温度减小,利于提升用户的使用体验。By setting the
可以理解,在设置降温结构119来降低出气口1112a的气溶胶的温度的前提下,雾化芯113的雾化面与进气孔1125a之间的距离h做如上设置(雾化器11第一实施例中具体介绍的内容:雾化芯113的雾化面与进气孔1125a之间的距离h)为可选的。相比于只在出气通道1112内设置降温结构119,在出气通道1112内设置降温结构119的基础上,雾化芯113的雾化面与进气孔1125a之间的距离h做如上设置,可以更好的降低出气口1112a的气溶胶的温度,采用那种方式来降低出气口1112a的气溶胶的温度可以根据具体需要进行设计。It can be understood that on the premise that the
降温结构119一方面可以吸收气溶胶的热量,另一方面可以对出气通道1112近壁面处的流场实现干扰,提高气溶胶与出气通道1112的壁面之间的热交换效率。在一具体实施方式中,降温结构119为螺旋件(图未示),螺旋件设置于出气通道1112内,且该螺旋件与出气通道1112的内壁面间隔设置,且能够对出气通道1112近壁面处的流场实现干扰,提高气溶胶与出气通道1112的壁面之间的热交换效率,以降低出气口1112a的气溶胶的温度。其中,螺旋件可通过固定结构固定于出气通道1112内。优选,螺旋件的材质为金属弹簧,制作工艺简单,且金属材质较其他材质具有更好的吸热效果,利于进一步降低出气口1112a的气溶胶的温度。On the one hand, the
在一具体实施方式中,降温结构119为设置于出气通道1112的内壁面的凸起1191。可选的,凸起1191与出气通道1112的侧壁一体成型;即,类似于波节管结构。可选的,降温结构119为独立元件,在出气通道1112的内设置有螺旋件(图未示),螺旋件的外壁面贴合出气通道1112的内壁面设置,以使螺旋件作为出气通道1112的内壁面的凸起1191。出气通道1112的内壁面为光滑表面,螺旋件通过螺旋件与出气通道1112之间的摩擦力实现固定;或,出气通道1112的内壁面设置有与螺旋件配合的螺旋槽以实现螺旋件的固定,且螺旋件的线径大于螺旋槽的深度,以形成凸起1191。例如,组装时将螺旋件旋转插入出气通道1112的螺旋槽内。优选,螺旋件为金属弹簧,金属材质较其他材质具有更好的吸热和导热效果,利于进一步降低出气口1112a的气溶胶的温度。在一个实施例中,金属弹簧的线径为0.2mm-0.3mm,金属弹簧的线径为形成的凸起1191的高度,金属弹簧的匝间距为相邻的凸起1191之间的距离;其中,金属弹簧的线径为制作金属弹簧的金属丝的直径。示例性的,当金属弹簧的线径为0.2mm-0.3mm,金属弹簧的直径为3mm,出气通道1112的长度为28mm时,可以实现较好的降温效果。In a specific embodiment, the
可以理解,当凸起1191与出气通道1112的侧壁一体成型时,凸起1191的尺寸设计、以及相邻的凸起1191之间的尺寸设计可参考后续介绍的凸起1191的高度、相邻的凸起1191的中心之间的距离与凸起1191的高度的比值。当通过螺旋件形成凸起1191时,对螺旋件的选择也可参考后续介绍的凸起1191的高度、相邻的凸起1191的中心之间的距离与凸起1191的高度的比值。It can be understood that when the
请参阅图20-图23,图20为第一实验件的结构示意图,图21为第二实验件的结构示意图,图22为第一实验件出口处的气流温度分布图,图23为第二实验件出口处的气流温度分布图。Please refer to Fig. 20-Fig. 23, Fig. 20 is the structural schematic diagram of the first experimental piece, Fig. 21 is the structural schematic diagram of the second experimental piece, Fig. 22 is the airflow temperature distribution diagram at the outlet of the first experimental piece, Fig. 23 is the second experimental piece Airflow temperature distribution at the outlet of the test piece.
图20所示的第一实验件为内壁面光滑的圆管30,圆管30的长度为50mm。圆管30的左侧的端口为入口,圆管30的右侧的端口为出口,气流从入口流向出口。The first test piece shown in FIG. 20 is a
图21所示的第二实验件为内壁面上设置有凸起31的圆管30,圆管30的长度为50mm,凸起31的高度为0.5mm;其中,沿着凸起31的高度方向,凸起31的截面形状为方形。凸起31沿着圆管30的内表面设置一周。圆管30的左侧的端口为入口,圆管30的右侧的端口为出口,气流从入口流向出口。The second experimental piece shown in Fig. 21 is the
使用同样的气体,以相同的流速分别流经第一实验件和第二实验件,得到第一实验件出口处的气流温度(如图22所示)和第二实验件出口处的气流温度(如图23所示)。对于第一实验件出口处的气流温度,从管壁到中心的温度逐渐升高,即,出口处的气流最高温度在中心区域;由图22可知,第一实验件出口处的气流最高温度为84.6℃。对于第二实验件出口处的气流温度,从管壁到中心的温度逐渐升高,即,出口处的气流最高温度在中心区域;由图23可知,第二实验件出口处的气流最高温度为73.3℃。可见,在圆管30的内壁面上设置凸起31使出口处的最高温度降低了13.4%,降温效果明显。也就是说,在出气通道1112的内壁面上设置凸起1191(即,降温结构119),可以明显降低出气口1112a处气溶胶的温度,利于提高用户的使用体验感。其中,进行实验的气体为气溶胶或其特性与气溶胶相似。Use the same gas to flow through the first experimental piece and the second experimental piece respectively at the same flow rate to obtain the airflow temperature at the outlet of the first experimental piece (as shown in Figure 22) and the airflow temperature at the outlet of the second experimental piece ( as shown in Figure 23). For the airflow temperature at the outlet of the first experimental piece, the temperature from the tube wall to the center gradually increases, that is, the highest temperature of the airflow at the outlet is in the central area; as can be seen from Figure 22, the highest airflow temperature at the outlet of the first experimental piece is 84.6°C. For the airflow temperature at the outlet of the second experimental piece, the temperature from the pipe wall to the center gradually increases, that is, the highest temperature of the airflow at the outlet is in the central region; as can be seen from Figure 23, the highest temperature of the airflow at the outlet of the second experimental piece is 73.3°C. It can be seen that the provision of
可以理解,将第二实验件中的凸起31沿着圆管30的内表面周向间隔设置,同样可以明显降低出气口处气溶胶的温度。It can be understood that arranging the
请参考图24和图25,图24为不同边界层形态对应的局部表面换热系数的变化规律示意图,图25为图19的出气通道内的气流的流动路径示意图。Please refer to FIG. 24 and FIG. 25 . FIG. 24 is a schematic diagram of the change law of the local surface heat transfer coefficient corresponding to different boundary layer shapes, and FIG. 25 is a schematic diagram of the flow path of the airflow in the outlet channel of FIG. 19 .
对于在出气通道1112内设置凸起1191(即,降温结构119)来降低出气口1112a处气溶胶的温度的原理如下:The principle of setting the protrusion 1191 (that is, the cooling structure 119) in the
在图24中,横轴x表示流体与管道入口之间的距离,纵轴hx表示换热系数。流体从管道的入口进入管道,流体进入管道后边界层的形态分为层流边界层、过渡区、湍流边界层,湍流边界层的换热系数要高于层流边界层的换热系数。对于层流边界层形态,层流边界层内的热量传递主要通过热传导方式进行,而空气的热传导系数小,因此换热系数整体上处于较低的水平;且在层流边界层中,随着层流边界层厚度增加换热系数减小。当边界层形态由过渡区转变为充分发展的湍流边界层形态后,湍流边界层内同时存在热传导和热对流两种形式的热量传递,因此局部表面换热系数可以一直维持在较高的数值。由于流体在流动的过程中,会有部分粘附在管道的管壁上,在湍流边界层存在有层流底层。In Fig. 24, the horizontal axis x represents the distance between the fluid and the inlet of the pipe, and the vertical axis h x represents the heat transfer coefficient. The fluid enters the pipeline from the inlet of the pipeline, and the shape of the boundary layer after the fluid enters the pipeline is divided into laminar boundary layer, transition zone, and turbulent boundary layer. The heat transfer coefficient of the turbulent boundary layer is higher than that of the laminar boundary layer. For the laminar boundary layer shape, the heat transfer in the laminar boundary layer is mainly through heat conduction, and the heat transfer coefficient of air is small, so the heat transfer coefficient is at a low level as a whole; and in the laminar boundary layer, with The heat transfer coefficient decreases as the thickness of the laminar boundary layer increases. When the boundary layer shape changes from the transition zone to the fully developed turbulent boundary layer shape, there are two forms of heat transfer in the turbulent boundary layer, heat conduction and heat convection, so the local surface heat transfer coefficient can always maintain a high value. Since the fluid will partially adhere to the pipe wall during the flow, there is a laminar bottom layer in the turbulent boundary layer.
在出气通道1112的内壁面为光滑的前提下,通常气溶胶在出气通道1112内的流速不大,其近壁面的流动边界层接近层流的形态;在出气通道1112的内壁面增加凸起1191结构后,相当于人为的对近壁面流动边界层进行干扰,使其从规则的层流形态向湍流形态转变,如图25所示,提升了出气通道1112的侧壁与出气通道1112内的气溶胶的换热系数。换热系数提升后有助于气溶胶与出气通道1112的侧壁换热,更多的热量被出气通道1112的侧壁吸收,从而达到降低出气口1112a处气溶胶的温度的目的。Under the premise that the inner wall surface of the
请参考图26和图27,图26为现有的雾化器中出气通道内速度场分布图,图27为本申请提供的雾化器第二实施例中出气通道内速度场分布图。Please refer to Fig. 26 and Fig. 27, Fig. 26 is a distribution diagram of the velocity field in the outlet channel of the conventional atomizer, and Fig. 27 is a distribution diagram of the velocity field in the outlet channel of the atomizer provided in the second embodiment of the present application.
通常出气通道1112内的流场可分为近壁面区和主流区,气溶胶与出气通道1112的侧壁的换热主要发生在近壁面区。参考图26和图27可知,在出气通道1112的内壁面上设置凸起1191(即,降温结构119),对近壁面区的气溶胶产生作用较大,使层流边界层状态转变成湍流边界层状态,提升气溶胶与出气通道1112的侧壁之间的换热效率,而主流区中的气溶胶影响较小。由图26和图27可知,近壁面区的流速小于3ms^-1,近壁面区的流速均是越靠近主流区部分的流速越快,主流区的流速大于3ms^-1。也就是说,在出气通道1112的内壁面上设置凸起1191(即,降温结构119),对出气通道1112的近壁面局部流场产生作用,对于主流区及其他区域的流场影响较小,不会影响用户的气溶胶吸入量。其中,流场为速度场。Generally, the flow field in the
在具体实施方式中,凸起1191的高度为0.3mm-0.6mm;和/或,相邻的凸起1191的中心之间的距离与凸起1191的高度的比值为1:20-1:7。通过对凸起1191进行如上尺寸设置,对降低出气口1112a处气溶胶的温度的效果较好。沿着凸起1191的高度方向,凸起1191的截面形状可以是圆形、正方形、长方形、三角形等,具体根据需要进行设计。下面以凸起1191的截面为正方形和圆形为例,对凸起1191的高度、凸起1191的高度与相邻的凸起1191的中心之间的距离的比值进行详细介绍。In a specific embodiment, the height of the
请参考图28和图29,图28为图19中凸起的截面为正方形的结构示意图,图29为另一实施方式中凸起的截面为圆形的结构示意图。Please refer to FIG. 28 and FIG. 29 , FIG. 28 is a schematic structural diagram of a protrusion with a square cross section in FIG. 19 , and FIG. 29 is a structural schematic diagram of a protrusion with a circular cross section in another embodiment.
在图28中,沿着凸起1191的高度方向,凸起1191的截面为正方形。在图29中,沿着凸起1191的高度方向,凸起1191的截面为圆形。图28和图29中,凸起1191的高度均用“H”表示,相邻的凸起1191的中心之间的距离均用“P”表示。In FIG. 28 , along the height direction of the
凸起1191的高度对于换热效率、雾化器11吸阻影响较大,因此可以综合考虑出气口1112a处气溶胶的降温效果、雾化器11的吸阻来对凸起1191的高度进行设计。相邻的凸起1191中心之间的距离影响着出气通道1112的近壁面处的流场,出气通道1112的近壁面处的流场还与凸起1191的高度相关,因此可通过流场分析及凸起1191的高度来对相邻的凸起1191中心之间的距离进行设计。The height of the
可以理解,凸起1191尺寸(例如,沿同一方向凸起1191的截面积)相差不大时,截面形状对于吸阻的影响较小。根据雾化器11设计标准的吸阻要求,将凸起1191额外导致的吸阻上限设定为100Pa。以凸起1191的截面为正方形为例,对凸起1191的高度、出气通道1112的长度与雾化器11吸阻的关系进行研究,并由此确定凸起1191的高度最佳数值。It can be understood that when the size of the protrusions 1191 (for example, the cross-sectional area of the
研究结果如图30和图31所示,图30为计算得到的不同出气通道长度的吸阻随凸起高度的变化规律图,图31为不同凸起高度对应的出气口的温度分布图。The research results are shown in Fig. 30 and Fig. 31. Fig. 30 is the calculated change law of the suction resistance with the protrusion height for different air outlet channel lengths. Fig. 31 is the temperature distribution diagram of the air outlet corresponding to different protrusion heights.
由图30可知,出气通道1112的吸阻随凸起1191高度、出气通道1112的长度的增大而增大;出气通道1112的长度越小,凸起1191高度可取的上限越大。例如,当出气通道1112的长度为20mm时,凸起1191高度可取0.6mm,甚至可取0.62mm;因此,优选凸起1191的高度的上限为0.6mm。其中,出气通道1112的长度在图30中用“L”表示。其中,实验条件:出气通道1112直径为3mm。It can be seen from Fig. 30 that the suction resistance of the
由图31可知,出气口1112a的气溶胶的最高温度在中心区域,在出气通道1112的长度相同的前提下,不设置凸起1191时,出气口1112a的气溶胶的最高温度为84.6℃;凸起1191的高度为0.1mm时,出气口1112a的气溶胶的最高温度为83.8℃,相比于不设置凸起1191,温度降低了0.9%;凸起1191的高度为0.2mm时,出气口1112a的气溶胶的最高温度为81.7℃,相比于不设置凸起1191,温度降低了3.4%;凸起1191的高度为0.3mm时,出气口1112a的气溶胶的最高温度为78.5℃,相比于不设置凸起1191,温度降低了7.2%;凸起1191的高度为0.4mm时,出气口1112a的气溶胶的最高温度为75.3℃,相比于不设置凸起1191,温度降低了11%;凸起1191的高度为0.5mm时,出气口1112a的气溶胶的最高温度为73.3℃,相比于不设置凸起1191,温度降低了13.4%。即,凸起1191的高度越高,出气口1112a的气溶胶的最高温度越低,降温效果越好;优选凸起1191的高度大于等于0.3mm。其中,实验条件:出气通道1112直径为3mm,气溶胶进出气通道1112的温度为100℃。It can be seen from Figure 31 that the highest temperature of the aerosol at the air outlet 1112a is in the central area, and on the premise that the length of the air outlet channel 1112 is the same, when the protrusion 1191 is not provided, the highest temperature of the aerosol at the air outlet 1112a is 84.6°C; When the height of the protrusion 1191 is 0.1mm, the maximum temperature of the aerosol at the air outlet 1112a is 83.8°C, which is 0.9% lower than that without the protrusion 1191; The maximum temperature of the aerosol at the air outlet 1112a is 81.7°C, which is 3.4% lower than that without the protrusion 1191; when the height of the protrusion 1191 is 0.3mm, the maximum temperature of the aerosol at the air outlet 1112a is 78.5°C, compared with Without the protrusion 1191, the temperature is reduced by 7.2%; when the height of the protrusion 1191 is 0.4mm, the maximum temperature of the aerosol at the air outlet 1112a is 75.3°C, which is 11% lower than that without the protrusion 1191 When the height of the protrusion 1191 is 0.5mm, the maximum temperature of the aerosol at the air outlet 1112a is 73.3°C, which is 13.4% lower than that without the protrusion 1191. That is, the higher the height of the
请参考图32,图32为凸起的截面为正方形的流场计算示意图。Please refer to FIG. 32 . FIG. 32 is a schematic diagram for calculation of a flow field with a convex section having a square shape.
参考图32,在一直径为1.5mm的圆管30中设置凸起31,沿着凸起31的高度方向,凸起31的截面为正方形,气体以2.6m/s的速度流过圆管30。其中,选用的气体的特性与气溶胶特性相似;气体的流速为出气通道1112中气溶胶的真实流速。凸起31的高度用“H”表示,相邻的凸起31中心之间的距离用“P”表示。Referring to Fig. 32, a
取不同的凸起31高度,以图32的结构示意图进行实验,研究换热系数随相邻的凸起31中心之间的距离与凸起31的高度的比值(P/H)的变化规律。研究结果如图33所示,图33为正方形截面凸起的不同高度的换热系数变化规律图。由图33可知,不同凸起31高度H,换热系数的变化规律基本一致。因此,凸起31的高度H仅影响换热系数的数值,换热系数的变化规律主要受相邻的凸起31中心之间的距离与凸起31高度的比值(P/H)的影响。Taking different heights of
以凸起31截面为正方形,凸起31高度H为0.2mm为例,对不同的P/H值对应的速度场分布继续进行研究,研究结果如图34和图35所示,图34为正方向截面凸起不同的P/H值对应的速度场分布图,图35为换热系数随正方向截面凸起不同的P/H值的变化规律图。Taking the cross-section of the
由图34可知,无论P/H值是多少,越远离壁面处的流速越快。从图可见,P/H数值过小,存在较大的低速区域;随着数值增大低速区域逐渐减小,等于17时刚好发生再附着,此时换热效果最好;继续增大数值后(P/H=25),低速区域减少,但是重新发展出新的层流边界层,影响换热效率。It can be seen from Figure 34 that no matter what the P/H value is, the farther away from the wall the faster the flow velocity is. It can be seen from the figure that the P/H value is too small, and there is a large low-velocity area; as the value increases, the low-velocity area gradually decreases, and when it is equal to 17, reattachment occurs, and the heat transfer effect is the best at this time; after continuing to increase the value (P/H=25), the low-velocity area is reduced, but a new laminar boundary layer is redeveloped, which affects the heat transfer efficiency.
可见,当P/H值过小时(例如,P/H为5),相邻的凸起31之间间隔区域的流场未被充分干扰,换热效率提升效果微弱;当P/H值为17时,气流在相邻的凸起31之间的间距面上发生了再附着,再附着区域边界层厚度薄、换热效率高;当P/H数值过大时(例如,P/H为25),气流发生再附着后重新发展出层流边界层,换热效率降低。因此,过小或过大的P/H值均不利于气溶胶与出气通道1112的壁面换热。It can be seen that when the P/H value is too small (for example, P/H is 5), the flow field in the interval area between
由图35可知,对于正方形截面的凸起31,相邻的凸起31中心之间的距离与凸起31高度的比值(P/H)为10-20时降温效果最好。因此,当设置于出气通道1112内壁面上的凸起1191的截面为正方形时,相邻的凸起1191中心之间的距离与凸起1191高度的比值为10-20,可选的,为13-17。It can be seen from FIG. 35 that for the
请参考图36,图36为凸起的截面为圆形的流场计算示意图。Please refer to FIG. 36 . FIG. 36 is a schematic diagram for calculation of a flow field with a circular section of the protrusion.
参考图36,在一直径为1.5mm的圆管30中设置凸起31,沿着凸起31的高度方向,凸起31的截面为圆形,气体以2.6m/s的速度流过圆管30。其中,选用的气体的特性与气溶胶特性相似;气体的流速为出气通道1112中气溶胶的真实流速。凸起31的直径用“H”表示,相邻的凸起31中心之间的距离用“P”表示。由于凸起31的截面为圆形,凸起31的高度与凸起31的直径相同。Referring to Figure 36, a
取不同的凸起31高度,以图36的结构示意图进行实验,研究换热系数随相邻的凸起31中心之间的距离与凸起31的高度的比值(P/H)的变化规律。研究结果如图37所示,图37为圆形截面凸起的不同高度的换热系数变化规律图。由图37可知,不同凸起31高度H,换热系数的变化规律基本一致。因此,凸起31的高度H仅影响换热系数的数值,换热系数的变化规律主要受相邻的凸起31中心之间的距离与凸起31高度的比值(P/H)的影响。Taking different heights of
以凸起31截面为圆形,凸起31高度H为0.2mm为例,对不同的P/H值对应的速度场分布继续进行研究,研究结果如图38和图39所示,图38为圆形截面凸起不同的P/H值对应的速度场分布图,图39为换热系数随圆形截面凸起不同的P/H值的变化规律图。Taking the cross-section of the
由图38可知,无论P/H值是多少,越远离壁面处的流速越快。从图可见,P/H数值过小,存在较大的低速区域;随着数值增大低速区域逐渐减小,等于14时刚好发生再附着,此时换热效果最好;继续增大数值后(P/H=20),低速区域减少,但是重新发展出新的层流边界层,影响换热效率。It can be seen from Figure 38 that no matter what the P/H value is, the farther away from the wall the faster the flow velocity is. It can be seen from the figure that the P/H value is too small, and there is a large low-speed area; as the value increases, the low-speed area gradually decreases, and when it is equal to 14, reattachment occurs, and the heat transfer effect is the best at this time; after continuing to increase the value (P/H=20), the low-velocity area is reduced, but a new laminar boundary layer is redeveloped, which affects the heat transfer efficiency.
可见,当P/H值过小时,相邻的凸起31之间间隔区域的流场未被充分干扰,换热效率提升效果微弱;当P/H值为14时,气流在相邻的凸起31之间的间距面上发生了再附着,再附着区域边界层厚度薄、换热效率高;当P/H数值过大时,气流发生再附着后重新发展出层流边界层,换热效率降低。因此,过小或过大的P/H值均不利于气溶胶与出气通道1112的壁面换热。It can be seen that when the P/H value is too small, the flow field in the interval area between
由图39可知,对于圆形截面的凸起31,相邻的凸起31中心之间的距离与凸起31高度的比值(P/H)为7-20时降温效果最好。因此,当设置于出气通道1112内壁面上的凸起1191的截面为圆形时,相邻的凸起1191中心之间的距离与凸起1191高度的比值为7-20,可选的,为11-16。It can be seen from FIG. 39 that for the
因此,对于凸起1191的截面为正方形或圆形时,凸起1191的高度、相邻的凸起1191的中心之间的距离与凸起1191的高度的比值的最佳设计如表2所示。Therefore, when the section of the
表2Table 2
也就是说,无论凸起1191的截面为正方形还是圆形,当出气通道1112的长度小于等于20mm时,凸起1191的高度为0.6mm-0.7mm;当出气通道1112的长度大于20mm且小于等于30mm时,凸起1191的高度为0.5mm-0.6mm;当出气通道1112的长度大于30mm且小于等于40mm时,凸起1191的高度为0.4mm-0.5mm;当出气通道的长度大于40mm且小于等于50mm时,凸起1191的高度为0.35mm-0.45mm;当出气通道的长度大于50mm时,凸起1191的高度为0.3mm-0.4mm。其中,当出气通道1112的长度小于20mm时,可选的,凸起1191的高度为0.6mm。当出气通道的长度大于40mm且小于50mm时,可选的,凸起1191的高度为0.4mm。That is to say, regardless of whether the section of the
当凸起1191的截面为正方形,相邻的凸起1191的中心之间的距离与凸起1191的高度的比值为10-20。当凸起1191的截面为圆形,相邻的凸起1191中心之间的距离与凸起1191的高度的比值为7-20。可以理解,当凸起1191的截面为正方形或圆形,凸起1191的宽度与凸起1191的高度相同,对相邻的凸起1191中心之间的距离以及相邻的凸起1191中心之间的距离与凸起1191的高度的比值进行设计,也就考虑了凸起191的宽度对出气口1112a处气溶胶的温度的影响。When the cross-section of the
请参阅图40,图40为本申请提供的雾化器第三实施例的局部结构示意图。Please refer to FIG. 40 . FIG. 40 is a schematic diagram of the partial structure of the third embodiment of the atomizer provided by the present application.
在雾化器11第三实施例中,雾化器11的结构与雾化器11第一实施例的结构基本相同,不同之处在于:雾化器11的出气通道1112在远离雾化芯113的一端先分流成多个子出气通道1112b再次汇聚在一起。In the third embodiment of the
用户在通过出气口1112a抽吸时,舌头位于或对应于出气口1112a的中心位置A,而舌头是感知温度的关键,通过降低出气口1112a的中心位置A的温度即可降低用户感知到的气溶胶的温度,进而提升用户的使用体验。本申请发明人研究发现,如果出气通道1112采用直通结构,出气口1112a中心位置A流出的气溶胶比周围流出的气溶胶的温度高(具体可参见图42的测试结果)。本申请通过使出气通道1112在远离雾化芯113的一端先分流成多个子出气通道1112b再次汇聚在一起的方式来降低出气口1112a的中心位置A的气溶胶温度。也就是说,雾化芯113雾化好的气溶胶在出气通道1112远离雾化芯113的一端先分流流入多个子出气通道1112b再汇聚在一起从出气口1112a流出,分流的过程中对气溶胶进行降温,相对于直通的出气通道1112,用户通过出气口1112a抽吸气溶胶时感知到的温度明显降低,利于提升用户的使用体验。其中,多个子出气通道1112b的个数可以根据需要进行设计。When the user sucks through the
在一实施方式中,在出气通道1112内设置隔板1112c,以将出气通道1112远离雾化芯113的一端分割成两个子出气通道1112b,以使出气通道1112先分流;其中,隔板1112c的延伸方向与出气通道1112的延伸方向相同。隔板1112c靠近出气口1112a的一端的端面与出气口1112a之间间隔设置,以使出气通道1112在分流后又汇聚在一起(如图40所示)。也就是说,出气通道1112包括第一部分、第二部分和第三部分,出气通道1112的入口即第一部分的入口,第三部分的出口即出气口1112a;第一部分和第三部分均为直通管,隔板1112c设置于第二部分,使得第二部分相对于第一部分和第三部分具有明显的分流效果,以实现分流降温。可以理解,多个子出气通道1112b的个数可以根据需要进行设计,隔板1112c的结构可以根据子出气通道1112b的个数进行设计。In one embodiment, a
其中,隔板1112c可以是与出气通道1112一体成型,也可以是与出气通道1112通过卡接等方式固定在一起,具体根据需要进行设计。隔板1112c的厚度根据需要进行设计,能够使出气通道1112远离雾化芯113的一端分割成两个子出气通道1112b,并能够对流经子出气通道1112b的气溶胶降温即可。可以理解,气溶胶与子出气通道1112b内的空气进行混合降温,流经子出气通道1112b的气溶胶被子出气通道1112b的腔壁吸热,从而降低出气口1112a的气溶胶温度。进一步,由于两个子出气通道1112b内的气溶胶在出气口1112a的中心位置A汇聚混合,使得中心位置A流出的气溶胶的温度进一步被降低(具体可参见图44的测试结果)。Wherein, the
可选的,隔板1112c可以是实心板,即,两个子出气通道1112b的部分腔壁是共用的,此时隔板1112c厚度的设置需能够使两个子出气通道1112b内的气溶胶温度降低。Optionally, the
可选的,隔板1112c可以是空心板,即,隔板1112c的内部是中空的,两个子出气通道1112b为完全分离的两个通道;隔板1112c的壁厚及其内部中空空腔的宽度(隔板1112c内部中空空腔的宽度为沿着隔板1112c厚度方向的尺寸大小)决定着隔板1112c的厚度,隔板1112c的壁厚及其内部中空空腔的宽度根据需要进行设计,能够实现分流降温即可。可选的,隔板1112c为矩形空心板。Optionally, the
可选的,无论隔板1112c是矩形实心板还是矩形空心板,隔板1112c的长度(隔板1112c的长度为沿着出气通道1112延伸方向的尺寸)与出气通道1112的长度的比值为1:5-1:4。通过如上设置,可以实现较好的分流降温效果;在雾化器11的整体尺寸几乎不变的前提下,并不会使储液腔1111的存储空间减少太多,避免储液腔1111的存储量无法满足用户需求。Optionally, no matter whether the
具体地,出气通道1112远离雾化芯113的一端在雾化器11宽度方向的尺寸变大形成加宽段B;加宽段B为出气通道1112的第二部分和第三部分。隔板1112c设置于加宽段B且平行于雾化器11的厚度方向,以将出气通道1112远离雾化芯113的一端分割成两个子出气通道1112b;隔板1112c靠近出气口1112a的端面与出气口1112a间隔设置,以使出气通道1112的第三部分为直通管,且两个子出气通道1112b中的气溶胶在第三部分汇聚在一起再从出气口1112a流出。通过在出气通道1112上设置加宽段B,设置于加宽段B的隔板1112c可以具有较大的厚度,能够更好的对两个子出气通道1112b中的气溶胶降温。在一实施方式中,加宽段B靠近雾化芯113的端面与隔板1112c靠近雾化芯113的端面齐平,即,设置有隔板1112c处才开始对出气通道1112的通道宽度进行加宽。Specifically, the dimension of the end of the
加宽段B可以是沿着其延伸方向的横截面形状、面积一致的;即,加宽段B为直通结构。加宽段B可以是包括第一段和第二段,第二段位于第一段远离雾化芯113的一侧;第一段沿着远离雾化芯113的方向的横截面积逐渐增大,使得第一段沿着远离雾化芯113的方向的纵截面为锥形结构;第二段沿着远离雾化芯113的方向的横截面积相同,即,第二段为直通结构(如图40所示)。通过将加宽段B的第一段设置为锥形结构,可以避免气溶胶在加宽段B的拐角处形成涡流,进而避免加宽段B的结构对气溶胶流出出气口1112a量的影响。The widened section B may have the same cross-sectional shape and area along its extending direction; that is, the widened section B is a straight-through structure. The widening section B may include a first section and a second section, the second section is located on the side of the first section away from the
两个子出气通道1112b可以沿着隔板1112c对称设置,以使雾化芯113雾化好的气溶胶流经两个子出气通道1112b,气溶胶分别在两个子出气通道1112b可以实现相同的降温效果。The two
请参阅图41-图44,图41为现有的雾化器局部结构示意图,图42为图41提供的雾化器的出气口的气溶胶温度分布云图,图43为图40提供的雾化器的出气口的气溶胶温度分布云图,图44为图40提供的雾化器的出气通道靠近出气口一端的几面流速矢量分布图。Please refer to Figure 41-Figure 44, Figure 41 is a schematic diagram of the partial structure of the existing atomizer, Figure 42 is the cloud map of the aerosol temperature distribution at the air outlet of the atomizer provided in Figure 41, and Figure 43 is the atomization provided in Figure 40 The cloud diagram of the aerosol temperature distribution at the air outlet of the nebulizer, and Fig. 44 is the flow velocity vector distribution diagram on several surfaces of the air outlet channel of the nebulizer near the air outlet provided in Fig. 40 .
图41提供的雾化器的结构与图40提供的雾化器11的结构只有出气通道的设置方式不同,图41中的雾化器的出气通道为直通结构,对图41提供的现有雾化器进行测试,测试条件为:出气通道的直径为2.5mm,出气通道的长度为32.9mm,雾化芯上的S型发热层1134的初始温度为250℃,雾化量为3s/9mg。对图40提供的雾化器11进行测试,测试条件为:出气通道1112靠近雾化芯113的一端未分流前的直径为2.5mm,出气通道入口至出气口1112a之间的记录为32.9mm,雾化芯113上的S型发热层1134的初始温度为250℃,雾化量为3s/9mg。测试结果如图42-图44所示。The structure of the atomizer provided in Figure 41 is different from the structure of the
通过图44可以看出,气溶胶在出气通道1112中分流进入两个子出气通道1112b之后汇聚混合时在中心位置A会存在混合涡旋区,即在汇聚混合过程中会进一步使出气口1112a中心位置A的气溶胶温度降低,使得出气口1112a的最高温度位于中心位置A的两侧,利于降低用户感知到的气溶胶温度。It can be seen from Fig. 44 that when the aerosol splits into the two
比较图42和图43,出气通道为直通结构时,气溶胶流经出气通道后直接流出,出气口的气溶胶混合较差,出气口的气溶胶温度相对集中在出气通道的中心位置,最高温度高达80℃;出气通道1112中设置有分流降温结构时,由于分流作用,气溶胶分别与两个子出气通道1112b内的空气混合降温以及被两个子出气通道1112b的腔壁吸热,虽然气溶胶在出气口1112a又再次汇聚在一起,但中心位置A的温度明显降低,中心位置A的温度约为69℃,出气口1112a的最高温度位于中心位置A的两侧,且出气口1112a的最高温度也降低至约74℃,整体的降温效果约5℃-10℃。Comparing Figure 42 and Figure 43, when the air outlet channel is a straight-through structure, the aerosol flows out directly after flowing through the air outlet channel, the aerosol mixing at the air outlet is poor, the aerosol temperature at the air outlet is relatively concentrated in the center of the air outlet channel, and the highest temperature up to 80°C; when the
经测试证明,出气通道1112在远离雾化芯113的一端先分流成多个子出气通道1112b再汇聚在一起,使得出气口1112a的气溶胶温度明显降低,提升了用户的使用体验。Tests have proved that the
下面对隔板1112c靠近出气口1112a的端面与出气口1112a之间间隔的间隔距离d进行研究。对具有分流结构的出气通道1112的雾化器11进行测试,测试条件为:出气通道1112靠近雾化芯113的一端未分流前的直径为2.5mm,出气通道入口至出气口1112a之间的记录为32.9mm,雾化芯113上的S型发热层1134的初始温度为250℃,雾化量为3s/9mg。测试结果如图45和图46所示,图45为出气口气溶胶最高温度与间隔距离d之间的关系曲线图,图46为出气口中心位置A的气溶胶温度与间隔距离d之间的关系曲线图。可以理解,图45中出气口1112a气溶胶最高温度指的是整个出气口1112a上的气溶胶最高温度。Next, the separation distance d between the end surface of the
对图45进行分析,可得出:隔板1112c靠近出气口1112a的端面与出气口1112a之间间隔的间隔距离d的大小对出气口1112a气溶胶最高温度影响不大。对图46进行分析,可得出:当隔板1112c靠近出气口1112a的端面与出气口1112a之间间隔的间隔距离d大于3mm后,出气口1112a的中心位置A处的气溶胶温度不再有比较大的变化,说明在间隔距离d等于3mm时,气溶胶的混合已经比较充分,继续增大间隔距离d对出气口1112a处的气溶胶温度分布的影响非常有限了。因此,优选d的范围为0mm<d≤3mm,更优选d的范围为0mm<d≤2.5mm。Analyzing Figure 45, it can be concluded that the distance d between the end surface of the
其中,得出图46实验数据的雾化器11除了具有分流结构的出气通道1112,还设置了雾化芯113的雾化面与进气孔1125a之间的距离h为0.4mm。Among them, the
可以理解,在通过使出气通道1112在远离雾化芯113的一端先分流成多个子出气通道1112b再汇聚在一起来降低出气口1112a的气溶胶的温度的前提下,雾化芯113的雾化面与进气孔1125a之间的距离h做如上设置(雾化器11第一实施例中具体介绍的内容:雾化芯113的雾化面与进气孔1125a之间的距离h)来降低出气口1112a的气溶胶温度为可选的,在出气通道1112中设置降温结构119(雾化器11第二实施例中具体介绍的降温结构119)来降低出气口1112a的气溶胶温度也为可选的。上述介绍的降低出气口1112a的气溶胶温度的三种实施方式,可以根据需要进行任意组合,能够使雾化器11的出气口1112a的气溶胶温度范围为55℃-85℃即可,可选的,使雾化器11的出气口1112a的气溶胶温度范围为70℃-80℃。It can be understood that, on the premise that the temperature of the aerosol at the
以上仅为本申请的实施方式,并非因此限制本申请的专利范围,凡是利用本申请说明书及附图内容所作的等效结构或等效流程变换,或直接或间接运用在其他相关的技术领域,均同理包括在本申请的专利保护范围内。The above is only the implementation mode of this application, and does not limit the scope of patents of this application. Any equivalent structure or equivalent process conversion made by using the contents of this application specification and drawings, or directly or indirectly used in other related technical fields, All are included in the scope of patent protection of the present application in the same way.
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