相关申请Related Applications
本申请要求2023年10月27日申请的，申请号为202311422022.2，名称为“导液机构及其加工装置、加工方法”的中国专利申请的优先权，在此将其全文引入作为请参阅。This application claims priority to Chinese patent application No. 202311422022.2, filed on October 27, 2023, entitled “Liquid-conducting mechanism and its processing device and processing method”, the full text of which is hereby incorporated by reference.
本申请涉及雾化设备技术领域，特别是涉及一种导液机构及其加工装置、加工方法。The present application relates to the technical field of atomization equipment, and in particular to a liquid guiding mechanism and a processing device and method thereof.
雾化器主要用于将液体进行雾化。雾化器包括储液机构、雾化机构和导液件，导液件设置于储液机构和雾化机构之间，以便对两个机构的腔室进行分隔，导液件吸取储液机构内的液体后，需要保持对液体的吸附状态使其不泄露，并将储存的液体快速供应至雾化机构。The atomizer is mainly used to atomize liquid. The atomizer includes a liquid storage mechanism, an atomization mechanism and a liquid guide. The liquid guide is arranged between the liquid storage mechanism and the atomization mechanism to separate the chambers of the two mechanisms. After the liquid guide absorbs the liquid in the liquid storage mechanism, it needs to maintain the adsorption state of the liquid to prevent leakage, and quickly supply the stored liquid to the atomization mechanism.
然而，为加强锁液效果，通常需要将导液件采用高密度设计，密度过高会导液不畅，影响雾化效果；密度过低，吸附锁液能力均下降，会有漏液风险。而且导液件的截面积越大，对导液和锁液性能要求会越高，锁液和导液效果难以平衡。However, in order to enhance the liquid locking effect, it is usually necessary to use a high-density design for the liquid guide. If the density is too high, the liquid will not be smoothly guided, affecting the atomization effect; if the density is too low, the adsorption and liquid locking capabilities will decrease, and there will be a risk of leakage. Moreover, the larger the cross-sectional area of the liquid guide, the higher the requirements for liquid guiding and liquid locking performance will be, and it is difficult to balance the liquid locking and liquid guiding effects.
本申请的目的在于提出一种导液机构及其加工装置、加工方法，以改善上述至少一项技术问题。本申请通过以下技术方案来实现上述目的。The purpose of this application is to propose a liquid guiding mechanism and a processing device and method thereof to improve at least one of the above technical problems. This application achieves the above purpose through the following technical solutions.
本申请实施方式提供了一种导液机构，所述导液机构包括：The present application provides a liquid guiding mechanism, which includes:
导液本体，具有内腔，所述导液本体设置有第一位置和第二位置，所述第一位置用于连接储液机构，所述第二位置用于连接雾化机构；A liquid guiding body having an inner cavity, wherein the liquid guiding body is provided with a first position and a second position, wherein the first position is used for connecting to a liquid storage mechanism, and the second position is used for connecting to an atomization mechanism;
其中，所述导液本体的密度由所述第一位置至所述第二位置逐渐增高，以形成渐变吸液通道。Wherein, the density of the liquid-conducting body gradually increases from the first position to the second position to form a gradual liquid-absorbing channel.
在其中一个实施例中，所述第一位置位于所述导液本体的外侧，且所述第二位置位于所述导液本体的内腔；或In one embodiment, the first position is located outside the liquid-conducting body, and the second position is located inside the inner cavity of the liquid-conducting body; or
所述第一位置位于所述导液本体的内腔，且所述第二位置位于所述导液本体的外侧。The first position is located in the inner cavity of the liquid-conducting body, and the second position is located outside the liquid-conducting body.
在其中一个实施例中，所述导液本体具有导液方向，所述导液方向由所述第一位置指向至所述第二位置；In one embodiment, the liquid guiding body has a liquid guiding direction, and the liquid guiding direction points from the first position to the second position;
所述导液本体包括至少两个导液层，至少两个所述导液层沿所述导液方向层叠设置，相邻两个所述导液层中，靠近所述第一位置的所述导液层的密度小于远离所述第一位置的所述导液层的密度。The liquid-conducting body includes at least two liquid-conducting layers, and at least two of the liquid-conducting layers are stacked along the liquid-conducting direction. Among two adjacent liquid-conducting layers, the density of the liquid-conducting layer close to the first position is smaller than the density of the liquid-conducting layer far from the first position.
在其中一个实施例中，所述导液本体由多个复合纤维连接制成，所述复合纤维的纤维结构包括皮芯式复合结构、半包式复合结构或海岛型复合结构。In one embodiment, the liquid-conducting body is made by connecting a plurality of composite fibers, and the fiber structure of the composite fibers includes a skin-core composite structure, a half-wrapped composite structure, or an island-in-the-sea composite structure.
在其中一个实施例中，所述复合纤维包括第一纤维丝和第二纤维丝，所述第一纤维丝和所述第二纤维丝相互连接；In one embodiment, the composite fiber includes a first fiber filament and a second fiber filament, and the first fiber filament and the second fiber filament are connected to each other;
所述第一纤维丝与所述第二纤维丝的材料熔点温差范围为30℃-90℃；The melting point temperature difference between the first fiber filament and the second fiber filament is in the range of 30°C to 90°C;
所述第一纤维丝与所述第二纤维丝的材料体积比范围为5:5-8:2；The material volume ratio of the first fiber filament to the second fiber filament is in the range of 5:5-8:2;
所述第一纤维丝与所述第二纤维丝的纤维直径为10微米-100微米。The fiber diameters of the first fiber filaments and the second fiber filaments are in the range of 10 micrometers to 100 micrometers.
在其中一个实施例中，所述第一纤维丝的材料包括聚丙烯、聚乙烯、聚对苯二甲酸乙二醇酯、聚酰胺和聚乳酸中的一种或多种；所述第二纤维丝的材料包括聚丙烯、聚乙烯、聚对苯二甲酸乙二醇酯、聚酰胺和聚乳酸中的一种或多种，所述第一纤维丝与所述第二纤维丝的材质不同。In one embodiment, the material of the first fiber filament includes one or more of polypropylene, polyethylene, polyethylene terephthalate, polyamide and polylactic acid; the material of the second fiber filament includes one or more of polypropylene, polyethylene, polyethylene terephthalate, polyamide and polylactic acid, and the material of the first fiber filament is different from that of the second fiber filament.
本申请实施方式提供了一种导液机构的加工装置，用于加工上述的导液机构，所述导液本体包括至少两个层叠设置的导液层，相邻两个所述导液层中，靠近所述第一位置的所述导液层的密度小于远离所述第一位置的所述导液层的密度；The embodiment of the present application provides a processing device for a liquid-conducting mechanism, which is used to process the above-mentioned liquid-conducting mechanism, wherein the liquid-conducting body comprises at least two liquid-conducting layers stacked in layers, and the density of the liquid-conducting layer close to the first position of two adjacent liquid-conducting layers is less than the density of the liquid-conducting layer far from the first position;
所述导液机构的加工装置包括管体以及设置于所述管体内的至少两个输送通道，所述输送通道沿所述管体的轴向设置，所述输送通道与所述导液层数量对应设置，每个所述输送通道用于输送不同所述导液层对应的不同密度的原料。The processing device of the liquid-conducting mechanism includes a tube body and at least two conveying channels arranged in the tube body. The conveying channels are arranged along the axial direction of the tube body. The conveying channels are arranged corresponding to the number of the liquid-conducting layers. Each of the conveying channels is used to convey raw materials of different densities corresponding to different liquid-conducting layers.
在其中一个实施例中，所述导液机构的加工装置还包括加热机构，所述加热机构用于对所述导液本体进行加热，所述加热机构与管体相连接，所述加热机构设置于所述导液本体的第一位置，所述加热机构的温度沿所述导液层的原料的输送方向逐渐升高。In one embodiment, the processing device of the liquid conducting mechanism also includes a heating mechanism, which is used to heat the liquid conducting body. The heating mechanism is connected to the tube body and is arranged at the first position of the liquid conducting body. The temperature of the heating mechanism gradually increases along the conveying direction of the raw material of the liquid conducting layer.
在其中一个实施例中，所述管体设置有至少两个，至少两个相互套设的所述管体中，相邻两个所述管体之间设置有间距，以形成所述输送通道。In one embodiment, at least two tubes are provided, and among the at least two tubes which are nested with each other, a distance is provided between two adjacent tubes to form the conveying channel.
在其中一个实施例中，所述导液机构的加工装置还包括隔板，所述隔板沿所述管体的轴向设置，所述隔板连接在相邻两个所述管体之间，所述隔板沿所述管体的周向设置有至少两个，以使所述输送通道形成至少两个输送分区。In one embodiment, the processing device of the liquid guiding mechanism also includes a partition, which is arranged along the axial direction of the tube body, and the partition is connected between two adjacent tube bodies. At least two partitions are arranged along the circumference of the tube body so that the delivery channel forms at least two delivery partitions.
本申请实施方式提供了一种导液机构的加工方法，基于上述的导液机构的加工装置，所述导液机构的加工方法包括：The embodiment of the present application provides a method for processing a liquid guiding mechanism. Based on the above-mentioned processing device for the liquid guiding mechanism, the method for processing the liquid guiding mechanism includes:
获取每个导液层的层密度；Obtain the layer density of each liquid-conducting layer;
根据每个所述导液层的层密度，分配所述导液层的原料至对应的输送通道内，以进行所述导液本体的分层划分；According to the layer density of each of the liquid-conducting layers, the raw materials of the liquid-conducting layers are distributed into corresponding conveying channels to perform layer division of the liquid-conducting body;
对所述导液层的原料进行加热。The raw material of the liquid conducting layer is heated.
在其中一个实施例中，获取导液层的层密度，包括：In one embodiment, obtaining the layer density of the liquid conducting layer includes:
获取所述导液本体的整体密度变化范围；Obtaining the overall density variation range of the liquid-conducting body;
在所述整体密度变化范围内，确定各个所述导液层的层密度。Within the overall density variation range, the layer density of each of the liquid conducting layers is determined.
在其中一个实施例中，所述导液本体的分层划分，包括：In one embodiment, the layered division of the liquid-conducting body includes:
所述导液层的原料配置为纤维丝；The raw material of the liquid-conducting layer is fiber filaments;
根据所述导液层的层密度，确定每个所述输送通道的纤维丝的数量；Determining the number of fiber filaments in each of the transport channels according to the layer density of the liquid-conducting layer;
将所述输送通道内装入对应数量的所述纤维丝。A corresponding number of the fiber filaments are loaded into the conveying channel.
在其中一个实施例中，对所述导液层的原料进行加热，包括：In one embodiment, heating the raw material of the liquid conducting layer comprises:
对所述导液层的原料沿自身输送路径进行分段加热，所述导液层的原料的加热温度沿输送方向逐渐升高。The raw material of the liquid-conducting layer is heated in sections along its own conveying path, and the heating temperature of the raw material of the liquid-conducting layer is gradually increased along the conveying direction.
在其中一个实施例中，对所述导液层的原料沿自身输送路径进行分段加热包括：In one embodiment, heating the raw material of the liquid conducting layer in sections along its own conveying path comprises:
将所述导液层的原料的输送路径划分为第一加热段和第二加热段，所述第一加热段的加热温度的范围为60℃-160℃，所述第二加热段的加热温度的范围为120℃-220℃。The conveying path of the raw material of the liquid-conducting layer is divided into a first heating section and a second heating section. The heating temperature of the first heating section ranges from 60°C to 160°C, and the heating temperature of the second heating section ranges from 120°C to 220°C.
上述导液机构，包括导液本体，通过将导液本体设计为由储液机构所在位置至雾化机构所在位置密度逐渐增高，能够提高导液本体的导液速度，并能够对液体进行良好锁液，减少漏液情况，较好地平衡锁液与导液效果，而且能够适应储液机构和雾化机构在导液本体的不同位置的安装，使用更加灵活。The above-mentioned liquid guiding mechanism includes a liquid guiding body. By designing the liquid guiding body to have a gradually increasing density from the position of the liquid storage mechanism to the position of the atomization mechanism, the liquid guiding speed of the liquid guiding body can be improved, and the liquid can be well locked, leakage can be reduced, and the liquid locking and liquid guiding effects can be better balanced. It can also adapt to the installation of the liquid storage mechanism and the atomization mechanism at different positions of the liquid guiding body, making it more flexible to use.
为了更清楚地说明本申请实施例或传统技术中的技术方案，下面将对实施例或传统技术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，还可以根据公开的附图获得其他的附图。In order to more clearly illustrate the embodiments of the present application or the technical solutions in the conventional technology, the drawings required for use in the embodiments or the conventional technology descriptions are briefly introduced below. Obviously, the drawings described below are merely embodiments of the present application, and ordinary technicians in this field can obtain other drawings based on the disclosed drawings without paying any creative work.
图1为本申请实施例的一种导液机构的横截面示意图。FIG1 is a schematic cross-sectional view of a liquid guiding mechanism according to an embodiment of the present application.
图2为本申请实施例的另一种导液机构的横截面示意图。FIG. 2 is a schematic cross-sectional view of another liquid guiding mechanism according to an embodiment of the present application.
图3为本申请实施例的导液机构的加工装置的加工状态示意图。FIG. 3 is a schematic diagram of a processing state of a processing device for a liquid guiding mechanism according to an embodiment of the present application.
图4为本申请实施例的导液机构的加工装置的管体的横截面示意图。FIG. 4 is a schematic cross-sectional view of a tube body of a processing device for a liquid guiding mechanism according to an embodiment of the present application.
图5为本申请实施例的导液机构的加工装置的管体的外部示意图。FIG. 5 is an external schematic diagram of a tube body of a processing device for a liquid guiding mechanism according to an embodiment of the present application.
图6为本申请实施例的导液机构的加工方法的示意图。FIG. 6 is a schematic diagram of a method for processing a liquid guiding mechanism according to an embodiment of the present application.
附图标记说明：Description of reference numerals:
1、导液本体；11、第一位置；12、第二位置；13、内腔；14、导液层；15、复合纤维；1. liquid-conducting body; 11. first position; 12. second position; 13. inner cavity; 14. liquid-conducting layer; 15. composite fiber;
2、管体；21、输送通道；211、输送分区；22、隔板；2. pipe body; 21. conveying channel; 211. conveying partition; 22. partition;
3、加热机构；31、第一加热段；32、第二加热段；3. Heating mechanism; 31. First heating section; 32. Second heating section;
4、压制模具。4. Pressing mold.
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，所描述的实施例仅仅是本申请一部分实施例，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 be combined with the drawings in the embodiments of the present application to clearly and completely describe the technical solutions in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, not all of the embodiments. Based on the embodiments in the present application, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of this application.
下面将结合附图对本申请技术方案的实施例进行详细的描述。以下实施例仅用于更加清楚地说明本申请的技术方案，因此只作为示例，而不能以此来限制本申请的保护范围。The following embodiments of the technical solution of the present application are described in detail in conjunction with the accompanying drawings. The following embodiments are only used to more clearly illustrate the technical solution of the present application, and are therefore only used as examples, and cannot be used to limit the scope of protection of the present application.
除非另有定义，本文所使用的所有的技术和科学术语与属于本申请的技术领域的技术人员通常理解的含义相同；本文中所使用的术语只是为了描述具体的实施例的目的，不是旨在于限制本申请；本申请的说明书和权利要求书及上述附图说明中的术语“包括”和“具有”以及它们的任何变形，意图在于覆盖不排他的包含。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by technicians in the technical field to which this application belongs; the terms used herein are only for the purpose of describing specific embodiments and are not intended to limit this application; the terms "including" and "having" in the specification and claims of this application and the above-mentioned figure descriptions and any variations thereof are intended to cover non-exclusive inclusions.
在本申请实施例的描述中，技术术语“第一”“第二”等仅用于区别不同对象，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、特定顺序或主次关系。在本申请实施例的描述中，“多个”的含义是两个以上，除非另有明确具体的限定。In the description of the embodiments of the present application, the technical terms "first", "second", etc. are only used to distinguish different objects, and cannot be understood as indicating or implying relative importance or implicitly indicating the number, specific order or primary and secondary relationship of the indicated technical features. In the description of the embodiments of the present application, the meaning of "multiple" is more than two, unless otherwise clearly and specifically defined.
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该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 to "embodiments" herein means that a particular feature, structure, or characteristic described in conjunction with the embodiments may be included in at least one embodiment of the present application. The appearance of the phrase in various locations in the specification does not necessarily refer to the same embodiment, nor is it an independent or alternative embodiment that is mutually exclusive with other embodiments. It is explicitly and implicitly understood by those skilled in the art that the embodiments described herein may be combined with other embodiments.
在本申请实施例的描述中，术语“和/或”仅仅是一种描述关联对象的关联关系，表示可以存在三种关系，例如A和/或B，可以表示：单独存在A，同时存在A和B，单独存在B这三种情况。另外，本文中字符“/”，一般表示前后关联对象是一种“或”的关系。In the description of the embodiments of the present application, the term "and/or" is only a description of the association relationship of the associated objects, indicating that there may be three relationships. For example, A and/or B can represent: A exists alone, A and B exist at the same time, and B exists alone. In addition, the character "/" in this article generally indicates that the associated objects before and after are in an "or" relationship.
在本申请实施例的描述中，术语“多个”指的是两个以上（包括两个），同理，“多组”指的是两组以上（包括两组），“多片”指的是两片以上（包括两片）。In the description of the embodiments of the present application, the term "multiple" refers to more than two (including two). Similarly, "multiple groups" refers to more than two groups (including two groups), and "multiple pieces" refers to more than two pieces (including two pieces).
在本申请实施例的描述中，技术术语“中心”“纵向”“横向”“长度”“宽度”“厚度”“上”“下”“前”“后”“左”“右”“竖直”“水平”“顶”“底”“内”“外”“顺时针”“逆时针”“轴向”“径向”“周向”等指示的方位或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本申请实施例和简化描述，而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此不能理解为对本申请实施例的限制。In the description of the embodiments of the present application, the technical terms "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings, which are only for the convenience of describing the embodiments of the present application and simplifying the description, and do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be understood as a limitation on the embodiments of the present application.
在本申请实施例的描述中，除非另有明确的规定和限定，技术术语“安装”“相连”“连接”“固定”等术语应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或成一体；也可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言，可以根据具体情况理解上述术语在本申请实施例中的具体含义。In the description of the embodiments of the present application, unless otherwise clearly specified and limited, technical terms such as "installed", "connected", "connected", "fixed" and the like should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, and it can be the internal connection of two elements or the interaction relationship between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the embodiments of the present application can be understood according to the specific circumstances.
参阅图1-2，本申请实施方式提供了一种导液机构，包括导液本体1，导液本体1具有内腔13，导液本体1设置有第一位置11和第二位置12，第一位置11用于连接储液机构，第二位置12用于连接雾化机构，导液本体1的密度由第一位置11至第二位置12逐渐增高，以形成渐变吸液通道，使得导液本体1内的液体能够沿吸液通道形成流动趋势。其中，导液本体1的整体密度变化范围可通过导液本体1的质量和体积进行确定。Referring to Figures 1-2, the embodiment of the present application provides a liquid guiding mechanism, including a liquid guiding body 1, the liquid guiding body 1 has an inner cavity 13, the liquid guiding body 1 is provided with a first position 11 and a second position 12, the first position 11 is used to connect the liquid storage mechanism, and the second position 12 is used to connect the atomization mechanism, and the density of the liquid guiding body 1 gradually increases from the first position 11 to the second position 12 to form a gradual liquid suction channel, so that the liquid in the liquid guiding body 1 can form a flow trend along the liquid suction channel. Among them, the overall density variation range of the liquid guiding body 1 can be determined by the mass and volume of the liquid guiding body 1.
如此设置，第一位置11和第二位置12可以但不限于分设在导液本体1的内外两侧或导液本体1上的不同位置。当第一位置11和第二位置12分设在导液本体1的内外两侧时，导液本体1的密度可由外至内逐渐增高，或者导液本体1的密度也可由内至外逐渐增高。由第一位置11至第二位置12，导液本体1的密度逐渐增高，毛细效应逐渐增强，导液本体1内的液体形成由第一位置11向第二位置12的流动趋势，即渐变吸液通道，储液机构内的液体由第一位置11逐渐向第二位置12沿渐变吸液通道流动，供应雾化机构进行雾化操作，导液本体1的导液速度明显提高，而且导液本体1的第二位置12处的密度较高，能够对液体进行良好地吸附锁液，减少液体漏出至雾化机构处的情况，从而较好地平衡锁液与导液效果，而且能够适应储液机构和雾化机构进行导液本体上不同位置的安装，使用更加灵活，解决了导液件的导液和锁液效果难以平衡的问题。In this way, the first position 11 and the second position 12 can be, but are not limited to, disposed at the inner and outer sides of the liquid guiding body 1 or at different positions on the liquid guiding body 1. When the first position 11 and the second position 12 are disposed at the inner and outer sides of the liquid guiding body 1, the density of the liquid guiding body 1 can be gradually increased from the outside to the inside, or the density of the liquid guiding body 1 can be gradually increased from the inside to the outside. From the first position 11 to the second position 12, the density of the liquid guiding body 1 gradually increases, and the capillary effect gradually increases. The liquid in the liquid guiding body 1 forms a flow trend from the first position 11 to the second position 12, that is, a gradual liquid absorption channel. The liquid in the liquid storage mechanism gradually flows from the first position 11 to the second position 12 along the gradual liquid absorption channel to supply the atomization mechanism for atomization operation. The liquid guiding speed of the liquid guiding body 1 is significantly improved, and the density at the second position 12 of the liquid guiding body 1 is relatively high, which can well adsorb and lock the liquid and reduce the situation where the liquid leaks to the atomization mechanism, thereby better balancing the locking and guiding effects. Moreover, it can adapt to the installation of the liquid storage mechanism and the atomization mechanism at different positions on the liquid guiding body, which is more flexible to use and solves the problem of the difficulty in balancing the guiding and locking effects of the liquid guiding part.
参阅图1，图1示出了一种导液机构的横截面示意图。示例性的，第一位置11位于导液本体1的外侧，且第二位置12位于导液本体1的内腔13，即储液机构可连接在导液本体1的外侧，雾化机构可连接在导液本体1的内腔13，此种设置方式中，导液本体1的密度由外至内逐渐增高，毛细效应逐渐增强，以使导液本体1内的液体形成由外向内的流动趋势，储液机构内的液体由导液本体1的外侧逐渐向其内腔13沿渐变吸液通道流动，供应雾化机构进行雾化操作，导液本体1的导液速度明显提高，而且导液本体1内侧的密度较高，能够对液体进行良好地吸附锁液，减少液体漏出至雾化机构处的情况，从而较好地平衡锁液与导液效果，也可适应导液件较大截面积的需要。Referring to FIG. 1 , FIG. 1 shows a schematic cross-sectional view of a liquid guiding mechanism. Exemplarily, the first position 11 is located outside the liquid guiding body 1, and the second position 12 is located in the inner cavity 13 of the liquid guiding body 1, that is, the liquid storage mechanism can be connected to the outside of the liquid guiding body 1, and the atomizing mechanism can be connected to the inner cavity 13 of the liquid guiding body 1. In this arrangement, the density of the liquid guiding body 1 gradually increases from the outside to the inside, and the capillary effect gradually increases, so that the liquid in the liquid guiding body 1 forms a flow trend from the outside to the inside, and the liquid in the liquid storage mechanism gradually flows from the outside of the liquid guiding body 1 to its inner cavity 13 along the gradual liquid suction channel, supplying the atomizing mechanism to perform atomization operation, the liquid guiding speed of the liquid guiding body 1 is significantly improved, and the density of the inner side of the liquid guiding body 1 is relatively high, which can well absorb and lock the liquid, reduce the situation where the liquid leaks to the atomizing mechanism, thereby better balancing the locking and guiding effects, and can also meet the needs of a larger cross-sectional area of the liquid guiding member.
参阅图2，图2示出了另一种导液机构的横截面示意图。示例性的，第一位置11位于导液本体1的内腔13，且第二位置12位于导液本体1的外侧，即储液机构可连接在导液本体1的内腔13，雾化机构可连接在导液本体1的外侧。此种设置方式中，导液本体1的密度由内至外逐渐增高，毛细效应逐渐增强，以使导液本体1内的液体形成由内向外的流动趋势，储液机构内的液体由导液本体1的内腔13逐渐向外侧沿渐变吸液通道流动，供应雾化机构进行雾化操作，导液本体1的导液速度明显提高，而且导液本体1的外侧的密度较高，能够对液体进行良好地吸附锁液，减少液体漏出至雾化机构处的情况，从而较好地平衡锁液与导液效果。同时，导液本体1的外侧壁面积远远大于导液本体1的内侧壁面积，导液本体1的外侧储液量能远远大于内侧储液量，雾化机构与面积较大的导液本体1的外侧壁相互作用，在加热温度等其他条件一定时，能够增强雾化效果，提高雾化气的流量。Refer to FIG. 2 , which shows a cross-sectional schematic diagram of another liquid guiding mechanism. Exemplarily, the first position 11 is located in the inner cavity 13 of the liquid guiding body 1, and the second position 12 is located on the outside of the liquid guiding body 1, that is, the liquid storage mechanism can be connected to the inner cavity 13 of the liquid guiding body 1, and the atomization mechanism can be connected to the outside of the liquid guiding body 1. In this arrangement, the density of the liquid guiding body 1 gradually increases from the inside to the outside, and the capillary effect gradually increases, so that the liquid in the liquid guiding body 1 forms a flow trend from the inside to the outside, and the liquid in the liquid storage mechanism gradually flows from the inner cavity 13 of the liquid guiding body 1 to the outside along the gradual liquid suction channel, supplying the atomization mechanism for atomization operation, the liquid guiding speed of the liquid guiding body 1 is significantly improved, and the density of the outer side of the liquid guiding body 1 is relatively high, which can well absorb and lock the liquid, reduce the situation where the liquid leaks to the atomization mechanism, and thus better balance the locking and guiding effects. At the same time, the outer wall area of the liquid-conducting body 1 is much larger than the inner wall area of the liquid-conducting body 1, and the outer liquid storage capacity of the liquid-conducting body 1 can be much larger than the inner liquid storage capacity. The atomization mechanism interacts with the outer wall of the liquid-conducting body 1 with a larger area. When other conditions such as the heating temperature are constant, the atomization effect can be enhanced and the flow rate of the atomization gas can be increased.
参阅图1-2，在其中一个实施例中，导液本体1具有导液方向，导液方向由第一位置11指向至第二位置12，即导液本体1内的液体由第一位置11流向第二位置12。导液本体1包括至少两个导液层14，至少两个导液层14沿导液方向层叠设置，形成密度梯度变化，使液体层层渗透。相邻两个导液层14中，靠近第一位置11的导液层14的密度小于远离第一位置11的导液层14的密度，如此设置，本实施例将导液本体1设计为层叠设置的多层型阶梯结构，能够使液体由导液本体1的第一位置11一层一层逐层流动至第二位置12，既能够形成快速导液操作，也便于对导液本体1进行加工。Referring to FIGS. 1-2 , in one embodiment, the liquid-conducting body 1 has a liquid-conducting direction, and the liquid-conducting direction points from the first position 11 to the second position 12, that is, the liquid in the liquid-conducting body 1 flows from the first position 11 to the second position 12. The liquid-conducting body 1 includes at least two liquid-conducting layers 14, and at least two liquid-conducting layers 14 are stacked along the liquid-conducting direction to form a density gradient change, so that the liquid penetrates layer by layer. Among the two adjacent liquid-conducting layers 14, the density of the liquid-conducting layer 14 close to the first position 11 is less than the density of the liquid-conducting layer 14 far from the first position 11. In this way, the liquid-conducting body 1 is designed as a stacked multi-layer stepped structure in this embodiment, which can make the liquid flow from the first position 11 of the liquid-conducting body 1 to the second position 12 layer by layer, which can form a fast liquid-conducting operation and facilitate the processing of the liquid-conducting body 1.
示例性的，每个导液层14的厚度可相等，也可沿导液方向，导液层14的厚度可逐渐增加，以便增强毛细效应，提高吸液及导液效果。导液层14可选设置有两个、三个或四个，可根据使用需要进行选用设计。导液本体1适用的液体可以但不限于为油或水。For example, the thickness of each liquid-conducting layer 14 can be equal, or the thickness of the liquid-conducting layer 14 can be gradually increased along the liquid-conducting direction, so as to enhance the capillary effect and improve the liquid absorption and liquid-conducting effect. Two, three or four liquid-conducting layers 14 can be optionally provided, and the design can be selected according to the use requirements. The liquid applicable to the liquid-conducting body 1 can be, but is not limited to, oil or water.
参阅图1，导液本体1可包括四个导液层14，四个导液层14由外至内层叠设置，分别记为导液层14a、导液层14b、导液层14c、导液层14d，导液层14a的密度记为ρ1，导液层14b的密度记为ρ2，导液层14c的密度记为ρ3，导液层14d的密度记为ρ4。当第一位置11位于导液本体1的外侧，且第二位置12位于导液本体1的内腔13时，ρ1＜ρ2＜ρ3＜ρ4。当第一位置11位于导液本体1的内腔13，且第二位置12位于导液本体1的外侧时，ρ1＞ρ2＞ρ3＞ρ4。Referring to FIG. 1 , the liquid-conducting body 1 may include four liquid-conducting layers 14, which are stacked from outside to inside and are respectively denoted as liquid-conducting layer 14a, liquid-conducting layer 14b, liquid-conducting layer 14c, and liquid-conducting layer 14d. The density of liquid-conducting layer 14a is denoted as ρ1, the density of liquid-conducting layer 14b is denoted as ρ2, the density of liquid-conducting layer 14c is denoted as ρ3, and the density of liquid-conducting layer 14d is denoted as ρ4. When the first position 11 is located outside the liquid-conducting body 1, and the second position 12 is located in the inner cavity 13 of the liquid-conducting body 1, ρ1＜ρ2＜ρ3＜ρ4. When the first position 11 is located in the inner cavity 13 of the liquid-conducting body 1, and the second position 12 is located outside the liquid-conducting body 1, ρ1＞ρ2＞ρ3＞ρ4.
在其中一个实施例中，导液本体1配置为柱体，内腔13沿导液本体1的轴向设置，以使导液本体1的内外导液过程更加均匀。导液层14沿内腔13的周向设置，内腔13可为柱型腔室，内腔13的截面轮廓可与导液本体1的外侧的截面轮廓相似。内腔13可贯穿导液本体1的两端部，以便于储液机构或雾化机构的安装，也可便于通气或通液。In one embodiment, the liquid-conducting body 1 is configured as a column, and the inner cavity 13 is arranged along the axial direction of the liquid-conducting body 1 to make the inner and outer liquid-conducting process of the liquid-conducting body 1 more uniform. The liquid-conducting layer 14 is arranged along the circumference of the inner cavity 13, and the inner cavity 13 can be a columnar chamber, and the cross-sectional profile of the inner cavity 13 can be similar to the cross-sectional profile of the outer side of the liquid-conducting body 1. The inner cavity 13 can pass through both ends of the liquid-conducting body 1 to facilitate the installation of the liquid storage mechanism or the atomization mechanism, and also to facilitate ventilation or liquid flow.
其中，导液本体1的横截面可以但不限于为圆形或多边形，多边形可以但不限于为方形、矩形或六边形，当然，导液本体1上也可设置有凸起部和/或凹入部，凸起部和凹入部均沿导液本体1的轴向设置。Among them, the cross-section of the liquid-conducting body 1 can be but not limited to a circle or a polygon, and the polygon can be but not limited to a square, a rectangle or a hexagon. Of course, the liquid-conducting body 1 can also be provided with a protrusion and/or a recessed portion, and the protrusion and the recessed portion are both arranged along the axial direction of the liquid-conducting body 1.
参阅图3，在其中一个实施例中，导液本体1可由多个复合纤维15连接制成，复合纤维15的纤维结构包括皮芯式复合结构、半包式复合结构或海岛型复合结构，具有三维立体卷曲、高蓬松性和覆盖性，对液体具有良好的吸附效果。Referring to FIG. 3 , in one embodiment, the liquid-conducting body 1 can be made by connecting a plurality of composite fibers 15 , the fiber structure of the composite fibers 15 includes a skin-core composite structure, a half-wrapped composite structure or an island-type composite structure, and has three-dimensional curling, high fluffiness and coverage, and has a good adsorption effect on liquids.
在其中一个实施例中，复合纤维15包括第一纤维丝和第二纤维丝，第一纤维丝和第二纤维丝相互连接，第一纤维丝与第二纤维丝的材料熔点温差范围为30℃-90℃，以便于对导液本体1进行成型加工。这里需要具体说明的是，若是第一纤维丝与第二纤维丝的材料熔点温差过大，生产第一纤维丝和第二纤维丝所需的纤维超长丝再增加卷曲时会不容易加工，加工工艺温度低，卷曲不明显，温度高又会使低熔点的纤维部分融化，极易粘连设备，造成残次品。若是第一纤维丝与第二纤维丝的材料熔点温差较小时，虽然纤维丝更好加工，但是，在进行多组第一纤维丝和第二纤维丝挤压形成导液本体1时，工艺温度加工区间较小，达到一定温度时，第一纤维丝和第二纤维丝的材料都融化或软化，无法成型为零件，也易出现残次品。In one embodiment, the composite fiber 15 includes a first fiber filament and a second fiber filament, the first fiber filament and the second fiber filament are connected to each other, and the temperature difference between the melting points of the materials of the first fiber filament and the second fiber filament is in the range of 30°C-90°C, so as to facilitate the molding of the liquid-conducting body 1. It should be specifically explained here that if the temperature difference between the melting points of the materials of the first fiber filament and the second fiber filament is too large, it will be difficult to process the super-long fiber filaments required for producing the first fiber filament and the second fiber filament when the curling is added. The processing temperature is low and the curling is not obvious. The high temperature will cause the low-melting-point fiber to partially melt, which is very easy to adhere to the equipment and cause defective products. If the temperature difference between the melting points of the materials of the first fiber filament and the second fiber filament is small, although the fiber filaments are easier to process, when multiple groups of the first fiber filament and the second fiber filament are extruded to form the liquid-conducting body 1, the process temperature processing range is small. When a certain temperature is reached, the materials of the first fiber filament and the second fiber filament are melted or softened, and cannot be formed into parts, and defective products are also prone to occur.
在其中一个实施例中，第一纤维丝与第二纤维丝的材料体积比范围为5:5-8:2，具体地，第一纤维丝的材料熔点可大于第二纤维丝的材料熔点，高熔点的第一纤维丝可起支撑作用，低熔点的第二纤维丝可与相邻纤维相接触黏合，起连接作用，第一纤维丝与第二纤维丝的体积比为5:5-8:2，也即1:1-4:1，高熔点的第一纤维丝的体积等于或大于低熔点的第二纤维丝的体积，具有较好的强度，使导液本体1具有良好吸液性的同时不易变形。In one embodiment, the material volume ratio of the first fiber filament to the second fiber filament is in the range of 5:5-8:2. Specifically, the melting point of the material of the first fiber filament may be greater than the melting point of the material of the second fiber filament. The first fiber filament with a high melting point can play a supporting role, and the second fiber filament with a low melting point can contact and bond with adjacent fibers to play a connecting role. The volume ratio of the first fiber filament to the second fiber filament is 5:5-8:2, that is, 1:1-4:1. The volume of the first fiber filament with a high melting point is equal to or greater than the volume of the second fiber filament with a low melting point, and has good strength, so that the liquid-conducting body 1 has good liquid absorption and is not easy to deform.
在其中一个实施例中，第一纤维丝与第二纤维丝的纤维直径为10微米-100微米，导液本体1为多孔隙结构，在质量相同时，即体积和密度相同，导液本体1内部是固体纤维与空气交错的微观空间结构，同等密度不变时，纤维直径可决定导液本体1的内部孔隙数量及大小，将第一纤维丝与第二纤维丝的纤维直径设计为10微米-100微米，能够使导液本体1具有较佳的孔隙形态，使得导液本体1具有较好的吸液效果。In one of the embodiments, the fiber diameters of the first fiber filament and the second fiber filament are 10 microns-100 microns, and the liquid-conducting body 1 is a porous structure. When the mass is the same, that is, the volume and density are the same, the interior of the liquid-conducting body 1 is a microscopic space structure in which solid fibers and air are interlaced. When the density is the same and unchanged, the fiber diameter can determine the number and size of the internal pores of the liquid-conducting body 1. Designing the fiber diameters of the first fiber filament and the second fiber filament to be 10 microns-100 microns can enable the liquid-conducting body 1 to have a better pore morphology, so that the liquid-conducting body 1 has a better liquid absorption effect.
在其中一个实施例中，导液本体1的孔隙率范围为80%-99%，以使导液本体1具有较佳的导液速率和锁油性。具体地，导液本体1可通过对复合纤维15结构的纤维直径和纤维数量的搭配，即可将某一体积的导液本体1组合不同的孔隙率。举例说明，针对体积为10立方厘米的导液本体1，可选择将复合纤维15结构的纤维直径设计为20微米，将纤维数量设计为0.075克每立方厘米，根据复合纤维15结构的重量和体积，即可确定导液本体1的孔隙率约为93%。其中，导液本体1可配置为储油棉，导液本体1的体积范围可选为0.2立方厘米至20立方厘米，根据所需的导液和储液效果，导液本体1的密度范围可选为0.04克每立方厘米至0.2克每立方厘米。In one embodiment, the porosity of the liquid-conducting body 1 ranges from 80% to 99%, so that the liquid-conducting body 1 has a better liquid-conducting rate and oil-locking property. Specifically, the liquid-conducting body 1 can combine different porosities of a certain volume of the liquid-conducting body 1 by matching the fiber diameter and the number of fibers of the composite fiber 15 structure. For example, for a liquid-conducting body 1 with a volume of 10 cubic centimeters, the fiber diameter of the composite fiber 15 structure can be designed to be 20 microns, and the number of fibers can be designed to be 0.075 grams per cubic centimeter. According to the weight and volume of the composite fiber 15 structure, it can be determined that the porosity of the liquid-conducting body 1 is about 93%. Among them, the liquid-conducting body 1 can be configured as oil storage cotton, and the volume range of the liquid-conducting body 1 can be selected from 0.2 cubic centimeters to 20 cubic centimeters. According to the required liquid-conducting and liquid-storing effects, the density range of the liquid-conducting body 1 can be selected from 0.04 grams per cubic centimeter to 0.2 grams per cubic centimeter.
在其中一个实施例中，第一纤维丝的材料包括聚丙烯、聚乙烯、聚对苯二甲酸乙二醇酯、聚酰胺和聚乳酸中的一种或多种；第二纤维丝的材料包括聚丙烯、聚乙烯、聚对苯二甲酸乙二醇酯、聚酰胺和聚乳酸中的一种或多种，第一纤维丝与第二纤维丝的材质不同，以使第一纤维丝和第二纤维丝形成不同的熔点温差，且材料便于加工。In one embodiment, the material of the first fiber filament includes one or more of polypropylene, polyethylene, polyethylene terephthalate, polyamide and polylactic acid; the material of the second fiber filament includes one or more of polypropylene, polyethylene, polyethylene terephthalate, polyamide and polylactic acid. The materials of the first fiber filament and the second fiber filament are different so that the first fiber filament and the second fiber filament form a different melting point temperature difference, and the material is easy to process.
参阅图3-4，本申请第二方面的实施例提供了导液机构的加工装置，用于加工上述的导液机构，导液机构包括导液本体1，导液本体1包括至少两个层叠设置的导液层14，相邻两个导液层14中，靠近第一位置11的导液层14的密度小于远离第一位置11的导液层14的密度。导液机构的加工装置包括管体2以及至少两个输送通道21，输送通道21设置于管体2内，输送通道21沿管体2的轴向设置，以便于导液层14的原料沿管体2的轴向输送。输送通道21与导液层14数量对应设置，每个输送通道21用于输送不同导液层14对应的不同密度的原料。Referring to FIGS. 3-4 , an embodiment of the second aspect of the present application provides a processing device for a liquid-conducting mechanism, which is used to process the above-mentioned liquid-conducting mechanism. The liquid-conducting mechanism includes a liquid-conducting body 1, and the liquid-conducting body 1 includes at least two stacked liquid-conducting layers 14. Among two adjacent liquid-conducting layers 14, the density of the liquid-conducting layer 14 close to the first position 11 is less than the density of the liquid-conducting layer 14 far from the first position 11. The processing device for the liquid-conducting mechanism includes a tube body 2 and at least two conveying channels 21. The conveying channels 21 are arranged in the tube body 2, and the conveying channels 21 are arranged along the axial direction of the tube body 2, so as to facilitate the conveying of the raw materials of the liquid-conducting layer 14 along the axial direction of the tube body 2. The conveying channels 21 are arranged corresponding to the number of liquid-conducting layers 14, and each conveying channel 21 is used to convey raw materials of different densities corresponding to different liquid-conducting layers 14.
如此设置，当需要对导液机构进行加工时，可根据导液层14的设计密度需要，在每个输送通道21中放置不同密度的原料，每个输送通道21内的原料经过加工后会形成对应密度的导液层14。本实施例通过设置多个输送通道21对导液本体1进行分层加工，能够使各个导液层14之间的分层更加明确，每个导液层14的密度更加均匀，使得加工后的导液本体1的导液和锁液效果更加准确和平衡。With such arrangement, when the liquid guiding mechanism needs to be processed, raw materials of different densities can be placed in each delivery channel 21 according to the design density requirements of the liquid guiding layer 14, and the raw materials in each delivery channel 21 will form a liquid guiding layer 14 of corresponding density after processing. In this embodiment, by providing multiple delivery channels 21 to perform layered processing on the liquid guiding body 1, the layering between each liquid guiding layer 14 can be more clear, the density of each liquid guiding layer 14 is more uniform, and the liquid guiding and liquid locking effects of the processed liquid guiding body 1 are more accurate and balanced.
其中，输送通道21与导液层14数量可一一对应，或者，至少两个导液层14可对应一个输送通道21，例如，导液本体1包括四个导液层14时，输送通道21可设置有两个，可以每两个导液层14对应一个输送通道21，或者，输送通道21可设置有四个，每个导液层14均对应一个输送通道21。Among them, the number of delivery channels 21 and the number of liquid-conducting layers 14 can correspond one to one, or, at least two liquid-conducting layers 14 can correspond to one delivery channel 21. For example, when the liquid-conducting body 1 includes four liquid-conducting layers 14, two delivery channels 21 can be provided, and every two liquid-conducting layers 14 can correspond to one delivery channel 21, or, four delivery channels 21 can be provided, and each liquid-conducting layer 14 corresponds to one delivery channel 21.
参阅图3-4，在其中一个实施例中，导液机构的加工装置还包括加热机构3，加热机构3用于对导液本体1进行加热，以使导液本体1内的原料能够膨化黏合，加热机构3与管体2相连接，即加热机构3能够以管体2为依托支撑。加热机构3设置于导液本体1的第一位置11，以使加热机构3靠近密度较低的导液本体1位置，使得导液本体1的第一位置11和第二位置12形成温度差，第一位置11的导液本体1会先膨化，第二位置12的导液本体1后膨化，使得每个导液层14均能够形成有第一位置11至第二位置12的变密度梯度。加热机构3的温度沿导液层14的原料的输送方向逐渐升高，即输送通道21可具有输入口和输出口，输入口和输出口可设置于管体2的两端部位置，导液层14的原料的输送方向可由输入口至输出口方向。本实施例通过对导液层14的原料进行逐渐升温加热，能够使导液层14的原料逐渐膨化卷曲后再逐渐黏合，能够使每个导液层14的密度更加均匀，以便使加工后的导液本体1的导液和锁液操作更加准确。Referring to Fig. 3-4, in one embodiment, the processing device of the liquid guiding mechanism further includes a heating mechanism 3, which is used to heat the liquid guiding body 1 so that the raw materials in the liquid guiding body 1 can expand and bond, and the heating mechanism 3 is connected to the tube body 2, that is, the heating mechanism 3 can be supported by the tube body 2. The heating mechanism 3 is arranged at the first position 11 of the liquid guiding body 1, so that the heating mechanism 3 is close to the position of the liquid guiding body 1 with lower density, so that a temperature difference is formed between the first position 11 and the second position 12 of the liquid guiding body 1, and the liquid guiding body 1 at the first position 11 will expand first, and the liquid guiding body 1 at the second position 12 will expand later, so that each liquid guiding layer 14 can form a variable density gradient from the first position 11 to the second position 12. The temperature of the heating mechanism 3 gradually increases along the conveying direction of the raw materials of the liquid guiding layer 14, that is, the conveying channel 21 can have an input port and an output port, and the input port and the output port can be arranged at the two end positions of the tube body 2, and the conveying direction of the raw materials of the liquid guiding layer 14 can be from the input port to the output port. In this embodiment, by gradually heating the raw material of the liquid conducting layer 14, the raw material of the liquid conducting layer 14 can be gradually expanded and curled and then gradually bonded together, so that the density of each liquid conducting layer 14 can be more uniform, so that the liquid conducting and liquid locking operations of the processed liquid conducting body 1 can be more accurate.
示例性的，加热机构3可以但不限于为加热管或加热片。加热机构3可包括多个加热段，每个加热段可沿管体2的周向设置，多个加热段可沿管体2的轴向分布。具体地，加热机构3可至少包括第一加热段31和第二加热段32，第一加热段31可用于将导液层14的原料加热进行预膨化卷曲，第二加热段32可用于将导液层14的原料进行加热黏合。Exemplarily, the heating mechanism 3 may be, but is not limited to, a heating tube or a heating sheet. The heating mechanism 3 may include a plurality of heating segments, each of which may be arranged along the circumference of the tube body 2, and the plurality of heating segments may be distributed along the axial direction of the tube body 2. Specifically, the heating mechanism 3 may include at least a first heating segment 31 and a second heating segment 32, wherein the first heating segment 31 may be used to heat the raw material of the liquid-conducting layer 14 for pre-expansion and curling, and the second heating segment 32 may be used to heat and bond the raw material of the liquid-conducting layer 14.
参阅图1和图4，在其中一个实施例中，管体2设置有至少两个，至少两个管体2相互套设，至少两个相互套设的管体2中，相邻两个管体2之间设置有间距，以形成输送通道21，以便于输送通道21与导液层14的轮廓相对应，使得各个导液层14加工后位置更加相互对应。Referring to FIG. 1 and FIG. 4 , in one embodiment, at least two tube bodies 2 are provided, and at least two tube bodies 2 are nested with each other. In the at least two tube bodies 2 nested with each other, a spacing is provided between two adjacent tube bodies 2 to form a conveying channel 21, so that the conveying channel 21 corresponds to the contour of the liquid-conducting layer 14, so that the positions of each liquid-conducting layer 14 after processing are more corresponding to each other.
示例性的，各个管体2可同轴设置，以使每个导液层14的厚度更加均匀。输送通道21的内外侧的周向轮廓与导液层14的内外侧的周向轮廓相同，输送通道21的周向轮廓可以但不限于为圆形或多边形。For example, each tube body 2 can be coaxially arranged to make the thickness of each liquid-conducting layer 14 more uniform. The inner and outer circumferential contours of the delivery channel 21 are the same as the inner and outer circumferential contours of the liquid-conducting layer 14, and the circumferential contour of the delivery channel 21 can be, but is not limited to, circular or polygonal.
参阅图3-4，在其中一个实施例中，导液机构的加工装置还包括隔板22，隔板22沿管体2的轴向设置，以便于与导液层14的输送方向保持一致，减少两者位置干涉。隔板22连接在相邻两个管体2之间，即隔板22的两个侧边分别与相邻的两个管体2的侧壁分别连接，以对相邻两个管体2之间的输送通道21进行分隔。隔板22沿管体2的周向设置有至少两个，以使输送通道21形成至少两个输送分区211，方便复杂截面的零件进行变密度设计。Referring to Fig. 3-4, in one embodiment, the processing device of the liquid guiding mechanism further includes a partition 22, which is arranged along the axial direction of the tube body 2 so as to be consistent with the conveying direction of the liquid guiding layer 14 and reduce the position interference between the two. The partition 22 is connected between two adjacent tube bodies 2, that is, the two sides of the partition 22 are respectively connected to the side walls of the two adjacent tube bodies 2 to separate the conveying channel 21 between the two adjacent tube bodies 2. At least two partitions 22 are arranged along the circumference of the tube body 2 so that the conveying channel 21 forms at least two conveying partitions 211, which facilitates the variable density design of parts with complex cross-sections.
示例性的，每一导液层14也可划分为至少两个导液条，输送分区211与导液条一一对应设置，每个输送分区211可用于输送对应的导液条的原料，以便于导液层14的多个导液条在对应的输送分区211内分别进行加热加工，加热面积大，受热均匀，更加便于导液层14膨胀黏合为对应密度，对导液层14的密度加工更加准确，而且通过多个输送分区211对每个导液层14的原料进行分流，减少了大量原料统一进入输送通道21内，易形成堵塞的情况。参阅图5，管体2上设置有多个连接点位，连接点位可用于供隔板22与管体2相连接。Exemplarily, each liquid-conducting layer 14 can also be divided into at least two liquid-conducting strips, and the conveying partitions 211 are arranged one by one with the liquid-conducting strips. Each conveying partition 211 can be used to convey the raw materials of the corresponding liquid-conducting strip, so that the multiple liquid-conducting strips of the liquid-conducting layer 14 can be heated and processed separately in the corresponding conveying partitions 211. The heating area is large and the heating is uniform, which makes it easier for the liquid-conducting layer 14 to expand and bond to the corresponding density, and the density processing of the liquid-conducting layer 14 is more accurate. In addition, the raw materials of each liquid-conducting layer 14 are diverted through multiple conveying partitions 211, which reduces the situation where a large amount of raw materials enter the conveying channel 21 at the same time and are prone to blockage. Referring to FIG. 5, a plurality of connection points are arranged on the tube body 2, and the connection points can be used to connect the partition 22 with the tube body 2.
参阅图2-3，在其中一个实施例中，导液机构的加工装置还可包括压制模具4，压制模具4可连接在管体2的出料口处，用于对将导液层14的原料经加热膨化黏合后形成的膨化物料进行压制成型，从而形成成品零件。Referring to Figures 2-3, in one embodiment, the processing device of the liquid guiding mechanism may also include a pressing mold 4, which can be connected to the discharge port of the tube body 2 to press and mold the expanded material formed by heating, expanding and bonding the raw materials of the liquid guiding layer 14, thereby forming a finished part.
参阅图1-4和图6，本申请第三方面的实施例提供的导液机构的加工方法，基于上述导液机构的加工装置，导液机构的加工方法包括：Referring to FIGS. 1-4 and 6 , the third aspect of the present application provides a method for processing a liquid guiding mechanism. Based on the above-mentioned processing device for the liquid guiding mechanism, the method for processing the liquid guiding mechanism includes:
获取每个导液层14的层密度，即根据导液本体1所需的导液和锁液需求，可分配每个导液层14所需的导液和锁液需求，匹配每个导液层14对应的层密度，每个导液层14可单层加工后进行组合，也可多层统一加工均可。The layer density of each liquid-conducting layer 14 is obtained, that is, according to the liquid-conducting and liquid-locking requirements of the liquid-conducting body 1, the liquid-conducting and liquid-locking requirements of each liquid-conducting layer 14 can be allocated, and the layer density corresponding to each liquid-conducting layer 14 can be matched. Each liquid-conducting layer 14 can be combined after single-layer processing, or can be processed uniformly in multiple layers.
根据每个导液层14的层密度，分配导液层14的原料至对应的输送通道21内，以进行导液本体1的分层划分，即每个输送通道21内通过放入不同数量的导液层14的原料，以使导液层14的原料膨化黏合后形成对应密度的导液层14，便于导液层14的层密度更加可控。According to the layer density of each liquid-conducting layer 14, the raw materials of the liquid-conducting layer 14 are distributed to the corresponding conveying channels 21 to perform layer division of the liquid-conducting body 1, that is, different amounts of raw materials of the liquid-conducting layer 14 are placed in each conveying channel 21, so that the raw materials of the liquid-conducting layer 14 are expanded and bonded to form liquid-conducting layers 14 of corresponding density, so that the layer density of the liquid-conducting layer 14 is more controllable.
对导液层14的原料进行加热，通过加热升温使导液层14的原料相互膨化黏合。The raw materials of the liquid conducting layer 14 are heated, and the raw materials of the liquid conducting layer 14 are expanded and bonded to each other by heating and increasing the temperature.
如此设置，通过在多个输送通道21内分配不同数量的导液层14的原料，并通过加热加工，以形成对应层密度的导液层14，不同层密度的导液层14相互层叠组合，以形成变密度的导液本体1，加工方便，而且每个导液层14中的层密度能够形成对应所需密度，以使导液本体1的密度变化更加规律，加工后的导液本体1更能达到所需的导液和锁液效果，便于导液本体1的导液和锁液效果的平衡。In this way, by distributing different quantities of raw materials of the liquid conducting layer 14 in multiple conveying channels 21 and performing heating processing to form liquid conducting layers 14 with corresponding layer densities, the liquid conducting layers 14 with different layer densities are stacked and combined with each other to form a liquid conducting body 1 with variable density. The processing is convenient, and the layer density in each liquid conducting layer 14 can form a corresponding required density, so that the density change of the liquid conducting body 1 is more regular. The processed liquid conducting body 1 can better achieve the required liquid conducting and liquid locking effects, which is convenient for balancing the liquid conducting and liquid locking effects of the liquid conducting body 1.
在其中一个实施例中，获取导液层14的层密度，包括：In one embodiment, obtaining the layer density of the liquid conducting layer 14 includes:
获取导液本体1的整体密度变化范围，即可根据导液本体1所需的导液和锁液需求，可先确定导液本体1所需的整体密度变化范围的阈值。By obtaining the overall density variation range of the liquid guiding body 1 , a threshold value of the overall density variation range required by the liquid guiding body 1 can be first determined according to the liquid guiding and liquid locking requirements of the liquid guiding body 1 .
根据整体密度变化范围，确定各个导液层14的层密度，即根据导液本体1所需的整体密度变化范围的阈值，可将整体密度变化范围的阈值由高到低进行数值划分，形成分段阈值，分段阈值的数量与导液层14的数量一一对应，每个导液层14的层密度至在对应的分段阈值内进行选取，以便于加工后的导液层14相互组合能够满足导液本体1所需的导液和锁液需求。According to the overall density variation range, the layer density of each liquid-conducting layer 14 is determined, that is, according to the threshold of the overall density variation range required by the liquid-conducting body 1, the threshold of the overall density variation range can be numerically divided from high to low to form segmented thresholds. The number of segmented thresholds corresponds to the number of liquid-conducting layers 14 one by one. The layer density of each liquid-conducting layer 14 is selected within the corresponding segmented threshold, so that the processed liquid-conducting layers 14 can be combined with each other to meet the liquid-conducting and liquid-locking requirements of the liquid-conducting body 1.
在其中一个实施例中，导液本体1的分层划分，包括：In one embodiment, the layered division of the liquid-conducting body 1 includes:
导液层14的原料配置为纤维丝，纤维丝可配置为上述的复合纤维15，当然也可配置为多个单材质纤维相组合的纤维结构，能够满足导液层14的制作需要即可。The raw material of the liquid-conducting layer 14 is fiber filaments, which can be configured as the composite fibers 15 mentioned above, or can be configured as a fiber structure composed of multiple single-material fibers, as long as the production requirements of the liquid-conducting layer 14 are met.
根据导液层14的层密度，确定每个输送通道21的纤维丝的数量，具体地，导液层14的层密度根据需要直接选取，或是可根据导液层14所需的体积和质量计算获得。纤维丝的数量记为N，纤维丝的单丝直线重量记为m，纤维丝对应的收缩比记为η，导液层14的层密度记为ρ，则纤维丝的数量N的计算公式可为：The number of fiber filaments in each delivery channel 21 is determined according to the layer density of the liquid-conducting layer 14. Specifically, the layer density of the liquid-conducting layer 14 can be directly selected according to the needs, or can be calculated according to the required volume and mass of the liquid-conducting layer 14. The number of fiber filaments is recorded as N, the linear weight of the single fiber of the fiber filament is recorded as m, the shrinkage ratio of the fiber filament is recorded as η, and the layer density of the liquid-conducting layer 14 is recorded as ρ. The calculation formula of the number of fiber filaments N can be:
N=ρ/m×ηN=ρ/m×η
通过上述公式，即可得到导液层14对应的纤维丝数量，然后将纤维丝分配至各个输送通道21内即可，示例性的，纤维丝可等分至各个输送通道21内，或者各个输送通道21内的纤维丝数量的差值需要在预设范围内，能够使导液层14的层密度满足使用需要即可。Through the above formula, the number of fiber filaments corresponding to the liquid-conducting layer 14 can be obtained, and then the fiber filaments can be distributed to each delivery channel 21. For example, the fiber filaments can be equally divided into each delivery channel 21, or the difference in the number of fiber filaments in each delivery channel 21 needs to be within a preset range, so that the layer density of the liquid-conducting layer 14 can meet the use requirements.
在其中一个实施例中，对导液层14的原料进行加热，包括：In one embodiment, heating the raw material of the liquid conducting layer 14 comprises:
对导液层14的原料沿自身输送路径进行分段加热，导液层14的原料的加热温度沿输送方向逐渐升高，即在导液层14的原料的输送路径上，能够形成不同温度区，导液层14的长度较长，多段温度区能够使导液层14的受热更加均匀，而且能使导液层14分段进行膨化黏合。The raw material of the liquid conducting layer 14 is heated in sections along its own conveying path, and the heating temperature of the raw material of the liquid conducting layer 14 gradually increases along the conveying direction, that is, different temperature zones can be formed on the conveying path of the raw material of the liquid conducting layer 14. The liquid conducting layer 14 is relatively long, and multiple temperature zones can make the liquid conducting layer 14 heated more evenly, and can make the liquid conducting layer 14 expand and bond in sections.
示例性的，加热位置可位于导液本体1的第一位置11，即加热位置可靠近层密度较低的导液层14，以使导液层14之间形成温度差，靠近加热位置的层密度较低的导液层14的温度较高，原料会先膨化，形成较大膨化空隙，远离加热位置的层密度较高的导液层14的温度较低，原料会后膨化，形成较小膨化空隙，使得每个导液层14也可形成第一位置11向第二位置12变化的密度梯度。Exemplarily, the heating position can be located at the first position 11 of the liquid-conducting body 1, that is, the heating position can be close to the liquid-conducting layer 14 with a lower layer density, so that a temperature difference is formed between the liquid-conducting layers 14. The temperature of the liquid-conducting layer 14 with a lower layer density close to the heating position is higher, and the raw material will expand first to form a larger expansion gap. The temperature of the liquid-conducting layer 14 with a higher layer density away from the heating position is lower, and the raw material will expand later to form a smaller expansion gap, so that each liquid-conducting layer 14 can also form a density gradient changing from the first position 11 to the second position 12.
在其中一个实施例中，对导液层14的原料沿自身输送路径进行分段加热包括：In one embodiment, heating the raw material of the liquid conducting layer 14 in sections along its conveying path includes:
将导液层14的原料的输送路径划分为第一加热段和第二加热段，第一加热段的加热温度的范围为60℃-160℃，能够适应纤维材料的特性，使纤维更易形成预膨化卷曲。第二加热段的加热温度的范围为120℃-220℃，能够适应纤维材料的特性，使纤维的低熔点的部分更易玻璃化黏合。The conveying path of the raw material of the liquid guide layer 14 is divided into a first heating section and a second heating section. The heating temperature of the first heating section ranges from 60°C to 160°C, which can adapt to the characteristics of the fiber material and make the fiber easier to form pre-expansion curls. The heating temperature of the second heating section ranges from 120°C to 220°C, which can adapt to the characteristics of the fiber material and make the low melting point part of the fiber easier to vitrify and bond.
以上实施例的各技术特征可以进行任意的组合，为使描述简洁，未对上述实施例中的各个技术特征所有可能的组合都进行描述，然而，只要这些技术特征的组合不存在矛盾，都应当认为是本说明书记载的范围。The technical features of the above embodiments may be combined arbitrarily. To make the description concise, not all possible combinations of the technical features in the above embodiments are described. However, as long as there is no contradiction in the combination of these technical features, they should be considered to be within the scope of this specification.
以上所述实施例仅表达了本申请的几种实施方式，其描述较为具体和详细，但并不能因此而理解为对申请专利范围的限制。应当指出的是，对于本领域的普通技术人员来说，在不脱离本申请构思的前提下，还可以做出若干变形和改进，这些都属于本申请的保护范围。因此，本申请专利的保护范围应以所附权利要求为准。The above-described embodiments only express several implementation methods of the present application, and the descriptions thereof are relatively specific and detailed, but they cannot be construed as limiting the scope of the patent application. It should be pointed out that, for a person of ordinary skill in the art, several variations and improvements can be made without departing from the concept of the present application, and these all belong to the protection scope of the present application. Therefore, the protection scope of the patent application shall be subject to the attached claims.
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311422022.2ACN117443635A (en) | 2023-10-27 | 2023-10-27 | Liquid guide mechanism and processing device and processing method thereof |
| CN202311422022.2 | 2023-10-27 |
| Publication Number | Publication Date |
|---|---|
| WO2025087160A1true WO2025087160A1 (en) | 2025-05-01 |
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2024/125756PendingWO2025087160A1 (en) | 2023-10-27 | 2024-10-18 | Liquid guide mechanism, and machining device and machining method therefor |
| Country | Link |
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| CN (1) | CN117443635A (en) |
| WO (1) | WO2025087160A1 (en) |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117443635A (en)* | 2023-10-27 | 2024-01-26 | 深圳市基克纳科技有限公司 | Liquid guide mechanism and processing device and processing method thereof |
| CN118952774A (en)* | 2024-09-04 | 2024-11-15 | 深圳市基克纳科技有限公司 | A kind of conductive liquid and preparation method thereof |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111528525A (en)* | 2019-01-21 | 2020-08-14 | 浙江迈博高分子材料有限公司 | A liquid storage element, a liquid conducting element, a cooling element, a condensate absorbing element and a supporting element |
| KR20220154515A (en)* | 2021-05-13 | 2022-11-22 | 주식회사 케이티앤지 | Aerosol generating device |
| CN219020213U (en)* | 2022-11-09 | 2023-05-16 | 迈博高分子材料（宁波）有限公司 | Aerosol bullet, aerosol bullet with liquid injection port and aerosol dispersing device |
| CN219645069U (en)* | 2023-04-26 | 2023-09-08 | 常州市派腾电子技术服务有限公司 | Atomizer and aerosol generating device |
| CN116784524A (en)* | 2023-06-30 | 2023-09-22 | 卓尔悦国际控股有限公司 | Liquid-absorbing part, atomizing core, aerosol generating device and liquid-absorbing part preparation method |
| CN117443635A (en)* | 2023-10-27 | 2024-01-26 | 深圳市基克纳科技有限公司 | Liquid guide mechanism and processing device and processing method thereof |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111528525A (en)* | 2019-01-21 | 2020-08-14 | 浙江迈博高分子材料有限公司 | A liquid storage element, a liquid conducting element, a cooling element, a condensate absorbing element and a supporting element |
| KR20220154515A (en)* | 2021-05-13 | 2022-11-22 | 주식회사 케이티앤지 | Aerosol generating device |
| CN219020213U (en)* | 2022-11-09 | 2023-05-16 | 迈博高分子材料（宁波）有限公司 | Aerosol bullet, aerosol bullet with liquid injection port and aerosol dispersing device |
| CN219645069U (en)* | 2023-04-26 | 2023-09-08 | 常州市派腾电子技术服务有限公司 | Atomizer and aerosol generating device |
| CN116784524A (en)* | 2023-06-30 | 2023-09-22 | 卓尔悦国际控股有限公司 | Liquid-absorbing part, atomizing core, aerosol generating device and liquid-absorbing part preparation method |
| CN117443635A (en)* | 2023-10-27 | 2024-01-26 | 深圳市基克纳科技有限公司 | Liquid guide mechanism and processing device and processing method thereof |
| Publication number | Publication date |
|---|---|
| CN117443635A (en) | 2024-01-26 |
| Publication | Publication Date | Title |
|---|---|---|
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