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CN115871152A - Hot-pressing pipe, organic porous foam material and preparation method and application thereof - Google Patents

Hot-pressing pipe, organic porous foam material and preparation method and application thereof Download PDF

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CN115871152A
CN115871152A CN202111162083.0A CN202111162083A CN115871152A CN 115871152 A CN115871152 A CN 115871152A CN 202111162083 A CN202111162083 A CN 202111162083A CN 115871152 A CN115871152 A CN 115871152A
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porous foam
organic
hot
foam material
organic porous
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江涛
杨波平
黄慧丽
吴明媚
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Shenzhen Smoore Technology Ltd
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Shenzhen Smoore Technology Ltd
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Abstract

The invention relates to the technical field of electronic cigarette atomized core materials, in particular to a hot-pressing tube, an organic porous foam material, and a preparation method and application thereof. The organic porous foam material provided by the invention has a cell structure with an oval cross section. The organic porous foam material provided by the invention has a cellular structure with an oval cross section, and compared with a porous material with a circular cellular structure, the organic porous foam material has the advantages that the capillary action formed by the cellular walls is greatly increased, the oil guiding speed is obviously improved, the tobacco tar atomization efficiency and the atomization amount are further favorably improved, and the liquid leakage phenomenon can be prevented.

Description

热压管、有机多孔泡沫材料及其制备方法和应用Heat-pressed tube, organic porous foam material, preparation method and application thereof

技术领域technical field

本发明涉及电子烟雾化芯材料技术领域,具体涉及一种热压管、有机多孔泡沫材料及其制备方法和应用。The invention relates to the technical field of electronic smoke core materials, in particular to a heat-pressed tube, an organic porous foam material and a preparation method and application thereof.

背景技术Background technique

电子烟发热体是电子烟设备的核心部件,其由富含多孔结构的导油材料和发热元件组合而成,现有多孔结构的导油材料包括有机棉、无纺布、多孔陶瓷、活性炭、合成纤维等。棉纤维或其他纤维棉存在机械强度差、结构不稳定、装配一致性差的问题;有机棉不耐热,常规的有机棉芯发热体,发热丝加热到200℃左右会发生部分分解,产生醛酮类有毒物质,继续升温,超过300℃开始烧焦、分解,吸油性能急剧下降,烟雾量变小,并且伴有严重的抽吸焦味。多孔陶瓷主要由金属氧化物、二氧化硅、碳化硅等无机材料加助烧剂、造孔剂通过烧结而成,具有耐高温、抗酸碱和有机介质腐蚀等优点,很大程度上解决了有机纤维导油材料的诸多缺陷,但多孔陶瓷发热体制备工艺难度大、生产能耗高,且孔隙率较低、密度大、容易粉化等缺点,从而限制了其在电子烟领域的应用。The electronic cigarette heating body is the core component of electronic cigarette equipment. It is composed of oil-conducting materials rich in porous structure and heating elements. The existing porous structure oil-conducting materials include organic cotton, non-woven fabrics, porous ceramics, activated carbon, Synthetic fibers etc. Cotton fiber or other fiber cotton has the problems of poor mechanical strength, unstable structure, and poor assembly consistency; organic cotton is not heat-resistant, and the conventional organic cotton core heating element will partially decompose when heated to about 200°C, producing aldehydes and ketones When the temperature continues to rise, it will start to burn and decompose when it exceeds 300°C, the oil absorption performance will drop sharply, the amount of smoke will become smaller, and it will be accompanied by a severe smoking smell. Porous ceramics are mainly made of metal oxides, silicon dioxide, silicon carbide and other inorganic materials through sintering with sintering aids and pore-forming agents. They have the advantages of high temperature resistance, acid and alkali resistance and organic medium corrosion, and have largely solved There are many defects in organic fiber oil-conducting materials, but the preparation process of porous ceramic heating elements is difficult, the production energy consumption is high, and the disadvantages such as low porosity, high density, and easy pulverization limit its application in the field of electronic cigarettes.

有机多孔泡沫材料采用高分子树脂如聚酰亚胺、聚甲基丙烯酰亚胺、聚芳醚酮、聚三聚氰胺甲醛树脂等基体材料添加发泡剂、表面活性剂等经过发泡工艺得到,具有丰富的三维网状结构、范围可调的高孔隙率等优点,然而如将有机多孔泡沫材料直接作为电子烟发热体导油材料,其导油速率有限,易出现漏液现象,进而会影响电子烟烟雾量,影响抽吸体验。The organic porous foam material is obtained by foaming process by adding foaming agent, surfactant, etc. Rich three-dimensional network structure, high porosity with adjustable range, etc. However, if the organic porous foam material is directly used as the oil-conducting material of the electronic cigarette heating element, its oil-conducting rate is limited, and it is prone to liquid leakage, which will affect the electronic cigarette. The amount of smoke and smoke affects the smoking experience.

发明内容Contents of the invention

本发明的目的在于克服利用现有有机多孔泡沫材料作为电子烟发热体导油材料,其导油速率有限,易出现漏液现象,进而会影响电子烟烟雾量的缺陷,进而提供一种热压管、有机多孔泡沫材料及其制备方法和应用。The purpose of the present invention is to overcome the disadvantages of using the existing organic porous foam material as the oil-conducting material of the heating element of the electronic cigarette. Tube, organic porous foam material and its preparation method and application.

为达到上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:

一种有机多孔泡沫材料,所述有机多孔泡沫材料具有横截面呈椭圆形的泡孔结构。An organic porous foam material has a cell structure with an oval cross section.

优选的,所述椭圆形的长宽比为(2-16):1;优选的,所述椭圆形的长宽比为(2-7):1。Preferably, the aspect ratio of the ellipse is (2-16):1; preferably, the aspect ratio of the ellipse is (2-7):1.

优选的,所述有机多孔泡沫材料的表观密度为10-300kg/m3,孔隙率为50-99%;优选的,所述有机多孔泡沫材料的表观密度为30-160kg/m3,孔隙率为80-95%。Preferably, the apparent density of the organic porous foam is 10-300kg/m 3 , and the porosity is 50-99%; preferably, the apparent density of the organic porous foam is 30-160kg/m 3 , The porosity is 80-95%.

优选的,所述有机多孔泡沫材料呈圆柱形,选自聚酰亚胺多孔泡沫、聚甲基丙烯酰亚胺多孔泡沫、聚芳醚酮多孔泡沫、三聚氰胺甲醛树脂多孔泡沫中的一种或多种。Preferably, the organic porous foam material is cylindrical, and is selected from one or more of polyimide porous foam, polymethacrylimide porous foam, polyaryletherketone porous foam, and melamine formaldehyde resin porous foam. kind.

本发明所述有机多孔泡沫材料呈三维结构。The organic porous foam material of the present invention has a three-dimensional structure.

本发明还提供一种有机多孔泡沫材料的制备方法,包括如下步骤:对聚合物多孔泡沫原料进行径向热压即得所述有机多孔泡沫材料。The present invention also provides a method for preparing an organic porous foam material, which includes the following steps: performing radial heat pressing on a polymer porous foam raw material to obtain the organic porous foam material.

优选的,所述径向热压处理在热压管中进行。Preferably, the radial hot-pressing treatment is carried out in a hot-press tube.

优选的,包括如下步骤:Preferably, the following steps are included:

将聚合物多孔泡沫原料置于热压管进料口,在牵引力的作用下使聚合物多孔泡沫原料从热压管的进料口一端移动到热压管的出料口一端,聚合物多孔泡沫原料在热压管中进行径向热压,得到所述有机多孔泡沫材料。The polymer porous foam material is placed in the feed port of the heat-pressed tube, and the polymer porous foam material is moved from the feed port end of the heat-pressed tube to the discharge port end of the heat-pressed tube under the action of traction, and the polymer porous foam The raw materials are radially heat-pressed in a hot-press tube to obtain the organic porous foam material.

优选的,所述聚合物多孔泡沫原料为圆柱形聚合物多孔泡沫原料,所述圆柱形聚合物多孔泡沫原料的直径大于热压管的进料口直径。本发明通过将大直径的圆柱形聚合物多孔泡沫原料在牵引力的作用下使其进入热压管的加热管中,在加热管中圆柱形原料在高温下沿指向圆心的方向被径向热压,可连续生产出固定压缩倍率的较小直径的圆柱形泡沫材料。Preferably, the polymer porous foam raw material is a cylindrical polymer porous foam raw material, and the diameter of the cylindrical polymer porous foam raw material is larger than the diameter of the feed port of the thermocompression tube. The present invention enters the large-diameter cylindrical polymer porous foam raw material into the heating tube of the hot-pressing tube under the action of traction force, and in the heating tube, the cylindrical raw material is radially hot-pressed in the direction of the center of the circle at high temperature. , can continuously produce smaller-diameter cylindrical foam materials with fixed compression ratios.

可选的,所述热压管可为径向热压管。Optionally, the heat-pressed tube may be a radial heat-pressed tube.

优选的,所述径向热压温度为150-260℃,直径压缩比为(2-6):1,优选的,直径压缩比为(2-4):1;Preferably, the radial hot pressing temperature is 150-260°C, the diameter compression ratio is (2-6):1, preferably, the diameter compression ratio is (2-4):1;

所述聚合物多孔泡沫原料在热压管中的移动速度为1-20mm/s,所述聚合物多孔泡沫原料在热压管中的停留时间为0.5-10min。The moving speed of the polymer porous foam raw material in the hot-press tube is 1-20mm/s, and the residence time of the polymer porous foam raw material in the hot-press tube is 0.5-10min.

在具体实施例中所述径向热压温度可为150℃、180℃、200℃、220℃、250℃、260℃;直径压缩比可为2:1、3:1、4:1、5:1、6:1。本发明所述的直径压缩比指的是圆柱形聚合物多孔泡沫原料径向热压之前与热压之后的直径长度之比。In a specific embodiment, the radial hot pressing temperature can be 150°C, 180°C, 200°C, 220°C, 250°C, 260°C; the diameter compression ratio can be 2:1, 3:1, 4:1, 5 :1, 6:1. The diameter compression ratio mentioned in the present invention refers to the ratio of the diameter length of the cylindrical polymer porous foam raw material before radial heat pressing and after heat pressing.

优选的,所述聚合物多孔泡沫原料选自聚酰亚胺多孔泡沫、聚甲基丙烯酰亚胺多孔泡沫、聚芳醚酮多孔泡沫、三聚氰胺甲醛树脂多孔泡沫中的一种或多种;Preferably, the polymer porous foam raw material is selected from one or more of polyimide porous foam, polymethacrylimide porous foam, polyaryletherketone porous foam, and melamine formaldehyde resin porous foam;

所述有机多孔泡沫材料具有横截面呈椭圆形的泡孔结构,所述椭圆形的长宽比为(2-16):1;优选的,所述椭圆形的长宽比为(2-7):1。The organic porous foam material has a cell structure with an elliptical cross section, and the aspect ratio of the ellipse is (2-16): 1; preferably, the aspect ratio of the ellipse is (2-7 ):1.

所述有机多孔泡沫材料的表观密度为10-300kg/m3,孔隙率为50-99%;优选的,所述有机多孔泡沫材料的表观密度为30-160kg/m3,孔隙率为80-95%。可选的,所述有机多孔泡沫材料的表观密度可为10kg/m3、16kg/m3、20kg/m3、39kg/m3、40kg/m3、50kg/m3、100kg/m3、150kg/m3、155kg/m3、200kg/m3、250kg/m3、300kg/m3,孔隙率可为80%、85%、90%、95%。The organic porous foam material has an apparent density of 10-300kg/m 3 and a porosity of 50-99%; preferably, the organic porous foam material has an apparent density of 30-160kg/m 3 and a porosity of 80-95%. Optionally, the apparent density of the organic porous foam material may be 10kg/m 3 , 16kg/m 3 , 20kg/m 3 , 39kg/m 3 , 40kg/ m 3 , 50kg/m 3 , or 100kg/m 3 , 150kg/m 3 , 155kg/m 3 , 200kg/m 3 , 250kg/m 3 , 300kg/m 3 , the porosity can be 80%, 85%, 90%, 95%.

可选的,所述热压管具有连通设置的加热管和导向收缩机构。Optionally, the heat press tube has a heating tube and a guiding shrinkage mechanism arranged in communication.

优选的,所述导向收缩机构呈喇叭状,细的一端与加热管的进料口相连接;所述加热管上设置有加热元件,优选的,所述导向收缩机构上设置有加热元件。可以理解的加热管的进料口与热压管的进料口为同一开口。Preferably, the guide shrinking mechanism is trumpet-shaped, and the thin end is connected to the feeding port of the heating tube; the heating tube is provided with a heating element, and preferably, the guide shrinking mechanism is provided with a heating element. It can be understood that the feed port of the heating tube is the same opening as the feed port of the heat press tube.

本发明还提供一种热压管,所述热压管具有连通设置的加热管和导向收缩机构。The present invention also provides a heat-pressed tube, which has a heating tube and a guiding shrinkage mechanism arranged in communication.

优选的,所述导向收缩机构呈喇叭状,细的一端与加热管的进料口相连接;所述加热管上设置有加热元件,优选的,所述导向收缩机构上设置有加热元件。可以理解的加热管的进料口与热压管的进料口为同一开口。Preferably, the guide shrinking mechanism is trumpet-shaped, and the thin end is connected to the feeding port of the heating tube; the heating tube is provided with a heating element, and preferably, the guide shrinking mechanism is provided with a heating element. It can be understood that the feed port of the heating tube is the same opening as the feed port of the heat press tube.

本发明还提供一种导液元件,所述导液元件材料为上述所述的有机多孔泡沫材料或上述所述的制备方法制备得到的有机多孔泡沫材料。The present invention also provides a liquid-guiding element, wherein the material of the liquid-guiding element is the above-mentioned organic porous foam material or the organic porous foam material prepared by the above-mentioned preparation method.

本发明还提供一种发热体,所述发热体包括上述所述的导液元件和发热元件,所述发热元件设置在导液元件上以加热所述导液元件导出的气溶胶形成基质。The present invention also provides a heating body, the heating body includes the above-mentioned liquid conducting element and a heating element, and the heating element is arranged on the liquid conducting element to heat the aerosol-forming substrate exported by the liquid conducting element.

本发明还提供一种雾化装置,包括雾化器,所述雾化器包括上述所述的发热体;The present invention also provides an atomizing device, including an atomizer, and the atomizer includes the above-mentioned heating element;

主机,与所述雾化器电连接且控制所述雾化器工作。The host is electrically connected with the atomizer and controls the operation of the atomizer.

本发明的有益效果:Beneficial effects of the present invention:

1)本发明提供的有机多孔泡沫材料,所述有机多孔泡沫材料具有横截面呈椭圆形的泡孔结构,发明人发现椭圆形泡孔结构的泡沫材料相对于圆形泡孔结构的多孔材料,泡孔壁形成的毛细作用大大增加,导油速率显著提高,进而有利于提升烟油雾化效率和雾化量,且能防止漏液现象发生;同时该泡孔结构的多孔材料耐温性大大提升,降低了抽吸焦味的风险。1) The organic porous foam material provided by the present invention, the organic porous foam material has an oval cell structure in cross-section, the inventors found that the foam material with oval cell structure is relative to the porous material with circular cell structure, The capillary action formed by the cell wall is greatly increased, and the oil conduction rate is significantly improved, which is conducive to improving the atomization efficiency and atomization volume of the e-liquid, and can prevent liquid leakage; at the same time, the porous material of the cell structure has a high temperature resistance. Lifting, reducing the risk of smoking burnt odors.

2)本发明提供的有机多孔泡沫材料,进一步的,所述椭圆形的长宽比为(2-16):1,该比例下的泡孔结构形成的多孔材料具有优异的导油速率、耐温性能和防漏液性能,进一步的,所述椭圆形的长宽比为(2-7):1,该比例下的泡孔结构形成的多孔材料更利于提升材料的导油速率和耐温性能。2) The organic porous foam material provided by the present invention, further, the aspect ratio of the ellipse is (2-16): 1, the porous material formed by the cell structure under this ratio has excellent oil conduction rate, resistance temperature performance and anti-leakage performance, further, the aspect ratio of the ellipse is (2-7): 1, the porous material formed by the cell structure under this ratio is more conducive to improving the oil conduction rate and temperature resistance of the material performance.

3)本发明提供的有机多孔泡沫材料,进一步的,所述有机多孔泡沫材料的表观密度为10-300kg/m3,孔隙率为50-99%;优选的,所述有机多孔泡沫材料的表观密度为30-160kg/m3,孔隙率为80-95%。经过研究发现,本发明配合上述表观密度、孔隙率可进一步保证材料具有优异的导油速率和耐温性能3) The organic porous foam material provided by the present invention, further, the apparent density of the organic porous foam material is 10-300kg/m 3 , and the porosity is 50-99%; preferably, the organic porous foam material The apparent density is 30-160kg/m 3 , and the porosity is 80-95%. After research, it is found that the present invention can further ensure that the material has excellent oil conduction rate and temperature resistance in combination with the above-mentioned apparent density and porosity.

4)本发明提供的有机多孔泡沫材料的制备方法,对聚合物多孔泡沫原料进行径向热压即得所述有机多孔泡沫材料。可选的,所述聚合物多孔泡沫原料为圆柱形聚合物多孔泡沫原料,通过将圆柱形状的泡沫材料沿指向圆心的方向进行径向热压,减少了孔密度,使材料内部的泡孔由球形泡孔变成横截面呈椭圆形的泡孔结构,热压后的泡孔呈橄榄球状,大大增强了毛细作用力,达到更高的导油速率,同时微观结构上具有更大长宽比的泡孔结构更有利于烟油在水平方向的传输,快速导油带来更大的烟雾量,且耐温性大大提升,降低了抽吸焦味的风险。同时,椭圆形的泡孔结构有利于液体吸附作用增强,锁液能力提高。4) The preparation method of the organic porous foam material provided by the present invention, the polymer porous foam raw material is radially hot-pressed to obtain the organic porous foam material. Optionally, the polymer porous foam raw material is a cylindrical polymer porous foam raw material, and by radially hot-pressing the cylindrical foam material in a direction pointing to the center of the circle, the pore density is reduced, so that the cells inside the material are formed by Spherical cells become elliptical in cross-section, and the cells after hot pressing are in the shape of rugby balls, which greatly enhances the capillary force and achieves a higher oil conduction rate. At the same time, the microstructure has a larger aspect ratio The unique cell structure is more conducive to the transmission of e-liquid in the horizontal direction, and the rapid oil conduction brings a greater amount of smoke, and the temperature resistance is greatly improved, which reduces the risk of smoking burnt smell. At the same time, the elliptical cell structure is conducive to the enhancement of liquid adsorption and the improvement of liquid locking ability.

5)本发明提供的有机多孔泡沫材料的制备方法,进一步的,所述径向热压温度为150-260℃,直径压缩比为(2-6):1,所述聚合物多孔泡沫原料在径向热压管中的移动速度为1-20mm/s,所述聚合物多孔泡沫原料在径向热压管中的停留时间为0.5-10min,本发明通过控制上述参数,尤其是控制热压温度和压缩比,使其材料的泡孔结构形成适宜比例的椭圆形泡孔结构,更利于增强材料的导油速率和耐温性能,优选的,直径压缩比为(2-4):1,在该直径压缩比下更利于提升材料的导油速率和耐温性能。5) The preparation method of the organic porous foam material provided by the present invention, further, the radial hot pressing temperature is 150-260°C, the diameter compression ratio is (2-6):1, and the polymer porous foam raw material is The moving speed in the radial hot-press tube is 1-20mm/s, and the residence time of the polymer porous foam raw material in the radial hot-press tube is 0.5-10min. The temperature and compression ratio make the cell structure of the material form an elliptical cell structure with an appropriate ratio, which is more conducive to enhancing the oil conduction rate and temperature resistance of the material. Preferably, the diameter compression ratio is (2-4):1, This diameter compression ratio is more conducive to improving the oil conduction rate and temperature resistance of the material.

附图说明Description of drawings

为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,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他的附图。In order to more clearly illustrate the specific implementation of the present invention or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the specific implementation or description of the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can obtain other drawings based on these drawings without any creative work.

图1是本发明径向热压管的结构示意图;Fig. 1 is the structural representation of radial heat-pressed tube of the present invention;

图2是圆柱形三聚氰胺甲醛树脂多孔泡沫原料的扫描电镜图;Fig. 2 is the scanning electron micrograph of cylindrical melamine formaldehyde resin porous foam raw material;

图3是实施例1制备得到的有机多孔泡沫材料的扫描电镜图;Fig. 3 is the scanning electron micrograph of the organic porous foam material that embodiment 1 prepares;

图4是实施例1制备得到的有机多孔泡沫材料和有机棉材料抽吸实验结果对比图,其中图(a)为实施例1制备得到的有机多孔泡沫材料抽吸实验测试图,图(b)为有机棉材料抽吸实验测试图;Fig. 4 is the comparison diagram of the results of the suction test of the organic porous foam material prepared in Example 1 and the organic cotton material, wherein Figure (a) is the test chart of the suction test of the organic porous foam material prepared in Example 1, and Figure (b) It is the test chart of organic cotton material suction experiment;

图5是本发明有机多孔泡沫材料制备工艺示意图。Fig. 5 is a schematic diagram of the preparation process of the organic porous foam material of the present invention.

其中,1-加热管;2-导向收缩机构;3-进料口;4-出料口;5-聚合物多孔泡沫原料;6-径向热压后得到的有机多孔泡沫材料。Among them, 1-heating tube; 2-guide shrink mechanism; 3-feed inlet; 4-discharge port; 5-polymer porous foam raw material; 6-organic porous foam material obtained after radial hot pressing.

具体实施方式Detailed ways

提供下述实施例是为了更好地进一步理解本发明,并不局限于所述最佳实施方式,不对本发明的内容和保护范围构成限制,任何人在本发明的启示下或是将本发明与其他现有技术的特征进行组合而得出的任何与本发明相同或相近似的产品,均落在本发明的保护范围之内。The following examples are provided in order to further understand the present invention better, are not limited to the best implementation mode, and do not limit the content and protection scope of the present invention, anyone under the inspiration of the present invention or use the present invention Any product identical or similar to the present invention obtained by combining features of other prior art falls within the protection scope of the present invention.

实施例中未注明具体实验步骤或条件者,按照本领域内的文献所描述的常规实验步骤的操作或条件即可进行。所用试剂或仪器未注明生产厂商者,均为可以通过市购获得的常规试剂产品。If no specific experimental steps or conditions are indicated in the examples, it can be carried out according to the operation or conditions of the conventional experimental steps described in the literature in this field. The reagents or instruments used, whose manufacturers are not indicated, are all commercially available conventional reagent products.

实施例1Example 1

本实施例提供一种有机多孔泡沫材料,其制备方法包括如下步骤:The present embodiment provides a kind of organic porous foam material, and its preparation method comprises the following steps:

将圆柱形三聚氰胺甲醛树脂多孔泡沫原料置于径向热压管的进料口3,使用牵引机将多孔泡沫原料从径向热压管的进料口3一端移动到径向热压管的出料口4一端,多孔泡沫原料在径向热压管中进行径向热压,得到所述有机多孔泡沫材料;所述径向热压温度为200℃,直径压缩比为2:1,所述多孔泡沫原料在径向热压管中的移动速度为2mm/s,所述多孔泡沫原料在径向热压管中的停留时间为10min。Place the cylindrical melamine formaldehyde resin porous foam raw material on the feed port 3 of the radial heat-pressed tube, and use a tractor to move the porous foam raw material from one end of the feed port 3 of the radial heat-pressed tube to the outlet of the radial heat-pressed tube At one end of the feed port 4, the porous foam raw material is radially hot-pressed in a radial hot-press tube to obtain the organic porous foam material; the radial hot-pressing temperature is 200° C., and the diameter compression ratio is 2:1. The moving speed of the porous foam material in the radial heat-pressed tube is 2 mm/s, and the residence time of the porous foam material in the radial heat-pressed tube is 10 min.

如图1所示,所述径向热压管具有连通设置的加热管1和导向收缩机构2,所述导向收缩机构2呈喇叭状,细的一端与加热管1的进料口相连接;所述加热管1和导向收缩机构2上均设置有加热丝,以对多孔泡沫原料进行加热。As shown in Figure 1, the radial heat press tube has a heating tube 1 and a guiding shrinkage mechanism 2 arranged in communication, the guiding shrinking mechanism 2 is trumpet-shaped, and the thin end is connected to the feeding port of the heating tube 1; Both the heating tube 1 and the guide shrink mechanism 2 are provided with heating wires to heat the porous foam material.

图2为圆柱形三聚氰胺甲醛树脂多孔泡沫原料的扫描电镜图,如图2所示,多孔泡沫原料泡孔结构的横截面为圆形,图3为上述实施例制备的有机多孔泡沫材料的扫描电镜图,如图3所示,上述实施例制备的有机多孔泡沫材料具有横截面呈椭圆形的泡孔结构。Fig. 2 is the scanning electron microscope figure of cylindrical melamine formaldehyde resin porous foam material, as shown in Figure 2, the cross section of porous foam material cell structure is circular, and Fig. 3 is the scanning electron microscope of the organic porous foam material prepared by above-mentioned embodiment As shown in Figure 3, the organic porous foam material prepared in the above embodiment has a cell structure with an elliptical cross section.

实施例2Example 2

本实施例提供一种有机多孔泡沫材料,其制备方法包括如下步骤:The present embodiment provides a kind of organic porous foam material, and its preparation method comprises the following steps:

将圆柱形三聚氰胺甲醛树脂多孔泡沫原料置于径向热压管的进料口,使用牵引机将多孔泡沫原料从径向热压管的进料口一端移动到径向热压管的出料口一端,多孔泡沫原料在径向热压管中进行径向热压,得到所述有机多孔泡沫材料;所述径向热压温度为200℃,直径压缩比为3:1,所述多孔泡沫原料在径向热压管中的移动速度为2mm/s,所述多孔泡沫原料在径向热压管中的停留时间为10min。Place the cylindrical melamine-formaldehyde resin porous foam raw material at the inlet of the radial heat-pressed tube, and use a tractor to move the porous foam raw material from the feed port of the radial heat-pressed tube to the outlet of the radial heat-pressed tube At one end, the porous foam raw material is radially hot-pressed in a radial hot-press tube to obtain the organic porous foam material; the radial hot-pressing temperature is 200°C, and the diameter compression ratio is 3:1, and the porous foam raw material The moving speed in the radial heat press tube is 2mm/s, and the residence time of the porous foam material in the radial heat press tube is 10min.

实施例3Example 3

本实施例提供一种有机多孔泡沫材料,其制备方法包括如下步骤:The present embodiment provides a kind of organic porous foam material, and its preparation method comprises the following steps:

将圆柱形三聚氰胺甲醛树脂多孔泡沫原料置于径向热压管的进料口,使用牵引机将多孔泡沫原料从径向热压管的进料口一端移动到径向热压管的出料口一端,多孔泡沫原料在径向热压管中进行径向热压,得到所述有机多孔泡沫材料;所述径向热压温度为200℃,直径压缩比为4:1,所述多孔泡沫原料在径向热压管中的移动速度为2mm/s,所述多孔泡沫原料在径向热压管中的停留时间为10min。Place the cylindrical melamine-formaldehyde resin porous foam raw material at the inlet of the radial heat-pressed tube, and use a tractor to move the porous foam raw material from the feed port of the radial heat-pressed tube to the outlet of the radial heat-pressed tube At one end, the porous foam raw material is radially hot-pressed in a radial hot-press tube to obtain the organic porous foam material; the radial hot-press temperature is 200°C, and the diameter compression ratio is 4:1, and the porous foam raw material The moving speed in the radial heat press tube is 2mm/s, and the residence time of the porous foam material in the radial heat press tube is 10min.

实施例4Example 4

本实施例提供一种有机多孔泡沫材料,其制备方法包括如下步骤:The present embodiment provides a kind of organic porous foam material, and its preparation method comprises the following steps:

将圆柱形三聚氰胺甲醛树脂多孔泡沫原料置于径向热压管的进料口,使用牵引机将多孔泡沫原料从径向热压管的进料口一端移动到径向热压管的出料口一端,多孔泡沫原料在径向热压管中进行径向热压,得到所述有机多孔泡沫材料;所述径向热压温度为200℃,直径压缩比为6:1,所述多孔泡沫原料在径向热压管中的移动速度为2mm/s,所述多孔泡沫原料在径向热压管中的停留时间为10min。Place the cylindrical melamine-formaldehyde resin porous foam raw material at the inlet of the radial heat-pressed tube, and use a tractor to move the porous foam raw material from the feed port of the radial heat-pressed tube to the outlet of the radial heat-pressed tube At one end, the porous foam raw material is radially hot-pressed in a radial hot-press tube to obtain the organic porous foam material; the radial hot-press temperature is 200° C., and the diameter compression ratio is 6:1. The porous foam raw material The moving speed in the radial heat press tube is 2mm/s, and the residence time of the porous foam material in the radial heat press tube is 10min.

实施例5Example 5

本实施例提供一种导液元件,所述导液元件材料可为实施例1-4任一实施例所述制备的有机多孔泡沫材料。This embodiment provides a liquid-guiding element, and the material of the liquid-guiding element can be the organic porous foam material prepared in any one of the embodiments 1-4.

实施例6Example 6

本实施例提供一种发热体,所述发热体包括实施例5所述的导液元件和发热元件,所述发热元件设置在导液元件上以加热所述导液元件导出的气溶胶形成基质。This embodiment provides a heating element, the heating element includes the liquid guiding element described in Embodiment 5 and the heating element, the heating element is arranged on the liquid guiding element to heat the aerosol-forming substrate derived from the liquid guiding element .

实施例7Example 7

本实施例提供一种雾化装置,包括雾化器,所述雾化器包括实施例6所述的发热体;还包括主机,与所述雾化器电连接且控制所述雾化器工作。This embodiment provides an atomizing device, including an atomizer, the atomizer includes the heating element described in Embodiment 6; it also includes a host, which is electrically connected to the atomizer and controls the operation of the atomizer .

对比例1Comparative example 1

本对比例提供一种有机多孔泡沫材料,其制备方法包括如下步骤:This comparative example provides a kind of organic porous foam material, and its preparation method comprises the steps:

将长方体形三聚氰胺甲醛树脂多孔泡沫原料置于平板热压机上进行热压成型,热压温度为200℃,热压时间为10min,厚度压缩比为4:1,得到所述有机多孔泡沫材料。The cuboid-shaped melamine formaldehyde resin porous foam raw material was placed on a flat-plate hot press for hot-press molding. The hot-press temperature was 200° C., the hot-press time was 10 minutes, and the thickness compression ratio was 4:1 to obtain the organic porous foam material.

测试例1test case 1

分别对圆柱形三聚氰胺甲醛树脂多孔泡沫原料、上述实施例1-4和对比例1制备得到的有机多孔泡沫材料测试其表观密度、孔隙率、储油量和导油速率,测试结果见表1。Test the apparent density, porosity, oil storage capacity and oil conduction rate of the cylindrical melamine formaldehyde resin porous foam raw material, the organic porous foam material prepared in the above-mentioned examples 1-4 and comparative example 1 respectively, and the test results are shown in Table 1 .

其中表观密度按照GB/T6343-2009测试标准进行测试;Among them, the apparent density is tested according to the GB/T6343-2009 test standard;

孔隙率按照GB/T21650.2-2008测试标准进行测试;The porosity is tested according to the GB/T21650.2-2008 test standard;

储油量按照如下测试方法进行测试:分别将圆柱形三聚氰胺甲醛树脂多孔泡沫原料、实施例1-4和对比例1制备得到的有机多孔泡沫材料切割成规整的2cm*2cm*2cm的样块,称取其质量(记为样块初始质量),然后将样块浸泡到50㎎烟草标准烟油中,真空脱除气泡,保证烟油充分浸湿样块,最后将样块从烟油中捞出,放在自制的钢丝网支架上,放置15min,等待烟油无滴落后,称取样块质量(记为样块浸泡后质量);储油量=(样块浸泡后质量-样块初始质量)/样块初始质量。The oil storage capacity is tested according to the following test method: the organic porous foam material prepared by the cylindrical melamine formaldehyde resin porous foam raw material, Examples 1-4 and Comparative Example 1 is cut into regular 2cm*2cm*2cm sample pieces, Weigh its mass (recorded as the initial mass of the sample block), then soak the sample block in 50㎎ tobacco standard e-liquid, remove air bubbles in a vacuum to ensure that the e-liquid fully wets the sample block, and finally remove the sample block from the e-liquid Put it on the self-made steel wire mesh support, place it for 15min, wait for the vape oil to stop dripping, weigh the mass of the sample block (recorded as the mass after soaking of the sample block); oil storage capacity = (mass after soaking of the sample block - initial mass of the sample block )/initial mass of sample block.

导油速率按照如下测试方法进行测试:分别将圆柱形三聚氰胺甲醛树脂多孔泡沫原料、实施例1-4和对比例1制备得到的有机多孔泡沫材料切割成规整的1cm*1cm*1cm的样块,使用10ml精密注射进样器向水平放置的样块表面滴下20微升的标准烟油(该标准烟油为50㎎烟草标准烟油)液体,在电子显微镜下观察液滴完全没入样块所需时间,计算标准烟油液体体积和烟油液滴完全没入样块所需时间的比值即可得到导油速率。The oil conduction rate is tested according to the following test method: the organic porous foam material prepared by the cylindrical melamine formaldehyde resin porous foam raw material, Examples 1-4 and Comparative Example 1 is cut into regular 1cm*1cm*1cm sample pieces, Use a 10ml precision injection injector to drop 20 microliters of standard e-liquid (the standard e-liquid is 50㎎ tobacco standard e-liquid) liquid on the surface of the horizontal sample block, and observe under the electron microscope that the droplet completely submerges into the sample block. Time, calculate the ratio of the volume of the standard e-liquid liquid and the time required for the e-liquid droplet to completely submerge into the sample block to obtain the oil conduction rate.

表1有机多孔泡沫材料物性测试结果Table 1 The physical property test results of organic porous foam materials

Figure BDA0003290612210000071
Figure BDA0003290612210000071

通过表1的结果可以看出,本发明制备的多孔泡沫材料压缩比越大其表观密度越大,但是随着密度增大,聚合物基体所占比例上升,导致孔隙率下降,电子烟油通过的孔道收到压缩,毛细作用增强,吸油能力增强,但如果压缩比过大,易引起泡孔塌陷,阻碍了泡孔结构对烟油的吸附能力。与此同时,表观密度变大使得材料微观结构更加致密,机械强度增加,产品装配一致性也大大提高。It can be seen from the results in Table 1 that the larger the compression ratio of the porous foam material prepared by the present invention, the higher the apparent density, but as the density increases, the proportion of the polymer matrix increases, resulting in a decrease in porosity, and the e-liquid The passing pores are compressed, the capillary action is enhanced, and the oil absorption capacity is enhanced. However, if the compression ratio is too large, it is easy to cause the collapse of the cells, which hinders the adsorption capacity of the cell structure to the e-liquid. At the same time, the increase in apparent density makes the microstructure of the material denser, the mechanical strength increases, and the consistency of product assembly is also greatly improved.

测试例2test case 2

分别对上述实施例1制备得到的有机多孔泡沫材料和有机棉(成分为天然纤维素纤维)材料测试其耐热性,测试方法包括如下步骤:The organic porous foam material prepared in above-mentioned embodiment 1 and organic cotton (component is natural cellulose fiber) material test its heat resistance respectively, and test method comprises the steps:

分别将有机多孔泡沫材料和有机棉采用相同的发热丝以及相同的缠绕方式制备成发热体,对制备得到的发热体用机器模拟抽吸过程,按照固定频率,每次抽3秒,停27秒,重复200次,吸200口后观察发热体表面状况,结果如图4所示,采用实施例1多孔材料制备的棉芯发热体,与有机棉芯发热体相比,其耐热性大大提高,棉芯表面没有出现明显焦黑现象。经测试采用实施例1提供的多孔材料耐温高达360℃,而有机棉耐温仅为230℃。The organic porous foam material and the organic cotton are respectively prepared into a heating element using the same heating wire and the same winding method, and the pumping process is simulated by a machine for the prepared heating element, according to a fixed frequency, each pumping is 3 seconds, and the stop is 27 seconds , repeat 200 times, observe the surface condition of the heating element after inhaling 200 mouthfuls, the result is shown in Figure 4, the cotton core heating element prepared by the porous material of Example 1, compared with the organic cotton core heating element, its heat resistance is greatly improved , There is no obvious scorching phenomenon on the surface of the cotton core. The temperature resistance of the porous material provided in Example 1 is as high as 360°C, while the temperature resistance of organic cotton is only 230°C.

同时人工品吸结果也表明,由于没有抽吸焦味的影响,这种多孔棉芯比有机棉芯发热体具有更好的口感体验。At the same time, the results of artificial smoking also show that this porous cotton core has a better taste experience than the organic cotton core heating element due to the absence of the influence of smoking burnt smell.

显然,上述实施例仅仅是为清楚地说明所作的举例,而并非对实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引伸出的显而易见的变化或变动仍处于本发明创造的保护范围之中。Apparently, the above-mentioned embodiments are only examples for clear description, rather than limiting the implementation. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. And the obvious changes or changes derived therefrom are still within the scope of protection of the present invention.

Claims (15)

1. An organic porous foam characterized by having a cell structure with an elliptical cross-section.
2. The organic cellular foam according to claim 1 wherein the elliptical shape has an aspect ratio of (2-16) to 1; preferably, the aspect ratio of the ellipse is (2-7): 1.
3. The organic porous foam according to claim 1 or 2, characterized in that the apparent density of the organic porous foam is 10-300kg/m 3 The porosity is 50-99%; preferably, the apparent density of the organic porous foam material is 30-160kg/m 3 The porosity is 80-95%.
4. The organic cellular foam material according to any one of claims 1 to 3, wherein the organic cellular foam material is cylindrical and is selected from one or more of polyimide cellular foam, polymethacrylimide cellular foam, polyaryletherketone cellular foam, and melamine formaldehyde resin cellular foam.
5. The preparation method of the organic porous foam material is characterized by comprising the following steps: and carrying out radial hot pressing on the polymer porous foam raw material to obtain the organic porous foam material.
6. The method for preparing an organic cellular foam according to claim 5, wherein the radial hot pressing process is performed in a hot pressing pipe.
7. The method for preparing an organic cellular foam material according to claim 6, comprising the steps of:
and (3) placing the polymer porous foam raw material at the feed inlet of the hot-pressing pipe, moving the polymer porous foam raw material from one end of the feed inlet of the hot-pressing pipe to one end of the discharge outlet of the hot-pressing pipe under the action of traction force, and carrying out radial hot pressing on the polymer porous foam raw material in the hot-pressing pipe to obtain the organic porous foam material.
8. The method of claim 6 or 7, wherein the polymer cellular foam feedstock is a cylindrical polymer cellular foam feedstock, and the diameter of the cylindrical polymer cellular foam feedstock is greater than the diameter of the inlet orifice of the hot-pressed pipe.
9. The method for preparing an organic cellular foam according to any of claims 5 to 8, characterized in that the radial hot pressing temperature is 150 to 260 ℃ and the diameter compression ratio is (2-6): 1, preferably the diameter compression ratio is (2-4): 1;
the moving speed of the polymer porous foam raw material in the hot-pressing pipe is 1-20mm/s, and the retention time of the polymer porous foam raw material in the hot-pressing pipe is 0.5-10min.
10. The method for preparing organic porous foam material according to any one of claims 5 to 9, wherein the polymer porous foam raw material is selected from one or more of polyimide porous foam, polymethacrylimide porous foam, polyaryletherketone porous foam, and melamine formaldehyde resin porous foam;
the organic porous foam material has a cellular structure with an oval cross section, wherein the aspect ratio of the oval is (2-16): 1, preferably, the aspect ratio of the oval is (2-7): 1;
the apparent density of the organic porous foam material is 10-300kg/m 3 The porosity is 50-99%; preferably, the apparent density of the organic porous foam material is 30-160kg/m 3 The porosity is 80-95%.
11. The hot-pressing pipe is characterized by comprising a heating pipe and a guiding and shrinking mechanism which are communicated.
12. The hot-pressing tube as claimed in claim 11, wherein the guiding and contracting mechanism is trumpet-shaped, and a thin end of the guiding and contracting mechanism is connected with a feed port of the heating tube; the heating pipe is provided with a heating element, and preferably, the guiding and shrinking mechanism is provided with a heating element.
13. A drainage member, wherein the material of the drainage member is the organic porous foam material according to any one of claims 1 to 4 or the organic porous foam material prepared by the preparation method according to any one of claims 5 to 10.
14. A heat-generating body characterized by comprising the liquid-conductive member as recited in claim 13 and a heating element provided on the liquid-conductive member to heat an aerosol-forming substrate led out by the liquid-conductive member.
15. An atomizing device characterized by comprising an atomizer including the heat-generating body according to claim 14;
and the host is electrically connected with the atomizer and controls the atomizer to work.
CN202111162083.0A 2021-09-30 2021-09-30 Hot-pressing pipe, organic porous foam material and preparation method and application thereof Pending CN115871152A (en)

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Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050063728A1 (en) * 2003-08-07 2005-03-24 Hirohmi Harada Cleaning member, cleaning device, charging device, transfer device, process cartridge, and image forming apparatus
JP2009199008A (en) * 2008-02-25 2009-09-03 Bridgestone Corp Roller manufacturing method for image forming apparatus
US20100168260A1 (en) * 2006-01-12 2010-07-01 Basf Se Porous materials and process for their production
US20140000638A1 (en) * 2012-06-28 2014-01-02 R.J. Reynolds Tobacco Company Reservoir and heater system for controllable delivery of multiple aerosolizable materials in an electronic smoking article
CN105084726A (en) * 2014-05-22 2015-11-25 德拉克通信科技公司 Method for manufacturing an optical preform
CN105916399A (en) * 2014-02-10 2016-08-31 菲利普莫里斯生产公司 Cartridge for an aerosol-generating system
CN108890951A (en) * 2018-08-23 2018-11-27 瑞典戴铂国际有限公司 One kind being used for hole blister high molecular polymer foam core material surface-sealing equipment and technique
CN109349680A (en) * 2018-11-15 2019-02-19 深圳市合元科技有限公司 Porous heating element, atomizer containing porous heating element and porous body preparation method
CN109734950A (en) * 2018-12-28 2019-05-10 青岛海尔股份有限公司 Aerogel composite and preparation method thereof
CN111002571A (en) * 2019-12-13 2020-04-14 邓权塑业科技(湖南)有限公司 PVC pipe temperature control flaring equipment and method thereof
CN112167725A (en) * 2019-07-03 2021-01-05 深圳市合元科技有限公司 Application of organic porous material in aerosol generating device and atomizer using organic porous material
CN113331484A (en) * 2021-06-04 2021-09-03 深圳麦克韦尔科技有限公司 Electronic atomization device and atomizer and atomization assembly thereof
JP2021525093A (en) * 2018-05-31 2021-09-24 ジェイティー インターナショナル エス.エイ.JT International S.A. Aerosol-generating articles, aerosol-generating systems, and methods for generating flavored aerosols.

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050063728A1 (en) * 2003-08-07 2005-03-24 Hirohmi Harada Cleaning member, cleaning device, charging device, transfer device, process cartridge, and image forming apparatus
US20100168260A1 (en) * 2006-01-12 2010-07-01 Basf Se Porous materials and process for their production
JP2009199008A (en) * 2008-02-25 2009-09-03 Bridgestone Corp Roller manufacturing method for image forming apparatus
US20140000638A1 (en) * 2012-06-28 2014-01-02 R.J. Reynolds Tobacco Company Reservoir and heater system for controllable delivery of multiple aerosolizable materials in an electronic smoking article
CN105916399A (en) * 2014-02-10 2016-08-31 菲利普莫里斯生产公司 Cartridge for an aerosol-generating system
CN105084726A (en) * 2014-05-22 2015-11-25 德拉克通信科技公司 Method for manufacturing an optical preform
JP2021525093A (en) * 2018-05-31 2021-09-24 ジェイティー インターナショナル エス.エイ.JT International S.A. Aerosol-generating articles, aerosol-generating systems, and methods for generating flavored aerosols.
CN108890951A (en) * 2018-08-23 2018-11-27 瑞典戴铂国际有限公司 One kind being used for hole blister high molecular polymer foam core material surface-sealing equipment and technique
CN109349680A (en) * 2018-11-15 2019-02-19 深圳市合元科技有限公司 Porous heating element, atomizer containing porous heating element and porous body preparation method
CN109734950A (en) * 2018-12-28 2019-05-10 青岛海尔股份有限公司 Aerogel composite and preparation method thereof
CN112167725A (en) * 2019-07-03 2021-01-05 深圳市合元科技有限公司 Application of organic porous material in aerosol generating device and atomizer using organic porous material
CN111002571A (en) * 2019-12-13 2020-04-14 邓权塑业科技(湖南)有限公司 PVC pipe temperature control flaring equipment and method thereof
CN113331484A (en) * 2021-06-04 2021-09-03 深圳麦克韦尔科技有限公司 Electronic atomization device and atomizer and atomization assembly thereof

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