TWM625693U - Filter structure - Google Patents

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Publication number
TWM625693U
TWM625693U TW110215466U TW110215466U TWM625693U TW M625693 U TWM625693 U TW M625693U TW 110215466 U TW110215466 U TW 110215466U TW 110215466 U TW110215466 U TW 110215466U TW M625693 U TWM625693 U TW M625693U
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Taiwan
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tubular
filter
molecular sieve
filter screen
adsorbents
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TW110215466U
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Chinese (zh)
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戴清智
潘信宏
張芳卿
徐芝琪
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純萃材料股份有限公司
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Publication of TWM625693U publication Critical patent/TWM625693U/en

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濾網結構Filter structure

本新型是有關於一種濾網結構,特別是有關一種以管狀吸附材進行過濾的濾網結構。The new model relates to a filter screen structure, in particular to a filter screen structure for filtering with a tubular adsorbent material.

風機過濾機組(Fan-Filter Unit,FFU)、外氣空調箱(Make-up Air Unit,MAU)以及其他氣體或液體過濾模組係透過濾網攔阻流體中的雜質及汙染物。為了達到良好的過濾效果,習知濾網中的過濾材料具有緻密的結構,以降低流體通過濾網的速度,並延長流體與過濾材料的接觸時間。Fan-Filter Unit (FFU), Make-up Air Unit (MAU) and other gas or liquid filter modules block the impurities and pollutants in the fluid through the filter screen. In order to achieve a good filtering effect, the filter material in the conventional filter screen has a dense structure, so as to reduce the speed of the fluid passing through the filter screen and prolong the contact time between the fluid and the filter material.

然而,當濾網中的過濾材料越緻密時,流體越不容易通過濾網,因此需要使用越多能源來抽送流體,故難以在維持良好過濾效果的情況下,達成節能的目標。除此之外,習知濾網僅能針對單一過濾需求進行製造,若要完成複雜度較高的過濾效果,則必須配置多個不同材質之濾網,安裝上較為不便,且濾網的總體積不易縮減。However, when the filter material in the filter screen is denser, it is more difficult for the fluid to pass through the filter screen, so more energy is required to pump the fluid, so it is difficult to achieve the goal of energy saving while maintaining a good filtering effect. In addition, the conventional filter can only be manufactured for a single filtration requirement. To achieve a more complex filtering effect, multiple filters of different materials must be configured, which is inconvenient to install, and the total size of the filter The volume is not easy to reduce.

有鑑於此,如何在不損及過濾效果的前提下節約能源,以及如何提高濾網配置上的靈活度,仍為待解決的問題。In view of this, how to save energy without compromising the filtering effect and how to improve the flexibility of the filter screen configuration are still problems to be solved.

本新型的目的是提供一種濾網結構,其透過靈活配置不同結構的吸附材,可以在減少能源消耗的同時達到優異的過濾效果。The purpose of this new model is to provide a filter screen structure, which can achieve excellent filtering effect while reducing energy consumption by flexibly configuring adsorbent materials of different structures.

本新型之一實施方式提供一種濾網結構,其包含一框體以及一過濾層,框體係呈一長方體狀且圍繞固定過濾層。過濾層包含複數個管狀吸附材,管狀吸附材彼此平行排列堆疊,各管狀吸附材具有至少一孔道,孔道係呈軸向穿設,且孔道的一內徑為0.1 mm~4.0 mm。An embodiment of the present invention provides a filter screen structure, which includes a frame body and a filter layer. The frame body is in the shape of a rectangular parallelepiped and surrounds the fixed filter layer. The filter layer includes a plurality of tubular adsorbents, the tubular adsorbents are arranged and stacked in parallel with each other, each tubular adsorbent has at least one channel, the channel is axially penetrated, and an inner diameter of the channel is 0.1 mm to 4.0 mm.

據此,本新型之濾網結構使用管狀吸附材,故能在低壓損的情況下達到良好的過濾效果,進而減少能源的使用量,且本新型之濾網結構可以依照需求,透過堆疊不同結構的管狀吸附材,以達成複雜度較高的過濾效果。Accordingly, the filter mesh structure of the present invention uses a tubular adsorbent material, so it can achieve a good filtering effect under the condition of low pressure loss, thereby reducing the consumption of energy, and the filter mesh structure of the new type can be stacked according to requirements by stacking different structures. Tubular adsorbent material to achieve a more complex filtration effect.

依據前述的濾網結構,各管狀吸附材的一長度可為3 cm~50 cm。According to the aforementioned filter screen structure, a length of each tubular adsorbent material may be 3 cm to 50 cm.

依據前述的濾網結構,各管狀吸附材可具有至少三所述孔道,孔道之其中一者的一中心軸可與對應的管狀吸附材的一中心軸為平行,其餘的孔道可圍繞所述其中一孔道並呈等角分布。According to the aforementioned filter structure, each tubular adsorbent may have at least three of the pores, a central axis of one of the pores may be parallel to a central axis of the corresponding tubular adsorbent, and the rest of the pores may surround the pores. A channel and an equiangular distribution.

依據前述的濾網結構,各管狀吸附材的一外徑可為2.0 mm~9.0 mm。According to the aforementioned filter screen structure, an outer diameter of each tubular adsorbent material may be 2.0 mm˜9.0 mm.

前述的濾網結構更可包含至少一後段過濾層,框體可圍繞固定後段過濾層,後段過濾層可設於過濾層之一側。後段過濾層可包含至少一管狀吸附材層或一纖維狀吸附材層。The aforementioned filter screen structure may further include at least one rear filter layer, the frame body may surround and fix the rear filter layer, and the rear filter layer may be disposed on one side of the filter layer. The rear filter layer may comprise at least one tubular adsorbent layer or one fibrous adsorbent layer.

依據前述的濾網結構,纖維狀吸附材層可為網狀交織型態。According to the aforementioned filter screen structure, the fibrous adsorbent material layer may be in the form of mesh interweaving.

依據前述的濾網結構,管狀吸附材層可包含複數個後段管狀吸附材,後段管狀吸附材可彼此平行排列堆疊,且各後段管狀吸附材可具有至少一孔道呈軸向穿設。According to the aforementioned filter screen structure, the tubular adsorbent material layer may include a plurality of rear-stage tubular adsorbent materials, the rear-stage tubular adsorbent materials may be arranged and stacked in parallel with each other, and each rear-stage tubular adsorbent material may have at least one channel extending axially.

依據前述的濾網結構,各後段管狀吸附材可具有至少三所述孔道,各後段管狀吸附材的孔道之其中一者的一中心軸可與對應的後段管狀吸附材的一中心軸為平行,各後段管狀吸附材中其餘的孔道可圍繞所述其中一孔道並呈等角分布。According to the aforementioned filter screen structure, each rear-stage tubular adsorbent material may have at least three of the pores, and a central axis of one of the pores of each rear-stage tubular adsorbent material may be parallel to a central axis of the corresponding rear-stage tubular adsorbent material, The remaining pores in each rear-stage tubular adsorbent may surround one of the pores and be distributed equiangularly.

依據前述的濾網結構,各後段管狀吸附材的一外徑可為2.0 mm~9.0 mm。According to the aforementioned filter screen structure, an outer diameter of each rear-stage tubular adsorbent material may be 2.0 mm to 9.0 mm.

依據前述的濾網結構,各後段管狀吸附材的孔道的一內徑可為0.1 mm~4.0 mm。According to the aforementioned filter screen structure, an inner diameter of the pores of the tubular adsorbent material in each rear section may be 0.1 mm to 4.0 mm.

依據前述的濾網結構,後段管狀吸附材之材質可選自由活性碳、沸石、碳分子篩、矽凝膠分子篩、氣凝膠、金屬有機骨架之分子篩、共價有機骨架之分子篩、膨潤土、絲光沸石、海泡石、硼族元素材料、氮族元素材料、金屬、金屬氧化物材料、有機-無機複合材料及鋰型分子篩所組成之群組。According to the aforementioned filter screen structure, the material of the latter tubular adsorbent can be selected from activated carbon, zeolite, carbon molecular sieve, silica gel molecular sieve, aerogel, molecular sieve of metal organic framework, molecular sieve of covalent organic framework, bentonite, mordenite , sepiolite, boron group element material, nitrogen group element material, metal, metal oxide material, organic-inorganic composite material and the group consisting of lithium molecular sieve.

依據前述的濾網結構,管狀吸附材之材質可選自由活性碳、沸石、碳分子篩、矽凝膠分子篩、氣凝膠、金屬有機骨架之分子篩、共價有機骨架之分子篩、膨潤土、絲光沸石、海泡石、硼族元素材料、氮族元素材料、金屬、金屬氧化物材料、有機-無機複合材料及鋰型分子篩所組成之群組。According to the aforementioned filter screen structure, the material of the tubular adsorbent can be selected from activated carbon, zeolite, carbon molecular sieve, silica gel molecular sieve, aerogel, molecular sieve of metal organic framework, molecular sieve of covalent organic framework, bentonite, mordenite, The group consisting of sepiolite, boron group element material, nitrogen group element material, metal, metal oxide material, organic-inorganic composite material and lithium molecular sieve.

下述將更詳細討論本新型各實施方式。然而,此實施方式可為各種新型概念的應用,可被具體實行在各種不同的特定範圍內。特定的實施方式是僅以說明為目的,且不受限於揭露的範圍。此外,為簡化圖式起見,一些習知慣用的結構與元件在圖式中將以簡單示意的方式繪示,並且重複之元件將可能使用相同的編號或類似的編號表示。Various embodiments of the present invention are discussed in greater detail below. However, this embodiment may be the application of various novel concepts, which may be embodied in various specific scopes. The specific embodiments are for illustrative purposes only, and are not intended to limit the scope of the disclosure. In addition, to simplify the drawings, some well-known and conventional structures and elements are shown in a simplified and schematic manner in the drawings, and repeated elements may be denoted by the same numerals or similar numerals.

請參照第1圖,第1圖為本新型一實施方式之濾網結構100的立體示意圖。濾網結構100包含一框體110以及一過濾層(未標號),框體110係呈一長方體狀且圍繞固定過濾層,過濾層包含複數個管狀吸附材120a,且管狀吸附材120a彼此平行排列堆疊。Please refer to FIG. 1 , which is a three-dimensional schematic diagram of a filter screen structure 100 according to an embodiment of the new model. The filter structure 100 includes a frame body 110 and a filter layer (not numbered). The frame body 110 is in the shape of a cuboid and surrounds the fixed filter layer. The filter layer includes a plurality of tubular adsorbents 120a, and the tubular adsorbents 120a are arranged in parallel with each other. stack.

請一併參考第2A圖,第2A圖為第1圖的濾網結構100中一種管狀吸附材120a的立體示意圖。各管狀吸附材120a具有至少一孔道121a,孔道121a係呈軸向穿設,孔道121a用以供流體通過。當流體通過管狀吸附材120a時,流體中的雜質及汙染物會被管狀吸附材120a吸附,藉此達到過濾流體之目的。Please also refer to FIG. 2A . FIG. 2A is a schematic three-dimensional view of a tubular adsorbent 120 a in the filter screen structure 100 of FIG. 1 . Each tubular adsorbent 120a has at least one channel 121a, the channel 121a is axially penetrated, and the channel 121a is used for fluid to pass through. When the fluid passes through the tubular adsorbent 120a, impurities and pollutants in the fluid will be adsorbed by the tubular adsorbent 120a, thereby achieving the purpose of filtering the fluid.

各管狀吸附材120a之孔道121a的一內徑d為0.1 mm~4.0 mm,以確保流體可以順利通過管狀吸附材120a,且通過時不會產生過大的壓損,進而達到節能的效果。各管狀吸附材120a的一長度L可為3 cm~50 cm,其可視濾網結構100之尺寸以及過濾需求而做調整。各管狀吸附材120a的一外徑D可為2.0 mm~9.0 mm,透過調整管狀吸附材120a的內徑d及外徑D之比例,可以改變過濾層中孔道121a的比例,有助於在過濾效果及能源消耗之間取得平衡。An inner diameter d of the channels 121a of each tubular adsorbent 120a is 0.1 mm˜4.0 mm, so as to ensure that the fluid can smoothly pass through the tubular adsorbent 120a without excessive pressure loss, thereby achieving the effect of energy saving. A length L of each tubular adsorbent 120a may be 3 cm˜50 cm, which can be adjusted according to the size of the filter screen structure 100 and the filtering requirements. An outer diameter D of each tubular adsorbent 120a can be 2.0 mm to 9.0 mm. By adjusting the ratio of the inner diameter d to the outer diameter D of the tubular adsorbent 120a, the ratio of the pores 121a in the filter layer can be changed, which is helpful for filtering. Balance between performance and energy consumption.

管狀吸附材120a之材質可依據過濾需求進行選擇,且可選自由活性碳、沸石、碳分子篩、矽凝膠分子篩、氣凝膠、金屬有機骨架之分子篩、共價有機骨架之分子篩、膨潤土(bentonite)、絲光沸石(mordenite)、海泡石(sepiolite)、硼族元素材料、氮族元素材料、金屬、金屬氧化物材料、有機-無機複合材料及鋰型分子篩所組成之群組,使得管狀吸附材120a可以吸附流體中不同的雜質或汙染物,例如粉塵、揮發性有機化合物、酸性物質、鹼性物質、凝結物、摻雜物、水氣或油氣等,且管狀吸附材120a更可以達到抑制流體內微生物生長以及殺菌等效果,惟本新型並不以此為限。The material of the tubular adsorbent 120a can be selected according to filtration requirements, and can be selected from activated carbon, zeolite, carbon molecular sieve, silica gel molecular sieve, aerogel, molecular sieve of metal organic framework, molecular sieve of covalent organic framework, bentonite (bentonite). ), mordenite, sepiolite, boron group element materials, nitrogen group element materials, metals, metal oxide materials, organic-inorganic composite materials and lithium molecular sieves. The material 120a can adsorb different impurities or pollutants in the fluid, such as dust, volatile organic compounds, acidic substances, alkaline substances, condensate, impurities, moisture or oil, etc., and the tubular adsorption material 120a can further inhibit the The effects of microbial growth and sterilization in the fluid, but the present invention is not limited to this.

請參照第2B圖及第2C圖,第2B圖為第1圖的濾網結構100中另一種管狀吸附材120b的立體示意圖,第2C圖為第1圖的濾網結構100中又一種管狀吸附材120c的立體示意圖。各管狀吸附材120b、120c可具有至少三所述孔道121b、121c,孔道121b、121c之其中一者的一中心軸可與對應的管狀吸附材120b、120c的一中心軸為平行,其餘的孔道121b、121c可圍繞所述其中一孔道121b、121c並呈等角分布。在第2B圖中,係以六個孔道121b為例,其中五孔道121b可將另一孔道121b作為中心並呈等角分布。在第2C圖中,係以七個孔道121c為例,其中六孔道121c可將另一孔道121c作為中心並呈等角分布。值得注意的是,過濾層中可以同時堆疊不同孔道數量的管狀吸附材,且適當的孔道數量可以增加吸附表面積,進而提升過濾效率。Please refer to FIGS. 2B and 2C. FIG. 2B is a three-dimensional schematic diagram of another tubular adsorption material 120b in the filter screen structure 100 of FIG. 1, and FIG. 2C is another tubular adsorption material in the filter screen structure 100 of FIG. 1. A perspective view of the material 120c. Each tubular adsorbent 120b, 120c may have at least three of the pores 121b, 121c, a central axis of one of the pores 121b, 121c may be parallel to a central axis of the corresponding tubular adsorbent 120b, 120c, and the rest of the pores The 121b and 121c may surround the one of the holes 121b and 121c and be distributed equiangularly. In FIG. 2B, the six holes 121b are taken as an example, among which the five holes 121b can be equiangularly distributed with the other hole 121b as the center. In FIG. 2C, the seven holes 121c are taken as an example, and the six holes 121c can be equiangularly distributed with another hole 121c as the center. It is worth noting that tubular adsorbents with different numbers of channels can be stacked in the filter layer at the same time, and the appropriate number of channels can increase the adsorption surface area, thereby improving the filtration efficiency.

請參照第3圖,第3圖為本新型另一實施方式之濾網結構200的立體示意圖。濾網結構200與前述之濾網結構100相似,其差異在於,濾網結構200更可包含至少一後段過濾層,在第3圖中,係以二後段過濾層(未標號)為例,惟本新型並不以此為限。框體210可圍繞固定後段過濾層,後段過濾層則可設於過濾層之一側。藉此,後段過濾層可以對通過過濾層的流體再次進行過濾,後段過濾層之材質及孔隙度皆可調整,且無須與過濾層之材質及孔隙度相同,以利去除不同雜質或汙染物,並調控流體通過過濾層及後段過濾層的速度,進而達到所需的過濾效果。Please refer to FIG. 3 . FIG. 3 is a three-dimensional schematic diagram of a filter screen structure 200 according to another embodiment of the novel. The filter screen structure 200 is similar to the aforementioned filter screen structure 100, the difference is that the filter screen structure 200 can further include at least one rear filter layer. The present invention is not limited to this. The frame body 210 can surround and fix the rear filter layer, and the rear filter layer can be arranged on one side of the filter layer. In this way, the rear filter layer can filter the fluid passing through the filter layer again, and the material and porosity of the rear filter layer can be adjusted, and the material and porosity of the rear filter layer do not need to be the same as those of the filter layer, so as to facilitate the removal of different impurities or pollutants. And the speed of the fluid passing through the filter layer and the rear filter layer is regulated to achieve the desired filtering effect.

後段過濾層可包含至少一管狀吸附材層或一纖維狀吸附材層,在此以一管狀吸附材層(未標號)與一纖維狀吸附材層240為例。請特別注意,於實際應用時,可任意調整後段管狀吸附材與纖維狀吸附材的設置範圍,且單一後段過濾層亦可同時包含後段管狀吸附材與纖維狀吸附材,是以本新型並不以第3圖的示例為限。The rear filter layer may include at least one tubular adsorbent layer or one fibrous adsorbent layer, a tubular adsorbent layer (not numbered) and a fibrous adsorbent layer 240 are used as examples here. Please pay special attention that in practical application, the setting range of the rear-stage tubular adsorbent and fibrous adsorbent can be adjusted arbitrarily, and a single rear-stage filter layer can also include the rear-stage tubular adsorbent and fibrous adsorbent at the same time, so this new model does not This is limited to the example in Figure 3.

管狀吸附材層可包含複數個後段管狀吸附材230,後段管狀吸附材230可彼此平行排列堆疊,各後段管狀吸附材230的結構及材質可與過濾層中的管狀吸附材220相同,亦即各後段管狀吸附材230可具有單一孔道或多個孔道之結構,故於此不再贅述。各後段管狀吸附材230的一中心軸可與過濾層中各管狀吸附材220的一中心軸為平行,以確保流體以最短路徑進入後段管狀吸附材230,有助於減少能源消耗。The tubular adsorbent material layer may include a plurality of rear-stage tubular adsorbent materials 230, and the rear-stage tubular adsorbent materials 230 may be arranged and stacked in parallel with each other. The rear-stage tubular adsorbent 230 may have a structure of a single channel or a plurality of channels, so it will not be repeated here. A central axis of each tubular adsorbent 230 in the rear section can be parallel to a central axis of each tubular adsorbent 220 in the filter layer, so as to ensure that the fluid enters the tubular adsorbent 230 in the shortest path, which helps to reduce energy consumption.

請參照第4圖,第4圖為第3圖的濾網結構200中纖維狀吸附材層240的立體示意圖。纖維狀吸附材層240可由複數條纖維241編織而成,呈網狀交織型態,並形成複數個孔洞供流體通過,纖維狀吸附材層240的編織方式、編織密度以及纖維241粗細等均可視過濾需求而調整,本新型並不以此為限。Please refer to FIG. 4 , which is a schematic perspective view of the fibrous adsorbent layer 240 in the filter screen structure 200 of FIG. 3 . The fibrous adsorbent layer 240 can be woven from a plurality of fibers 241, in a mesh-like interweaving pattern, and forms a plurality of holes for fluid to pass through. It can be adjusted according to the filtering requirements, and the present invention is not limited to this.

以下將針對比較例及第一實施例至第六實施例的濾網結構進行壓損測試。其中,比較例為填充顆粒狀吸附材的習知濾網,而顆粒狀吸附材之外徑約為2.4 mm;第一實施例至第六實施例則是包含不同管狀吸附材的濾網結構,其管狀吸附材的結構參數已列於下表一: 表一 實施例 管狀吸附材結構 孔道數量 孔道內徑 (mm) 管狀吸附材 外徑(mm) 1 0.8 2 1 2.1 4 6 1.7 6.6 7 1.1 5.2 7 1.1 6.2 7 0.85 3.8 In the following, pressure loss tests will be performed on the filter screen structures of the comparative example and the first to sixth embodiments. Among them, the comparative example is a conventional filter screen filled with granular adsorbent materials, and the outer diameter of the granular adsorbent materials is about 2.4 mm; the first to sixth embodiments are filter screen structures including different tubular adsorbent materials, The structural parameters of its tubular adsorbent are listed in Table 1 below: Table I Example Tubular Adsorbent Structure Number of channels Inner diameter of hole (mm) Outer diameter of tubular adsorbent (mm) one 1 0.8 2 two 1 2.1 4 three 6 1.7 6.6 Four 7 1.1 5.2 five 7 1.1 6.2 six 7 0.85 3.8

請參照第5圖,第5圖為比較例與第一實施例的壓損測試圖。由第5圖可以看出,在相同流速下,比較例的壓損大於第一實施例,且當流速越快,比較例與第一實施例之間的壓損差距越明顯,其差距更可達到六倍以上。本新型的濾網結構藉由使用管狀吸附材,可以提供較短的質傳路徑與較大的接觸面積,進而降低能源消耗,並提升流體的過濾效率。Please refer to FIG. 5 , which is a pressure loss test chart of the comparative example and the first embodiment. It can be seen from Figure 5 that under the same flow rate, the pressure loss of the comparative example is greater than that of the first embodiment, and when the flow rate is faster, the pressure loss gap between the comparative example and the first embodiment is more obvious, and the difference is more likely. more than six times. The novel filter screen structure can provide a shorter mass transfer path and a larger contact area by using a tubular adsorbent material, thereby reducing energy consumption and improving fluid filtration efficiency.

再請參照第6圖,第6圖為第二實施例至第六實施例的壓損測試圖。由第6圖可以看出,當管狀吸附材的孔道數量越多(請參考第二實施例、第三實施例及第五實施例之實驗結果)或孔徑越小(請參考第四實施例及第六實施例之實驗結果)時,流體通過時所產生的壓損越大;當管狀吸附材的堆疊密度越高(請參考第四實施例及第五實施例之實驗結果),流體通過時所產生的壓損則會下降。故可以視過濾需求,調整管狀吸附材的內徑及外徑大小,使流體產生不同的壓力變化,進而控制流體通過管狀吸附材的時間以及過濾時所使用的能源,使本新型之濾網結構在使用上更加靈活。Please refer to FIG. 6 again. FIG. 6 is a pressure loss test chart of the second embodiment to the sixth embodiment. As can be seen from Figure 6, when the number of pores of the tubular adsorbent is larger (please refer to the experimental results of the second, third and fifth embodiments) or the pore size is smaller (please refer to the fourth embodiment and The experimental results of the sixth embodiment), the greater the pressure loss generated when the fluid passes; when the stacking density of the tubular adsorbent is higher (please refer to the experimental results of the fourth and fifth embodiments), the fluid passing through The resulting pressure loss will decrease. Therefore, depending on the filtration requirements, the inner diameter and outer diameter of the tubular adsorbent can be adjusted to make the fluid produce different pressure changes, thereby controlling the time for the fluid to pass through the tubular adsorbent and the energy used during filtration. More flexible in use.

綜上所述,本新型之濾網結構使用管狀吸附材,故能在低壓損的情況下達到良好的過濾效果,進而減少能源的使用量,且本新型之濾網結構可以依照需求,透過堆疊不同結構的管狀吸附材,以達成複雜度較高的過濾效果。To sum up, the filter structure of the present invention uses a tubular adsorbent material, so it can achieve a good filtering effect under the condition of low pressure loss, thereby reducing the consumption of energy, and the filter structure of the present invention can be stacked according to requirements. Tubular adsorbents with different structures to achieve a more complex filtration effect.

雖然本新型已以實施例揭露如上,然其並非用以限定本新型,任何熟習此技藝者,在不脫離本新型之精神和範圍內,當可作各種之更動與潤飾,因此本新型之保護範圍當視後附之申請專利範圍所界定者為準。Although the present invention has been disclosed by the above examples, it is not intended to limit the present invention. Anyone who is familiar with this technology can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the protection of the present invention The scope shall be determined by the scope of the appended patent application.

100,200:濾網結構 110,210:框體 120a,120b,120c,220:管狀吸附材 121a,121b,121c:孔道 230:後段管狀吸附材 240:纖維狀吸附材層 241:纖維 d:內徑 L:長度 D:外徑 100,200: Filter structure 110,210: Frame 120a, 120b, 120c, 220: Tubular adsorbents 121a, 121b, 121c: Orifice 230: Tubular absorbent material in the rear section 240: fibrous adsorbent layer 241: Fiber d: inner diameter L: length D: outer diameter

為讓本新型之上述和其他目的、特徵、優點與實施例能更明顯易懂,所附圖式之說明如下: 第1圖為本新型一實施方式之濾網結構的立體示意圖; 第2A圖為第1圖的濾網結構中一種管狀吸附材的立體示意圖; 第2B圖為第1圖的濾網結構中另一種管狀吸附材的立體示意圖; 第2C圖為第1圖的濾網結構中又一種管狀吸附材的立體示意圖; 第3圖為本新型另一實施方式之濾網結構的立體示意圖; 第4圖為第3圖的濾網結構中一纖維狀吸附材層的立體示意圖; 第5圖為比較例與第一實施例的壓損測試圖;以及 第6圖為第二實施例至第六實施例的壓損測試圖。 In order to make the above-mentioned and other objects, features, advantages and embodiments of the present invention more clearly understood, the accompanying drawings are described as follows: FIG. 1 is a three-dimensional schematic diagram of a filter screen structure according to an embodiment of the new model; FIG. 2A is a schematic perspective view of a tubular adsorbent in the filter screen structure of FIG. 1; Fig. 2B is a perspective view of another tubular adsorbent in the filter screen structure of Fig. 1; FIG. 2C is a schematic perspective view of another tubular adsorbent in the filter screen structure of FIG. 1; FIG. 3 is a three-dimensional schematic diagram of a filter screen structure according to another embodiment of the new model; FIG. 4 is a schematic perspective view of a fibrous adsorbent layer in the filter screen structure of FIG. 3; FIG. 5 is a pressure loss test chart of the comparative example and the first embodiment; and FIG. 6 is a pressure loss test chart of the second embodiment to the sixth embodiment.

100:濾網結構 100: Filter structure

110:框體 110: Frame

120a:管狀吸附材 120a: Tubular adsorbent

Claims (12)

一種濾網結構,其包含: 一框體,係呈一長方體狀;以及 一過濾層,該框體圍繞固定該過濾層; 其中,該過濾層包含複數個管狀吸附材,該些管狀吸附材彼此平行排列堆疊,各該管狀吸附材具有至少一孔道,且該孔道係呈軸向穿設; 其中,該孔道的一內徑為0.1 mm~4.0 mm。 A filter structure, which includes: a frame body in the shape of a rectangular parallelepiped; and a filter layer, and the frame body surrounds and fixes the filter layer; Wherein, the filter layer includes a plurality of tubular adsorbents, the tubular adsorbents are arranged and stacked in parallel with each other, each of the tubular adsorbents has at least one channel, and the channel is axially penetrated; Wherein, an inner diameter of the hole is 0.1 mm to 4.0 mm. 如請求項1所述之濾網結構,其中各該管狀吸附材的一長度為3 cm~50 cm。The filter screen structure according to claim 1, wherein a length of each of the tubular adsorbents is 3 cm to 50 cm. 如請求項1所述之濾網結構,其中各該管狀吸附材具有至少三該孔道,該些孔道之其中一者的一中心軸與對應的該管狀吸附材的一中心軸為平行,其餘的該些孔道圍繞該其中一孔道並呈等角分布。The filter structure according to claim 1, wherein each of the tubular adsorbents has at least three of the pores, a central axis of one of the pores is parallel to a central axis of the corresponding tubular adsorbent, and the rest The channels surround one of the channels and are equiangularly distributed. 如請求項1所述之濾網結構,其中各該管狀吸附材的一外徑為2.0 mm~9.0 mm。The filter screen structure according to claim 1, wherein an outer diameter of each of the tubular adsorbents is 2.0 mm to 9.0 mm. 如請求項1所述之濾網結構,更包含至少一後段過濾層,該框體圍繞固定該後段過濾層,該後段過濾層設於該過濾層之一側; 其中,該後段過濾層包含至少一管狀吸附材層或一纖維狀吸附材層。 The filter screen structure according to claim 1, further comprising at least one rear filter layer, the frame body surrounds and fixes the rear filter layer, and the rear filter layer is arranged on one side of the filter layer; Wherein, the rear filter layer includes at least one tubular adsorption material layer or a fibrous adsorption material layer. 如請求項5所述之濾網結構,其中該纖維狀吸附材層為網狀交織型態。The filter screen structure as claimed in claim 5, wherein the fibrous adsorbent layer is in the form of mesh interweaving. 如請求項5所述之濾網結構,其中該管狀吸附材層包含複數個後段管狀吸附材,該些後段管狀吸附材彼此平行排列堆疊,且各該後段管狀吸附材具有至少一孔道呈軸向穿設。The filter screen structure according to claim 5, wherein the tubular adsorbent material layer comprises a plurality of rear-stage tubular adsorbent materials, the rear-stage tubular adsorbent materials are arranged and stacked in parallel with each other, and each of the rear-stage tubular adsorbent materials has at least one channel in the axial direction. wear. 如請求項7所述之濾網結構,其中各該後段管狀吸附材具有至少三該孔道,各該後段管狀吸附材的該些孔道之其中一者的一中心軸與對應的該後段管狀吸附材的一中心軸為平行,各該後段管狀吸附材中其餘的該些孔道圍繞該其中一孔道並呈等角分布。The filter structure according to claim 7, wherein each of the rear-stage tubular adsorbents has at least three of the pores, and a central axis of one of the pores of each of the rear-stage tubular adsorbents corresponds to the rear-stage tubular adsorbent. A central axis of the tube is parallel, and the remaining pores in each of the rear tubular adsorbents surround one of the pores and are equiangularly distributed. 如請求項7所述之濾網結構,其中各該後段管狀吸附材的一外徑為2.0 mm~9.0 mm。The filter screen structure according to claim 7, wherein an outer diameter of each of the rear tubular adsorbents is 2.0 mm to 9.0 mm. 如請求項7所述之濾網結構,其中各該後段管狀吸附材的該孔道的一內徑為0.1 mm~4.0 mm。The filter screen structure according to claim 7, wherein an inner diameter of the pores of each of the rear-section tubular adsorbent materials is 0.1 mm to 4.0 mm. 如請求項7所述之濾網結構,其中該些後段管狀吸附材之材質係選自由活性碳、沸石、碳分子篩、矽凝膠分子篩、氣凝膠、金屬有機骨架之分子篩、共價有機骨架之分子篩、膨潤土、絲光沸石、海泡石、硼族元素材料、氮族元素材料、金屬、金屬氧化物材料、有機-無機複合材料及鋰型分子篩所組成之群組。The filter screen structure according to claim 7, wherein the material of the latter tubular adsorbent is selected from activated carbon, zeolite, carbon molecular sieve, silica gel molecular sieve, aerogel, molecular sieve of metal organic framework, covalent organic framework The group consisting of molecular sieve, bentonite, mordenite, sepiolite, boron group element material, nitrogen group element material, metal, metal oxide material, organic-inorganic composite material and lithium molecular sieve. 如請求項1所述之濾網結構,其中該些管狀吸附材之材質係選自由活性碳、沸石、碳分子篩、矽凝膠分子篩、氣凝膠、金屬有機骨架之分子篩、共價有機骨架之分子篩、膨潤土、絲光沸石、海泡石、硼族元素材料、氮族元素材料、金屬、金屬氧化物材料、有機-無機複合材料及鋰型分子篩所組成之群組。The filter screen structure according to claim 1, wherein the material of the tubular adsorbents is selected from activated carbon, zeolite, carbon molecular sieve, silica gel molecular sieve, aerogel, molecular sieve of metal organic framework, and molecular sieve of covalent organic framework. The group consisting of molecular sieve, bentonite, mordenite, sepiolite, boron group element material, nitrogen group element material, metal, metal oxide material, organic-inorganic composite material and lithium molecular sieve.
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