JPH082409B2 - Deodorizing filter for air conditioner - Google Patents
Deodorizing filter for air conditionerInfo
- Publication number
- JPH082409B2 JPH082409B2 JP1258748A JP25874889A JPH082409B2 JP H082409 B2 JPH082409 B2 JP H082409B2 JP 1258748 A JP1258748 A JP 1258748A JP 25874889 A JP25874889 A JP 25874889A JP H082409 B2 JPH082409 B2 JP H082409B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- activated carbon
- air conditioner
- substrate
- deodorizing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 230000001877 deodorizing effect Effects 0.000 title claims description 39
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 98
- 239000002245 particle Substances 0.000 claims description 39
- 239000000758 substrate Substances 0.000 claims description 33
- 239000000853 adhesive Substances 0.000 claims description 14
- 230000001070 adhesive effect Effects 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 6
- 239000000839 emulsion Substances 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 claims 1
- 230000003647 oxidation Effects 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- 210000004027 cell Anatomy 0.000 description 33
- 239000003463 adsorbent Substances 0.000 description 20
- 235000019645 odor Nutrition 0.000 description 9
- 239000000123 paper Substances 0.000 description 8
- 239000011230 binding agent Substances 0.000 description 7
- 238000004332 deodorization Methods 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 230000001953 sensory effect Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 235000019504 cigarettes Nutrition 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 210000004128 D cell Anatomy 0.000 description 1
- 239000004820 Pressure-sensitive adhesive Substances 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 210000003719 b-lymphocyte Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 238000011990 functional testing Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000000979 retarding effect Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 230000008786 sensory perception of smell Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Treating Waste Gases (AREA)
- Separation Of Gases By Adsorption (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明はエアコンディショナ用脱臭フィルタ及びこれ
を具備するエアコンディショナに関し、より具体的には
圧力損失の低いこの種フィルタ及びこれを具備するエア
コンディショナに関する。Description: TECHNICAL FIELD The present invention relates to a deodorizing filter for an air conditioner and an air conditioner including the same, and more specifically, to a filter of this type having a low pressure loss and the same. Regarding air conditioners.
[従来の技術] 従来のエアコンディショナには粗目の除塵フィルタし
か装着されていないのが一般的であり、同フィルタの圧
力損失は0.1−0.2mmAq(エア流速1m/secにおける測定
値、以下同じ)程度であった。これに対して近年たばこ
の煙り、花粉等のサブミクロン粒子を除去する要望が強
くなったことから、圧力損失2−3mmAq程度の高密度の
フィルタがオプショナルに使用されるようになった。し
かし上記高密度のフィルタの使用は、圧力損失が大きい
ことから、これに起因して、風量が低下する、或いは騒
音が大きくなる等の問題が生じた。そこでこの問題に対
応する為、電気集塵機や、エレクトレット繊維(半永久
的に分極されたポリオレフィン系繊維、特公昭56−4729
9等に開示される)を用いたフィルタ等の、低圧力損失
の除塵機構が用いられるようになった。[Prior Art] A conventional air conditioner is generally equipped only with a coarse dust removal filter, and the pressure loss of the filter is 0.1-0.2 mmAq (measured value at an air velocity of 1 m / sec, the same below. ) Was about. On the other hand, in recent years, there has been a strong demand for removing submicron particles such as cigarette smoke and pollen, so that a high-density filter with a pressure loss of about 2 to 3 mmAq has been optionally used. However, since the use of the above-mentioned high-density filter causes a large pressure loss, it causes a problem such as a decrease in air volume or an increase in noise. Therefore, in order to address this problem, electrostatic precipitators and electret fibers (semi-permanently polarized polyolefin fibers, JP-B-56-4729) are used.
The dust removal mechanism with low pressure loss has come to be used, such as a filter using the above (disclosed in 9 etc.).
上記低圧力損失の除塵機構はしかし、本来的に脱臭を
目的とするものではない為、その脱臭能力は低い。However, since the dust removal mechanism with low pressure loss is not originally intended for deodorization, its deodorizing ability is low.
他方、活性炭が接着されたフィルタは従来より種々の
タイプのものが提案されている。例えば、1)特公昭59
−19727、特開昭53−64675、実開昭57−119724等には、
微粉状活性炭を抄紙段階で紙に混抄させ、ハニカム或い
は片段ボール積層状に成形したフィルタが開示される。
2)特開昭58−175560、特開昭63−88014、実開昭62−7
9522等には、繊維状活性炭をハニカム状に成形したフィ
ルタが開示される。3)特開昭57−48325、特開昭59−1
42843、特開昭59−227704等には、粉末活性炭とバイン
ダとの混合物を押出して格子状またはハニカム状とし、
これを焼成して活性化したフィルタが開示される。On the other hand, various types of filters to which activated carbon is adhered have been conventionally proposed. For example, 1) Japanese Patent Publication Sho 59
-19727, Japanese Patent Laid-Open No. 53-64675 and Japanese Utility Model Laid-Open No. 57-119724,
A filter is disclosed in which finely powdered activated carbon is mixed with paper at the papermaking stage and formed into a honeycomb or a single corrugated cardboard laminate.
2) JP-A-58-175560, JP-A-63-88014, and JP-A-62-7
9522 and the like disclose a filter in which fibrous activated carbon is formed into a honeycomb shape. 3) JP-A-57-48325 and JP-A-59-1
42843, JP-A-59-227704 and the like, a mixture of powdered activated carbon and a binder is extruded into a lattice shape or a honeycomb shape,
A filter is disclosed which is activated by firing it.
[発明が解決しようとする課題] 上記1のフィルタは、活性炭の使用量が上げられず、
また紙の表面で有効に脱臭に寄与している活性炭が少な
く、脱臭効果が低い。上記2のフィルタは、繊維状活性
炭が高価で大量に使えず、また繊維状活性炭は吸着速度
は高いが脱臭も速く、直ぐにフィルタから臭気が漏れて
くるという欠点がある。上記3のフィルタは、脱臭効果
は高いがフィルタ自体が高価であり、また成形時に歪み
が生じるので広い面積に使用できない。従って、エアコ
ンディショナに使用するのに適当な脱臭フィルタは見出
だすことができない。[Problems to be Solved by the Invention] In the above filter 1, the amount of activated carbon used cannot be increased,
In addition, the amount of activated carbon that effectively contributes to deodorization on the surface of paper is small, and the deodorization effect is low. The filter of the above-mentioned 2 has a drawback that fibrous activated carbon is expensive and cannot be used in a large amount, and that fibrous activated carbon has a high adsorption rate but also a quick deodorization, so that an odor immediately leaks from the filter. The above-mentioned filter 3 has a high deodorizing effect, but the filter itself is expensive, and since distortion occurs during molding, it cannot be used in a wide area. Therefore, a deodorizing filter suitable for use in an air conditioner cannot be found.
本発明はかかる観点に基づいてなされたものであり、
上記除塵機構と併用若しくは単独で使用でき、且つ低圧
力損失(1.0mmAq以下、望ましくは0.5mmAq以下)で、煙
草の臭い等の室内臭気を脱臭できるエアコンディショナ
用の脱臭フィルタを提供することを目的とする。The present invention has been made based on such a viewpoint,
It is possible to provide a deodorizing filter for an air conditioner which can be used together with the above dust removing mechanism or can be used alone and has a low pressure loss (1.0 mmAq or less, preferably 0.5 mmAq or less) and can deodorize indoor odors such as cigarette odor. To aim.
[課題を解決する為の手段] 上記目的を達成する為、本発明の脱臭フィルタは、格
子状のフィルタ基体と前記基体に接着された活性炭粒子
とを有するフィルタであって、前記活性炭粒子が粘着剤
により前記基体の表面に添着されることと、前記活性炭
粒子が、触媒を担持しない状態で、脱臭効果を目的とし
て使用されることと、を特徴とする。[Means for Solving the Problems] In order to achieve the above object, the deodorizing filter of the present invention is a filter having a lattice-shaped filter substrate and activated carbon particles adhered to the substrate, wherein the activated carbon particles are adhered. It is characterized in that it is attached to the surface of the substrate with an agent, and that the activated carbon particles are used for the purpose of a deodorizing effect in the state where they do not carry a catalyst.
[作用] 上記構成により本発明に係る脱臭フィルタによれば、
上記エア流速条件において1.0mmAq以下の圧力損失を達
成することが可能となる。また本脱臭フィルタの脱臭効
果は脱臭フィルタとしての一般的条件に適うものとな
り、脱臭効果の継続性はエアコンディショナに対して使
用されるフィルタとしての条件に適うものとなる。[Operation] According to the deodorizing filter of the present invention having the above configuration,
It is possible to achieve a pressure loss of 1.0 mmAq or less under the above air flow rate conditions. Further, the deodorizing effect of the present deodorizing filter meets the general conditions as a deodorizing filter, and the continuity of the deodorizing effect meets the conditions as a filter used for an air conditioner.
[実施例] 構造及び材質 第1図は本発明に係る脱臭フィルタ10の一実施例を示
す平面図である。このフィルタは、格子状のフィルタ基
体12と、フィルタ基体12に接着されたガス吸着剤粒子14
とからなる。[Embodiment] Structure and Material FIG. 1 is a plan view showing an embodiment of the deodorizing filter 10 according to the present invention. This filter includes a grid-shaped filter base 12 and gas adsorbent particles 14 adhered to the filter base 12.
Consists of
本発明に係る脱臭フィルタ10は開口率(第1図の紙面
に対して平行な平面における)が約50−約80%で、この
値は後述する種々の条件に従う結果として得られる。ま
たフィルタ10の厚さ(第1図の紙面に対して垂直な方
向)は15mm以下で望ましくは約3mm以上となっている。
本フィルタ10は、第1図図示の如くガス吸着剤粒子14の
寸法が比較的大きく、またフィルタ10の厚さが小さい点
で、従来のフィルタと異なる。これらの特徴は、エアコ
ンディショナ用の脱臭フィルタとして、低圧力損失、適
当な脱臭能力、長寿命等の条件を満たす為の鍵となる。The deodorizing filter 10 according to the present invention has an aperture ratio (in a plane parallel to the paper surface of FIG. 1) of about 50 to about 80%, which is obtained as a result of complying with various conditions described later. The thickness of the filter 10 (direction perpendicular to the paper surface of FIG. 1) is 15 mm or less, preferably about 3 mm or more.
The present filter 10 is different from the conventional filter in that the size of the gas adsorbent particles 14 is relatively large and the thickness of the filter 10 is small as shown in FIG. These features are key to satisfying conditions such as low pressure loss, appropriate deodorizing ability, and long life as a deodorizing filter for an air conditioner.
基体12は、紙、アルミ、プラスチック等の薄肉の材料
からなる。紙を材料として用いる場合は、フェノール樹
脂等を含浸させて強度を補強することもできる。また基
体12には難燃化処理を施すこともできる。基体12の厚さ
は実質的に本フィルタ10の厚さとなるから、約15mm以下
で望ましくは3mm以上となる。この厚さは、本フィルタ1
0が最終的に第2図図示の如くエアコンディショナの筐
体内に収納されることから決定される。The base 12 is made of a thin material such as paper, aluminum or plastic. When paper is used as the material, it can be impregnated with a phenol resin or the like to reinforce the strength. Further, the substrate 12 can be subjected to flame retarding treatment. Since the thickness of the substrate 12 is substantially the same as the thickness of the filter 10, it is about 15 mm or less, preferably 3 mm or more. This thickness is for this filter 1
0 is finally determined because it is stored in the housing of the air conditioner as shown in FIG.
図示実施例において、基体12の格子のパターン形状は
6角形のいわゆるハニカム状となっているが、このパタ
ーン形状は、例えば矩形、3角形等いかなる形状とする
こともできる。但し、格子の1つのセル16の平面積(第
1図の紙面に対して平行な平面における)は約0.20−約
0.35cm2となる。この数値は、ガス吸着剤粒子14を支持
する為の区画壁18の密度を実質的に意味することとな
る。この数値の選択理由は後述する。In the illustrated embodiment, the lattice pattern of the base 12 is a hexagonal so-called honeycomb shape, but this pattern can be any shape such as a rectangle and a triangle. However, the plane area of one cell 16 of the grid (in the plane parallel to the paper surface of FIG. 1) is about 0.20-about
It becomes 0.35 cm 2 . This numerical value substantially means the density of the partition wall 18 for supporting the gas adsorbent particles 14. The reason for selecting this numerical value will be described later.
ガス吸着剤粒子14は活性炭からなるが、添着活性炭等
他のタイプのものを使用することも可能である。また石
油ストーブ等室内のCO発生源に対処する為、COを接触酸
化処理できる触媒を脱臭剤と併用することができる。こ
の触媒としては、水分があっても死活しない金/酸化物
触媒(特開昭60−238148等で開示される)が望ましい。The gas adsorbent particles 14 are made of activated carbon, but other types such as impregnated activated carbon can also be used. In addition, in order to deal with CO generation sources such as petroleum stoves, a catalyst capable of catalytically oxidizing CO can be used in combination with a deodorant. As this catalyst, a gold / oxide catalyst (disclosed in JP-A-60-238148, etc.) that does not die and activate even in the presence of water is desirable.
ガス吸着剤粒子14の寸法は約20−約60メッシュ、基体
12の平面単位面積当りのガス吸着剤粒子14の使用量は約
400−約2000g/m2である。この数値の選択理由は後述す
る。The size of the gas adsorbent particles 14 is about 20 to about 60 mesh, the substrate
The amount of gas adsorbent particles 14 used per unit area of 12 planes is approximately
400-about 2000 g / m 2 . The reason for selecting this numerical value will be described later.
ガス吸着剤粒子14を基体12に接着する為のバインダ
は、粒子の脱落を防止する為に粘着剤が使用されること
が望ましい。上記バインダは、フィルタ製造時に、ブラ
ンク基体に供された後に乾燥され、粘性が高められる。
上記乾燥作業により溶媒の匂いが飛び、活性炭が溶媒の
匂いを吸着しなくなる。As the binder for adhering the gas adsorbent particles 14 to the base 12, it is desirable to use a pressure-sensitive adhesive in order to prevent the particles from falling off. When the filter is manufactured, the binder is dried on the blank substrate and then dried to increase its viscosity.
The odor of the solvent is blown off by the above-mentioned drying operation, and the activated carbon does not adsorb the odor of the solvent.
望ましくは本フィルタ10は、ガス吸着剤粒子14の粒径
よりも目の細かな不織布、紙等で形成された通気性カバ
ー(図示せず)により覆って使用するようにする。この
通気性カバーにはまた不燃化処理、防黴、防菌処理を施
すことが望ましい。Desirably, the filter 10 is used by being covered with a breathable cover (not shown) formed of a non-woven fabric, paper or the like having a finer grain size than the gas adsorbent particles 14. It is desirable that the breathable cover is also subjected to a non-combustible treatment, a mildew-proof treatment, and a germ-proof treatment.
使用態様 第2図は本フィルタ10をエアコンディショナの室内機
30の筐体32内に組込んだ状態を示す側面図である。図中
矢印はエアの流れ方向を示す。本フィルタ10は、通常用
いられている防塵フィルタ34に続いて、エアの導入通路
に配設される。本フィルタ10を通過して脱臭されたエア
は、熱交換器36で加熱若しくは冷却され、送風機40の作
用により室内に供給される。本フィルタ10はまた、エア
の導入通路の代わりに、熱交換器36後のエアの排出通路
に配設することも可能である。なお図中符号38は露受け
皿である。Usage mode Fig. 2 shows this filter 10 as an indoor unit of an air conditioner.
FIG. 4 is a side view showing a state where the device is incorporated into a housing 32 of 30. The arrow in the figure indicates the direction of air flow. The filter 10 is provided in the air introduction passage subsequent to the dust filter 34 that is normally used. The air that has passed through the filter 10 and is deodorized is heated or cooled by the heat exchanger 36, and is supplied indoors by the action of the blower 40. The filter 10 can also be arranged in the air discharge passage after the heat exchanger 36, instead of the air introduction passage. Reference numeral 38 in the figure is a dew tray.
製造方法 第3図は本フィルタ10の製造工程の一例を示す図であ
る。先ず基体供給機52から所定の厚さのブランク基体が
供給され、バインダ浸漬部54において、粘着剤が全体に
塗布される。次にブランク基体は10分間程度乾燥機56に
掛けられ、バインダに所定の粘性が付与されると共に、
バインダの溶剤の匂いが飛ばされる。乾燥後、ブランク
基体は吸着剤添着部62に送込まれる。Manufacturing Method FIG. 3 is a diagram showing an example of a manufacturing process of the filter 10. First, a blank substrate having a predetermined thickness is supplied from the substrate feeder 52, and the adhesive is applied to the whole in the binder dipping portion 54. Next, the blank substrate is put on a dryer 56 for about 10 minutes to give a predetermined viscosity to the binder,
The odor of the binder solvent is blown off. After drying, the blank substrate is sent to the adsorbent impregnation section 62.
他方、吸着剤添着部62に対しては、吸着剤供給機58か
ら所定サイズの吸着剤が供給され、ブランク基体表面に
バインダを介して接着される。次に、基体や吸着剤に不
完全に付着している余分な吸着剤は払落とし部64で除去
される。そして上記吸着剤が十分に基体に接着した後、
切断機66により1次製品の基体が所望の寸法に切断さ
れ、最終製品フィルタ10が完成となる。またその後必要
に応じ、包装部68でフィルタ10の両面或いは片面に通気
性カバーを積層させてもよい。On the other hand, an adsorbent of a predetermined size is supplied from the adsorbent supplier 58 to the adsorbent impregnating portion 62, and the adsorbent is bonded to the blank substrate surface via a binder. Next, the excess adsorbent that is incompletely attached to the substrate or the adsorbent is removed by the scrubbing section 64. And after the adsorbent has sufficiently adhered to the substrate,
The cutting machine 66 cuts the substrate of the primary product to a desired size, and the final product filter 10 is completed. Further, after that, a breathable cover may be laminated on both surfaces or one surface of the filter 10 in the packaging section 68, if necessary.
本脱臭フィルタの機能試験の方法 脱臭フィルタの圧力損失の測定は、内寸10×10cm、長
さ220cmの角形透明アクリル製風胴を用い、この中央部
に脱臭フィルタを装着して行った。フィルタの通過風速
は1.0m/secとし、フィルタ前後の静圧差を測定した。Method of functional test of this deodorizing filter The pressure loss of the deodorizing filter was measured by using a square transparent acrylic wind tunnel with an inner size of 10 × 10 cm and a length of 220 cm, and mounting the deodorizing filter in the center. The air velocity passing through the filter was 1.0 m / sec, and the static pressure difference before and after the filter was measured.
また脱臭効果を確認する為の官能試験に関しては次の
通りである。先ず容積が17m3のステンレス鋼製チャンバ
内において、2本の市販の煙草を自然燃焼させた。15分
後にチャンバ内の扇風機を作動させ、内部を均一な状態
にした後、市販の空気清浄機のフィルタ装着部に本脱臭
フィルタを取付けて運転を行った。フィルタの開口部は
0.065m2、処理風量は3.9m3/minである。空気清浄機運転
開始30分後に、チャンバ内の空気を無臭の10リットル容
量プラスチックバッグに捕集し、官能試験に供した。官
能試験は予め嗅覚異常者を除外した15名により行われ
た。The sensory test for confirming the deodorizing effect is as follows. First, two commercially available cigarettes were spontaneously burned in a stainless steel chamber having a volume of 17 m 3 . After 15 minutes, the fan in the chamber was operated to make the inside uniform, and the deodorizing filter was attached to the filter mounting portion of the commercially available air purifier to perform the operation. The opening of the filter
The amount of treated air is 0.065m 2 and 3.9m 3 / min. Thirty minutes after the start of the operation of the air purifier, the air in the chamber was collected in an odorless plastic bag of 10 liter capacity and subjected to a sensory test. The sensory test was conducted by 15 people excluding those with abnormal olfaction in advance.
またCO濃度の低減効果に関しては次の通りである。先
ず上記官能試験と同一のチャンバ内を、CO濃度が100ppm
となるように調整した。次に上記官能試験と同一の空気
清浄機及び条件下において本脱臭フィルタを使用し、CO
濃度の減衰を測定した。使用測定器は、ガステック製CM
2510である。The effect of reducing CO concentration is as follows. First, in the same chamber as the above sensory test, CO concentration is 100ppm.
Was adjusted so that Next, using this deodorizing filter under the same air purifier and conditions as in the above sensory test, CO
The concentration decay was measured. The measuring instrument used is Gastech CM
2510.
本脱臭フィルタの条件の検討 基体12の格子のセルサイズ、ガス吸着剤粒子14の寸法
及びその使用量等の条件は以下の通りに検討した。Examination of Conditions of the Deodorizing Filter The conditions such as the cell size of the lattice of the substrate 12, the size of the gas adsorbent particles 14 and the usage amount thereof were examined as follows.
a.格子のセルサイズ 第5図は格子のセルサイズの変化に基づく活性炭担持
量と圧力損失との関係を示すグラフである。実験に使用
されたフィルタは第3図図示の本発明に係る工程により
製造された。基体12は全て第4図に示すようなハニカム
状の格子構造をなし、厚さは5mmである。格子のセルサ
イズという用語はここでは第4図中の「l」を指示す
る。またガス吸着剤という活性炭が使用された。a. Lattice cell size Fig. 5 is a graph showing the relationship between the amount of activated carbon supported and the pressure loss based on changes in the cell size of the lattice. The filter used in the experiment was manufactured by the process according to the present invention shown in FIG. The base 12 has a honeycomb-shaped lattice structure as shown in FIG. 4 and has a thickness of 5 mm. The term cell size of the lattice here refers to "l" in FIG. In addition, activated carbon called a gas adsorbent was used.
第5図のグラフ中、曲線aは活性炭粒子寸法が32−60
メッシュのフィルタ、曲線bは活性炭粒子寸法が20−42
メッシュのフィルタに関する結果を示す。また曲線Dは
圧力損失一次限界(0.5mmAq)線、直線Lは圧力損失の
二次限界線(1.0mmAq)を示す。In the graph of FIG. 5, the curve a has an activated carbon particle size of 32-60.
Mesh filter, curve b has activated carbon particle size of 20-42
The result about a filter of a mesh is shown. The curve D shows the pressure loss primary limit line (0.5 mmAq), and the straight line L shows the pressure loss secondary limit line (1.0 mmAq).
第5図のグラフ中、各プロット記号が指示するところ
は下記の通りである。In the graph of FIG. 5, the points designated by the plot symbols are as follows.
「×」…セルサイズ3/8 in(セル平面積約0.8cm2) 「△」…セルサイズ1/4 in(セル平面積約0.35cm2) 「○」…セルサイズ3/16 in(セル平面積約0.2cm2) 「□」…セルサイズ1/8 in(セル平面積約0.09cm2) 同図から分かるように、「□」で示されるセルサイズ
1/8 inの基板では、圧力損失が二次限界線Lをも越えて
しまう。他方「×」で示されるセルサイズ3/8 inの基板
では、十分な活性炭担持量が得られない。従って、基板
格子のセルサイズは約1/4−約3/16inの範囲が適当とな
る。前述の如く格子の形状はハニカム状に限定される必
要はない為、上記サイズをセル平面積で表すと、この範
囲は約0.2−約0.35cm2となる。“×”… cell size 3/8 in (cell flat area approx. 0.8 cm 2 ) “△”… cell size 1/4 in (cell flat area approx. 0.35 cm 2 ) “○”… cell size 3/16 in (cell Flat area approx. 0.2 cm 2 ) “□”… Cell size 1/8 in (cell flat area approx. 0.09 cm 2 ) As shown in the figure, the cell size indicated by “□”
With a 1 / 8-inch substrate, the pressure loss exceeds the secondary limit line L. On the other hand, with a substrate having a cell size of 3/8 in, which is indicated by “x”, a sufficient amount of activated carbon cannot be obtained. Therefore, a suitable cell size of the substrate grid is about 1/4 to about 3/16 in. As described above, the shape of the lattice does not have to be limited to the honeycomb shape, and therefore, when the above size is expressed by the cell plane area, this range is about 0.2 to about 0.35 cm 2 .
b.ガス吸着剤の粒子寸法と使用量 第6図は活性炭の粒子寸法の変化に基づく活性炭担持
量と圧力損失との関係を示すグラフである。実験に使用
されたフィルタは第3図図示の本発明に係る工程により
製造された。基体12は全て第4図に示すようなハニカム
状の格子構造をなす。b. Particle size of gas adsorbent and amount used Fig. 6 is a graph showing the relationship between the amount of activated carbon carried and the pressure loss based on changes in the particle size of activated carbon. The filter used in the experiment was manufactured by the process according to the present invention shown in FIG. All the substrates 12 have a honeycomb lattice structure as shown in FIG.
第6図のグラフ中、曲線cはセルサイズ3/16 in(セ
ル平面積約0.2cm2)で厚さ5mmの基板のフィルタ、曲線
dはセルサイズ1/4 in(セル平面積約0.35cm2)で厚さ5
mmの基板のフィルタ、曲線eはセルサイズ3/16 in(セ
ル平面積約0.2cm2)で厚さ10mmの基板のフィルタ、曲線
fはセルサイズ1/4 in(セル平面積約0.35cm2)で厚さ1
0mmの基板のフィルタに関する結果を示す。また直線D
は圧力損失一次限界(0.5mmAq)線、直線Lは圧力損失
の二次限界線(1.0mmAq)を示す。In the graph of FIG. 6, a curve c is a filter of a substrate having a cell size of 3/16 in (cell flat area of about 0.2 cm 2 ) and a thickness of 5 mm, and a curve d is a cell size of 1/4 in (cell flat area of about 0.35 cm). 2 ) with thickness 5
mm substrate filter, curve e is cell size 3/16 in (cell flat area about 0.2 cm 2 ) and thickness 10 mm substrate filter, curve f is cell size 1/4 in (cell flat area about 0.35 cm 2 ) With thickness 1
Results are shown for a filter on a 0 mm substrate. Straight line D
Shows the pressure loss primary limit line (0.5 mmAq), and the straight line L shows the pressure loss secondary limit line (1.0 mmAq).
第6図のグラフ中、各プロット記号が指示するところ
は下記の通りである。In the graph of FIG. 6, the points designated by the plot symbols are as follows.
「×」…粒子寸法60−100メッシュ 「△」…粒子寸法32− 60メッシュ 「○」…粒子寸法20− 42メッシュ 「□」…粒子寸法 6− 10メッシュ 同図から分かるように、「□」で示される6−10メッ
シュの活性炭では、圧力損失が二次限界線Lをも遥かに
越えてしまう。他方「×」で示される60−100メッシュ
の活性炭では、十分な活性炭担持量が得られない。従っ
て、活性炭の粒子寸法は約20−60メッシュの範囲が適当
となる。“×”… Particle size 60-100 mesh “△”… Particle size 32-60 mesh “○”… Particle size 20-42 mesh “□”… Particle size 6-10 mesh As can be seen from the figure, “□” In the case of 6-10 mesh activated carbon represented by, the pressure loss far exceeds the secondary limit line L. On the other hand, a sufficient amount of activated carbon cannot be obtained with the 60-100 mesh activated carbon indicated by "x". Therefore, the particle size of the activated carbon is appropriately in the range of about 20-60 mesh.
また第6図は、基板の全面に活性炭が接着された状態
における、各条件での基体平面単位面積当りの活性炭の
担持量(即ち使用量)が示される。この使用量の範囲
を、フィルタの厚さ15mmまで考慮した場合、上記活性炭
の粒子寸法の範囲における使用量は約2000g/m2以下と考
えられる。また同使用量は、脱臭効果を考慮した場合、
少なくとも約400g/m2必要となる。この値は約3mmの厚さ
の基板における使用量に対応する。Further, FIG. 6 shows the amount of activated carbon supported (that is, the amount used) per unit area of the substrate plane under each condition in a state where the activated carbon is adhered to the entire surface of the substrate. Considering this usage amount range up to the filter thickness of 15 mm, the usage amount in the particle size range of the activated carbon is considered to be about 2000 g / m 2 or less. In addition, the same amount, when considering the deodorizing effect,
At least about 400 g / m 2 is required. This value corresponds to the usage on substrates with a thickness of about 3 mm.
また第6図から、上記本発明に係る活性炭の粒子寸法
の範囲において、基板の厚さの変化により圧力損失は大
きな影響を受けないことが分かる。Further, from FIG. 6, it can be seen that the pressure loss is not significantly affected by the change in the thickness of the substrate within the range of the particle size of the activated carbon according to the present invention.
活性炭の寸法とセルサイズとの関係による脱臭フィル
タの機能評価は第7図に示される通りである。同図中斜
線で示される部分が本発明に係るフィルタの条件範囲と
なる。The functional evaluation of the deodorizing filter based on the relationship between the size of activated carbon and the cell size is shown in FIG. The shaded area in the figure is the condition range of the filter according to the present invention.
例及び機能試験結果 空気清浄機を設置しなかった場合と、本発明の条件範
囲内のフィルタA、B、C、D、Eを取付けた空気清浄
機を用いた場合とについて、脱臭効果の比較を前記官能
試験により行った結果を第2表に示す。同表中の数値
は、6段階臭気強度法(第1表参照)に基づく。下記比
較結果から、1%の危険率で有意差が認められ、本発明
に係るフィルタA−Eの脱臭に対する有効性が証明され
た。Example and Function Test Results Comparison of deodorizing effect between the case where no air cleaner is installed and the case where an air cleaner equipped with filters A, B, C, D and E within the condition range of the present invention is used. Table 2 shows the results of the sensory test. The values in the table are based on the 6-level odor intensity method (see Table 1). From the following comparison results, a significant difference was observed at a risk rate of 1%, demonstrating the effectiveness of the filters A-E according to the present invention for deodorization.
またフィルタEについては、上記CO濃度低減試験も合
わせて行われた。その結果、第8図に示されるように、
フィルタEのCO濃度低減に対する有効性が証明された。
第8図中、曲線hはフィルタEを取付けた場合、曲線i
はフィルタを取付けなかった場合の結果を示す。The filter E was also subjected to the CO concentration reduction test. As a result, as shown in FIG.
The effectiveness of the filter E for reducing the CO concentration was proved.
In FIG. 8, the curve h is the curve i when the filter E is attached.
Shows the result when no filter was attached.
使用したフィルタの製造条件は次の通りである。 The manufacturing conditions of the used filter are as follows.
a.フィルタA、B セルサイズ3/16 in(セル平面積約0.2cm2)、厚さ5mm
の紙製ハニカムコアを手で展張後、市販のエマルジョン
系粘着剤(綜研化学製SKダインE−3008B)の槽中に入
れて粘着剤を塗布した。乾燥機に入れて100℃で2時間
かけて乾燥し、重量を測定したところ、粘着剤の塗布量
は1300g/m2であった。これに市販の活性炭(クラレケミ
カル製GG)の、2種類の粒度(20−42メッシュ、、32−
60メッシュ)のものを添着させた。粒度20−42メッシュ
の活性炭を添着したものをフィルタA、粒度32−60メッ
シュの活性炭を添着したものをフィルタBとした。フィ
ルタA、Bの活性炭使用量は夫々790、600g/m2、圧力損
失は夫々0.43、0.23mmAqであった。a. Filter A, B Cell size 3/16 in (cell flat area approx. 0.2 cm 2 ), thickness 5 mm
The paper-made honeycomb core of No. 1 was spread by hand, and then put in a tank of a commercially available emulsion-based adhesive (SK Dyne E-3008B manufactured by Soken Chemical Industry Co., Ltd.) to apply the adhesive. It was placed in a drier and dried at 100 ° C. for 2 hours, and the weight was measured. As a result, the coating amount of the adhesive was 1300 g / m 2 . There are two types of particle size (20-42 mesh, 32-mesh) of commercially available activated carbon (Kuraray Chemical GG).
(60 mesh) was attached. Filter A was impregnated with activated carbon having a particle size of 20-42 mesh, and filter B was impregnated with activated carbon having a particle size of 32-60 mesh. The amounts of activated carbon used in filters A and B were 790 and 600 g / m 2 , respectively, and the pressure losses were 0.43 and 0.23 mmAq, respectively.
b.フィルタC、D セルサイズ1/4 in(セル平面積約0.35cm2)、厚さ10m
mの展張済みのアルミニウム製ハニカムコアを、市販の
溶剤系粘着剤(綜研化学製SKダインE−1200)の槽中に
入れて粘着剤を塗布した。乾燥機に入れて120℃で3時
間かけて乾燥し、重量を測定したところ、粘着剤の塗布
量は500g/m2であった。これに市販の活性炭(クラレケ
ミカル製GG)の、2種類の粒度(20−42メッシュ、32−
60メッシュ)のものを添着させた。粒度20−42メッシュ
の活性炭を添着したものをフィルタC、粒度32−60メッ
シュの活性炭を添着したものをフィルタDとした。フィ
ルタC、Dの活性炭使用量は夫々1300、1000g/m2、圧力
損失は夫々0.32、0.13mmAqであった。b. Filters C, D Cell size 1/4 in (cell flat area about 0.35 cm 2 ), thickness 10 m
The spread aluminum honeycomb core of m was placed in a tank of a commercially available solvent-based adhesive (SK Dyne E-1200 manufactured by Soken Chemical Co., Ltd.) to apply the adhesive. It was placed in a drier and dried at 120 ° C. for 3 hours, and the weight was measured. As a result, the coating amount of the adhesive was 500 g / m 2 . Two types of particle size (20-42 mesh, 32-
(60 mesh) was attached. Filter C was prepared by impregnating activated carbon having a particle size of 20-42 mesh, and filter D was prepared by impregnating activated carbon having a particle size of 32-60 mesh. The amounts of activated carbon used in filters C and D were 1300 and 1000 g / m 2 , respectively, and the pressure loss was 0.32 and 0.13 mmAq, respectively.
c.フィルタE セルサイズ3/16 in(セル平面積約0.2cm2)、厚さ10m
mの展張済みのアルミニウム製ハニカムコアを、市販の
溶剤系粘着剤(綜研化学製SKダインE−1200)の槽中に
入れて粘着剤を塗布した。乾燥機に入れて100℃で2時
間かけて乾燥し、重量を測定したところ、粘着剤の塗布
量は600g/m2であった。これに夫々粒度20−42メッシュ
の市販の活性炭(クラレケミカル製GG)と、金/酸化物
触媒(東洋CCI製)とを体積比で8:2の割合で添着させ
た。活性炭の使用量は約1200g/m2、圧力損失は0.59mmAq
であった。c. Filter E Cell size 3/16 in (cell flat area 0.2 cm 2 ), thickness 10 m
The spread aluminum honeycomb core of m was placed in a tank of a commercially available solvent-based adhesive (SK Dyne E-1200 manufactured by Soken Chemical Co., Ltd.) to apply the adhesive. It was placed in a drier and dried at 100 ° C. for 2 hours, and the weight was measured. As a result, the coating amount of the adhesive was 600 g / m 2 . Commercially available activated carbon (GG manufactured by Kuraray Chemical Co., Ltd.) having a particle size of 20-42 mesh and a gold / oxide catalyst (manufactured by Toyo CCI) were impregnated at a volume ratio of 8: 2. Activated carbon usage is about 1200g / m 2 , pressure loss is 0.59mmAq
Met.
第 1 表 6段階臭気強度 0−感じない 1−微かに感じる 2−明らかに感じる 3−強く感じる 4−非常に強く感じる 5−極端に強く感じる 第 2 表 条件 臭気強度 空気清浄機なし 平均 2.50 変動 0.37 フィルタA 平均 1.53 変動 0.44 フィルタB 平均 1.52 変動 0.27 フィルタC 平均 1.70 変動 0.44 フィルタD 平均 1.75 変動 0.48 フィルタE 平均 1.45 変動 0.41 [発明の効果] 本発明によれば、脱臭フィルタとしての一般的な脱臭
効果と、エアコンディショナに対して使用されるフィル
タとしての低圧力損失及び脱臭効果の継続性とを適当に
備えたエアコンディショナ用の脱臭フィルタを提供する
ことが可能となる。Table 1 6-level odor intensity 0-Not felt 1-Feeling 2-Feeling clearly 3-Feeling strongly 4-Feeling extremely 5-Table 2 Conditions Odor intensity Without air purifier Average 2.50 Fluctuation 0.37 Filter A Average 1.53 Fluctuation 0.44 Filter B Average 1.52 Fluctuation 0.27 Filter C Average 1.70 Fluctuation 0.44 Filter D Average 1.75 Fluctuation 0.48 Filter E Average 1.45 Fluctuation 0.41 [Effect of the Invention] According to the present invention, general deodorization as a deodorizing filter It is possible to provide a deodorizing filter for an air conditioner, which is appropriately provided with the effect and low pressure loss as a filter used for the air conditioner and continuity of the deodorizing effect.
第1図は本発明に係る脱臭フィルタの一実施例を示す平
面図である。 第2図は本発明に係るフィルタをエアコンディショナの
室内機の筐体内に組込んだ状態を示す側面図である。 第3図は本発明に係るフィルタの製造工程の一例を示す
図である。 第4図はハニカム状格子の構造を示す斜視図である。 第5図は格子のセルサイズの変化に基づく活性炭担持量
と圧力損失との関係を示すグラフである。 第6図は活性炭の粒子寸法の変化に基づく活性炭担持量
と圧力損失との関係を示すグラフである。 第7図は活性炭の寸法とセルサイズとの関係による脱臭
フィルタの機能評価を示す図である。 第8図はフィルタのCO濃度低減に関する実験結果を示す
グラフである。 10……脱臭フィルタ、12……基板、14……ガス吸着剤、
16……セル、30……エアコンディショナの室内機、34…
…防塵フィルタ、36……熱交換器FIG. 1 is a plan view showing an embodiment of the deodorizing filter according to the present invention. FIG. 2 is a side view showing a state in which the filter according to the present invention is incorporated in the housing of the indoor unit of the air conditioner. FIG. 3 is a diagram showing an example of a manufacturing process of the filter according to the present invention. FIG. 4 is a perspective view showing the structure of the honeycomb lattice. FIG. 5 is a graph showing the relationship between the amount of activated carbon carried and the pressure loss based on the change in the cell size of the lattice. FIG. 6 is a graph showing the relationship between the amount of activated carbon carried and the pressure loss based on changes in the particle size of activated carbon. FIG. 7 is a diagram showing the functional evaluation of the deodorizing filter based on the relationship between the size of activated carbon and the cell size. FIG. 8 is a graph showing the experimental results regarding the reduction of the CO concentration of the filter. 10 …… deodorizing filter, 12 …… substrate, 14 …… gas adsorbent,
16 …… cell, 30 …… air conditioner indoor unit, 34…
… Dust filter, 36 …… Heat exchanger
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/94 (56)参考文献 特開 昭61−28422(JP,A) 特開 昭50−79475(JP,A) 特開 昭50−81959(JP,A) 特公 昭54−17311(JP,B2)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location B01D 53/94 (56) References JP-A 61-28422 (JP, A) JP-A 50- 79475 (JP, A) JP 50-81959 (JP, A) JP 54-17311 (JP, B2)
Claims (4)
れた活性炭粒子とを有し、エアコンディショナのエアの
通路に配設される脱臭フィルタであって、 前記基体の厚さ=3−15mm、 前記活性炭粒子の寸法=20−60メッシュ、 本フィルタの開口率=50−80%、 の各条件を全て満たすことと、 前記活性炭粒子が粘着剤により前記基体の表面に添着さ
れることと、 前記活性炭粒子が、触媒を担持しない状態で、脱臭効果
を目的として使用されることと、 を特徴とするエアコンディショナ用脱臭フィルタ。1. A deodorizing filter having a lattice-shaped filter base and activated carbon particles adhered to the base, which is disposed in an air passage of an air conditioner, wherein the thickness of the base is 3-. 15 mm, the size of the activated carbon particles = 20-60 mesh, the aperture ratio of the filter = 50-80%, and the activated carbon particles are attached to the surface of the substrate by an adhesive. A deodorizing filter for an air conditioner, characterized in that the activated carbon particles are used for the purpose of deodorizing without supporting a catalyst.
0.35cm2、 前記基体平面単位面積当りの前記活性炭粒子の使用量=
400−2000g/m2、 の各条件を全て満たす請求項1に記載のエアコンディシ
ョナ用脱臭フィルタ。2. A plane area of one cell of the substrate lattice = 0.20-
0.35 cm 2 , the amount of the activated carbon particles used per unit area of the substrate plane =
The deodorizing filter for an air conditioner according to claim 1, which satisfies all the conditions of 400-2000 g / m 2 .
は溶剤系粘着剤からなる請求項1または2に記載のエア
コンディショナ用脱臭フィルタ。3. The deodorizing filter for an air conditioner according to claim 1, wherein the adhesive is an emulsion adhesive or a solvent adhesive.
の触媒が前記基体の表面に添着される請求項1乃至3の
いずれか一項に記載のエアコンディショナ用脱臭フィル
タ。4. The deodorizing filter for an air conditioner according to claim 1, wherein a catalyst for CO catalytic oxidation treatment is attached to the surface of the substrate together with the activated carbon particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1258748A JPH082409B2 (en) | 1989-10-05 | 1989-10-05 | Deodorizing filter for air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1258748A JPH082409B2 (en) | 1989-10-05 | 1989-10-05 | Deodorizing filter for air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03123625A JPH03123625A (en) | 1991-05-27 |
| JPH082409B2 true JPH082409B2 (en) | 1996-01-17 |
Family
ID=17324537
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1258748A Expired - Fee Related JPH082409B2 (en) | 1989-10-05 | 1989-10-05 | Deodorizing filter for air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH082409B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107529919A (en) * | 2015-04-03 | 2018-01-02 | 皇家飞利浦有限公司 | Cooking equipment with filter element |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7955570B2 (en) | 2006-02-28 | 2011-06-07 | 3M Innovative Properties Company | Low pressure drop, highly active catalyst systems using catalytically active gold |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5079475A (en) * | 1973-11-17 | 1975-06-27 | ||
| JPS5081959A (en) * | 1973-11-26 | 1975-07-03 | ||
| US4129742A (en) * | 1977-07-01 | 1978-12-12 | Southwire Company | Plasma arc vertical shaft furnace |
| JPS6128422A (en) * | 1984-07-20 | 1986-02-08 | Agency Of Ind Science & Technol | Water-proof deodorizing sheet material |
-
1989
- 1989-10-05 JP JP1258748A patent/JPH082409B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107529919A (en) * | 2015-04-03 | 2018-01-02 | 皇家飞利浦有限公司 | Cooking equipment with filter element |
| US11490762B2 (en) | 2015-04-03 | 2022-11-08 | Koninklijke Philips N.V. | Cooking apparatus with filter element |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03123625A (en) | 1991-05-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |