JPH0732851B2 - Glass fiber filter paper for high performance air filter - Google Patents

Glass fiber filter paper for high performance air filter

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Publication number
JPH0732851B2
JPH0732851B2 JP3047146A JP4714691A JPH0732851B2 JP H0732851 B2 JPH0732851 B2 JP H0732851B2 JP 3047146 A JP3047146 A JP 3047146A JP 4714691 A JP4714691 A JP 4714691A JP H0732851 B2 JPH0732851 B2 JP H0732851B2
Authority
JP
Japan
Prior art keywords
glass fiber
filter paper
pressure loss
filter
maximum pore
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 - Lifetime
Application number
JP3047146A
Other languages
Japanese (ja)
Other versions
JPH04284803A (en
Inventor
智彦 楚山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hokuetsu Paper Mills Ltd
Original Assignee
Hokuetsu Paper Mills Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hokuetsu Paper Mills Ltd filed Critical Hokuetsu Paper Mills Ltd
Priority to JP3047146A priority Critical patent/JPH0732851B2/en
Publication of JPH04284803A publication Critical patent/JPH04284803A/en
Publication of JPH0732851B2 publication Critical patent/JPH0732851B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、半導体製造工場のクリ
ーンルーム等に用いられる空気清浄用の高性能エアフィ
ルタ用ガラス繊維濾紙に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a glass fiber filter paper for a high-performance air filter for air cleaning used in a clean room of a semiconductor manufacturing factory.

【0002】[0002]

【従来の技術】従来、クリーンルーム、クリーンベン
チ、無菌室など高度な清浄環境を要求される分野、ある
いは原子炉などから放射される放射性超微粉塵などを除
去する必要のある分野に、高性能エアフィルタ用ガラス
濾紙が用いられている。高性能エアフィルタ用ガラス濾
紙としては、粒径0.3μm DOP(ジオクチルフタレ
ート)粒子を99.97% 以上捕集するHEPA(高性
能エアフィルタ)濾紙と、粒径0.1μm のDOP粒子
を対象としHEPA以上の捕集効率を持つULPA(超
高性能エアフィルタ)用濾紙がある。これら濾紙につい
て要求されるクリーンルーム等の清浄度に応じて、各種
捕集効率の濾紙が濾材メーカーにより準備されている。
捕集効率を上げるためには、繊維径のより小さい極細ガ
ラス繊維の配合率を上げることで対処できるが、それに
伴い圧力損失も上昇し、HEPAよりULPA、またU
LPAの中でも捕集効率の要求度の高くなるほど圧力損
失もまた上昇しているのが現状である。ちなみに現在実
用化されている高性能エアフィルタ用ガラス繊維の圧力
損失は、面風速5.33cm/秒の条件で24〜63m
mH2 Oの範囲にある。圧力損失60mmH2 O以上の
ULPA用濾紙は、16メガビットLSIを製造する際
に必要なクリーンルームの空気清浄度に充分対応できる
と言われているが、圧力損失が高いことによる運転負荷
が大きいため、省エネの目的で圧力損失の低減が望まれ
ている。またHEPA用濾紙においては、MIL規格で
規定される捕集効率99.97% を満足させ、かつ圧力
損失が24mmH2 O以下のものはまだ実用化されてい
ない。
2. Description of the Related Art Conventionally, high-performance air is used in fields such as clean rooms, clean benches, aseptic chambers that require a highly clean environment, or in fields where it is necessary to remove radioactive ultrafine dust emitted from nuclear reactors. Glass filter paper for filters is used. For high-performance air filter glass filter paper, HEPA (high-performance air filter) filter paper that collects 99.97% or more of DOP (dioctyl phthalate) particles with a particle size of 0.3 μm and DOP particles with a particle size of 0.1 μm are targeted. There is a filter paper for ULPA (Ultra High Performance Air Filter) which has a collection efficiency higher than HEPA. Filter media with various collection efficiencies are prepared by filter media manufacturers according to the cleanliness requirements of these filter papers such as in a clean room.
In order to improve the collection efficiency, it is possible to deal with it by increasing the compounding ratio of the ultrafine glass fiber having a smaller fiber diameter, but the pressure loss also increases accordingly, and ULPA and U
In the current situation, the pressure loss also rises as the collection efficiency of LPA becomes higher. By the way, the pressure loss of the glass fiber for high-performance air filters currently in practical use is 24 to 63 m under the condition that the surface wind velocity is 5.33 cm / sec.
It is in the range of mH 2 O. It is said that the ULPA filter paper with a pressure loss of 60 mmH 2 O or more can sufficiently support the air cleanliness of the clean room required when manufacturing a 16-megabit LSI, but the operating load due to the high pressure loss is large. Reduction of pressure loss is desired for the purpose of energy saving. Further, as the HEPA filter paper, one having a trapping efficiency of 99.97% specified by the MIL standard and a pressure loss of 24 mmH 2 O or less has not yet been put into practical use.

【0003】[0003]

【発明が解決しようとする課題】本発明の課題は、従来
のHEPA、ULPA用ガラス繊維濾紙の捕集効率を維
持しながら、圧力損失が従来品に比べ4〜8mmH2
低い高性能エアフィルタ用濾紙を提供することにある。
SUMMARY OF THE INVENTION The object of the present invention is to maintain the collection efficiency of conventional glass fiber filter papers for HEPA and ULPA while maintaining a pressure loss of 4 to 8 mmH 2 O as compared with conventional products.
It is to provide a low-performance filter paper for an air filter.

【0004】[0004]

【課題を解決するための手段】本発明者等は、圧力損失
および捕集効率のフィルタ特性と濾紙物性の関係につい
て鋭意検討した結果、最大孔径で示される濾材内部の細
孔径サイズにより、上記フィルタ特性が大いに影響を受
けるという点に着目し、本発明に至った。
Means for Solving the Problems The inventors of the present invention have made diligent studies on the relationship between filter characteristics such as pressure loss and collection efficiency and physical properties of filter paper. The present invention has been made paying attention to the fact that the characteristics are greatly affected.

【0005】本発明の濾紙についてさらに詳しく説明す
る。
The filter paper of the present invention will be described in more detail.

【0006】本発明でいう高性能エアフィルタ用ガラス
繊維濾紙とは、0.3μm DOP粒子の捕集効率が面風
速5.33cm/秒の条件下で99.97%以上の性能
を示すガラス繊維濾紙を意味し、通常HEPA及びUL
PAと呼ばれるエアフィルタ用ガラス繊維濾紙を意味す
るものである。
The glass fiber filter paper for high performance air filters referred to in the present invention is a glass fiber having a collection efficiency of 0.3 μm DOP particles of 99.97% or more under the condition that the surface wind velocity is 5.33 cm / sec. Means filter paper, usually HEPA and UL
It means a glass fiber filter paper for air filters called PA.

【0007】ガラス繊維濾紙の最大孔径は、主に液体フ
ィルター、バッテリーセパレーター関係の最大孔径の測
定に使用される細孔サイズ/サイズ分布測定装置を用
い、溶媒としてポロフィル(商品名; Coulter Electro
nics社) を用いて測定される。
The maximum pore size of the glass fiber filter paper is determined by using a pore size / size distribution measuring device which is mainly used for measuring the maximum pore size related to a liquid filter and a battery separator, and is used as a solvent for porphyll (trade name; Coulter Electro
nics).

【0008】本発明では上記方法で測定される最大孔径
m が、Pc =−0.135×ΔP+15で計算される
最大孔径に対し、Pm ≦Pc であることが必要であり、
m がPc と比較し、低い程性能が向上する。
[0008] maximum pore size P m measured by the above method in the present invention, with respect to the maximum pore size is calculated by P c = -0.135 × ΔP + 15 , must be a P m ≦ P c,
The lower P m is compared with P c , the better the performance.

【0009】前記Pc =−0.135×ΔP+15とい
う式は、市販の高性能エアフィルタ用ガラス繊維濾紙お
よび圧力損失を極細ガラス繊維の配合量を変え作成した
濾紙について分析した結果、見出した式である。すなわ
ちガラス繊維濾紙の圧力損失と最大孔径は逆比例の関係
にあり、圧力損失が高くなる程、最大孔径は小さくな
り、また同一圧力損失では最大孔径が小さい程、捕集効
率が向上することを見出した。図1に示すように、従来
品の分析結果では、実測される最大孔径Pm は圧力損失
から計算されるPc に対し、Pm >Pc の関係にあっ
た。
The above expression P c = -0.135 × ΔP + 15 is an expression found as a result of analysis of a commercially available glass fiber filter paper for high performance air filters and filter papers prepared by changing pressure loss with an extra fine glass fiber content. Is. That is, the pressure loss and the maximum pore diameter of the glass fiber filter paper are inversely proportional to each other.The higher the pressure loss, the smaller the maximum pore diameter, and the same pressure loss, the smaller the maximum pore diameter, the higher the collection efficiency. I found it. As shown in FIG. 1, the analysis results of the conventional product, the maximum pore size P m to be measured whereas P c calculated from pressure loss was in relation P m> P c.

【0010】図2は、抄造条件を変えて実際の抄紙機で
抄造したエアフィルタ用濾紙について最大孔径と圧力損
失、捕集効率の関係を見たものである。本発明の最大孔
径P m <Pc であるガラス繊維濾紙はその差が大きい
程、同一圧力損失における捕集効率が上昇することが判
った。また、Pm <Pc であるガラス繊維濾紙は圧力損
失26mmH2 Oにおいて0.3μm DOP粒子の捕集
効率がHEPAクラスに必要な99.97% 以上を満た
しているのに対し、Pm >Pc の濾紙は99.97% 以
下となっている。0.1μm のDOP粒子を用い、UL
PA用濾紙で行っても同様のことが観察できる。
FIG. 2 shows an actual paper machine with different papermaking conditions.
Maximum pore size and pressure loss of manufactured filter paper for air filter.
This is the relationship between loss and collection efficiency. Maximum hole of the present invention
Diameter P m<PcThe difference is great in the glass fiber filter paper
It was found that the collection efficiency increases with increasing pressure loss.
It was. Also, Pm<PcThe glass fiber filter paper is
Lost 26 mmH2Collection of 0.3 μm DOP particles in O
Efficiency meets 99.97% or more required for HEPA class
In contrast, Pm> PcThe filter paper of 99.97% or more
It is below. UL with 0.1 μm DOP particles
The same thing can be observed even if it carries out with PA filter paper.

【0011】ガラス繊維濾紙の最大孔径PをPより
小さくする方法としては各種の方法が考えられ、特に1
つの方法に限定されるものでないが、本発明のガラス繊
維濾紙で特定する最大孔径レベルに到達するには原料配
合、とりわけ極細ガラス繊維とチョップドストランド繊
維の配合率を一定範囲内におさめることが極めて有効で
あることを本発明者は見出した。すなわち、ガラス繊維
の組成において繊維径10μm以下のチョップドストラ
ンド繊維の含有率が10〜50重量%、極細ガラス繊維
の含有率が90〜50重量%である高性能エアフィルタ
用濾紙は本発明の有利な実施形態である。通常、濾紙を
構成する極細ガラス繊維の繊維径を細くすることによ
り、最大孔径Pを低めること、またそれによって捕集
効率を上げることが可能である。しかるに繊維径をたん
に細くすることは濾紙の圧力損失の増大をまねいてしま
い、本発明のP≦Pを満足させる濾紙を得る方法と
しては不適当である。本発明では、強度保持の目的で通
常数%配合されているチョップドガラス繊維の割合を規
定値以上に高め、これにより圧力損失の増大を防ぐこと
ができかつ最大孔径を小さくし、P≦Pの濾紙を得
ることができる。チョップドガラス繊維の割合が高くな
る程、繊維径の細い極細ガラス繊維を配合することがで
きるので、最大孔径は小さくなり、フィルタ性能は向上
する。 ≦P にするためには、チョップドストラン
ドガラス繊維の配合率は10%以上にすることが必要で
ある。さらに好ましくは15%以上である。
Various methods are conceivable for making the maximum pore diameter P m of the glass fiber filter paper smaller than P c , and particularly 1
Although not limited to one method, in order to reach the maximum pore size level specified in the glass fiber filter paper of the present invention, it is extremely necessary to keep the raw material blending, especially the blending ratio of the ultrafine glass fiber and the chopped strand fiber within a certain range. The present inventor has found that it is effective. That is, a filter paper for a high-performance air filter in which the content of chopped strand fibers having a fiber diameter of 10 μm or less and the content of ultrafine glass fibers in the composition of glass fiber is 90 to 50% by weight is advantageous in the present invention. It is an embodiment. In general, it is possible to reduce the maximum pore diameter P m by increasing the fiber diameter of the ultrafine glass fibers constituting the filter paper, and thereby to improve the collection efficiency. However, simply reducing the fiber diameter causes an increase in pressure loss of the filter paper, and is not suitable as a method for obtaining the filter paper satisfying P m ≤P c of the present invention. In the present invention, the proportion of chopped glass fibers, which is usually blended by several percent for the purpose of maintaining strength, is increased to a specified value or more, whereby pressure loss can be prevented from increasing and the maximum pore diameter can be reduced to P m ≤P The filter paper of c can be obtained. As the proportion of chopped glass fibers becomes higher, the finer glass fibers having a smaller fiber diameter can be blended, so that the maximum pore diameter becomes smaller and the filter performance improves. In order to satisfy P m ≤P c , it is necessary that the compounding ratio of chopped strand glass fibers is 10% or more. More preferably, it is 15% or more.

【0012】本発明の高性能エアフィルタ用ガラス繊維
濾紙は、極細ガラス繊維およびチョップドガラス繊維の
他にバインダーを含有している。このバインダーは有機
系バインダーであり、その量は10% 以下、好ましくは
7% 以下であり、必要強度が維持される範囲内で少ない
程好ましい。バインダーの量が増加するにつれた、圧力
損失は上昇し、捕集効率を低下させる。
The glass fiber filter paper for a high performance air filter of the present invention contains a binder in addition to the ultrafine glass fiber and the chopped glass fiber. This binder is an organic binder, and the amount thereof is 10% or less, preferably 7% or less, and it is preferable that the amount is as small as possible within the range in which the required strength is maintained. As the amount of binder increases, the pressure loss increases, reducing the collection efficiency.

【0013】[0013]

【作用】エアフィルタの最大孔径を小さくすることによ
る捕集効率の上昇の作用機構についてはこれまで理論づ
けされてはいないが、次の様に推定される。
The mechanism of action of increasing the collection efficiency by reducing the maximum pore size of the air filter has not been theorized so far, but it is estimated as follows.

【0014】極細ガラス繊維を使用した高性能エアフィ
ルタ用ガラス繊維濾紙の捕集機構は、濾紙を構成するガ
ラス繊維の充填のばらつきに関係していると言われてい
る。従って、充填のばらつきが大きければ、これに伴っ
て濾紙内で形成される細孔のばらつきが大きくなり、最
大孔径が大きくなり捕集効率は低下する。最大孔径が小
さくなるように細孔のばらつきを減少させる方向にコン
トロールすれば、繊維の充填は均一になりフィルタ性能
は向上すると考えられる。チョップドストランドの配合
割合の増加は、より繊維径の細い極細ガラス繊維の使用
割合増加による細孔全体のサイズの減少と同時に、充填
の均一性に影響していると考える。従来エアフィルタの
最大孔径については注目されていないかったが、これを
制御することにより捕集効果が有効に発揮され、その結
果フィルタ性能の向上につながると考える。
It is said that the mechanism of collecting glass fiber filter paper for high performance air filters using ultrafine glass fiber is related to the variation in the filling of the glass fiber constituting the filter paper. Therefore, if the variation of the filling is large, the variation of the pores formed in the filter paper is increased accordingly, the maximum pore diameter is increased, and the collection efficiency is lowered. It is considered that if the variation in pores is controlled so as to reduce the maximum pore diameter, the filling of the fibers becomes uniform and the filter performance is improved. It is considered that the increase in the mixing ratio of the chopped strands has an effect on the filling uniformity as well as the decrease in the size of the entire pores due to the increase in the usage ratio of the ultrafine glass fibers having a smaller fiber diameter. Conventionally, no attention was paid to the maximum pore size of an air filter, but by controlling this, the trapping effect is effectively exhibited, and as a result, the filter performance is improved.

【0015】[0015]

【実施例】実施例1 平均繊維径1μm以下の極細ガラス繊維90重量% 、平
均繊維径6μmのチョップドガラス繊維10重量% をパ
ルパーでpH3.5の酸性水を用い、濃度0.5%で1
0分間離解した。次いでインレット濃度0.05重量%
で抄紙機にて抄紙した。アクリル系ラテックス(HA−
16、製造元:日本アクリル)を湿紙に付与し、その後
ドライヤーで乾燥し、後記表1に記載の通りPm <Pc
である目付69g/m2 のHEPA用ガラス繊維濾紙を
得た。
Example 1 90% by weight of ultrafine glass fibers having an average fiber diameter of 1 μm or less and 10% by weight of chopped glass fibers having an average fiber diameter of 6 μm were acidified with a pulper at pH 3.5 to 1% at a concentration of 0.5%.
Disaggregated for 0 minutes. Next, the inlet concentration is 0.05% by weight
Paper was made using a paper machine. Acrylic latex (HA-
16, manufacturer: Japan Acrylic) is applied to a wet paper, then dried with a drier, and P m <P c as shown in Table 1 below.
A glass fiber filter paper for HEPA having a basis weight of 69 g / m 2 was obtained.

【0016】実施例2 実施例1においてチョップドガラス繊維の配合率を30
重量% とし、圧力損失が同レベルになるように平均繊維
径1μm 以下の極細ガラス繊維70重量% 中の平均繊維
径0.65μm のガラス繊維成分を増加させて調節した
以外は実施例1と同様にして後記表1に記載の通りPm
<Pc である目付71g /m2 のHEPA用ガラス繊維
濾紙を得た。
Example 2 In Example 1, the chopped glass fiber content was 30%.
%, And the same as in Example 1 except that the glass fiber component having an average fiber diameter of 0.65 μm in 70% by weight of the ultrafine glass fibers having an average fiber diameter of 1 μm or less was increased to adjust the pressure loss to the same level. Then, as shown in Table 1 below, P m
A glass fiber filter paper for HEPA having a basis weight of 71 g / m 2 of <P c was obtained.

【0017】実施例3 実施例1においてチョップドガラス繊維の配合率を45
重量% とし、圧力損失が同レベルになるように平均繊維
径1μm 以下の極細ガラス繊維55重量% 中の平均繊維
径0.65μm のガラス繊維成分を増加させて調節した
以外は実施例1と同様にして後記表1に記載の通りPm
<Pc である目付70g /m2 のHEPA用ガラス繊維
濾紙を得た。
Example 3 In Example 1, the chopped glass fiber content was 45%.
%, And the same as Example 1 except that the glass fiber component having an average fiber diameter of 0.65 μm in 55% by weight of the ultrafine glass fibers having an average fiber diameter of 1 μm or less was increased to adjust the pressure loss to the same level. Then, as shown in Table 1 below, P m
A glass fiber filter paper for HEPA having a basis weight of 70 g / m 2 of <P c was obtained.

【0018】実施例4 実施例1において平均繊維径1μm 以下の極細ガラス繊
維90重量% 中の平均繊維径0.32μm の極細ガラス
繊維を5重量% 配合した以外は実施例1と同様にして後
記表1に記載の通りPm <Pcである目付73g /m2
のULPA用ガラス繊維濾紙を得た。
Example 4 The same as Example 1 except that 5% by weight of ultrafine glass fibers having an average fiber diameter of 0.32 μm in 90% by weight of the ultrafine glass fibers having an average fiber diameter of 1 μm or less was added. As shown in Table 1, 73 g / m 2 of basis weight with P m <P c
To obtain a glass fiber filter paper for ULPA.

【0019】実施例5 実施例1においてチョップドガラス繊維の配合率を30
重量% とし、平均繊維径1μm 以下の極細ガラス繊維7
0重量% 中の平均繊維径0.32μm のガラス繊維成分
を実施例4と圧力損失が同レベルになるように増加させ
て調節した以外は実施例1と同様にして後記表1に記載
の通りPm<Pc である目付74g /m 2 のULPA用
ガラス繊維濾紙を得た。
[0019]Example 5 In Example 1, the chopped glass fiber content was 30.
Ultrafine glass fiber 7 with an average fiber diameter of 1 μm or less in weight%
Glass fiber component with an average fiber diameter of 0.32 μm in 0% by weight
Is increased so that the pressure loss becomes the same level as in Example 4.
Described in Table 1 below in the same manner as in Example 1 except that
Street Pm<PcThe unit weight is 74g / m 2For ULPA
A glass fiber filter paper was obtained.

【0020】比較例 比較例1、2および3は実施例1〜3に、比較例4は実
施例4、5に対応するものである。
Comparative Examples Comparative Examples 1, 2 and 3 correspond to Examples 1 to 3, and Comparative Example 4 corresponds to Examples 4 and 5.

【0021】比較例1 実施例1において、1μm 以下の極細ガラス繊維を10
0重量% とし、圧力損失が同レベルになるよう平均繊維
径0.65μm のガラス繊維成分を減少させて調節した
以外は実施例1と同様にして後記表1に記載の通りPm
>Pc である目付68g /m2 のHEPA用ガラス繊維
濾紙を得た。
Comparative Example 1 In Example 1, 10 μm or less of ultrafine glass fiber was used.
And 0 wt%, as described in the following Table 1, except that the pressure loss is adjusted to reduce the glass fiber component of the average fiber diameter 0.65μm to the same level in the same manner as in Example 1 P m
A glass fiber filter paper for HEPA having a basis weight of 68 g / m 2 of> P c was obtained.

【0022】比較例2 実施例1においてチョップドガラス繊維の配合率を3重
量% とし、平均繊維径1μm 以下の極細ガラス繊維97
重量% とし、圧力損失が同レベルになるよう調節した以
外は実施例1と同様にして後記表1に記載の通りPm
c である目付70g /m2 のHEPA用ガラス繊維濾
紙を得た。
Comparative Example 2 Extra fine glass fiber 97 having an average fiber diameter of 1 μm or less with the chopped glass fiber content of 3% by weight in Example 1.
P m > as described in Table 1 below in the same manner as in Example 1 except that the pressure loss was adjusted to the same level.
A glass fiber filter paper for HEPA having a basis weight of 70 g / m 2 of P c was obtained.

【0023】比較例3 実施例1において、配合率をチョップドガラス繊維を6
0重量% とし、極細ガラス繊維を40重量% とし、圧力
損失が同レベルになるよう調節した以外は実施例1と同
様にして後記表1に記載の通りPm >Pc である目付6
8g /m2 のHEPA用ガラス繊維濾紙を得た。
Comparative Example 3 In Example 1, the compounding ratio was 6 for chopped glass fiber.
And 0 wt%, ultrafine glass fibers and 40 wt%, except that the pressure loss is adjusted to the same level are as P m> P c according to the following Table 1 in the same manner as in Example 1 having a basis weight 6
8 g / m 2 of glass fiber filter paper for HEPA was obtained.

【0024】比較例4 実施例4において、チョップドガラス繊維を3重量% と
し、極細ガラス繊維を97重量% とし、圧力損失が同レ
ベルになるよう調節した以外は実施例4と同様にして後
記表1に記載の通りPm >Pc である目付72g /m2
のULPA用ガラス繊維濾紙を得た。
Comparative Example 4 The same procedure as in Example 4 was repeated except that chopped glass fiber was 3% by weight, ultrafine glass fiber was 97% by weight, and pressure loss was adjusted to the same level. 72 g / m 2 with a basis weight of P m > P c as described in 1.
To obtain a glass fiber filter paper for ULPA.

【0025】実施例1〜5、比較例1〜4の濾紙の分析
を下記の方法で行ない、結果を表1に示した。 (1) 最大孔径 Pmax Coulter Electronics 製コールターポロメータを使用
し、異なる場所で3点測定し、それらの平均を持って最
大孔径とした。
The filter papers of Examples 1 to 5 and Comparative Examples 1 to 4 were analyzed by the following method, and the results are shown in Table 1. (1) Maximum pore size P max Coulter Electronics Coulter Porometer was used to measure 3 points at different locations, and the average of these was used as the maximum pore size.

【0026】(2) 圧力損失 自製の装置を用い有効面積100cm2 の濾紙に面風速
5.33cm/秒(=S)で通風し、その時の圧力損失
を微差圧計で測定した。
(2) Pressure loss Using a self-made device, air was passed through a filter paper having an effective area of 100 cm 2 at a surface wind velocity of 5.33 cm / sec (= S), and the pressure loss at that time was measured by a fine differential pressure gauge.

【0027】(3) DOP捕集効率 ラスキンノズルで発生させた多分散DOP粒子を含む空
気を、有効面積100cm2 の濾紙に面風速で5.33
cm/秒で通風した時のDOP捕集効率をリオン社製レ
ーザーパーティクルカウンターを使用し測定した。尚、
HEPA用ガラス繊維濾紙については0.3μm 、UL
PA用ガラス繊維濾紙については0.1μm のDOP粒
子について測定した。
(3) DOP collection efficiency Air containing polydisperse DOP particles generated by a Ruskin nozzle was filtered through a filter paper having an effective area of 100 cm 2 at a surface wind velocity of 5.33.
The DOP collection efficiency when ventilated at cm / sec was measured using a laser particle counter manufactured by Rion. still,
0.3μm for glass fiber filter paper for HEPA, UL
The glass fiber filter paper for PA was measured for 0.1 μm DOP particles.

【0028】(4) 可燃物 925±25℃、10分間電気炉にて加熱し、加熱前後
の重量差を加熱前重量で割り、百分率として求めた。
(4) Combustible material: 925 ± 25 ° C., heated in an electric furnace for 10 minutes, and the weight difference before and after heating was divided by the weight before heating to obtain a percentage.

【0029】(5) 引張強度 濾紙の縦方向および横方向より採取した25mm幅の試
験片について、スパン長100mm、引張速度12.5
mm/分で定速引張試験機を用い測定した。
(5) Tensile strength A test piece having a width of 25 mm sampled from the longitudinal and lateral directions of the filter paper had a span length of 100 mm and a pulling speed of 12.5.
It was measured using a constant speed tensile tester at mm / min.

【0030】(6) α値 濾紙のフィルタ性能の指標となるα値は、(2) と(3) の
測定値に基づき、次式より求めた。( α値の値が高い
程、同一圧力損失で高捕集効率を示す。)
(6) α value The α value, which is an index of the filter performance of the filter paper, was calculated from the following equation based on the measured values of (2) and (3). (The higher the α value, the higher the collection efficiency with the same pressure loss.)

【0031】[0031]

【表1】 [Table 1]

【0032】[0032]

【効果】本発明は従来クリーンルーム用として用いられ
てきたHEPAおよびULPA用ガラス繊維濾紙につい
て、最大孔径を圧力損失との関係で規定値以下に制御す
ることでより低圧損、高捕集効率の新規なガラス繊維濾
紙を提供するものであり以下の効果が期待できる。 (1) 捕集効率を従来品と同一レベルにした場合、圧力損
失の低減が可能であり、クリーンルームに用いた場合、
クリーンルームの空気清浄度を落とすことなく、省エネ
ルギー、ファンの騒音低減に寄与する。 (2) 圧力損失を同一レベルにした場合、捕集効率は上昇
し、同一エネルギー消費量でクリーンルームの空気清浄
度を上げることができる。 (3) 従来品にくらべ、ほぼ同様のコストで製造できる。 (4) 強度が向上するため、濾紙の目付重量を下げること
ができ、フィルタ加工品中の濾紙の使用量を節減でき
る。
[Effect] The present invention is a novel glass fiber filter for HEPA and ULPA which has been conventionally used for clean rooms. It has a new low pressure loss and a high collection efficiency by controlling the maximum pore size to a specified value or less in relation to the pressure loss. The following effects can be expected. (1) When the collection efficiency is the same level as the conventional product, pressure loss can be reduced, and when used in a clean room,
It contributes to energy saving and fan noise reduction without lowering the air cleanliness of the clean room. (2) If the pressure loss is at the same level, the collection efficiency will increase and the air cleanliness of the clean room can be increased with the same energy consumption. (3) Compared with conventional products, it can be manufactured at almost the same cost. (4) Since the strength is improved, the weight per unit area of the filter paper can be reduced, and the amount of the filter paper used in the processed filter product can be reduced.

【0033】以上に述べたように本発明の実用的価値は
極めて高く、半導体産業のみならず、クリーンルームを
使用する食品産業、医療産業等、他産業にも十分貢献す
るものである。
As described above, the practical value of the present invention is extremely high, and contributes not only to the semiconductor industry but also to other industries such as the food industry using a clean room and the medical industry.

【図面の簡単な説明】[Brief description of drawings]

【図1】図1は圧力損失の異なるガラス繊維濾紙につい
て圧力損失と最大孔径の関係を示したグラフである。
FIG. 1 is a graph showing the relationship between pressure loss and maximum pore size for glass fiber filter papers having different pressure losses.

【図2】図2は最大孔径条件の異なるガラス繊維濾紙に
ついて圧力損失と捕集効率との関係を示すグラフであ
る。
FIG. 2 is a graph showing the relationship between pressure loss and collection efficiency for glass fiber filter papers having different maximum pore size conditions.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 濾紙の最大孔径Pm が下記式(a)で計
算される最大孔径P c に対し、Pm ≦Pc の関係にある
ことを特徴とする高性能エアフィルタ用ガラス繊維濾
紙。 Pc = −0.135×ΔP+15 (a) Pc :最大孔径(単位:μm ) ΔP:面風速5.33cm/Sにおける圧力損失(mm
2 O)
1. The maximum pore size P of the filter paper.mIs calculated by the following formula (a)
Maximum pore size calculated P cOn the other hand, Pm≤PcHave a relationship
Glass fiber filter for high performance air filters characterized by
paper. Pc= −0.135 × ΔP + 15 (a) Pc: Maximum pore diameter (unit: μm) ΔP: Pressure loss at surface wind velocity 5.33 cm / S (mm
H2O)
【請求項2】 ガラス繊維の組成において、繊維径10
μm 以下のチョップストランドガラス繊維の含有率が1
0〜50重量% 、極細ガラス繊維の含有率が90〜50
重量% であることを特徴とする、請求項 1に記載の高性
能エアフィルタ用ガラス繊維濾紙。
2. The glass fiber composition has a fiber diameter of 10
The chopped strand glass fiber content of μm or less is 1
0-50% by weight, ultrafine glass fiber content 90-50
The glass fiber filter paper for a high performance air filter according to claim 1, wherein the glass fiber filter paper is characterized by being in a weight percentage.
JP3047146A 1991-03-13 1991-03-13 Glass fiber filter paper for high performance air filter Expired - Lifetime JPH0732851B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3047146A JPH0732851B2 (en) 1991-03-13 1991-03-13 Glass fiber filter paper for high performance air filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3047146A JPH0732851B2 (en) 1991-03-13 1991-03-13 Glass fiber filter paper for high performance air filter

Publications (2)

Publication Number Publication Date
JPH04284803A JPH04284803A (en) 1992-10-09
JPH0732851B2 true JPH0732851B2 (en) 1995-04-12

Family

ID=12766964

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3047146A Expired - Lifetime JPH0732851B2 (en) 1991-03-13 1991-03-13 Glass fiber filter paper for high performance air filter

Country Status (1)

Country Link
JP (1) JPH0732851B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4639419B2 (en) * 2000-02-04 2011-02-23 日本無機株式会社 Filter paper for high-temperature air filter and manufacturing method thereof
JP6964033B2 (en) * 2018-03-30 2021-11-10 北越コーポレーション株式会社 Filter material for air filter

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS624418A (en) * 1985-06-29 1987-01-10 Nippon Muki Kk Glass fiber filter paper for air filter having ultrahigh performance
JPS6393316A (en) * 1986-10-07 1988-04-23 Yoshimi Oshitari Filter layer
JPH07102293B2 (en) * 1989-03-24 1995-11-08 北越製紙株式会社 Glass fiber filter paper for high performance air filter and method for producing the same

Also Published As

Publication number Publication date
JPH04284803A (en) 1992-10-09

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