JPS63270516A - Filter sheet for removing microbe and pyrogen in liquid chemical or water - Google Patents

Filter sheet for removing microbe and pyrogen in liquid chemical or water

Info

Publication number
JPS63270516A
JPS63270516A JP10590587A JP10590587A JPS63270516A JP S63270516 A JPS63270516 A JP S63270516A JP 10590587 A JP10590587 A JP 10590587A JP 10590587 A JP10590587 A JP 10590587A JP S63270516 A JPS63270516 A JP S63270516A
Authority
JP
Japan
Prior art keywords
water
filtration
activated carbon
sheet
perlite
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.)
Granted
Application number
JP10590587A
Other languages
Japanese (ja)
Other versions
JPH0829212B2 (en
Inventor
Reiko Kaneda
金田 玲子
Mitsuhiro Taguchi
田口 光裕
Hidekatsu Shoji
英克 庄司
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.)
TOYO ROSHI KK
Toyo Roshi Kaisha Ltd
Otsuka Pharmaceutical Co Ltd
Original Assignee
TOYO ROSHI KK
Toyo Roshi Kaisha Ltd
Otsuka Pharmaceutical Co 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 TOYO ROSHI KK, Toyo Roshi Kaisha Ltd, Otsuka Pharmaceutical Co Ltd filed Critical TOYO ROSHI KK
Priority to JP62105905A priority Critical patent/JPH0829212B2/en
Publication of JPS63270516A publication Critical patent/JPS63270516A/en
Publication of JPH0829212B2 publication Critical patent/JPH0829212B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Filtering Materials (AREA)

Abstract

PURPOSE:To efficiently and completely remove the microbes and pyrogens in a liq. chemical or water by using the title sheet consisting at least of powdery activated carbon, perlite, and a fiber matrix. CONSTITUTION:Filtration is carried out by using the filter sheet obtained by mixing powdery activated carbon, perlite, and a fibrous matrix, and the microbes and pyrogens in a liq. chemical or water are efficiently removed. In this case, the powdery activated carbon, perlite, and fiber matrix must be uniformly mixed, and hence the sheet having optimum adsorbing and removing performance and filtration quantity is obtained. The amt. of the activated carbon to be added is controlled to >=140%, based on the cellulose fiber which is one component of the fiber matrix, and the amt. of perlite to be added is adjusted to >=70%, based on the cellulose fiber.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は薬液中又は水中の微生物及びパイロジエンを除
去するための濾過シートに関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a filter sheet for removing microorganisms and pyrogens from a chemical solution or water.

(従来の技術) 製薬、医療関係で薬液中又は水中の微生物及びパイロジ
エンの除去は極めて大切であり、又屡々実施されている
操作である。
(Prior Art) In the pharmaceutical and medical fields, the removal of microorganisms and pyrogienes from medicinal solutions or water is extremely important and is a frequently performed operation.

特にパイロジエンは注射製剤関係で問題になり、これで
汚染された注射剤を投与すると副作用として悪寒、発熱
などの現象が見られる。更にこのパイロジエンについて
は血管作用、骨髄反応、細胞傷害作用、抗しゅよう作用
、致死作用、内毒素過敏症等多くの生体反応が報告され
ている。パイロジエンは細菌の内毒素とほぼ考えてよく
、その主成分は燐脂質多糖体(リポ多vM>であり、特
にダラム陰性菌からのものが発熱性が強いといわれてい
る。
Pyrodiene is particularly problematic when it comes to injectable preparations, and when injectables contaminated with this are administered, symptoms such as chills and fever can be seen as side effects. Furthermore, many biological reactions have been reported regarding this pyrodiene, such as vascular effects, bone marrow reactions, cytotoxic effects, anti-inflammatory effects, lethal effects, and endotoxin hypersensitivity. Pyrogen can be considered to be a bacterial endotoxin, and its main component is phospholipid polysaccharide (lipopolysaccharide), and it is said that those from Durham-negative bacteria are particularly pyrogenic.

パイロジエンの除去法としては従来から高圧蒸気、乾熱
、煮沸等の加熱法、濾過法、放射線、紫外線、高周波等
の照射法、エチレンオキサイドやホルムアルデヒド等の
ガス法、エタノール、フェノール水、ホルマリン水等に
よる薬液法等が、それぞれの目的、対象によって使い分
けられている。
Conventional methods for removing pyrodiene include heating methods such as high-pressure steam, dry heat, and boiling, filtration methods, irradiation methods such as radiation, ultraviolet rays, and high frequency waves, gas methods such as ethylene oxide and formaldehyde, ethanol, phenol water, formalin water, etc. Chemical liquid methods, etc., are used depending on the purpose and target.

特に濾過法は「対象試料を多孔性媒体中に通過させるだ
け」の操作のため試料を変質させる心配が一番少なく、
そのため気体(ガス)、水を始め、可溶性で熱に不安定
な物質を含む液状培地や液状の各種医薬品等の場合に屡
々用いられている。
In particular, the filtration method is an operation in which the target sample is simply passed through a porous medium, so there is the least risk of deterioration of the sample.
Therefore, it is often used for liquid media and various liquid pharmaceuticals that contain gases, water, and other soluble and thermally unstable substances.

この濾過による液体中の微生物、パイロジエン除去用の
濾材としては、古くからのアスベスト濾過シートの他に
ケイソウ土濾過シート、荷電処理濾過シート等があり、
最近は更に逆浸透膜、限外濾過膜等の「膜」濾材による
方法も提案されている。しかし、これらはいずれも除去
性能、濾過速度、取り扱い性、価格等で実際に満足でき
るものはない。特にアスベスト濾過シートは人体に対す
る医学的問題からその使用がのぞましくない。
In addition to the traditional asbestos filtration sheets, diatomaceous earth filtration sheets, electrically charged filtration sheets, etc. are used as filter media for removing microorganisms and pyrogen from the liquid through this filtration.
Recently, methods using "membrane" filter media such as reverse osmosis membranes and ultrafiltration membranes have also been proposed. However, none of these methods is actually satisfactory in terms of removal performance, filtration rate, ease of handling, price, etc. In particular, asbestos filtration sheets are not recommended for use due to medical problems to the human body.

(発明が解決しようとする問題点) 現在、製薬、医療関係で実際におこなわれている薬液や
水中のパイロジエン除去法としては活性炭ボディフィー
ド法がある。この方法は所要量の粉末活性炭を薬液や水
等の対象液体に添加し、よく混合後一定時間放置し、液
中の微生物、パイロジエンを吸着させた活性炭を濾別す
る方法である。
(Problems to be Solved by the Invention) Currently, there is an activated carbon body feed method as a method for removing pyrodiene from medicinal solutions and water that is actually used in the pharmaceutical and medical fields. In this method, a required amount of powdered activated carbon is added to a target liquid such as a chemical solution or water, and after mixing well, the mixture is left to stand for a certain period of time, and the activated carbon that has adsorbed microorganisms and pyrodiene in the liquid is filtered out.

この方法は最も確実なパイロジエン除去方法として広〈
実施されているが、尚次ぎの様な欠点が指摘されている
This method is widely used as the most reliable pyrogen removal method.
Although it has been implemented, the following drawbacks have been pointed out.

(イ)操作がバッチ式のため煩雑で能率がわるい。(b) Operation is batch-type, which is complicated and inefficient.

(II)濾過機のケーク捕集容積上の制約がある。(II) There is a restriction on the cake collection capacity of the filter.

(ハ)使用済み粉末活性炭の処理が必要で、且つ此の為
の設備が必要である。
(c) It is necessary to dispose of used powdered activated carbon, and equipment for this purpose is also required.

(ニ)粉末活性炭の秤量操作及びその設備が必要であり
、又その為に作業環境が汚染されやすい。
(d) The operation of weighing powdered activated carbon and its equipment are necessary, and the working environment is likely to be contaminated because of this.

(ネ)工程の完全なりローズ化が困難であり、このため
製造工程での細菌、パイロジエン等の汚染の恐れがある
。等 そしてこれらの欠点のないパイロジエン防止法が望まれ
ていた。
(f) It is difficult to achieve a complete rose-containing process, and therefore there is a risk of contamination with bacteria, pyrogen, etc. during the manufacturing process. etc., and a pyrogen prevention method that does not have these drawbacks has been desired.

(発明の目的) 本発明はこの様な点に鑑み、濾過法によって、薬液中ま
たは水中の微生物及びパイロジエンをより能率的且つ完
全に除去できる濾過シートを提供することを目的として
いる。即ち、微生物、パイロジエンの除去性能にすぐれ
、処理量が大きく、操作しやすく作業環境を汚染する恐
れの少ない低価格の濾過シートを装填した濾過機によっ
て薬液又は水等を濾過することによって微生物、パイロ
ジエンを除去する濾過シートを提供することを目的とす
る。
(Object of the Invention) In view of the above points, an object of the present invention is to provide a filter sheet that can more efficiently and completely remove microorganisms and pyrogen in a chemical solution or water by a filtration method. In other words, microorganisms and pyrogens can be removed by filtering chemical solutions or water using a filter equipped with a low-cost filter sheet that has excellent performance in removing microorganisms and pyrogens, has a large throughput, is easy to operate, and has little risk of contaminating the working environment. The purpose is to provide a filter sheet that removes.

(問題点を解決するための手段) 本発明の要旨とするところは、少なくとも粉末活性炭、
パーライト及び繊維マトリックスからなることを特徴と
する薬液中または水中の微生物及びパイロジエンの除去
用濾過シートにある。
(Means for Solving the Problems) The gist of the present invention is that at least powdered activated carbon,
A filtration sheet for removing microorganisms and pyrogens in a chemical solution or water, characterized by comprising perlite and a fiber matrix.

濾過シートには従来からケイソウ土をセルローズ繊維等
と混抄したものがあり、清澄、滅菌濾過用として使われ
ているが、特にパイロジエンの除去性能の点では実用的
でない。更に活性炭を繊維マトリックスに混抄してシー
ト状にしたものも従来からあり、着色液の脱色、脱臭等
に使われているが、薬液又は水中の微生物、パイロジエ
ンを濾過によって除去するものは見いだされていなかっ
た。これらの点に鑑み、本発明者らは鋭意研究し結果、
活性炭及びパーライトを繊維状マトリックスと混抄して
つくった濾過シートで濾過することによって、薬液中又
は水中の微生物、パイロジエンを効率的に除去できるこ
とを見出し、本発明をなすに至った。
Filter sheets have traditionally been made by mixing diatomaceous earth with cellulose fibers, etc., and have been used for clarification and sterilization filtration, but they are not practical, especially in terms of pyrogen removal performance. Furthermore, sheets made by mixing activated carbon with a fiber matrix have been available for some time, and have been used to decolorize and deodorize colored liquids, but no material has been found that can remove microorganisms and pyrogens in chemical liquids or water by filtration. There wasn't. In view of these points, the inventors of the present invention conducted extensive research, and as a result,
The present inventors have discovered that microorganisms and pyrogens in a chemical solution or water can be efficiently removed by filtering through a filter sheet made by mixing activated carbon and perlite with a fibrous matrix, and have accomplished the present invention.

活性炭は木炭、やしから、鋸屑などの木質或いは石炭な
どを原料として炭化後、高温水蒸気法や塩化亜鉛法によ
って活性化(賦活)させて作った比表面積が大きく、高
い吸着能を示す炭素系物質である。主成分である炭素以
外に酸素、水素等の構成元素やその他の無機成分(灰分
)を含む。又形状側に粒状炭、粉末炭の二つがあり、か
さ密度は約0.3g/cd、平均細孔半径は1〜2n1
)、比表面積は800〜1500m”/g程度である。
Activated carbon is a carbon-based material with a large specific surface area and high adsorption capacity that is made by carbonizing wood such as charcoal, palm, sawdust, or coal, and then activating it using a high-temperature steam method or zinc chloride method. It is a substance. In addition to carbon, which is the main component, it also contains constituent elements such as oxygen and hydrogen, and other inorganic components (ash). There are two types of coal, granular coal and powdered coal, with a bulk density of approximately 0.3g/cd and an average pore radius of 1 to 2n1.
), the specific surface area is about 800 to 1500 m''/g.

一般に活性炭は疏水性(非極性)吸着剤として取り扱わ
れ、非極性物質を選択的によく吸着する性質があるほか
、炭素表面の官能基による化学吸着能、触媒能あるいは
イオン交換等の機能があり、それらの性質を利用されて
各種液体、気体の脱色、脱臭、精製、分離などに幅広く
使われているものである。
Activated carbon is generally treated as a hydrophobic (non-polar) adsorbent, and in addition to having the property of selectively adsorbing non-polar substances, it also has functions such as chemisorption ability, catalytic ability, and ion exchange due to the functional groups on the carbon surface. Taking advantage of these properties, it is widely used for decolorizing, deodorizing, purifying, and separating various liquids and gases.

本発明においては粉末活性炭が好ましく、特に一般に「
製薬用」と呼ばれている精製度の高く、灰分などの不純
物の少ないものが好ましい。この粉末活性炭の比表面積
は800〜15001Ilz/g。
Powdered activated carbon is preferred in the present invention, and is particularly commonly used in
It is preferable to use a highly purified product known as ``pharmaceutical grade'' and low in impurities such as ash. The specific surface area of this powdered activated carbon is 800 to 15001 Ilz/g.

カラメル吸着量(JIS−に1470)は85〜98%
、メチレンブルー吸着量(JIS−に1470)は12
0〜170m l / g sかさ密度は0.20〜0
.35 g/cJ程度のものがよい。
Caramel adsorption amount (JIS-1470) is 85-98%
, methylene blue adsorption amount (JIS-1470) is 12
0~170ml/g s Bulk density is 0.20~0
.. Something around 35 g/cJ is good.

パーライトは濾過助剤の一種で真珠岩を800−120
0℃で加熱、膨張させ、粉砕、分級したもので、その代
表的組成はSiO□ニア6%、A7z03:14%、F
ezOz  : 0.8%、CaO:0.8%、MgO
:0.3%、Ti0z : 0.1%、Na、O:4%
、KzO:5%程度である。又「かさ密度」は0.2〜
0.3 g /cd、粒径は平均1ミクロンから20ミ
クロン程度のものまである。本発明の用途には粒径はな
るべく細かいものが好ましく、その代表的粒径分布は2
0ミクロン以上;1.8%、20−10ミクロン:3.
8%、10〜5ミクロン:14.1%、5〜2ミクロン
57.8%、2ミクロン以下:22.5%、真比重:2
.2、かさ密度: 0.26 g/crl、 pH: 
8〜9である。マトリックス繊維としては天然セルロー
ス繊維、例えば精製リンターパルプや晒クラフトパルプ
のような精製木材パルプが一般的であるが、場合によっ
てはガラス繊維等の無機繊維や、各種合成繊維等も使用
しうる。
Perlite is a type of filter aid, and pearlite is 800-120
It is heated at 0℃, expanded, crushed, and classified, and its typical composition is SiO□nia 6%, A7z03: 14%, F
ezOz: 0.8%, CaO: 0.8%, MgO
: 0.3%, Ti0z: 0.1%, Na, O: 4%
, KzO: about 5%. Also, the "bulk density" is 0.2~
0.3 g/cd, and the particle size ranges from an average of 1 micron to about 20 microns. For the purpose of the present invention, the particle size is preferably as fine as possible, and the typical particle size distribution is 2.
0 micron or more; 1.8%, 20-10 micron: 3.
8%, 10-5 microns: 14.1%, 5-2 microns 57.8%, 2 microns or less: 22.5%, true specific gravity: 2
.. 2. Bulk density: 0.26 g/crl, pH:
It is 8-9. The matrix fibers are generally natural cellulose fibers, such as refined linter pulp or refined wood pulp such as bleached kraft pulp, but in some cases, inorganic fibers such as glass fibers and various synthetic fibers may also be used.

一般にセルロース繊維の叩解度はクレム沈降時間(パル
プ濃度:0.1%)で20〜100seC10〜b ましい。大きい沈降時間は濾過シート中の粉末活性炭や
パーライトの移動、脱落を防ぐのに有効であり、又濾過
効率を高め、シートの強度をあげる。
In general, the degree of freedom of cellulose fibers is preferably 20 to 100 secC10-b in Klemm sedimentation time (pulp concentration: 0.1%). A long settling time is effective in preventing the movement and falling off of powdered activated carbon and perlite in the filter sheet, and also increases the filtration efficiency and strength of the sheet.

セルロース繊維の叩解は単独で行った後に活性炭、パー
ライトを混合するのが一般的であるが、場合によっては
予め活性炭、パーライトと混ぜてから一緒に叩解を行っ
てもよい。いずれにしても粉末活性炭、パーライト及び
繊維マトリックスは均一に混合していることが必要であ
り、それによって最適の吸着、除去性能と濾過量をもっ
たシートが得られる。活性炭の添加量はセルロース繊維
に対して140%以上は必要で、一般に160〜240
%程度が最も好ましい。一方、パーライトの添加量はセ
ルロース繊維に対して70%以上、好ましくは80〜1
20%程度である。シート強度をあげ、或いは吸着性を
更に増加させるためにポリアミドエピクロールヒドリン
縮合体等のカチオン性高分子化合物を固形物全体量に対
して0.5〜5.0%程度添加することも可能である。
Generally, cellulose fibers are beaten alone and then mixed with activated carbon and perlite, but in some cases, they may be mixed with activated carbon and perlite in advance and then beaten together. In any case, it is necessary that the powdered activated carbon, perlite and fiber matrix be uniformly mixed to obtain a sheet with optimum adsorption and removal performance and filtration rate. The amount of activated carbon added must be 140% or more based on the cellulose fiber, and is generally 160 to 240%.
% is most preferable. On the other hand, the amount of perlite added is 70% or more, preferably 80 to 1% of the cellulose fiber.
It is about 20%. In order to increase sheet strength or further increase adsorption properties, it is also possible to add a cationic polymer compound such as polyamide epichlorohydrin condensate in an amount of about 0.5 to 5.0% based on the total amount of solids. It is.

又これらのカチオン性高分子化合物で予めカチオン変性
させたパーライトを使用することも可能である。
It is also possible to use pearlite that has been cationically modified in advance with these cationic polymer compounds.

本発明の濾過シートの厚さは一濾過室当たり3〜9龍、
特に4〜8鰭程度がよい。厚さが薄いと液体の透過流路
が短すぎて吸着が不完全になりやすいし、101)以上
では「わき洩れ」 (エツジリーク)の恐れがある。通
常は一濾過室当たり1枚のシートで作られるが、場合に
よっては薄いものを2枚以上積層して所要の厚さにして
もよい。又シートの重量は一濾過室当たり1700〜2
000 g /m”程度で、その時の水運過速度は濾過
面積18.8cd、濾過圧力1kg/cI1)の条件下
で水100mA’当たり10〜30sec 、特に20
sec程度がこのましい。
The thickness of the filtration sheet of the present invention is 3 to 9 yen per filtration chamber,
In particular, 4 to 8 fins are good. If the thickness is too thin, the liquid permeation channel will be too short and adsorption will tend to be incomplete, and if the thickness exceeds 101), there is a risk of "edge leakage". Usually, one sheet is used for each filtration chamber, but in some cases, two or more thin sheets may be laminated to obtain the desired thickness. Also, the weight of the sheet is 1700~2 per filtration chamber.
000 g/m", and the water transport rate at that time is 10 to 30 seconds per 100 mA' of water, especially 20
Preferably about sec.

60sec以上では濾過速度がかかりすぎ実用的でない
、又10sec以下と早すぎるとシートの空隙が大きく
、吸着時間が不十分である。
If it is 60 seconds or more, the filtration speed is too high and is not practical, and if it is too fast, 10 seconds or less, the voids in the sheet become large and the adsorption time is insufficient.

取り扱い中及び濾過作業中の濾過シートからの活性炭や
パーライト粒子等の脱落を防止するため、第2図に示す
如く予めシートの二次側に目の細かいセルロース繊維や
ガラス繊維製濾紙、或は精密濾過膜等の多孔性シート濾
材3を、−次側には比較的口の粗い濾紙や不織布等の不
織シートを貼付して該濾過シートの保護を行うことも可
能である。
In order to prevent activated carbon and perlite particles from falling off the filter sheet during handling and filtration work, fine cellulose fibers, glass fiber filter paper, or precision It is also possible to protect the porous sheet filter medium 3 such as a filter membrane by attaching relatively coarse filter paper or a non-woven sheet such as non-woven fabric to the downstream side thereof.

この時の接着材料としては液状、固状等いろいろあるが
、特にポリプロピレン等の熱溶融性の不織布が衛生上か
ら好ましい。濾過シートの上に熱溶融性繊維不織布を置
き、更にその上に保護用の上記シートをおいて軽く熱圧
することによって貼付出来る。
At this time, there are various adhesive materials such as liquid and solid, but heat-melting nonwoven fabrics such as polypropylene are particularly preferred from a sanitary standpoint. It can be attached by placing a heat-fusible fibrous nonwoven fabric on top of the filter sheet, and then placing the above-mentioned protective sheet on top of it and applying light heat pressure.

濾過装置は一般に加圧濾過機が使われるが、本発明の濾
過シートを安定的に支持可能の支持多孔部をもち、パツ
キン等のシール部が完全で、「わき洩れ」の心配のない
構造トなっていることが必要である。材質はその用途か
ら考えてステンレスが好ましい。
A pressure filtration machine is generally used as a filtration device, but the filter sheet of the present invention has a support porous part that can stably support it, a seal part such as a packing is perfect, and there is no risk of "spillage". It is necessary that the Considering the intended use, stainless steel is preferable as the material.

(実施例) 以下、本発明の濾過シート及び比較用の濾過シートの製
造例を実施例として挙げ、次いで試験例を挙げて本発明
を具体的に説明する。
(Example) Hereinafter, the present invention will be specifically explained by giving examples of manufacturing a filter sheet of the present invention and a filter sheet for comparison, and then giving test examples.

実施例1 表−1に示す様な組成で本発明に従った濾過シート2種
及び比較例3種の濾過シートを次の方法で作製した。
Example 1 Two types of filter sheets according to the present invention and three types of filter sheets of Comparative Examples having the compositions shown in Table 1 were produced by the following method.

所要量のセルロース繊維を水を張ったビータ−に約1%
濃度に添加し、離解後にビータ−の刃を下ろして所定の
クレム叩解度まで叩解し、ビータ−の刃をあげて所定量
の活性炭及び助剤を添加し、よくかきまぜ混合して抄紙
原料とする。この抄紙原料を使って減圧手抄き装置で厚
さ5〜71)、乾燥重量1500〜1800g/m2の
濾過シートを作製し、105℃で乾燥した。
Add the required amount of cellulose fiber to a beater filled with water at approximately 1%.
After disintegration, lower the beater blade to beat to the specified cream freeness, raise the beater blade, add the specified amount of activated carbon and auxiliary agents, and stir well to mix and use as papermaking raw material. . Using this papermaking raw material, a filtration sheet having a thickness of 5 to 71 mm and a dry weight of 1500 to 1800 g/m2 was produced using a vacuum hand-sheet machine and dried at 105 DEG C.

試験例1 前記実施例1に示す濾過シートによって、パイロジエン
含有脱イオン水及び0.9%食塩水を濾過し、その除去
能及び除去容量を測定した。結果を表−2に示す。
Test Example 1 Pyrodiene-containing deionized water and 0.9% saline were filtered using the filter sheet shown in Example 1, and their removal ability and removal capacity were measured. The results are shown in Table-2.

測定条件: 検液: Ecolt LPS  2.5 ng/ml含
有の脱イオン水及び0.9%食塩水 濾過面積:50d 濾過速度:3cIII/l1in パイロジエン検出法:リムラス法(LimulusAm
ebocyte Lysate Te5t)による。
Measurement conditions: Test solution: Deionized water and 0.9% saline containing Ecolt LPS 2.5 ng/ml Filtration area: 50 d Filtration rate: 3cIII/l1in Pyrogen detection method: Limulus method (LimulusAm
ebocyte Lysate Te5t).

表中の記号: (W):パイロジエン含有脱イオン水 (S):0.9%食塩水 十 :パイロジエン反応あり 一;〃     なし ± :   〃    やや有り 試験例2 前記の実施例1に示す濾過シートによって、パイロジエ
ン含有脱イオン水及び0.9%食塩水を濾過速度をいろ
いろ変えて濾過し、その場合のパイロジエン除去能力の
変化を調べた。結果を表−3に示す。
Symbols in the table: (W): Pyrodiene-containing deionized water (S): 0.9% saline 10: Pyrodiene reaction present - None ±: Slightly present Test Example 2 Filter sheet shown in Example 1 above Pyrodiene-containing deionized water and 0.9% saline were filtered at various filtration speeds, and changes in pyrodiene removal ability were investigated. The results are shown in Table-3.

測定条件:濾過速度以外は試験例1と同じ。Measurement conditions: Same as Test Example 1 except for filtration rate.

表中の記号: (W):パイロジェン含有脱イオン水 (S):0.9%食塩水 + :パイロジェン反応あり 一:〃     なし ± 二   〃    やや有り 3大騒例3 前記の実施例1で作製したr本発明濾過シート2ノを使
って表−4に示すごとき、パイロジエン含有濃度の違っ
た各種検液を濾過し、その場合のパイロジエン除去性能
を調べた。
Symbols in the table: (W): Pyrogen-containing deionized water (S): 0.9% saline +: Pyrogen reaction 1: None ± 2 Slightly present 3 Major case 3 Produced according to Example 1 above Using the filtration sheet 2 of the present invention, various test solutions having different pyrodiene concentrations as shown in Table 4 were filtered, and the pyrodiene removal performance in each case was investigated.

測定条件: 濾過速度=2c!l/1Ilin、これ以外は試験例1
と同じ 表−4 N、D  :不検出 (W):パイロジエン含有脱イオン水 (S):0.9%食塩水 表−5 (発明の効果) 以上詳しく説明したごとく、本発明濾過シートは薬液中
及び水中の微生物、パイロジエンを効率的に除去できる
ばかりが、作業環境を汚染する恐れがなく、処理量の大
きい、微生物及びパイロジエンの新規且つ実用的な濾過
シートであり、医療、医薬関係に益するところ極めて大
である。
Measurement conditions: Filtration rate = 2c! l/1Ilin, other than this test example 1
Same Table-4 N, D: Not detected (W): Pyrodiene-containing deionized water (S): 0.9% saline Table-5 (Effects of the invention) As explained in detail above, the filtration sheet of the present invention can be used in chemical solutions. This is a new and practical filtration sheet for microorganisms and pyrogens, which not only can efficiently remove microorganisms and pyrogens in water, but also has no risk of contaminating the working environment and has a large throughput, and is beneficial for medical and pharmaceutical applications. It is extremely large.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の濾過シートの断面模式図、第2図は両
面に多孔性シートを貼付した本発明の濾過シートの断面
模式図である。 特許出願人 東洋濾紙株式会社他1名 第1図 第2図
FIG. 1 is a schematic cross-sectional view of a filter sheet of the present invention, and FIG. 2 is a schematic cross-sectional view of a filter sheet of the present invention with porous sheets pasted on both sides. Patent applicant: Toyo Roshi Co., Ltd. and one other person Figure 1 Figure 2

Claims (2)

【特許請求の範囲】[Claims] (1)少なくとも粉末活性炭、パーライト及び繊維マト
リックスからなることを特徴とする薬液中または水中の
微生物及びパイロジェンの除去用濾過シート。
(1) A filtration sheet for removing microorganisms and pyrogens in a chemical solution or water, characterized by comprising at least powdered activated carbon, perlite, and a fiber matrix.
(2)濾過シートの両面に多孔性シートを貼付してなる
特許請求の範囲第1項記載の薬液中または水中の微生物
及びパイロジェンの除去用濾過シート。
(2) A filtration sheet for removing microorganisms and pyrogens in a chemical solution or water as set forth in claim 1, which is obtained by pasting porous sheets on both sides of the filtration sheet.
JP62105905A 1987-04-28 1987-04-28 Filtration sheet for removing microorganisms and pyrodiene in chemicals or water Expired - Lifetime JPH0829212B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62105905A JPH0829212B2 (en) 1987-04-28 1987-04-28 Filtration sheet for removing microorganisms and pyrodiene in chemicals or water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62105905A JPH0829212B2 (en) 1987-04-28 1987-04-28 Filtration sheet for removing microorganisms and pyrodiene in chemicals or water

Publications (2)

Publication Number Publication Date
JPS63270516A true JPS63270516A (en) 1988-11-08
JPH0829212B2 JPH0829212B2 (en) 1996-03-27

Family

ID=14419890

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62105905A Expired - Lifetime JPH0829212B2 (en) 1987-04-28 1987-04-28 Filtration sheet for removing microorganisms and pyrodiene in chemicals or water

Country Status (1)

Country Link
JP (1) JPH0829212B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997047330A1 (en) * 1996-06-10 1997-12-18 Johannes Eichenauer Process for disinfecting and/or sterilising of medical instruments or materials, and device for carrying out said process
JP2005161308A (en) * 2003-11-11 2005-06-23 Yamatoyo Sangyo Kk Filter

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55134620A (en) * 1979-04-06 1980-10-20 Amf Inc Filter and preparation of its filter
JPS57207519A (en) * 1981-04-28 1982-12-20 Amf Inc Filter

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55134620A (en) * 1979-04-06 1980-10-20 Amf Inc Filter and preparation of its filter
JPS57207519A (en) * 1981-04-28 1982-12-20 Amf Inc Filter

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997047330A1 (en) * 1996-06-10 1997-12-18 Johannes Eichenauer Process for disinfecting and/or sterilising of medical instruments or materials, and device for carrying out said process
JP2005161308A (en) * 2003-11-11 2005-06-23 Yamatoyo Sangyo Kk Filter
JP4641408B2 (en) * 2003-11-11 2011-03-02 ヤマトヨ産業株式会社 filter

Also Published As

Publication number Publication date
JPH0829212B2 (en) 1996-03-27

Similar Documents

Publication Publication Date Title
ES2367850T3 (en) MANUFACTURING PROCEDURE FOR AN ADSORBENT FILTER MEDIA DESPROVISED OF CELLULOSE FOR THE ELIMINATION OF BIOLOGICAL POLLUTANTS FOR THE TREATMENT OF LIQUIDS.
EP0179495B1 (en) Modified cellulose separation matrix
EP0099586B1 (en) Fibrous media containing millimicron-sized particulates
US8033400B2 (en) Non-woven polymeric fabric including agglomerates of aluminum hydroxide nano-fibers for filtering water
US6838005B2 (en) Nanosize electropositive fibrous adsorbent
JP2005515880A (en) Microporous filter medium, filtration system containing the same, method for production and use thereof
US4596660A (en) Fibrous media containing millimicron-sized particulates
US7601262B1 (en) Sub-micron filter
CN102361689A (en) Sorbent for endotoxins
JP6157751B2 (en) LAMINATED ARTICLE FOR MICROBODY REMOVAL AND LOW PRESSURE LOW FILTRATION, PROCESS FOR PRODUCING THE SAME
JPS63270516A (en) Filter sheet for removing microbe and pyrogen in liquid chemical or water
TWI830845B (en) Filters for water purification and water purifiers equipped with filters
US4404285A (en) Process for preparing a zero standard serum
CN100482316C (en) Microbe filter made from micropore ceramics
CN109518292A (en) A kind of air purifying magnetic coupling fiber and preparation method
SU562173A3 (en) Filter material
CN107998748A (en) Filtering material and preparation method thereof, fluid treatment method and fluid treating plant
EP0082191A1 (en) Process for preparing a zero standard serum.
JPH0342008A (en) Filter sheet used for removing suspended matter in distilled liquor
JPH06312133A (en) Shaped adsorbent
JPS6349212A (en) Adsorptive filter sheet
CN115990361A (en) Depth filter and related method
JPH04247232A (en) Molded adsorbent
Zhenkun et al. A new type of porous membrane filter for the regulation of dust and the removal of particles from aqueous solutions
JPH0716458A (en) Compacted adsorptive body

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080327

Year of fee payment: 12