JPH01139108A - Filtration system - Google Patents
Filtration systemInfo
- Publication number
- JPH01139108A JPH01139108A JP29513287A JP29513287A JPH01139108A JP H01139108 A JPH01139108 A JP H01139108A JP 29513287 A JP29513287 A JP 29513287A JP 29513287 A JP29513287 A JP 29513287A JP H01139108 A JPH01139108 A JP H01139108A
- Authority
- JP
- Japan
- Prior art keywords
- liq
- filtration
- liquid
- housing
- sectional area
- 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.)
- Pending
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 49
- 239000012528 membrane Substances 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims description 52
- 230000002093 peripheral effect Effects 0.000 claims description 10
- 238000000034 method Methods 0.000 abstract description 9
- 230000001681 protective effect Effects 0.000 abstract description 6
- 238000012360 testing method Methods 0.000 abstract description 6
- 239000000706 filtrate Substances 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000004891 communication Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 229910021642 ultra pure water Inorganic materials 0.000 description 2
- 239000012498 ultrapure water Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000011016 integrity testing Methods 0.000 description 1
- 239000008258 liquid foam Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000010186 staining Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は微孔性濾過膜を組込んだ濾過システムに関する
ものであり、特に製薬工業における薬剤の濾過や薬剤製
造に用いられる洗浄水の製造のだめの精製水、純水の濾
過、或いは半導体製造工業を初めとする微細な加工を行
う電子工業分野において使用される超純水製造のための
精製水、純水の濾過、または食品工業におけるアルコー
ル飲料の製造工程における濾過、実験室における超純水
製造のための精製水、純水の濾過その他精密濾過に用い
られ、１０μｍ以下、特に１μｍ以下のサブミクロンオ
ーダーの微粒子や微生物を濾過する精密ｌＲ適用の濾過
システムに関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a filtration system incorporating a microporous filtration membrane, and is particularly applicable to the filtration of drugs in the pharmaceutical industry and the production of washing water used in drug production. Nodame's purified water, filtration of pure water, or purified water for the production of ultrapure water used in the electronics industry that performs fine processing, including the semiconductor manufacturing industry, filtration of pure water, or alcohol in the food industry. Precision IR is used for filtration in the beverage manufacturing process, purified water for ultrapure water production in laboratories, pure water filtration, and other precision filtration, and is used to filter fine particles and microorganisms of submicron order of 10 μm or less, especially 1 μm or less. The present invention relates to a filtration system of application.
従来、第２図に示すように、支持体ｌの上下に濾過膜２
を有した平板型濾過ユニット３を積層し、該濾過ユニッ
トの周辺開口部５より液を取入れ濾過膜２を通し中央開
口部６．コア１５の連通口１４を経てコア１５より濾過
液を取出す平板積層型のフィルターカートリッジ１にお
いて、該フィルターカートリッジの演歌入側保護板８と
ハウジング９との間にはチャンバー１０が存在し、濾過
される液をハウジング９と積層した濾過ユニット３との
間の周辺部４に供給していた。Conventionally, as shown in FIG.
A stack of flat plate type filtration units 3 having a filtration unit 3 and a central opening 6. In the filter cartridge 1 of the flat plate laminated type from which the filtrate is taken out from the core 15 through the communication port 14 of the core 15, a chamber 10 exists between the enka entry side protection plate 8 and the housing 9 of the filter cartridge, and the filtrate is filtered. The liquid was supplied to the peripheral portion 4 between the housing 9 and the stacked filtration units 3.
〔発明が解決しようとする問題点］
しかしながら、従来のフィルターカートリソジのハウジ
ング９は、チャンバー１０の空間が大きいので濾過終了
時のハウジング９内の残液が多いいこと、或はフィルタ
ーカートリッジの濾過前と濾過後に行われるプレッシャ
ーホールド法による完全性試験において、測定精度が不
十分であるという問題があった。[Problems to be Solved by the Invention] However, since the housing 9 of the conventional filter cartridge cartridge has a large space in the chamber 10, there is a problem that there is a lot of liquid remaining in the housing 9 when filtration is completed, or that the filter cartridge is There was a problem in that the measurement accuracy was insufficient in the integrity test using the pressure hold method, which was performed before and after filtration.
このチャンバー１０内の残液は濾過終了時当初は空気圧
によって濾過するよう圧送されたが、その際液の４過の
みならず圧送空気も濾過膜を通過することから濾過液の
汚染および濾過膜の寿命の低下等不都合が生じ最後の空
気圧による圧送は行なわず、フィルターカートリッジ内
の液をそのま〜にしてｉｌ通過作を終了するという作業
を行うこともある。At the end of filtration, the residual liquid in the chamber 10 was initially forced to be filtered by air pressure, but at that time, not only the liquid but also the pressurized air passed through the filtration membrane, resulting in contamination of the filtrate and damage to the filtration membrane. In some cases, due to problems such as shortened service life, the final pneumatic pumping is not performed, and the liquid in the filter cartridge is left as it is to complete the il passing operation.
したがって、フィルターカートリッジを収納するハウジ
ング９内の液を残留させることになるので、残留液を少
くすることが望まれている。またプレッシャーホールド
法による完全試験ではフィルターカートリッジの１次側
の体積が大きく、前述の如く測定精度が良くないのでな
るべく１次側の体積を小さくしたいという望みがあった
。Therefore, since the liquid remains in the housing 9 that houses the filter cartridge, it is desired to reduce the amount of residual liquid. Further, in a complete test using the pressure hold method, the volume of the primary side of the filter cartridge is large, and as mentioned above, the measurement accuracy is not good, so there was a desire to reduce the volume of the primary side as much as possible.
本発明は上記要望に応じ、濾過液のｌＦｉ染をなくし、
濾過膜の寿命も長く保ち、且つ残留液の少なくプレンシ
ャーホールド法による完全性試験の精度を向上させる濾
過システムを提供することを目的とする。In response to the above needs, the present invention eliminates lFi staining of the filtrate,
It is an object of the present invention to provide a filtration system that maintains the life of a filtration membrane for a long time, has a small amount of residual liquid, and improves the accuracy of an integrity test using a pressure hold method.
〔問題点を解決するための手段］
本発明の上記目的は支持体の上下に濾過膜を有した平板
型１１ｔｉｌＪユニツトを積層し、該濾過ユニッｉ・の
周辺開口部より液を取入れ、濾過膜を通し、中央開口部
より濾過液を取出すフィルターカートリッジとハウジン
グからなる濾過システムにおいて、該フィルターカート
リッジの液収入口側保護板とハウジング蓋面との間の液
体取入流路の小間隙の断面積Ｙが液取入口の断面積Ｘに
対し０．７≦÷≦１．２であることを特徴とする濾過シ
ステムによって達成される。[Means for Solving the Problems] The above object of the present invention is to stack flat plate-type 11tilJ units having filtration membranes on the upper and lower sides of a support, take in liquid from peripheral openings of the filtration units, and remove the filtration membranes. In a filtration system consisting of a filter cartridge and a housing, through which the filtrate is taken out from the central opening, the cross-sectional area Y of the small gap of the liquid intake channel between the liquid inlet side protection plate of the filter cartridge and the housing lid surface This is achieved by a filtration system characterized in that 0.7≦÷≦1.2 for the cross-sectional area X of the liquid intake port.
本発明において該フィルターカートリッジの液収入口側
保護板、とハウジング蓋面との間の液体取入流路として
の小間隙の断面積Ｙが液取入口の断面積Ｘに対し０．７
≦−’！−＜１．２ということは、従来のごとく液が寥
入口より一度広いチャンバーに入るそのチャンバーを設
けることなく、平板積７ｉ型フィルターカートリッジの
ハウジングの蓋面を液収入口側保護板の上面に近接させ
る様に配置し、ハウジング蓋面か又は演歌入口側ハウジ
ングの内面と液収入口側保護板のそれより広い通路面積
で上面の間に液体の取入流路としての小間隙を例えば放
射状または平面状に設は液取入口の面積に近く多少低い
流れ抵抗で濾過液を濾過ユニットの周辺部に分布させる
ことをいう。In the present invention, the cross-sectional area Y of the small gap serving as the liquid intake channel between the liquid inlet side protective plate of the filter cartridge and the housing lid surface is 0.7 with respect to the cross-sectional area X of the liquid inlet.
≦−'! -<1.2 means that the lid surface of the housing of the flat plate type 7i filter cartridge is placed on the top surface of the protective plate on the liquid inlet side, without providing a chamber where the liquid enters a wider chamber once from the main inlet as in the conventional case. A small gap between the housing lid surface or the inner surface of the housing on the enka inlet side and the upper surface with a passage area wider than that of the liquid inlet side protective plate is formed as a liquid intake flow path, for example, in a radial or planar manner. The method of distributing the filtrate around the periphery of the filtration unit is close to the area of the liquid intake port and has a somewhat lower flow resistance.
本発明は上記の如く、該フィルターカートリッジの液取
入口の下に液を分布する広い空間を設けることなく、液
収入口側保護板とハウジング蓋面との間にどちら側が接
近してもよいが液取入口の断面積Ｘに対し液体取入れ流
路としての小間隙の断面積Ｙを０．７≦−≦１．２に設
定させたことによって、液の溜りがなくなるので残留液
の少ない濾過システムを提供することが出来る。また同
様にフィルターカートリッジのハウジング内の１次側空
間体積が小さいので、プレッシャーホールｌ法による完
全試験の精度を向上させることができる。As described above, in the present invention, there is no need to provide a wide space for distributing the liquid under the liquid intake port of the filter cartridge, and either side may be close between the liquid inlet side protective plate and the housing cover surface. By setting the cross-sectional area Y of the small gap serving as the liquid intake flow path to 0.7≦-≦1.2 with respect to the cross-sectional area X of the liquid intake port, there is no accumulation of liquid, resulting in a filtration system with less residual liquid. can be provided. Similarly, since the primary space volume within the housing of the filter cartridge is small, the accuracy of the complete test using the pressure hole method can be improved.
本発明の１実施例を図によって説明する。但し本発明は
本実施例のみに限られるものではない。An embodiment of the present invention will be described with reference to the drawings. However, the present invention is not limited to this embodiment.
第１図は本発明の１実施例の部分横断面図である。平板
積層型フィルターカートリッジ−７−に入る液は液取入
口１１より液収入側保護板８とハウジングの蓋面１３と
の間に分布して設けられた小間隙の断面積を液取入口の
断面積の１． ２倍にとった、液体取入流路１２を通っ
て濾過ユニット３の周囲ハウジング９の周辺部４に分布
させる。FIG. 1 is a partial cross-sectional view of one embodiment of the present invention. The liquid entering the flat plate laminated filter cartridge -7- passes through the liquid intake port 11 through the cross-sectional area of the small gap distributed between the liquid intake side protection plate 8 and the lid surface 13 of the housing. Area 1. It is distributed to the periphery 4 of the peripheral housing 9 of the filtration unit 3 through the liquid intake channel 12, which is doubled.
０液は周辺部４より、濾過ユニット３の周辺開口部５を
通って濾過ユニット３間の間隙部内に取入れられ、支持
体ｌの上下に取付けられた濾過膜２によって精密濾過さ
れた液が中央開口部６を通って連通口 １４よりコア１
５に流れ込み集まってフィルターカートリッジの外部に
導かれるようになっている。The 0 liquid is taken into the gap between the filtration units 3 from the peripheral part 4 through the peripheral opening 5 of the filtration unit 3, and the liquid microfiltered by the filtration membranes 2 attached above and below the support l is taken into the center. Core 1 through the opening 6 and from the communication port 14
5, where it gathers and is guided to the outside of the filter cartridge.
濾過開始時、濾過される液は先ず平板積層型フィルター
カートリッジエの取入口１１より周辺部４を満たすがそ
の際のハウジング９内の空気は空気抜き１６より排出さ
れてハウジング内は液のみで満たされる。液泡入口保護
板８とハウジング蓋１３又は９との関係の変形について
は第３図（ａ）。At the start of filtration, the liquid to be filtered first fills the peripheral portion 4 from the intake port 11 of the flat plate laminated filter cartridge, but at this time the air inside the housing 9 is exhausted from the air vent 16 and the inside of the housing is filled only with liquid. . FIG. 3(a) shows a modification of the relationship between the liquid bubble inlet protection plate 8 and the housing lid 13 or 9.
（ｂ）の様なものも本発明の範囲に含まれる。Items like (b) are also included within the scope of the present invention.
本発明は従来のチャンバー１０が小間隙の液体取入流路
１２になったため、空気抜きの時間も短縮出来るし、濾
過操作が終了した時もハウジング内の溜る液が少なくな
ったことにより濾過される液の無駄を少なくすることお
よびプレッシャーホールド法による完全性試験による測
定結果の精度も向上する。In the present invention, since the conventional chamber 10 is replaced with a liquid intake passage 12 with a small gap, the time for air removal can be shortened, and even when the filtration operation is completed, the amount of liquid accumulated in the housing is reduced, so that the liquid to be filtered is reduced. This also improves the accuracy of measurement results from integrity testing using the pressure hold method.
〔発明の効果］
本発明は支持体の上下に濾過膜を有した平板型濾過ユニ
ットを積層し、該濾過ユニットの周辺開口部より液を取
入れ、濾過膜を通し、中央開口部より濾過液を取出すフ
ィルターカートリッジとハウジングからなる濾過システ
ムにおいて、該フィルターカートリッジの液泡入口側保
護板とハウジングとの間の液体取入流路の小間隙の断面
積Ｙが液泡入口の断面積Ｘに対し０．７≦五≦１ 、
２であることを特徴とする濾過システムによって、ｉ！
ｌｉＡ後の残留液の少ないフィルターカートリッジを堤
供することが出来た。これによって濾過液の品質向上及
び濾過膜の寿命を伸ばすことも出来た。[Effects of the Invention] The present invention stacks flat plate type filtration units having filtration membranes above and below a support, takes in liquid from the peripheral openings of the filtration units, passes through the filtration membranes, and drains the filtrate from the central opening. In a filtration system consisting of a filter cartridge to be taken out and a housing, the cross-sectional area Y of the small gap of the liquid intake channel between the liquid bubble inlet side protection plate of the filter cartridge and the housing is 0.7≦with respect to the cross-sectional area X of the liquid bubble inlet. 5≦1,
By means of a filtration system characterized by 2, i!
We were able to provide a filter cartridge with less residual liquid after liA. This also improved the quality of the filtrate and extended the life of the filtration membrane.
第１図は本発明の平板積層型フィルターカートリッジの
部分横断面図、第２図は従来の平板積層型フィルターカ
ートリッジの部分横断面図、第３図は本発明の液泡入口
保護板とハウジング蓋面との関係の他の実施例の部分断
面図である。
１・・・支持体 ２・・・濾過膜３・・・濾過
ユニット ４・・・周辺部５・・・周辺開口部
６・・・中央開口部−７−・・・平板積層型フィルター
カートリッジ８・・・液泡入口側保護板
９・・・ハウジング １０・・・チャンバー１１・・
・液泡入口
１２・・・液体取入流路
１３・・・蓋面 １４・・・連通口１５・・・コ
ア １６・・・空気抜き代理人 弁理士（８１
０７）佐々木 清隆第 １ 図FIG. 1 is a partial cross-sectional view of a flat laminated filter cartridge of the present invention, FIG. 2 is a partial cross-sectional view of a conventional flat laminated filter cartridge, and FIG. 3 is a liquid bubble inlet protection plate and housing lid surface of the present invention. FIG. 1... Support body 2... Filtration membrane 3... Filtration unit 4... Peripheral part 5... Peripheral opening
6...Central opening -7-...Flat stacked filter cartridge 8...Liquid bubble inlet side protection plate 9...Housing 10...Chamber 11...
・Liquid foam inlet 12...Liquid intake channel 13...Lid surface 14...Communication port 15...Core 16...Air vent agent Patent attorney (81
07) Kiyotaka Sasaki Figure 1
Claims (1)
層し、該濾過ユニットの周辺開口部より液を取入れ、濾
過膜を通し、中央開口部より濾過液を取出すフィルター
カートリッジとハウジングからなる濾過システムにおい
て、該フィルターカートリッジの液取入口側保護板とハ
ウジング蓋面との間の液体取入流路の小間隙の断面積Ｙ
が液取入口の断面積Ｘに対し０．７≦Ｘ／Ｙ≦１．２で
あることを特徴とする濾過システム。Filtration consisting of a filter cartridge and a housing in which flat plate type filtration units with filtration membranes are stacked on top and bottom of a support, liquid is taken in from the peripheral opening of the filtration unit, passed through the filtration membrane, and filtrated liquid is taken out from the central opening. In the system, the cross-sectional area Y of the small gap of the liquid intake channel between the liquid intake side protection plate of the filter cartridge and the housing lid surface
is 0.7≦X/Y≦1.2 with respect to the cross-sectional area X of the liquid intake port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29513287A JPH01139108A (en) | 1987-11-25 | 1987-11-25 | Filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29513287A JPH01139108A (en) | 1987-11-25 | 1987-11-25 | Filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01139108A true JPH01139108A (en) | 1989-05-31 |
Family
ID=17816698
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29513287A Pending JPH01139108A (en) | 1987-11-25 | 1987-11-25 | Filtration system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01139108A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008264779A (en) * | 2007-04-23 | 2008-11-06 | Millipore Corp | Filtration cartridge |
| US10617603B2 (en) | 2016-01-22 | 2020-04-14 | Baxter International Inc. | Sterile solutions product bag |
| US11021275B2 (en) | 2016-01-22 | 2021-06-01 | Baxter International Inc. | Method and machine for producing sterile solution product bags |
-
1987
- 1987-11-25 JP JP29513287A patent/JPH01139108A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008264779A (en) * | 2007-04-23 | 2008-11-06 | Millipore Corp | Filtration cartridge |
| US10617603B2 (en) | 2016-01-22 | 2020-04-14 | Baxter International Inc. | Sterile solutions product bag |
| US11021275B2 (en) | 2016-01-22 | 2021-06-01 | Baxter International Inc. | Method and machine for producing sterile solution product bags |
| US11564867B2 (en) | 2016-01-22 | 2023-01-31 | Baxter International Inc. | Sterile solutions product bag |
| US11623773B2 (en) | 2016-01-22 | 2023-04-11 | Baxter International Inc. | Method and machine for producing sterile solution product bags |
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