WO2011072008A2 - Moyen permettant de tester l'intégrité de filtration dans un système de purification de liquide - Google Patents
Moyen permettant de tester l'intégrité de filtration dans un système de purification de liquide Download PDFInfo
- Publication number
- WO2011072008A2 WO2011072008A2 PCT/US2010/059454 US2010059454W WO2011072008A2 WO 2011072008 A2 WO2011072008 A2 WO 2011072008A2 US 2010059454 W US2010059454 W US 2010059454W WO 2011072008 A2 WO2011072008 A2 WO 2011072008A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filter
- pressure
- liquid
- integrity test
- filter element
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/10—Testing of membranes or membrane apparatus; Detecting or repairing leaks
- B01D65/104—Detection of leaks in membrane apparatus or modules
Definitions
- the present invention relates to filtration equipment, and in particular, the present invention relates to a purification system that includes a single stage filter and a means to perform a filter integrity test on this filter.
- the other filter serves as a back-up.
- a purification system includes a single stage filter and a means to perform a filter integrity test on this filter, whereby the purification system is able to detect when water is being used by the downstream equipment and thereby coordinate when a filter integrity test is to be performed that does not adversely effect the operation of the downstream
- the system permits a flushing of the upstream filter compartment to remove accumulated particulate from the source water which can increase the life of the filter.
- the filter flush steps can also be coordinated so as not to interfere with the operation of the downstream equipment. For example, the filter is flushed only when no water is being commanded by the downstream equipment.
- a method for performing a filter integrity test in a liquid purification system that is configured to purify a liquid from a liquid source using a filter device and deliver the purified liquid to external
- downstream equipment includes the steps of: (1 ) monitoring when the external downstream equipment is receiving and using purified liquid from the filter device; and (2) initiating the filter integrity test only when the external downstream equipment is not commanding purified liquid.
- FIG. 1 illustrates components of a liquid purification system in accordance with one embodiment of the present invention
- Fig. 2 is a cross-sectional view of a filter device used in the system of Fig. 1 ;
- Fig. 3 illustrates the liquid purification system of Fig. 1 in a first standard operating mode where purified liquid is not delivered to external equipment;
- Fig. 4 illustrates the liquid purification system of Fig. 1 in a second standard operating mode where purified liquid is delivered to the external equipment;
- Fig. 5 illustrates the liquid purification system of Fig. 1 when a first step of a filter test operation is performed
- Fig. 6 illustrates the liquid purification system of Fig. 1 when a second step of a filter test operation is performed;
- Fig. 7 illustrates the liquid purification system of Fig. 1 when a third step of a filter test operation is performed.
- Fig. 8 illustrates the liquid purification system of Fig. 1 when a filter flush operation is performed.
- Fig. 1 illustrates a purification system 100 in accordance with the present invention.
- the purification system 100 includes a water source 110 that contains raw (unfiltered) water.
- the purification system 100 includes a filtration device 200 that is connected to the water source 10 via a first conduit 120.
- a first connector 130 can be used to connect the first conduit 120 to the filtration device 200.
- a conduit segment 122 extends from the first connector 130 to an inlet 210 of the filtration device 200 which can include a second connector 225.
- a first valve 140 is provided and at least includes an open position and a closed position.
- the first valve 140 can be any number of different types of valves. As described below, the first valve 140 is in communication with a controller 105 that controls operation of the first valve 140.
- the filtration device 200 includes a first end 202 and an opposing second end 204 with the inlet 210 being formed at the first end 202 and an outlet 220 being formed at the second end 204.
- the filtration device 200 includes a housing 230 that contains a plurality of semi-permeable membranes (first filter elements) 235 that serve as the filtering media of the device 200.
- the semipermeable membranes 235 can be in the form of a plurality of fibers that are arranged in a bundle.
- the housing 230 also includes a pair of potting compounds 231 , 232 that are disposed at opposite ends 202, 204 of the housing 230.
- the potting compound (e.g., polyurethane) provides an environmental barrier and encapsulates the semi-permeable membranes 235 in the housing 230.
- the potting compound forms a seal around the outside surfaces of the semi-permeable membranes.
- the potting compounds 231 , 232 do not seal the ends of the semi-permeable membranes 235 but instead, the ends of the semi-permeable membranes 235 are open at ends 202, 204 of the housing 230.
- the housing includes a first header cap 240 that is coupled to the first end 202 of the housing 230 and a second header cap 242 that is coupled to the second end 204 of the housing 230.
- first and second header caps 240, 242 are removably (detachably) coupled to the housing 230.
- the first header cap 240 defines a first header space 244 that is formed between the first header cap 240 and the open ends of the semi-permeable membranes 235 and first potting compound 231.
- the second header cap 242 defines a second header space 246 that is formed between the second header cap 242 and the opposite open ends of the semi-permeable membranes 235 and second potting compound 232.
- the first header cap 240 includes a port that provides communication with the first header space 244 and thus, provides fluid communication with the semipermeable membranes 235.
- the port is in the form of inlet 2 0 since it permits fluid (from the source 110) to enter the first header space 244.
- the second header cap 242 includes a port that communicated with the second header space 246 and thus, provides fluid communication with the semipermeable membranes 235.
- This port is in the form of outlet 220 since it permits liquid to flow out of the housing.
- the filtering media has been described as a plurality of semi-permeable membranes (fibers), it will be appreciated that it can take other forms that suitable for the disclosed filter applications.
- the housing can have any number of different shapes.
- a third connector 250 (Fig.1 ) that permits a conduit or line to be fluidly attached to the housing at this end.
- the housing also includes a third port 260 that is located along a side thereof and communicates within an interior of the housing and in particular, is in
- the third port 260 attaches to a fourth connector 270 (Fig. 1 ) that is connected to an output conduit or line 280 that is intended to carry purified (ultrafiltered) liquid (water) from the filter device 200 to an external device 300 that demands purified liquid.
- the external device 300 can be in the form of medical reprocessing equipment that as discussed herein requires purified, ultrafiltered water.
- a fifth connector 290 can connect the conduit 280 to the external device 300.
- the external device 300 includes a valve 301 that can be operated between an open position where fluid flows into the external device 300 and a closed position where fluid is prevented from flowing to the external device 300.
- the valve 301 is thus in fluid communication with the output conduit 280.
- the purification system 100 includes a number of components that are configured to test the integrity of the filter device 200 in a manner that overcomes the disadvantages associated with conventional integrity test systems as described above.
- the system 100 includes an air input component 400 that is designed to introduce ambient air, at a selected time, into the filter device 200. More specifically, the air input component 400 serves to introduce ambient air into the interior of the filter device 200 and more particularly, into the hollow lumens of the semi-permeable membranes 235.
- the air is delivered from a source (e.g.
- a device 500 is provided for detecting and sensing pressure. More particularly, the device 500 is in the form of a differential pressure sensor (transducer) that measures the difference between two pressures introduced as inputs to a sensing unit that is part of the device 500. In the present embodiment, the pressure sensing device 500 can be used to measure the pressure differential across the filter media (i.e., semi-permeable membranes 235).
- the pressure within the semi-permeable membranes 235 can be sensed and compared to an external pressure (outside the semipermeable membranes 235).
- the pressure sensing device 500 can be operatively connected to the device 200 to sense the pressure within the semi-permeable membranes 235 and the pressure within the ouput conduit or line 280 (e.g., of the output liquid downstream of the filter). In this manner, the pressure differential across the filter media (semi-permeable
- membranes 235 can be determined.
- the purification system 00 includes a mechanism for flushing the filter device 200 and in particular, the filter device 200 can include a flush device 600 that includes a flush conduit or line 610.
- the flush conduit 610 is in fluid communication with a drain or waste 700 to permit the fluid that is used to flush the filter device 200 to be disposed of.
- a third valve 620 is provided along the flush conduit 610.
- the third valve 620 is operational between an open position where the fluid is delivered to the drain or waste 700 and a closed position.
- the third valve 620 is in communication with the controller 105.
- the purification system 100 also includes a vent line or conduit 800.
- the vent line 800 includes a first end 802 and a second end 804 with the first end 802 being in fluid communication with the output conduit 280 and in particular, the first end 802 of the vent line 800 is located proximate the fourth connector 270.
- the second end 804 of the vent line 800 is in communication with the flush conduit 610 at a location downstream of the third valve 620.
- the vent line 800 is thus in fluid communication with the drain or waste 700.
- a fourth valve 810 is provided along the vent line 800.
- the fourth valve 810 is operational between an open position where the fluid is delivered to the drain or waste 700 and a closed position.
- the fourth valve 810 is in communication with the controller 105.
- the drain or waste 700 can be fluidly connected to another conduit that delivers waste fluid to the waste 700.
- a waste or drain line 900 that is associated with the external device 300 delivers waste fluid to the drain or waste 700.
- a tee connector 1000 can be provided for linking the flush conduit 610 and the drain line 900 with the drain or waste 700.
- a device 1 100 for displaying an integrity status signal can be provided.
- the device 1 100 can display different information and indicia for indicating the operating status of the purification system 100.
- the device 1 100 can display an indicator that the filter (filter device 200) passed the integrity test and an indicator that the filter failed the integrity test.
- the word "PASS" or "FAIL” can be displayed or a green light can be displayed when the filter passes and a red light can be displayed when the filter fails.
- a user interface 1200 can be provided and includes a display 1210, a first button 1220 and a second button 1230.
- the user interface 1200 may allow the user to set various parameters associated with its operation for a particular type of equipment.
- the display 1210 can be a single line display showing the filtration process step as described below.
- buttons 1220, 1230 can include buttons, such as buttons 1220, 1230 to reset the summed number of "Fill” or “Use” operations at any point in time such that is stays coordinated with the downstream equipment operations.
- An additional Button may also be included to allow the user to replace the filter without shutting off the source water and perform an automated priming routine (not shown).
- the button 1220 can be a filter "install” button and upon actuation, results in the closing of the first valve 40 and allows one to install a new filter 200 and then prime the filter 200.
- the button 1230 can be a reset "fill counter” button to provide a means for the purification system 100 to be in sync, with the start of the reprocessing equipment cycle.
- the purification system 100 is configured using a single stage filter (filter device 200) and a means to perform a filter integrity test on this filter, whereby the purification system 100 is able to detect when water is being used by the downstream equipment and thereby coordinate when a filter integrity test is to be performed that does not adversely affect the operation of the downstream equipment.
- a flushing of the upstream filter compartment to remove accumulated particulate from the source water is used to increase the life of the filter.
- the filter flush steps can also be coordinated so as not to interfere with the operation of the downstream equipment 300.
- the filter (filter device 200) can be flushed only when no water is being commanded by the downstream equipment 300.
- Fig. 3 shows a standard operating mode when the external downstream equipment 300 does not command water and the valve 301 is closed. In this operating mode, purified water that has been filtered by the device 200 is not delivered to the external equipment 300.
- the pressure sensing device 500 detects that the differential pressure across the filter membrane (semi-permeable
- the membranes 235 is zero since the upstream pressure (pressure within the semipermeable membranes 235) is at least substantially equal to the downstream pressure (the pressure within the output conduit or line 280) when no flow across the membrane occurs.
- valves 420, 620, 8 0 are closed in this operating mode.
- Fig. 4 shows another standard operating mode when the external downstream equipment 300 commands purified fluid (water) by opening its fluid inlet valve 301.
- Purified fluid (water) is delivered to the external downstream equipment 300, for example during a FILL or RINSE operation.
- the differential pressure across the filter membrane becomes positive (upstream pressure is greater than downstream pressure) as detected by the device 500.
- the signal is monitored by the control unit (controller 105) and upon seeing a positive level (e.g., a level that exceeds a pre-determined threshold), the control unit 105 stores this as a "fill” or "use” operation in its memory. Successive "fill” or “use” operations are also detected, whereby a total sum of "fill” or “use” operations detected can be stored in the internal memory of the control unit.
- a positive level e.g., a level that exceeds a pre-determined threshold
- the fluid (water) is filtered by flowing from the source 110 into the filter device 200 and is then filtered across the semi-permeable membranes 235 to generate purified liquid that is flows out through the third port 260 into the output conduit 280 to the external device 300.
- the valves 420, 620, 810 are closed in this operating mode.
- Fig. 5 shows an integrity filter test process and in particular, Fig. 5 shows a first step of the integrity filter test process.
- the first step is process where the filter device 200 is vented.
- a filter test routine or process is initiated whereby the inlet valve (first valve) 140 is closed and the vent valve 810 is open to vent the filter pressure.
- fluid water
- the differential pressure transducer 500 detects the differential pressure transducer 500.
- Fig. 6 shows an integrity filter test process and in particular, Fig. 6 shows a second step of the integrity filter test process.
- the second step is a step where the filter device 200 is pressurized with air. In this operating mode, the air valve 420 is opened and the pump 410 is turned on to fill the upstream compartment
- membrane 235 of the filter 200 with air.
- the air displaces the internal water whereby it is pushed across the filter membrane 235 and flows along the vent line 800 to the drain output 700.
- Fig. 7 shows an integrity filter test process and in particular, Fig. 7 shows a third step of the integrity filter test process.
- the third step is a pressure decay measurement step.
- the air valve 420 is closed and a specified stabilization period is performed to allow pressures to stabilize.
- the starting pressure measured at the differential pressure transducer 500 is recorded and the ending pressure is recorded after a specified test period has elapsed. The net difference between these readings (starting pressure minus ending pressure) is compared to a pre-established value to determine if the filter (filter device 200) passes or fails the integrity test.
- the "fill" or “use” counter may be reset to zero and the system 100 may be put into its standard operating mode as described above.
- the inlet valve 40 may be kept closed to prevent any subsequent passage of water to the downstream equipment 300.
- An optional red status light (display 1100) can be illuminated to alert the user that the filter 200 failed and must be replaced.
- the user can repeat the cycle performed by the downstream equipment. This assures that only good purified liquid (water) from an intact filter is delivered to the downstream equipment 300.
- Fig. 8 shows a filter flush operation which involves the periodic flushing of the upstream filter compartment.
- downstream equipment 300 In other words, it can be performed when the downstream equipment 300 is IDLE (i.e., not calling for water).
- the flush valve 620 may be open for a specified period of time to flush accumulated particulate from the upstream side of the filter 200. This has the effect of increasing the useful life of the filter before it becomes too fouled to produce a sufficient quantity of water for the downstream equipment.
- the flush operation can be programmed to occur at a set frequency or it can be tied to a set number of "fill" or "use” operations that have been detected.
- the flush valve 620 is closed and the system 00 is placed back in the standard operating mode as described herein.
- a separate signal (such as an electrical signal) can be generated by the system and sent to the downstream equipment 300 which can be used to determine the status of water purification unit 100, e.g. the signal could be different when the filter has FAILED an integrity test - this signal can be used to alert the user of the downstream equipment that there is a problem with the water purification unit; (3) different mechanisms that are known in the art can be used to detect when the water is being commanded by the downstream equipment 300.
- a flow detector or flow switch can be used to detect the flowing condition; and (4) it will be appreciated that different methods that are known in the art can be used to test filter integrity - this can include an air bubble detection unit on the downstream side of the filter as a Bubble-point type measurement, or an Air Flow test whereby the flow rate of air is measured which is needed to maintain a constant pressure in the upstream compartment.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2783544A CA2783544A1 (fr) | 2009-12-10 | 2010-12-08 | Moyen permettant de tester l'integrite de filtration dans un systeme de purification de liquide |
EP10836607A EP2509705A2 (fr) | 2009-12-10 | 2010-12-08 | Moyen permettant de tester l'intégrité de filtration dans un système de purification de liquide |
JP2012543242A JP2013513470A (ja) | 2009-12-10 | 2010-12-08 | 液体浄化システムにおいてフィルター完全性を検査するための手段 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US28529209P | 2009-12-10 | 2009-12-10 | |
US61/285,292 | 2009-12-10 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2011072008A2 true WO2011072008A2 (fr) | 2011-06-16 |
WO2011072008A3 WO2011072008A3 (fr) | 2011-12-15 |
Family
ID=44141423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2010/059454 WO2011072008A2 (fr) | 2009-12-10 | 2010-12-08 | Moyen permettant de tester l'intégrité de filtration dans un système de purification de liquide |
Country Status (5)
Country | Link |
---|---|
US (1) | US20110138936A1 (fr) |
EP (1) | EP2509705A2 (fr) |
JP (1) | JP2013513470A (fr) |
CA (1) | CA2783544A1 (fr) |
WO (1) | WO2011072008A2 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109932199A (zh) * | 2019-03-22 | 2019-06-25 | 中国家用电器研究院 | 一种用于***测试的方法 |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3536361B1 (fr) | 2011-03-23 | 2020-10-07 | NxStage Medical Inc. | Systèmes, dispositifs et procédés de dialyse péritonéale |
US9861733B2 (en) | 2012-03-23 | 2018-01-09 | Nxstage Medical Inc. | Peritoneal dialysis systems, devices, and methods |
DE102011082284A1 (de) * | 2011-09-07 | 2013-03-07 | Krones Aktiengesellschaft | Hygienischer Integritätstest bei Ultrafiltrationsanlagen |
BR112015015236A2 (pt) | 2012-12-27 | 2017-07-11 | Medi Physics Inc | conjunto de conduto de teste de integridade dupla de filtro duplo, e, método para dispensar um líquido de produto |
WO2016109230A2 (fr) * | 2014-12-30 | 2016-07-07 | Emd Millipore Corporation | Soupape à évent de filtre aseptique et orifice pour essai d'intégrité |
DE102015104539B4 (de) * | 2015-03-25 | 2022-04-28 | Sartorius Stedim Biotech Gmbh | Verfahren zur Qualitätssicherung von Filtrationsprozessen |
KR102189598B1 (ko) | 2015-11-20 | 2020-12-11 | 이엠디 밀리포어 코포레이션 | 향상된 안정도의 필터 완전성 시험 |
WO2018162981A1 (fr) * | 2017-03-07 | 2018-09-13 | 1934612 Ontario Inc. | Systèmes et procédés de test direct d'intégrité de membranes basé sur un marqueur |
CA3092575A1 (fr) | 2018-02-28 | 2019-09-06 | Nxstage Medical, Inc. | Dispositifs, procedes et systemes de preparation de fluide et de traitement |
EP3560577A1 (fr) | 2018-04-25 | 2019-10-30 | Gambro Lundia AB | Appareil et procédé pour tester l'intégrité d'une membrane d'ultrafiltration |
US10859459B2 (en) * | 2019-01-24 | 2020-12-08 | R.J. Reynolds Tobacco Company | System and method for pressure sensor testing and verification |
US20230211260A1 (en) * | 2021-12-31 | 2023-07-06 | Pall Corporation | Fluid filtration system with single use filter and method of using same for automated filter conditioning |
US20230211263A1 (en) * | 2021-12-31 | 2023-07-06 | Pall Corporation | Fluid filtration system with single use filter and integrated integrity test device and method of using same |
US20230211265A1 (en) * | 2021-12-31 | 2023-07-06 | Pall Corporation | Bulk fill system with serial fluid filtration assembly and method of using same for automated air transfer |
CN114713037B (zh) * | 2022-06-10 | 2022-09-20 | 北京先通国际医药科技股份有限公司 | 在线滤膜完整性测试装置及方法、及其用途 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4806912A (en) * | 1987-06-19 | 1989-02-21 | Clack Robert A | Monitoring system for a liquid purification system |
US5401399A (en) * | 1993-08-27 | 1995-03-28 | Magnusson; Jan H. | Water purification system |
US5779911A (en) * | 1996-04-10 | 1998-07-14 | Haug; Irving M. | Aqueous fluid purification monitoring and control system and process |
US6090294A (en) * | 1995-06-23 | 2000-07-18 | Ajt & Associates, Inc. | Apparatus for the purification of water and method therefor |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995006515A1 (fr) * | 1993-08-30 | 1995-03-09 | Pfizer Inc. | Appareil et procede de test de filtres hydrophobes |
US5788927A (en) * | 1996-07-30 | 1998-08-04 | Bayer Corporation | Unified fluid circuit assembly for a clinical hematology instrument |
US6906292B2 (en) * | 1998-10-29 | 2005-06-14 | Applera Corporation | Sample tray heater module |
US6649063B2 (en) * | 2001-07-12 | 2003-11-18 | Nxstage Medical, Inc. | Method for performing renal replacement therapy including producing sterile replacement fluid in a renal replacement therapy unit |
US7569182B2 (en) * | 2003-08-01 | 2009-08-04 | American Sterilizer Company | Filter assembly for a reprocessor |
US7650805B2 (en) * | 2005-10-11 | 2010-01-26 | Millipore Corporation | Integrity testable multilayered filter device |
AU2007224278B2 (en) * | 2006-03-06 | 2010-07-29 | American Sterilizer Company | A container for holding items to be microbially deactivated in a reprocessor |
-
2010
- 2010-12-08 CA CA2783544A patent/CA2783544A1/fr not_active Abandoned
- 2010-12-08 WO PCT/US2010/059454 patent/WO2011072008A2/fr active Application Filing
- 2010-12-08 EP EP10836607A patent/EP2509705A2/fr not_active Withdrawn
- 2010-12-08 US US12/963,150 patent/US20110138936A1/en not_active Abandoned
- 2010-12-08 JP JP2012543242A patent/JP2013513470A/ja active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4806912A (en) * | 1987-06-19 | 1989-02-21 | Clack Robert A | Monitoring system for a liquid purification system |
US5401399A (en) * | 1993-08-27 | 1995-03-28 | Magnusson; Jan H. | Water purification system |
US6090294A (en) * | 1995-06-23 | 2000-07-18 | Ajt & Associates, Inc. | Apparatus for the purification of water and method therefor |
US5779911A (en) * | 1996-04-10 | 1998-07-14 | Haug; Irving M. | Aqueous fluid purification monitoring and control system and process |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109932199A (zh) * | 2019-03-22 | 2019-06-25 | 中国家用电器研究院 | 一种用于***测试的方法 |
Also Published As
Publication number | Publication date |
---|---|
CA2783544A1 (fr) | 2011-06-16 |
WO2011072008A3 (fr) | 2011-12-15 |
JP2013513470A (ja) | 2013-04-22 |
EP2509705A2 (fr) | 2012-10-17 |
US20110138936A1 (en) | 2011-06-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20110138936A1 (en) | Means for testing filter integrity in a liquid purification system | |
US8617093B2 (en) | Method and device for monitoring a fluid system of an extracorporeal blood treatment device | |
JP4101382B2 (ja) | 血液処理装置 | |
JP5148568B2 (ja) | 血液処理装置の流体系における漏洩を検出する方法および装置 | |
EP1088210B1 (fr) | Procede et dispositif de determination de l'existence de fuites dans un systeme a fluide circulant | |
JP4959229B2 (ja) | 血液ライン内圧力を監視するシステム及びそれに使用される装置 | |
US6187207B1 (en) | Method and device for checking proper replacement of a used filter in a device for extracorporeal treatment of blood | |
KR20080027357A (ko) | 필터 테스트 장치 및 방법 | |
US20100089837A1 (en) | Blood purification apparatus and method of confirming circuit continuity failure thereof | |
JPH0775668A (ja) | 血液透析装置の透析器の透析セクションにおける構成部品の操作性を決定するための方法、およびこの方法を実施するための装置 | |
JP6853190B2 (ja) | 医療流体調整の試験 | |
CN102427835A (zh) | 用于识别体外血液处理装置的管道***的设备和方法 | |
JPH08187284A (ja) | 血液浄化装置 | |
JP3243677B2 (ja) | 膜濾過装置における膜破損時のリーク検出器 | |
JP3807552B2 (ja) | 膜ろ過装置の膜損傷検知方法および装置 | |
CN114235657B (zh) | 测试过滤介质完整性的方法 | |
KR20180067813A (ko) | 배관용 자동 클리닝 필터 장치 | |
BR112014011037B1 (pt) | método para detecção de vazamento de membrana em um dispositivo de filtro de membrana, e, placa de recesso para um dispositivo de filtro de membrana | |
JP2007117904A (ja) | 膜ろ過処理装置 | |
JP4728684B2 (ja) | 膜ろ過装置の膜破損診断方法および装置 | |
JP4461288B2 (ja) | ろ過膜異常検知方法およびその装置 | |
JP4267197B2 (ja) | 血液透析装置の除菌フィルタ検査方法 | |
JP4205984B2 (ja) | 膜ろ過装置およびその運転方法 | |
JPH0578347B2 (fr) | ||
WO2017119819A1 (fr) | Crépine avec indicateur de pression |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 10836607 Country of ref document: EP Kind code of ref document: A1 |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 10836607 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2783544 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2012543242 Country of ref document: JP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2010836607 Country of ref document: EP |