CN1724084A - Dual-stage filtration cartridge - Google Patents

Abstract

A dual-stage filtration cartridge (10) is provided. The cartridge (10) can be embedded as a mid-dilution hemodiafiltration cartridge or a redundant sterilization filtration cartridge. The cartridge (10) includes a housing (12) having a first end and an opposing second end. The housing (12) has a primary fluid inlet (20) and outlet (60) at the first end of the cartridge (10). The housing (12) also defines first and second filtration stages (14, 16) with the first filtration stage (14) including first filtering elements (40) disposed between the first and second ends of the housing (12). The second filtration stage (16) includes second filtering elements (42) disposed between the first and second ends of the housing (12) with the fluid outlet (64) communicating with the second filtering elements at the first end.

Description

Dual-stage filtration cartridge

Invention field

The present invention relates to defecator and method, and relate in particular to a kind of cartridge filter, it is used as the fluid filter of production sterile liquid in one application as the hemodiafiltration device in Another Application.

Background of invention

The most frequently used treatment mainly is made up of blood dialysis for latter stage nephropathy (ESRD), wherein the blood that will be cleaned is in semi permeability thin film one side flow, physiological solution, dialysis solution flows at the opposite side of thin film, and the toxin in the blood is sent to opposite side from a side whereby.Main driving force in this treatment is a diffusion.This process is effective when removing small-molecular weight (MW, Molecular Weight) toxin as carbamide and creatinine.Yet this process is being removed medium range molecular weight (MW) material, and is during greater than the material of about 1kDa, not too effective owing to the low diffusion coefficient of these materials as molecular weight.

The hemodiafiltration device is used as therapeutic equipment on not half.In the hemodiafiltration device, diffusion combines with filtration removes toxin from blood.Replacement liquid aseptic, non-pyrogenicity joined in the blood before or after it enters the hemodiafiltration tube.Replace liquid and replaced in the hemodiafiltration process blood plasma (plasma water) by the semi permeability membrane filtration, hemodiafiltration has been to use filtration to combine with diffusion than the advantage of hemodialysis and has removed toxin.Because this combination, the hemodiafiltration device is removing small-molecule substance by filtering, and as creatinine and carbamide, and all becomes more effective when removing the medium range material of bigger quantity.

Hemodiafiltration is become effectively, must satisfy two basic demands.The firstth, be used for the high rate of filtration of needs to produce the patient treatment dialysis filter (diafilter) that the toxin high definition is removed.The secondth, be used for sterilizing filter or in-line filter, these filters can provide high capacity aseptic conveying liquid in a continuous manner.

About first kind of demand, the art designs state of hemodiafiltration device is equal to those high flow capacity dialysers basically.These filters are made up of a branch of hollow fibre in a cylinder blanket.In hemodiafiltration system operating period, replace in the blood that liquid is expelled to cartridge filter upstream (pre-dilution) or downstream (back dilution).

Use the diafiltration device of pre-dilution or back dilution scheme to have the efficient limitation of self.Pre-dilution scheme allows to be used for unrestricted relatively filtration, yet because blood is diluted before arriving filter, so solute has reduced by the gross mass transmission of spreading.In other words, the efficient of removal toxin is less than expection.Back dilution scheme has and keeps the high advantage of haemoconcentration, makes solute more effectively spread and convection current, yet, the concentration that blood cell increases during filtration and thereby higher blood viscosity, caused the Fluid Volume that can be filtered to be restricted.Generally only limit to be similar to 25% blood flow.

For second kind of demand, hemodiafiltration needs jumbo aseptic conveying liquid, and therefore, IV carries the standard method of (hanging 1 liter bag of saline) improper.Usually need use a kind of method of making sterile liquid in a continuous manner instead and satisfy this demand.

There is several different methods to make aseptic conveying liquid that hemodiafiltration uses obtain filtering, so that its sterilization earlier before being transported to patient's blood flow by one or a series of filter.The defecator of these processes must be removed endotoxin, antibacterial and other cause the chemical compound of heating.If filter breaks down in this process, patient can be owing to septicemia or exothermic reaction take place in inadequate filtration.

There are several filtering techniques and device at present.For example at " international artificial organ periodical " the 20th volume, 1997 the 3rd phases, the 153-157 page or leaf, the online manufacturing of the displacement liquid of people such as D.Limido described in " being used to have the clinical identification of AK-100 ULTRA of the pre-dilution HF of online preparation sodium bicarbonate displacement liquid " literary composition.The U.S. Pat 4 784768 of Mathieu has been described another kind of sterilizing filter.The most prior art scheme has critical defective, they or rely on an independent filter to come sterilised liq, perhaps use two independences and placed in-line filter, can raise the cost and complexity.

There is such demand for filter, promptly can provides follow-up sterilised filtration, make the physiological fluid that is fit to patient's conveying.

Summary of the invention

Attempting satisfying first demand, when a kind of dialysis filter that adapts to the high rate of filtration promptly is provided, the defective of the embodiment of a dialysis filter by providing a kind of like this scheme to reduce and/or eliminated the prior art apparatus for blood dialysis and filtration, promptly blood is being filtered the back redilution by part or incomplete through mode.Through mode filtering scheme of the present invention combines the advantage of pre-dilution scheme, as the advantage of the high rate of filtration and back dilution scheme, as height diffusion and high convection efficiency.This dialysis filter includes but not limited to Fresenius 4008 On-Line Plus, Gambro AK 200 Ultra applicable to operating in conjunction with traditional diafiltration machine.In addition, this dialysis filter can be used for traditional haemodialysis control unit, includes but not limited to Fresenius2008H, Baxter SPS 1550, and Cobe Centry System 3 etc., these machines are through improving the displacement liquid source that is used to provide.For example, the dialysis solution of the measurable next autonomous dialysis fluid flow tee T of pump or valve, and make it pass through sterilizing filter.

When as the through mode cartridge filter, the present invention has blood and dialysis solution input port and delivery outlet.Cartridge filter comprises single shell, a column type shell for example, and this shell has covered two hemodiafiltration levels, and wherein the first order has a blood input port, and there is a blood outlet second level.Correspondingly, the present invention has finished the twin-stage diafiltration in an independent column type shell, be provided with a cylinder type hollow fibre bundle in this shell.Dialysis filter thereby have the outward appearance of traditional dialyser, but the structure of its two ends or end cap is different from the structure of traditional dialyser design.First end cap had both comprised the blood inlet, also comprised the blood outlet, and the two is separated by inwall and sealing member, and design is used for filter is isolated into the first through mode filtration grade and the second through mode filtration grade.Second end cap has one and is used for receiving the input port of replacing liquid as blood/displacement liquid hybrid chamber.

In dialysis filter embodiment of the present invention, blood input port and delivery outlet are positioned at the first end of filter cylinder.The dialysis solution outlet also is positioned at first end or its vicinity at last.For example, in an one exemplary embodiment, blood input port and delivery outlet and dialysis solution inlet all are positioned at the top (first end) of cartridge filter.Main column type shell comprises a branch of semi permeability of high flow capacity longitudinally hollow fibre, and it,, seals with dialysate chamber as polyurethane by potting compound mutually in each end.Replacement liquid inlet and dialysis solution inlet are positioned at a second opposed end, as the cartridge filter bottom, or its vicinity.Replacing place, liquid input port, aseptic displacement liquid mixes mutually with the blood of part diafiltration.This occurs in a general top area, and blood leaves the hollow fibre of the first order and enters partial hollow fibre there.Dialysis fluid flow is general for two filtration grades, and it moves in the first order and blood flow adverse current, and in the second level and blood flow merging maneuver.

The adverse current fluid of the first order keeps urotoxic Cmax gradient, makes small-molecular weight (MW) solute obtain the cleaning of high diffusion.The necessary partial and stream dialysis fluid flow of this cartridge design is owing to clean and diffusion is cleaned to compare and preponderated thereby can accept in this one-level convection current.The first order and the partial relative rate of filtration are by the effect institute control passively of flowing through thin film in this two-stage hemodilution and haemoconcentration opposing.

After blood flow was crossed partial hollow fibre, blood left dialysis filter by the blood outlet that is positioned at the same end in blood input port.

Another embodiment of the present invention attempts satisfying second demand that high capacity aseptic delivery liquid is provided.It filters by series connection (follow-up) is provided in single filter cylinder and single fibre bundle, is devoted to overcome the defective of prior art.Because follow-up filtration has increased disinfectant and has guaranteed and endotoxic removal.Because single bundle design is compared with the current techniques state, also more simplify and made things convenient for.

The sterilizing filter embodiment of filter cylinder is similar with through mode filtration embodiment on outward appearance and function, and some differences are only arranged.Sterilizing filter has a single cylinder blanket, and a column type hollow fiber bundle wherein is set.Yet, only need an end cap for sterilizing filter.This end cap is to have a not twoport end cap of fluids for sterilization input port and fluids for sterilization delivery outlet, and two mouths are separated by an inwall with the sealing member that filter is divided into the major-minor filtration grade.At the other end of device, fiber continues to be encased by the end that is enclosed in the potting compound.Because the filtration of this dead end has not just needed second end cap.

In the sterilizing filter embodiment of filter cylinder, the end that delivery outlet is positioned at device is drunk in the fluid input port, as the top.Fluid can be a dialysis solution, and it is discharged from as the part of machine dialysis fluid flow, so that as the displacement liquid in the diafiltration treatment.The port that is used as the dialysis solution mouth in the diafiltration embodiment of filter cylinder is normally sealing in sterilizing filter embodiment.In this embodiment, they can be used for starting, test or the sterilization of filter.

In operation, disinfectant solution does not enter the input port and the fiber of the first order (the main filtration).Because fiber core is sealing at the other end, the mandatory membrane filtration that passes of all fluids, and enter shell (filtration) space.Thin film in this embodiment is such, and during filtering, it removes endotoxin and all antibacterials from fluid, make it become the fluid of aseptic conveying quality.General outer casing space is similar to the dialysate chamber among the diafiltration embodiment between two filtration grades.So the disinfectant solution after-filtration in the universal space enters the fiber core of the second level (the secondary filtration).Disinfectant solution leaves filter cylinder at the top delivery outlet then.This design has advantageously provided secondary filtering safety, has guaranteed sterilization, has the facility of the single bundle of tradition filter cylinder again.

Other features and advantages of the present invention will become clearer in conjunction with the accompanying drawings from following specific descriptions.

Description of drawings

Fig. 1 is the cross sectional representation according to the single beam filter tube that is used as dialysis filter of an embodiment;

Fig. 2 is the cross-sectional view according to the end cap that is used for Fig. 1 dialysis filter of an embodiment;

Fig. 3 is the cross-sectional view that is used for the another kind of end cap of Fig. 1 dialysis filter;

Fig. 4 is the cross sectional representation that is used to make single beam filter tube of aseptic conveying liquid according to an embodiment;

Fig. 5 is the cross-sectional view that is used for an end cap of Fig. 4 cartridge filter according to an embodiment;

Fig. 6 is the cross-sectional view that is used for an end cap of Fig. 4 cartridge filter according to another embodiment.

The specific descriptions of preferred embodiment

With reference to figure 1, schematically shown cross-sectional view according to the intermediate dilute blood filter cylinder 10 of an embodiment.Filter cylinder 10 comprises a shell 12, and as will more specifically describing following, it has the first order 14 and the second level 16.Shell 12 is preferably cylindrical, is made of rigid plastic material.Shell 12 comprises a semi permeability hollow fibre 18 of vertically restrainting, and as the device that transmits toxin, these toxin are removed from blood flow by the inner chamber part of fiber 18.Can use commercial at the existing many semi permeability hollow fibres 18 of this purpose.For example, semi permeability hollow fibre 18 can be multiple size, can be made of as polysulfones polymer, or is base with the cellulose.

In one embodiment of the invention, filter cylinder 10 is suitable for operating with the hemodiafiltration machine, as Fresenius 4008 On-Line Plus or Gambro AK 200 Ultra or improved hemodialysis machine, as Fresenius 2008H, Cobe Centry System 3 or Baxter SPS 1550.

In when operation, by means of the blood that blood pump and blood line transmit from patient, by the first order 14 that input port 20 enters filter cylinder 10, this input port 20 preferably is integrally formed on the top cover 22 that is installed in shell 12 first ends.Top cover 22 has an inner top space 24, in fact is divided between first inner top space peace, the 26 and second inner head space 28.Because it is circular that top cover 22 is preferably, 26 and 28 equally also is circular between the first and second inside top head spaces.In this embodiment, the first inner top space 26 is the annulars around the second inner top space 28.

The first and second inner top spaces 26 and 28 separate by first potting compound 30 other parts with filter cylinder 10, and this potting compound forms a sealant at the first end place of shell 12 around hollow fibre 18 outer surfaces.As directed, top cover 22 is dismountable types, can screw tight on shell 12.

Inner top space 24 is sealed in external environment condition by O shape ring 32, and this O shape ring seals against potting compound 30.Those skilled in the art as can be seen, top cover 22 also can for good and all connect in this structure, also can pass through additive method, connects as snapping type structure.

Blood enters the first inner top space 26 by input port 20, preferably enters with the tangent line flow path direction, so that blood before entering hollow fibre 18 from interface 34, can be filled into the first inner top space 26 more equably.In the present embodiment, interface 34 is upper surfaces of potting compound 30.Interface 34 preferably includes a polyurethane interface structure.The first inner top space 26 can be come to separate with the second inner top space 28 by several technology.For example, as shown in Figure 1, the first inner top space can separate by an annular wall 36 and the second inner top space 28, and this annular wall is divided into first and second spaces 26,28 respectively with inner top space 24.Better, inwall 36 forms top cover 22 part of the whole.Inwall 36 extends internally, from the inner surface on top cover 22 tops towards fiber 18.To between the first and second inner top spaces, provide a sealant, preferably will comprise an inner O shape ring 38.In the illustrated embodiment, inner O shape ring 38 is arranged on inwall 36 ends, and inwall is being connected to top cover 22 with its opposite position.When top cover 22 engaged with interface 34, interior O shape ring 38 provided a sealing function.

According to the present invention, the each several part of hollow fibre 18 is divided into first and second portion, generally indicates with 40 and 42 respectively.Be easy to find out that first pars fibrosa 40 has a plurality of independently hollow fibres 18, similarly, second pars fibrosa 42 also has a plurality of independently hollow fibres 18.First pars fibrosa 40 and the first inner top space, 26 fluid communication, second pars fibrosa 42 and the second inner top space, 28 fluid communication.The separation of hollow fibre 18 can realize by using multiple different technologies, includes but not limited to before encapsulation process, at the first end place of shell 12 spacer 44 is inserted in the hollow fiber bundle 18.

In an one exemplary embodiment, spacer 44 is by suitable material, the annular ring form of making as plastic material.Spacer 44 is divided into first pars fibrosa 40 (being called the outer fiber beam ring at this) and second with single column type hollow fiber bundle 18 and now is part 42 (being called inner cylinder fiber type bundle at this).In other words, outer fiber beam ring 40 is round inner circular column type bundle 42.Spacer 44 also can have dual function, as the O shape ring seat of inner O shape ring 38.Outer fiber beam ring 40 has constituted tremulous pulse (arterial) fibre bundle, and interior cylindrical fibre bundle 42 is called vein (venous) fibre bundle at this.Tremulous pulse fibre bundle 40 and first inner top (tremulous pulse) space, 26 fluid communication, vein fibre bundle 42 and space, second top (vein) 28 fluid communication.

During encapsulation process (potting process), spacer 44 can wrap in first potting compound 30.Spacer 44 preferably by relative non-rigid plastics, is made as polyethylene, and it can be trimmed to equal with first potting compound.

When blood entered the first inner top space 26 by input port 20, blood crossed the inside of tremulous pulse fiber 40 downwards, and this tremulous pulse fiber is arranged in the dialysis filter filter space (dialysate chamber) 46 of diafiltration generation.The outside of tremulous pulse fiber 40 is inserted in the dialysis solution.The first order hemodiafiltration that this has produced toxin promptly filters and spreads, and this occurs in the filter space 46 along on the whole length of tremulous pulse fiber 40.This also makes partly hemodiafiltration of blood, in other words, has finished in this one-level and to have removed some toxin that exist in the blood.In one embodiment of the invention, quite a few in the blood plasma is as about 20%-60%, along with blood flow is crossed the first order 14 and obtained filtration.Blood through the part hemodiafiltration leaves tremulous pulse fiber 40, enters the intergrade headroom 48 that is connected to shell 12 other ends.The blood that enters intergrade headroom 48 is in the blood enrichment stage, that is to say that blood cell concentration (hematocrit) level in the blood has increased.According to one embodiment of present invention, for the general filter space 46 in the first order 14 and the second level 16, be similar to the isolated description of front, for example separated by one second potting compound 50 and intergrade headroom 48 with reference to the inner top space 24 and first potting compound 30.

Leave the switching stage that the first order 14 enters the second level 16 as blood, intergrade headroom 48 has second top cover 54 of preferably being made by rigid plastic material, and is connected to second end of shell 12.In this sketch map, but second top cover 54 is removal types, and is connected to shell 12 by threaded screw rod.Those of ordinary skills can find that top cover 54 can connect in many ways, comprise the snapping technology.Intergrade headroom 48 can be sealed in external environment by one the 2nd O shape circle 56.As shown in Figure 1, the 2nd O shape circle 56 is arranged between the polyurethane interface 52 and second top cover 54.

In operation, blood pumps into by input port 20, passes the first inner top space 26, enters tremulous pulse fiber 40.The pressure at 20 places thereby be higher than the pressure of other positions of dialysis filter in the input port.Blood can naturally and understandably flow to the area of low pressure, so blood flow is to intergrade headroom 48.

Before entering the second level 16, reside in the blood of intergrade headroom 48, diluted by the physiology sterile solution that enters filter cylinder 10 by input port, top 58.Blood in intergrade headroom 48 obtains dilution, that is to say that blood blood cell concentration level has reduced.

Because the second inner top space 28 is compared with intergrade headroom 48 with the first order and is in low pressure, the blood of dilution enters the vein fiber 42 that is arranged on the second level 16, and, be transported to the second inner top space 28 by vein fiber 42 to be similar to the front with reference to the first order 14 described modes.Further hemodiafiltration is taking place on the length of these vein fibers, leaves and enter the second inner top space 28 (vein space) of first top cover 22 until blood, and leaves from the delivery outlet 60 that is formed on first top cover 22.Delivery outlet 60 has been represented and other positions of dialysis filter, comprises the input port 20 of having represented the maximum pressure position, the position of the low-pressure of comparing, and therefore, the blood of dilution flows to delivery outlet 60 from intergrade headroom 48.Delivery outlet 60 is called ostium venosum cordis.Ostium venosum cordis 60 and input port 20 same-types are as standard twist-lock interface (standard twist lock connector).Cross vein fiber 42 when dilution and the blood flow of part diafiltration, other toxin is removed from blood by diffusion and filtration, thereby when blood was discharged into the second inner top space 28, blood had been in the diafiltration state.

In one embodiment of the invention, blood carries out diafiltration with such speed by filter cylinder 10, that is, making blood blood cell concentration level when leaving the second level 16 by ostium venosum cordis 60, is level identical when entering the first order 14 with blood by input port 20 basically.As the standard hemodialysis process, blood blood cell level needs little variation and controls basic filtration fully, and keeps the patient fluid balance.

It is best the same with the normal dialysis process with connection that dialysis solution flows.Dialysis solution is by dialysis solution input port 62, and standard Hansen interface enters filter cylinder 10 as known in the art.Dialysis solution among the present invention pours into and flows through and is centered around the filter space 46 in hollow fibre 18 outsides.Dialysis solution leaves filter cylinder 10 by dialysis solution outlet 64.Best, dialysis solution inlet 62 and dialysis solution outlet 64 are mouths of same type, for example the Hansen interface.Dialysis solution pumps into the inlet 62 of having represented locations of high pressure, export 64 simultaneously and represented locations of low pressure, so dialysis solution is along flowing from 62 directions to outlet 64 that enter the mouth.

In one embodiment of the invention, dialysis solution is along flowing from 62 directions to outlet 64 that enter the mouth.Because filter space (dialysate chamber) 46 be general for two-stage, so dialysis solution is in the first order 14 and blood back flow operation, in the second level 16 with the blood merging maneuver.In the first order, blood flows to second potting compound 50 from inner top space 26, is that package interface 52 places enter before the second level 16, and the intergrade of flowing through headroom 48 is then because the pressure reduction of system flows to vein outlet 60.Hollow fibre 18 (vein and tremulous pulse fiber 40,42) is passed in filtration from blood to the dialysis solution semi-permeable wall takes place.Integral filter speed is the function of dialysis solution output stream and displacement liquid inlet flow, and its advantage is to be far longer than the speed that traditional back dilute blood diafiltration is obtained.According to one embodiment of present invention, integral filter speed is to about 85%, preferably from about velocity of blood flow of 40% to 60% from about 25%.These flow and can control by the pump in traditional hemodiafiltration machine.

First and second grade 14,16 the relative rate of filtration can be controlled with the relative transmembrane pressure (TMP) between the filter space (dialysate chamber) 46 passively by blood chamber 40,42, it is relied in a plurality of factors, as the haemoconcentration in each blood chamber, velocity of blood flow.For example, the blood in the first order 14 is spissated, and is more viscous, but be in high pressure; And the blood in the second level 16 dilutes, and is few heavy-gravity, is in low pressure.Along with pressure becomes stable, the higher relative rate of filtration can realize in the second level 16.

The manufacturing of filter cylinder 10 is similar to the manufacturing of hemodialyzer (not shown) in this sketch map.Hollow fibre 18 bundles are arranged in the shell 12.Spacer 44 inserts first end of hollow fibre 18.Therefore, that follow hard on is standard packaging technology (potting technique), and it makes potting compound be inserted into by dialysis solution entrance and exit 62,64, and filter cylinder 10 rotates in a centrifuge to form first and second potting compounds 30,50 simultaneously. Top cover 22,54 is connected to shell 12 by many suitable technology, includes but not limited to threaded screw rod.The design of dismountable top cover is more favourable for re-using of dialysis filter, and it makes and is formed on the coagulated material at package interface 34 and 52 places or fragment is easier is removed.The regeneration of dialysis filter is similar to the normal dialysis device, and wherein blood input port 20 and delivery outlet 60 and dialysis solution entrance and exit 62,64 are connected to a dialyser regeneration machine.Unique restriction is to have added lid in displacement input port 58.

For illustrated purpose, indicate with arrow 66 according to the blood flow in the filter cylinder 10 of an embodiment.

With reference now to Fig. 2 and Fig. 3,, they have been represented to isolate fiber 18 and have connected the other method of the top cover of two mouths with the formation two-stage.The operation of dialysis filter is identical, and the manufacture method difference is only arranged.

In Fig. 2, shading ring 82 designs have a hollow core.When ring 82 and polyurethane 30 when pruning after encapsulation process is finished, core is opened, and encircles like this to have had a passage in 82.Also be provided with an inwall 84, it extends internally from top cover 86.In this embodiment, inwall 84 is annular; Yet, also can be other shapes.Inwall 84 has an elongated end that inserts, and this elongated end can weld with the inner surface of shading ring 82 or be bonding.In other words, elongated end is contained in the passage of ring 82, with fixing and locating this elongated end.In this sketch map, top cover 86 also is fixedly connected on the overcoat (shell) 88.Top cover 86 is bonding or be welded on the circumferential ring 90 of shell 88, so that sealing inner top space and external environment.For the ease of making, interior bonding and outer bondingly preferably carry out simultaneously.

In Fig. 3, top cover 86 is identical with Fig. 2 to the connection of shell 88.Difference is in the sealing of inwall 84.In this sketch map, the top of inwall 84 directly seals mutually with potting compound 30.Those of ordinary skills can find out here can use several different methods.Some examples as: heating polyurethane is pressed into interface 34 until deliquescing with the top, makes polyurethane cooling then and is sealed in around the wall 84; And additionally, a thin annular ring is inserted in the potting compound, then by bonding agent or press fit with the wall end sealing to anchor ring.

Be inserted into the spacer in the fibre bundle before top fixing means does not as shown in Figure 3 need to encapsulate, because this encapsulation process very advantageously, it is equal to the encapsulation process of the normal dialysis device of this technology.The defective of this design is that the little annular ring that also can be used for the fiber of filtering blood is in addition sealed by inwall 84.These fibers are original fiber basically.

With reference to figure 4, it has schematically shown the cross-sectional view that is used as according to the sterilizing filter filter cylinder 110 of an embodiment.This cartridge design is similar to dialysis filter embodiment, except the end structure difference.

Filter cylinder 110 comprises a shell 112, and it has an inceptive filtering level 114 and a follow-up filtration grade 116.As in dialysis filter embodiment, shell 112 is column type preferably, and comprises vertical semi permeability hollow fibre 118 bundles.As previously mentioned, fiber 118 has multiple size, can be made of multiple different materials.Fiber 118 is used as from the fluid of introducing and filters out antibacterial and endotoxic device, and produces the fluid of aseptic conveying quality.Filter cylinder 110 can in officely be what is the need for and be used in the application of wanting sterile liquid, comprises that being appointed as only is the online hemodiafiltration of example use.

In operation, physiological liquid enters inceptive filtering level 114 as dialysis solution by input port 120, and this input port preferably is integrally formed on the top cover 122 that is installed in shell 112 first ends.Input port 120 can be the fluid connector of any suitable type.The top cover 122 of once mounting is divided into two inner top spaces, basic inner top space 126 and secondary inner top space 128.Fundamental sum secondary headroom 126,128 all is assumed to semicircle in this embodiment, link to each other with follow-up filtration grade 116 with inceptive filtering level 114 respectively.Fundamental sum secondary headroom 126,128 is not limited to semicircle, and many difformities can be supposed in these spaces 126,128 on the contrary.For example, those of ordinary skills as can be seen the fibre bundle among the sterilizing filter embodiment can be divided into annular section rather than semicircle level.This can influence the formation of centre grade.Shape at different levels is also not serious for the performance impact of sterilizing filter; Therefore can use multiple shape.

Inner top space 126,128 is isolated with the filter space 124 of filter cylinder 110 by first potting compound 130, this potting compound be sealed in fiber 118 outsides and shell 112 those ends around.

As directed, top cover 122 fixes by welding or the circumferential ring 132 that bonds to the shell outside and is connected on the shell 112.Thisly bondingly provide a kind of sealing with external environment for inner top space 126,128.Those of ordinary skills 122 can finish with multiple mode to the lasting connection of shell 112 from the top as can be seen.It can also be seen that the top can be similar to that Fig. 1 dialysis filter embodiment illustrated, connects with dismountable form with O-ring packing.Yet those of ordinary skills can find out that also the sterilizing filter that does not use with blood does not need a dismountable top cover.

In the embodiment shown, the inner top space the is isolated from each other sealing member that comes also can be used as second sealant with external environment.As shown in the figure, top cover 122 has two integrated formation, across the inwall 136 of top cover 122 cross sections.Between two walls 136 is open slot 134, and it is also across the cross section of crossing top cover 122, and opens to the external world.When the end of inwall 136 with bonding or when being welded or otherwise attached to one or two chamber fiber barrier ribs 138, each inner top space 126,128 both had been sealed in the external world, also sealing each other.The cross section that barrier ribs 138 strides across shell 112 extends.As the shading ring 44 of the dialysis filter of Fig. 1, barrier ribs 138 plays dual purpose.Rib 138 is divided into first pars fibrosa 140 and second pars fibrosa 142 with hollow fibre 118 before encapsulation.Thereby rib 138 is pruned by polyurethane and is left two passages after encapsulation, and these two passages are as the seal point of the wall 136 in inner top space 126,128.

The physiological liquid of not sterilizing 120 pumps into by entering the mouth, and enters first headroom 126, and it enters the fiber 118 of first 140 by package interface 144 there.Because liquid pumps into inlet 120 under pressure, thereby to enter the mouth 120 are locations of high pressure.First pars fibrosa 140 has constituted inceptive filtering level 114.Fluid flows into fiber 118, and this fiber has been removed antibacterial and endotoxin effectively from liquid.Because hollow fibre 118 relative ends are sealed by second potting compound 146, all liq is forced to pass fiber membrane., wherein compare with the pressure of first 140 fibers, 118 inboards owing to the pressure reduction that exists is guided through fiber membrane at first pars fibrosa, 140 flowing liquids, be in low pressure around the zone of first pars fibrosa, 140 fibers.

Liquid behind the sterilised filtration resides in the interior shell-space 124 of hollow fibre 118 now.This space 124 is similar to the dialysate chamber of Fig. 1 dialysis filter embodiment.Yet in sterilizing filter operating period, outer faucal 148 keeps sealing to prevent any interchange in sterile liquid and the external world.So the pressure in space 124 moves on to liquid in the fiber 118 of second portion 142.The thin film that liquid passes these fibers 118 enters fiber lumens, carries out secondary filter.Such second filtration fraction 142 has constituted follow-up filtration grade 116.

Twice filtering sterile liquid left then, enters the second inner top space 128, again from 150 outputs of top delivery outlet.Delivery outlet 150 is in than all lower pressure in other positions of filter, thereby make liquid flow by aforementioned flow channel, promptly allow the fluid that enters first's 140 fibers 118 be guided through two independently fibrous membranes,, and finally pass delivery outlet 150 so that flow into the second inner top space 128.Delivery outlet 150 can be any type (for example luer mouth) that is suitable for the IV conveyer device easily.Flowing substantially of liquid represented with arrow 152 in the sterilization filter cylinder.Solid arrow is represented the inner chamber liquid flow, and dotted arrow is represented flowing between the two-stage simultaneously.

Inwall 136 and barrier ribs 138 also can be disposed with multitude of different ways by those of ordinary skills.Yet as shown in Figure 4, the design has a ultra-safe feature.At the top cover place in the input sap cavity 126 of disinfectant not and sterile liquid output cavity 128 these two chambeies, a potential danger is fluidic branch between two chambeies, may have potential pollution to output stream.This can not only pass through to isolate two tangible sealing members in each chamber, and can pass through the existence of two sealing members of open slot 134, is alleviated.If two kinds of sealings have all damaged, liquid can withdraw from open slot 134 as can be seen, and this is a path of minimum drag, rather than is sent to another chamber possibly.

Sealed outer faucal 148 can be used for starting and test when the filter normal operation.Mouth 148 can be to be used for carrying out any suitable type that leakproof connects, and comprises the Hansen mouth among the dialysis filter embodiment.In starting filling operation, sterile liquid pump intake 148, it will force air to discharge filter chamber 124 and fiber core 118 there, and finally leave two top openings 120 and 150.Although the starting filling by input port 120 is plugged at the one end owing to fiber 118, and causes having in the fiber 118 air that sandwiches, this design is still a cover advantageous method.A plurality of mouth is used for the leakage of detection fibers, for example carries out the air pressure attenuation test.By pumping air into filter chamber 124, people can test the fiber 118 of two filtration grades 114 and 116 simultaneously effectively.

Now attention is turned to Fig. 5 and Fig. 6, they have represented to be used for top cover is connected to two kinds of Aided Design of shell end.Those of ordinary skills can also use other certain methods as can be seen.

Fig. 5 has represented to have a single channel core rather than a twin-channel barrier ribs 162 shown in Figure 4.Therefore, the inwall end 166 of top cover 164 just bonds to barrier ribs 162 at its outer surface.Portion's surface channel 168 does not have bonding within it.

Fig. 6 has represented not have the structure of barrier ribs.Therefore, encapsulation process is simplified, and a same normal dialysis device also is simplified.The tip designs of the inwall 172 of top cover 174 becomes they can be sealed directly in the polyurethane 130.As in dialysis filter embodiment, can adopt several different methods to realize sealing, comprise: go out to heat polyurethane until deliquescing at interface 144, then end is pressed into wherein, and passage is inserted in the potting compound 130, come seal end by welding or press fit.By these two kinds of technology, along the some fibre of central shielding wire, comprise open slot 134 places, all can be sealed and be not used in filtration.

Those of ordinary skills as can be seen, the present invention is not limited to described with reference to the accompanying drawings embodiment.The present invention is only limited by following claims.

Claims (6)

1. the method for a hemodiafiltration comprises step:

Reception blood becomes a mandarin;

Become a mandarin at the described blood of first order diafiltration, provide the blood of part diafiltration to go out stream;

The blood that mixes described part diafiltration goes out stream and displacement liquid, so that blood/displacement liquid fluid mixture to be provided; And

At the described blood of second level diafiltration/displacement liquid fluid mixture, wherein first and second grades all are included in the independent filter cylinder shell.

2. the process of claim 1 wherein that the step of miscible displacement liquid comprises:

The blood of receiving unit hemodiafiltration goes out to flow to into an intergrade part;

By an intergrade inlet base fluid is imported the intergrade space.

3. the method for a hemodiafiltration comprises step:

Reception blood becomes a mandarin;

Become a mandarin at the described blood of first order diafiltration, provide blood to go out stream with first toxin concentration;

Go out stream and replace liquid-phase mixing at the blood of intergrade part so that blood/displacement liquid mixture to be provided with described part diafiltration; At the described blood of second level diafiltration/displacement liquid mixture, have the blood of second toxin concentration with generation, first concentration is greater than second concentration, and wherein dialysis solution is general for first and second grades.

4. the method for claim 3 further comprises step:

The twin-stage filter cylinder is provided, and this filter cylinder has the blood inlet at first end, is used for receiving blood and becomes a mandarin, and has the intergrade adapter at second end, and wherein dialysis solution is in the first order and blood flow counter-current flow, in the second level and blood flow concurrent flow.

5. the method for a filtered fluid comprises:

Receive a fluid in the input port of double-stage filtering filter cylinder;

Make fluid pass through the inner chamber part of first filter element;

Make fluid pass the inner chamber that first filter element enters shell;

Make fluid pass second filter element and enter its inner chamber part; And

Make fluid pass through the inner chamber part of second filter element, arrive delivery outlet, be discharged from by the delivery outlet fluid, wherein input port and delivery outlet are all at the same end of twin-stage filter cylinder, first and second filter elements all comprise opening and blind end, and blind end is all at the same end of twin-stage filter cylinder.

6. the method for claim 5, wherein at least a portion fluid flows at the first direction of first filter element, and at least a portion fluid flows in the second direction of second filter element, and first and second directions are respect to one another.

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