Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F21/00—Dissolving
  • B01F21/30—Workflow diagrams or layout of plants, e.g. flow charts; Details of workflow diagrams or layout of plants, e.g. controlling means
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
  • A61M1/00—Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
  • A61M1/14—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
  • A61M1/16—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
  • A61M1/1654—Dialysates therefor
  • A61M1/1656—Apparatus for preparing dialysates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F21/00—Dissolving
  • B01F21/20—Dissolving using flow mixing
  • B01F21/22—Dissolving using flow mixing using additional holders in conduits, containers or pools for keeping the solid material in place, e.g. supports or receptacles
  • B01F21/221—Dissolving using flow mixing using additional holders in conduits, containers or pools for keeping the solid material in place, e.g. supports or receptacles comprising constructions for blocking or redispersing undissolved solids
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F21/00—Dissolving
  • B01F21/50—Elements used for separating or keeping undissolved material in the mixer
  • B01F21/503—Filters
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
  • B01F25/30—Injector mixers
  • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
  • B01F25/30—Injector mixers
  • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
  • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
  • B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
  • B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
  • B01F25/53—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
  • B01F35/20—Measuring; Control or regulation
  • B01F35/21—Measuring
  • B01F35/213—Measuring of the properties of the mixtures, e.g. temperature, density or colour
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
  • B01F35/20—Measuring; Control or regulation
  • B01F35/22—Control or regulation
  • B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
  • B01F2101/22—Mixing of ingredients for pharmaceutical or medical compositions

Definitions

• the present invention relates to a device for producing a dialysis concentrate or another liquid, the device containing an inlet for a solvent for dissolving or mixing with a raw material located in a container, the device having connecting means for connecting to the container and wherein the raw material is soluble in the solvent or miscible with it.
• the present invention further relates to an arrangement comprising a device according to the invention with a container connected thereto that contains the raw material, and a method for producing a dialysis concentrate or another liquid, and a blood treatment device with an arrangement according to the invention.
• the present invention also relates to the use of the device or arrangement according to the invention for producing a dialysis concentrate or for producing another liquid, in particular a cleaning, sterilizing or disinfecting liquid which is used in particular for blood treatment machines, preferably for dialysis machines. It is known from the prior art to supply dialysis machines with dialysis solutions or with dialysis concentrate in various ways.
• the dialysis machines are often supplied with dialysis concentrate from a ring line system by means of a central supply unit. This is associated with the disadvantage of comparatively high investment costs for the ring line system and for the central supply unit. Another disadvantage is the limited flexibility with regard to the composition of the dialysis concentrate, since different dialysis concentrates can only be made available via the ring line to a very limited extent. If additional dialysis concentrates are required, this can only be done through other types of care.
• Another known procedure consists in supplying dialysis machines with dialysis concentrate via canisters.
• the canisters contain the finished dialysis concentrate.
• This procedure is very flexible compared to the supply via the ring line, but has the disadvantage of a high expenditure of work and time, since each dialysis machine has to be individually equipped with a canister for each new treatment.
• large storage areas are required for stocking the canisters and the canisters have to be transported to and from the warehouse to the dialysis machines, which is time-consuming and pollutes the environment, since a large amount of water (as a solvent in the canisters) is transported, which would also be available in the dialysis centers.
• the canisters have to be disposed of after they have been used once, which is associated with a corresponding accumulation of plastic waste.
• a concentrate bag containing a raw material is known from the prior art according to WO 99/06083 A1.
• the dialysis concentrate is produced by adding water to the concentrate bag itself and by dissolving the raw material in the bag.
• DE 10 2017 127 637 A1 discloses a fluid system with a main circuit and a branch section connected thereto for the production of dialysis concentrate.
• the main circuit there is a mixing chamber and a container for receiving the concentrate and a pump that pumps the fluid in the circuit in the main circuit.
• the branch section there is a container containing a raw material that is fed to the main circuit.
• the object of the present invention is to provide a method and a device for the production of dialysis concentrate or other solutions, in which the investment costs and the expenditure of time are low and at the same time there is a high degree of flexibility with regard to the solution to be produced.
• the device has a mixing unit which is self-regulating and comprises a mixing line and a suction unit arranged in the mixing line and a mixing chamber, wherein the suction unit can be brought into fluid connection with the inlet for the solvent and with the container by means of a suction line and wherein downstream of the mixing chamber leads a return line back to the container connectable to the device.
• a mixing unit which is self-regulating and comprises a mixing line and a suction unit arranged in the mixing line and a mixing chamber, wherein the suction unit can be brought into fluid connection with the inlet for the solvent and with the container by means of a suction line and wherein downstream of the mixing chamber leads a return line back to the container connectable to the device.
• the raw material When the container is connected to the device, the raw material is sucked out of the container by the suction unit and mixed with the water or other solvent flowing in through the inlet. This mixture then enters the mixing chamber, where the raw material is mixed with the solvent. The solution prepared in this way enters the container via the return line.
• mixture is also to be understood as meaning a dissolving process which occurs when the raw material is solid or solid-liquid.
• solution can also refer to a pure mixing process that occurs when the raw material is liquid.
• a retaining element is arranged in the mixing or fine mixing chamber, which can be designed as a filter element, for example. If undissolved raw material collects on this filter element, the pressure loss in the system increases and the flow through the filter element is reduced or prevented altogether. This minimizes the flow rate over the suction unit and thus further suction of further raw material from the container. Even with a low flow, the undissolved raw material is overflowed with fresh solvent, thus optimizing the dissolution. If the raw material is sufficiently dissolved in the fine mixing chamber, the pressure loss decreases and the flow rate of the solvent through the suction unit increases, which promotes further suction of raw material through the suction unit into the fine mixing chamber. that. For the implementation of such self-regulation, we also refer to DE 10 2017 127 637 A1, the disclosure content of which is part of the subject matter of the present invention.
• the mixing chamber can be a filter chamber, preferably a fine mixed filter chamber.
• the raw material in the container i.e. the raw concentrate
• the raw material can be solid, liquid, granular, powdery, slurry-like or in any other form.
• the container is preferably a disposable.
• the container can be designed as a bag or as a vessel with rigid walls, e.g. as a cartridge.
• the container can be connected directly to a blood treatment machine, preferably to a dialysis machine, and thus have appropriate connection means that interact with the blood treatment machine connection means, so that the container filled with dialysis concentrate, preferably a bag, can be connected to the blood treatment machine.
• the mixing or dissolving takes place completely or essentially in the mixing chamber.
• the container is connected via the suction line and the return line to the blood treatment device or other device for producing the dialysis sec concentrate etc. connected.
• the suction line is used to remove the raw material from the container and the return line is used to return the finished concentrate to the container, which is then in the form of a bag or the like filled with dialysis concentrate and can then be used to produce the ready-to-use dialysis solution.
• the opening of the suction line is preferably arranged near the bottom of the container, where the undissolved concentrate or solid, ie the undissolved raw material, collects.
• the suction unit can be arranged, for example, in the inlet or in the mixing line or between them.
• It can be designed, for example, as a Venturi nozzle, the negative pressure of which is generated by the flow of solvent. If the inflow of solvent is started, raw material or pre-concentrate is sucked out of the container into the device-side mixing line through the suction unit. This is where the mixing chamber is located, which - as explained above - sets the suction speed from the container in a self-regulating manner. Ideally, this regulation means that a finished concentrate can be produced from the raw material in a single pass, i.e. without a circulating flow of the raw material.
• a specific volume of solvent is preferably used, which is determined by the amount of electrolyte in the container. In this way, a batch with the desired volume and composition can be produced.
• a valve is preferably arranged in the mixing line or in the inlet upstream of the suction unit.
• a valve can be arranged in the mixing line downstream of the mixing chamber.
• the device preferably has no mixing tank and apart from the container no other storage container for the solution produced.
• a discharge line is provided for discharging the finished dialysis concentrate or other liquid produced, the discharge line being fluidically connected to the container or to the suction line or to the mixing chamber.
• a mixing circuit can be switched on, through which the concentrate is circulated until the undissolved substances still present in the mixing chamber are completely dissolved. This is particularly possible when all of the raw material has already been sucked into the mixing chamber. This is a variant.
• the entire raw material from the container does not have to be in the mixing chamber for the mixing circuit to be switched on, since the mixing circuit or the fluid contained therein circulates via the suction unit and can therefore continue to suck raw material from the container. Switching on the mixing circuit is therefore also conceivable and covered by the invention when there is still raw material in the container.
• the mixed circuit flow provides a flow over the suction unit so that raw material can also be sucked in without the need for additional solvent to be introduced into the mixing line.
• a circuit line can thus be provided which is arranged parallel to the suction unit and/or the mixing chamber and which opens into the mixing line upstream of the suction unit or the mixing chamber and downstream of the mixing chamber.
• a pump and preferably at least one valve can be arranged in the circuit line.
• a sensor can be provided which is designed to detect a parameter value (and/or its change over time) of the liquid that is characteristic of the progress of the dissolution of the raw material in the solvent, such as a concentration or conductivity in or downstream of the mixing chamber, wherein a control unit is present which is connected to the sensor and which is designed to open or close the circuit line depending on the parameter value. If an insufficient solution is detected, the circulation line is opened so that the concentrate is circulated until sufficient or complete dissolution is achieved.
• the intake unit can be a venturi nozzle.
• the present invention further relates to a blood treatment machine, in particular a dialysis machine such as a hemodialysis machine or a peritoneal dialysis machine with a device for producing a dialysis concentrate or another liquid according to the invention.
• a blood treatment machine in particular a dialysis machine such as a hemodialysis machine or a peritoneal dialysis machine with a device for producing a dialysis concentrate or another liquid according to the invention.
• the blood treatment device preferably has a water supply line in which water, in particular RO water, flows during the online production of ready-to-use dialysis solution.
• a concentrate line branches off from this feed line and is in fluid communication with the container filled with liquid dialysis concentrate.
• a concentrate pump can be arranged in the concentrate line to promote it.
• the water supply line can also contain a means for the measured delivery of water, so that a specific and desired dilution of the dialysis concentrate or the desired mixing ratio results.
• a mixing unit for example a mixing chamber, can be provided downstream of where the concentrate line joins the water supply line be where the dialysis concentrate is mixed with the water.
• the subject matter of the disclosure is the device and/or the blood treatment device and/or the method and/or the use with and without a container connected to the device or to the blood treatment device.
• the present invention also relates to a method for producing a dialysis concentrate or another liquid, the method being carried out using a device or arrangement according to the invention.
• the production of the dialysis concentrate or the other liquid is preferably carried out in such a way that the raw material does not circulate through the container.
• the solution itself After flowing through the mixing chamber, the solution itself returns to the container and can be sucked back into the mixing line from there by means of the suction unit, so that a circulatory flow of the solution via the container is possible and covered by the invention.
• the circulation line is flowed through if the solution of the raw material in the solvent is not complete after metering in a certain amount of solvent.
• part or all of the liquid can be diverted from the mixing line by a pump and fed back through the suction unit. If available, the other part of the liquid can be poured into the holder to be returned. Undissolved concentrate is then sucked out of the container into the mixing line by the flow through the suction unit.
• a first partial flow is branched off from the mixing line downstream of the suction unit and is routed again via the suction unit and possibly the mixing chamber in order to convey still undissolved substances out of the container.
• the remaining, second partial flow is fed to the container from the mixing line.
• the dialysis concentrate or other liquid is degassed in the mixing chamber. In this case, there is no need for a separate degassing device.
• the present invention also relates to the use of a device according to the invention for producing a dialysis concentrate or for producing another liquid, in particular a cleaning, sterilizing or disinfecting liquid, which is used in particular for blood treatment machines, preferably for dialysis machines.
• Figure 1 a schematic view of a first embodiment of the device without a circuit line
• Figure 2 a schematic view of a second embodiment of the device with circuit line
• FIG. 3 a schematic view of a third embodiment of the device for degassing the dialysis concentrate.
• FIGS 1 to 3 show different embodiments of the device for the production of dialysis concentrate. Elements that are the same or have the same function are identified in the figures with the same reference symbols.
• the mixing unit comprises the suction unit P1 and the mixing chamber F1.
• the suction unit P1 is connected on the one hand to a source of water, such as RO water or other solvent, via the inlet line Z and on the other hand to the suction line L1, which in turn is fluidly connected to the container B1 containing the concentrate raw material.
• a source of water such as RO water or other solvent
• valve V1 is arranged in the inlet line Z upstream of the intake unit P1.
• Valve V2 is located downstream of the mixing chamber F1.
• the dialysis concentrate flows through the return line L2 to the container B1.
• the discharge line A is connected to the suction line L1, by means of which the dialysis concentrate is withdrawn from the container B1, for example by the blood treatment device, and can be used to produce the ready-to-use dialysis solution.
• a concentrate pump can be used, which conveys the liquid dialyse concentrate from the container into a line in which the dialyse concentrate is mixed with water or the like for the purpose of producing the ready-to-use dialysis solution.
• one or more dosing or throttling means can be present in the feed line into which the concentrate line opens, which ensure a specific mixing ratio between dialysis concentrate and water and thus a specific dilution of the dialysis concentrate.
• the process for producing the dialysis concentrate is as follows.
• the container B1 that contains the raw material (hereinafter also referred to as “raw material container”) is connected to connections of the device or the dialysis machine or the mixing unit by means of the lines L1, L2.
• dialysis machine instead of a dialysis machine, it can also be another preparation device, so that the term “dialysis machine” used in the context of the invention is to be understood in general terms and includes any preparation units.
• the raw material container B1 must be of a size such that the entire volume of the ready-mixed dialysis concentrate can be accommodated in it.
• the raw material container B1 has two connections, one for line L1 and another for line L2.
• the raw material container B1 can have flexible or rigid walls and can be designed, for example, as a bag or cartridge.
• it can be a flexible disposable container, for example in the form of one or more bags.
• the line L1 is preferably a suction line that extends to the lowest point of the raw material container B1.
• the container B1 there is a concentrate which preferably forms an acidic or else a basic dialysis concentrate when it is dissolved. After mixing this dialysis concentrate with another concentrate and dialysis water, if necessary, it is used to produce a ready-to-use dialysis solution.
• the water or other solvents required for mixing or dissolving the raw material is fed from the inlet connection, i.e. the inlet line Z, to the mixing circuit of the dialysis machine with a defined flow, quantity and pressure.
• the valve V1 is located in the inlet Z.
• the exact dosing of the dialysis water can be done, for example, by means of flow sensors or by determining the volume or mass or, in the case of constant inflow conditions, by timing the inflow valve(s) V1 or by any other dosing device.
• the dialysis water flowing in from the dialysis system or from another source flows via the suction unit P1, which is designed to generate a negative pressure in the line L1 leading from the container B1 to the mixing circuit.
• the suction unit P1 is arranged between the inlet line Z and the mixing line M.
• the suction unit P1 is designed so that it can suck in the different forms of the raw material, if necessary, and then mix them with the dialysis water.
• the raw material is dissolved in the fine mixing chamber F1 and the solution then flows back into the container B1 via the line L2. If it is a liquid raw material, a mixture of raw material and dialysis water takes place in the mixing chamber, which is also referred to as fine mixing chamber F1 within the scope of the invention.
• the fine mixing chamber F1 contains a retaining element, such as a filter element, and is self-regulating: if undissolved raw material collects on this retaining element, the pressure loss in the system increases and the flow through the filter element is reduced or prevented altogether. This minimizes the flow rate over the suction unit and thus further suction of further raw material from the container. Even with a low flow, the undissolved raw material is overflowed with fresh solvent, thus optimizing the dissolution. If the raw material is sufficiently dissolved in the fine mixing chamber, the pressure loss across the retaining element decreases and the flow rate of the solvent through the suction unit increases, which promotes further suction of raw material through the suction unit into the fine mixing chamber.
• the mixing process in the fine mixing chamber F1 is self-regulating due to the combination of the design of the suction unit P1 and the fine mixing chamber F1.
• the pressure loss decreases and the flow rate through the suction unit P1 increases, which promotes further suction of raw material through the suction unit P1 into the fine mixing chamber F1. If, on the other hand, the raw material in the fine mixing chamber F1 is not yet sufficiently dissolved, the pressure drop across the suction unit P1 and across the fine mixing chamber F1 increases, which means that the flow rate across the suction unit P1 increases. is correspondingly low and thus further suction of raw material from the container B1 is minimized or completely prevented.
• the valve V1 is closed when a specific amount or a specific volume of dialysis water has been supplied.
• the mixing unit comprises the suction unit P1, the fine mixing chamber F1 and the raw material container B1.
• a valve V2 which can be designed as a non-return valve VR2. From this, the dialysis concentrate flows into the container B1.
• the raw material is mixed outside of the container B1 and without a further mixing branch.
• the mixing circuit with suction unit P1 and fine mixing chamber is - as explained above - self-regulating and thus preferably ensures the complete dissolution/mixing of the raw material.
• the blockage by the raw material is prevented.
• a sensor system/control unit for monitoring and controlling the mixing process can thus be dispensed with.
• the invention encompasses the use of exactly one mixing chamber F1 or also the use of a plurality of mixing chambers which are connected in series or in parallel. In the case of several mixing chambers, these can be identical or designed with mixing elements of different fineness.
• an additional mixing drive branch can be provided, as is shown in FIG.
• This includes a pump P2 or another pressure generator that is suitable for generating a liquid flow through the circuit line L3, as well as a valve V4 and/or a check valve VR1.
• the mixing drive branch is connected in parallel to the suction unit P1 and the mixing chamber F1.
• the mixing drive branch preferably opens into the mixing line downstream of the valve V1 and upstream of the valve V2 or VR2, as is shown in FIG.
• a valve V4 can optionally be provided upstream of the pump P1 of the mixing branch, by means of which the circuit line containing the pump P2 can be shut off.
• the solution or suspension is drawn off from the line section between F1 and V2/VR2 by means of the pressure generator P2, conveyed by the pump P2 and then added back into the line section of the mixing line M between V1 and F1.
• This creates a circulatory flow through the mixing chamber F1 and the mixing time can be extended independently of the dialysis water supply or the amount of dialysis water supplied.
• the dialysis machine or other device can suck the dialysis concentrate produced or the dialysis solution or another finished mixed solution out of the container B1 through the suction line A, for which purpose the valve V3 is opened and the container B1 is emptied.
• the line A can also be designed as a pressure line.
• the mixing process does not require a storage tank in which to carry out the mixing process.
• the concentrate raw material is dissolved / mixed without prior intermediate storage of dialysis water.
• the suction line A is connected to the suction line L1.
• the finished dialysis concentrate is withdrawn from the container B1 by means of the suction line A.
• the line A is connected directly to the mixing chamber F1 and/or directly to the return line L2.
• the dialysis concentrate produced with this device can be degassed via the mixing chamber F1 with the valve V3 open and the valves V1 and possibly V2 and V4 closed.
• the system or all flow paths can be flushed or disinfected, just as is possible according to the prior art with the canister connections on dialysis machines.
• a disinfectant could be supplied via the inlet (inlet line Z) or the bag B1 could contain a disinfectant instead of the raw material container.
• the method according to the invention can be combined, for example, with: A density measurement for (automatic) quality control or determination of the progress of the mixing process.
• the dialysis machine or another source can provide temperature-controlled dialysis water.
• the device according to the invention can be combined with a system for online quality monitoring and approval.
• Another possible embodiment of the invention is the integration of the mixing device according to the invention in a system or a unit that is upstream of the dialysis machine and connected to a dialysis water supply or integrated into it, so that the preparation of the solution in container B1 can take place in preparation.
• the high-precision dosing system of a dialysis machine for the correct dosing of the dialysis water for the mixture of the raw material could be connected upstream of the inlet (inlet line Z) of the mixing system and thus be integrated into the mixing process.
• the method according to the invention is carried out as follows:
• the raw material bag or container B1 containing raw material is connected to the corresponding connections of the dialysis machine via the lines L1, L2.
• Dialysis water is transferred from the inlet connection (inlet line Z) with shut-off device V1 to the mixing circuit with a defined flow, quantity and pressure.
• the dialysis water provided by the dialysis system or from another source with a defined flow, quantity and pressure flows through the suction unit P1 and thus sucks the raw material or the raw material-dialysis water mixture from the container B1, such as a bag or cartridge, and transports the raw material -Dialysis water mixture in the fine mixing chamber F1.
• the raw material is dissolved in the dialysis water or mixed with it and the finished solution in the form of the dialysis concentrate flows back into the container B1 via the line L2.
• the shut-off device V1 is closed. If a raw material is used that does not completely dissolve during the dialysis water feed phase, the raw material can be completely dissolved with the aid of the optional mixing drive branch according to FIG. 2 or 3 .
• the dialysis machine can suck the dialysis concentrate or the dialysis solution or another ready mixed solution from the bag B1 by means of the line 2 and the open valve V3. 7.
• density measurement or similar methods can be used for (automatic) quality control or determination of the progress of the mixing process.
• temperature-controlled dialysis water can be used, which could be provided by the dialysis machine, for example.
• the bag B1 can be completely emptied by the machine and then disconnected and disposed of. Alternatively, the bag can also be uncoupled first and then emptied and disposed of manually.
• the dialysis machine performs a cleaning or disinfection process with feedback connections, analogous to the cleaning process for the canister connections.
• a cleaning or disinfection process can be carried out by connecting a bag with cleaning Zdisinfecting solution.
• the cleaning/disinfecting solution used could also be produced by mixing the device according to the invention on the basis of a concentrate analogously to the production of the dialysis concentrate, in which case the production would then be an integral part of the cleaning/disinfection process.
• the integration of the mixing process of the raw material from a raw material container is essential, for example in dialysis machines.
• a second mixing circuit with mixing tank is not necessary.
• the design of the suction unit P1 and the fine mixing unit F1 for the automatic, self-regulating, safe resolution or production of the dialysis concentrate or the Cleaning or disinfecting solution and the combination of container or bag with raw material concentrate, method and device for safe self-regulated dissolution advantageous.
• a storage tank or active pumping device is not absolutely necessary for the mixing method according to the present invention.
• Bag with concentrate raw material is lighter than canister with dialysis concentrate or a container with ready-to-use solution for dialysis treatment

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• 2020
  • 2020-12-08 DE DE102020132659.9A patent/DE102020132659A1/de active Pending
• 2021
  • 2021-12-08 EP EP21831021.7A patent/EP4255617A1/de active Pending
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