Water Preparation System For Dialysis Treatments

Abstract

The invention relates to a water treatment system (1) for dialysis treatments, wherein the water treatment system (1) comprises a permeate circuit with a reverse osmosis system (RO) and at least one tap (ES.sub.1, 2 . . . N) for permeate, whereby the reverse osmosis system (RO) is fed by the reflux of the at least one tap (ES.sub.1, 2 . . . N) for dialysis treatments and/or a raw water inflow (RZ), whereby the water treatment system further comprises a heat exchanger (WT), whereby a primary circuit (PK) of the heat exchanger (WT) is connected with a buffer tank (PT) for storing thermal energy, whereby a second circuit (SK) of the heat exchanger (WT) is integrated into the permeate circuit, whereby heat is transferred in a controlled manner from the buffer tank (PT) via the heat exchanger (WT) to permeate in the permeate circuit.

Claims

1. Water treatment system for dialysis treatments wherein the water treatment system comprises a permeate circuit having a reverse osmosis system (RO) and at least one tap (ES.sub.1, 2 . . . N) for permeate, whereby the reverse osmosis system (RO) is fed by the reflux of the at least one tap (ES .sub.1, 2 . . . N) for dialysis treatments and/or a raw water inflow (RZ), whereby the water treatment system further comprises a heat exchanger (WT), whereby a primary circuit (PK) of the heat exchanger (WT) is connected with a buffer tank (PT) for storing thermal energy, whereby a secondary circuit (SK) of the heat exchanger (WT) is integrated into the permeate circuit, whereby heat is transferred in a controlled manner from the buffer tank (PT) via the heat exchanger (WT) to permeate in the permeate circuit.

2. Water treatment system for dialysis treatments according to claim 1, characterised in that in a first operational mode of the water treatment system for dialysis treatments the temperature of the permeate is increased to a temperature from 20 degrees Celsius up to 37 degrees Celsius after the passage of the heat exchanger (WT).

3. Water treatment system for dialysis treatments according to claim 1, characterised in that in a second operational mode of the water treatment system for hygienic treatment of at least parts of the permeate circuit the temperature of the permeate is increased to a temperature of 70 degrees Celsius and more after the passage of the heat exchanger (WT).

4. Water treatment system for dialysis treatments according to claim 1, characterised in that the water treatment system further comprises a solar thermal or geothermal source or a phase change storage to feed the buffer tank (PT) with thermal energy.

5. Water treatment system for dialysis treatments according to claim 1, characterised in that the permeate circuit further comprises a bypass (BP) to shorten the permeate circuit, wherein the bypass is arranged for bypassing the at least one tap (ES .sub.1, 2 . . . N) for dialysis treatments.

6. Water treatment system for dialysis treatments according to claim 1, characterised in that the heat exchanger comprises a degree of efficiency of 75% and more.

7. Water treatment system for dialysis treatments according to claim 1, characterised in that the permeate circuit does not comprise any thermal buffer storage.

8. Water treatment system for dialysis treatments according to claim 1, characterised in that furthermore a first temperature sensor (TF.sub.1) is arranged after the outlet of the secondary circuit (SK), wherein the inflow of the primary circuit (PK) to the heat exchanger (WT) is controlled in dependence on the permeate circuit outlet temperature (T.sub.PKout) measured by the first temperature sensor (TF.sub.1)

9. Water treatment system for dialysis treatments according to claim 1, characterised in that furthermore a second temperature sensor (TF.sub.2) is arranged ahead of the inlet of the secondary circuit (SK), wherein the inflow of the primary circuit (PK) to the heat exchanger (WT) is controlled in dependence on the permeate circuit inlet temperature (T.sub.PKin) measured by the second temperature sensor (TF.sub.2).

10. Water treatment system for dialysis treatments according to claim 1, characterised in that furthermore a flow meter (VM) is positioned in the secondary circuit (SK), wherein the inflow of the primary circuit (PK) to the heat exchanger (WT) is controlled in dependence on the volume measured by the flow meter (VM).

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0020] In FIG. 1 a schematic diagram according to the embodiments of the invention is illustrated.

DETAILED DESCRIPTION

[0021] Subsequently, the invention will be presented in greater detail with reference to the figure. It is to be noted that different aspects will be depicted that can be employed individually or in combination with each other. i.e. any aspect can be utilised with different embodiments of the invention if not explicitly presented simply as an alternative.

[0022] Moreover, to simplify matters hereinafter normally only one entity will be referred to. Unless explicitly stated otherwise, the invention may also comprise several of the concerned entities respectively. In this respect, the usage of the terms a or an is only indicative as to that in a simple embodiment at least one entity is used.

[0023] In a water treatment system 1 according to the present invention for dialysis treatments the water treatment system 1 comprises a permeate circuit with a reverse osmosis system (RO) and at least one tap ES.sub.1 or more than one taps ES.sub.2 . . . N for permeate.

[0024] The reverse osmosis system RO may be fed on the one hand by the reflux from the at least one tap ES.sub.1 or more than one taps ES.sub.2 . . . N for dialysis treatments, or on the other hand alternatively or additionally by a raw water inflow RZ.

[0025] The water treatment system further comprises a heat exchanger WT. A primary circuit PK (primary circuit) of the heat exchanger WT is connected with a buffer tank PT wherein the buffer tank is installed to store thermal energy. A secondary circuit SK (secondary circuit) of the heat exchanger WT is, however, integrated into the permeate circuit, wherein heat is now transferred in a controlled manner from the buffer tank PT via the heat exchanger WT to permeate in the permeate circuit.

[0026] I.e. the invention allows to keep the volume that is to be disinfected small, whereas at the same time the option is provided to bring on the one hand large volumes of provided permeate to near-body temperatures with the help of the heat exchanger WT or on the other hand to also rapidly provide high temperatures for heat disinfection, whereby all system parts through which permeate flows can now be heat disinfected.

[0027] In one embodiment of the invention the temperature of the permeate is increased to a temperature from 20 degrees Celsius up to 37 degrees Celsius after the passage of the heat exchanger WT in a first operational mode of the water treatment system (1) for dialysis treatments. Hereby the heating power of devices at the taps ES.sub.1, 2 . . . N can be lowered which makes these devices more cost-effective in operation and production.

[0028] In another embodiment of the invention, the temperature of the permeate is increased to a temperature of 70 degrees Celsius and more after the passage of the heat exchanger (WT) in a second operational mode of the water treatment system (1) for hygienic treatment of at least parts of the permeate circuit. In particular, the temperature can be increased to 85 degrees Celsius or up to over 100 degrees Celsius in order to thus provide a quicker heat disinfection. Thereby e.g. the execution time of the second operation mode can be dependent on the temperature the permeate comprises ahead of and/or behind the heat exchanger.

[0029] Of particular advantage is that in one embodiment the invention can also comprise a solar thermal or geothermal source or a phase change storage to feed the buffer tank (PT) with thermal energy. In FIG. 1, for instance, feeding via solar collectors is suggested. Hereby areas in which continuous supply of electrical energy is a problem or that dispose of a suitable energy supply can be suitably provided with thermal energy for the buffer tank PT. In particular, the degrees of efficiency of directly consumed thermal energy are considerably higher than a conversion from electrical energy. A pump P.sub.1 can also be provided for circulation.

[0030] Without loss of generality of the invention, the permeate circuit may further comprise a bypass BP to shorten the permeate circuit, wherein the bypass is arranged for bypassing the at least one tap (ES.sub.1, 2 . . . N) for dialysis treatments. This can be an advantage for certain operating modes of the water treatment system 1.

[0031] In another embodiment of the invention the heat exchanger WT comprises a degree of efficiency of 75% and more. In particular, the heat exchanger WT comprises a degree of efficiency of 90% and more.

[0032] Without loss of generality, the permeate circuit may comprise a buffer storage for permeate or may not comprise any buffer storage for permeate. In this respect, there are no limits for the system design. It is advantageous that for instance the buffer tank PT only needs to be adjusted to the heating power that is to be provided, whereas a possibly existing buffer tank for permeate only needs to be adjusted to the amount of permeate that is to be provided and the cleaning capacity of the reverse osmosis RO. I.e. the invention permits a highly flexible system design so that the invention can be utilised in a variety of application scenarios.

[0033] In another embodiment of the invention, a first temperature sensor TF.sub.1 is arranged after the outlet of the secondary circuit SK. Then the inflow of the primary circuit PK to the heat exchanger WT can be controlled in dependence on the permeate circuit outlet temperature T.sub.PKout measured by the first temperature sensor TF.sub.1 so that a required target temperature, for instance near-body temperature or temperature for heat disinfection will be reached.

[0034] For instance, the pump P.sub.2 can be controlled respectively.

[0035] Alternatively or additionally a second temperature sensor (TF.sub.2) can be arranged in front of the inlet of the secondary circuit (SK), wherein the inflow of the primary circuit (PK) to the heat exchanger (WT) is controlled also in dependence on the permeate circuit inlet temperature (T.sub.PKin) measured by the second temperature sensor (TF.sub.2). In particular, if a first temperature sensor TF.sub.1 as well as a second temperature sensor TF.sub.2 are provided, entering the temperature into the heat exchanger via the first circuit can be controlled in a particularly precise manner.

[0036] Furthermore it can be provided that in embodiments of the invention a flow meter VM is arranged in the secondary circuit SK. The exact place of the flow meter can thereby be suitably selected and does not have to be selected as shown in FIG. 1. In particular, a flow meter VM can also be arranged at the place of a possibly existing temperature sensor TF.sub.1, TF.sub.2. Now, alternatively or additionally also in dependence on the volume measured by the flow meter (VM) the inflow of the primary circuit PK to the heat exchanger WT can be controlled.

[0037] For instance, the flow meter can also be provided by a pump P.sub.3 .

[0038] I.e. the embodiments of the invention allow a hygienic design of a water treatment system, since the separation of the permeate circuit and the buffer tank permits a more compact design of the permeate circuit in combination with simpler disinfectability of the permeate circuit.

[0039] Although only one heat exchanger WT has been displayed above, for efficiency reasons of course also two or more heat exchangers can be provided for the permeate circuit. Thus for instance a first heat exchanger can be optimised for heat supply for a first operational mode, whereas a second heat exchanger is optimised for heat supply for a second operational mode. I. e. the heat exchangers are for instance optimised with regard to the operating parameters and the respective degree of efficiency. Obviously it may also be provided for this type of system configuration that each heat exchanger is fed by its own primary circuit with its own buffer tank. However, it may also be provided that both heat exchangers are fed from a shared primary circuit with only one buffer tank.

[0040] I.e. the invention is characterised by a hydraulic separation. The volume and the inner surface of the permeate circuit are thus noticeably decreased which significantly improves the disinfectability and significantly reduces the energy necessary to reach the temperature that is required for the heat disinfection.

[0041] The buffer tank PT serves in the system of the invention exclusively as energy storage, i.e. tapping permeate from the tank is not possible.

[0042] Since the buffer tank buffers the energy required for a heat disinfection, it can be slowly warmed whereby the required power can be reduced. As the volume in the permeate circuit may be kept low, the permeate can quickly be heated up to the heat disinfection temperature. Furthermore, by means of a higher temperature that is possible because of the lower volume also the duration for a complete circulation line disinfection is reduced.