The present invention relates to an analyzer device of the kind using purified water, in particular for medical analyses.
An analyzer device of the above kind is used to analyze blood, for example, to indicate if a given substance is present in the blood, and if so the corresponding concentration.
Conventional analyzer devices require pure water in particular:
The accuracy of an analysis can be decisive in the adoption of a treatment or the dosage of medication.
The water supply system must therefore supply points of use with water of a quality such that it does not influence the analysis results.
The US National Committee for Clinical Laboratory Standards (NCCLS) issues a document entitled “Preparation and testing of reagent water in the clinical laboratory” defining the quality of the water that must be used in the field of medical analyses, the influence of contaminants on the results of analyses, the preferred method of maintaining a particular quality of the water, the manner of testing the water and the measures to be effected if it is suspected that the water has influenced the results of an analysis. In the above document, the NCCLS also defines three types of water:
As the influence of contaminants on the results of analyses is not well known, the NCCLS recommends using Type I water in analysis devices to prevent and eliminate all potential problems.
Existing autonomous water treatment systems connected to analyzer devices to supply them with water of given purity generally guarantee the quality of the water at the inlet of the analyzer devices. When water of Type I is stored, whether outside or inside the analyzer device, its resistivity decreases, metallic and/or organic contaminants pass from the storage tank to the water stored therein, and microbiological contamination occurs. The storage tank is generally inside the analyzer device in a warm environment (temperature from 30° C. to 37° C.), which further encourages the growth of bacteria.
Accordingly, the water reaching the points of use in the analyzer device no longer corresponds to the Type I requirements previously cited, even if, as suggested by the NCCLS, the water storage tank is agitated, the water storage tank in all prior art analyzer devices being a container into which purified water from the water treatment system is fed, and from which it is subsequently extracted by the analyzer device. This has the following consequences:
Another problem in existing applications is that the water treatment system and the analyzer device do not exchange information, and prior art analyzer devices are not designed to monitor the quality of the water or to maintain it at a given quality.
The present invention aims to alleviate these problems.
To this end, the present invention consists in an analyzer device of the kind using purified water and including analyzer means adapted to carry out predetermined analyses and defining at least one point of use of the purified water, characterized in that it further includes water purification means adapted to produce purified water for said analyzer means having a predetermined purity and in that the purified water is taken up by the analysis means immediately after it has been purified.
Thanks to the above features, it is possible to monitor the quality of the water and to maintain a predetermined purity as far as the point of use at which analyses, chemical reactions, washing, etc. are carried out.
Furthermore, the present invention simplifies analyzer device decontamination procedures and guarantees improved reproducibility of tests and analyses.
In this regard, it is important to note that, in the context of the present invention, the water itself is considered as a reagent.
According to preferred features of the invention, some of which may be combined:
Other features and advantages of the invention will emerge further from the following description, which is given by way of example and with reference to the accompanying diagrammatic drawings.
In the embodiment shown in
This kind of pretreatment module contains, for example, grains of activated carbon, front-end prefiltration elements and the like as are known to one of skill in the art.
The water pretreated in this way is fed to a reverse osmosis module 6. This module is also known in the art and is not in itself particularly relevant to the present invention. However, note that in practice the flow of water to be purified is continuous and tangential to a membrane of the reverse osmosis module 6, with the result that the water to be purified is divided at the membrane into two portions with different concentrations:
The osmosis module is preceded by a pressure regulator 3 for regulating the pressure at the inlet of the reverse osmosis module, generally to 2 bar. The water is then fed by a pump 4 to the reverse osmosis module 6 at a predetermined pressure and flowrate to guarantee a constant flow of permeate at a temperature from 5° C. to 30° C.
A device 5 for introducing an agent for cleaning the reverse osmosis membrane and the pipes is provided between the pump 4 and the reverse osmosis module 6.
A portion of the retentate passes through a flowrate regulator 19 and is returned to the pressure regulator 3 via a check valve 21 and another portion of said retentate is drained off via a flowrate limiter 20.
Furthermore, a rinsing valve 7 on the upstream side of the reverse osmosis membrane maintains good purification performance.
In normal operation, the flowrate regulator 19 and the pressure regulator 3 maintain a constant pressure on the upstream side of the reverse osmosis membrane. The flowrate limiter 20 in series with the flowrate regulator 19 limits the flowrate to a maximum value specific to it, even when the regulator 19 is fully open. There is therefore always a counterpressure that ensures the pressure necessary for correct operation of the reverse osmosis module 6.
When the valve 7 is opened, there is no longer any significant restriction of flow, and the water entering the reverse osmosis module 6 is no longer subject to any counterpressure from the regulator 19. Accordingly, most of the water leaves the module 6 before it has passed through the membrane and expels the impurities deposited thereon to the drain via the valve 7.
On closing said valve 7, the regulator 3 and the pump 4 reestablish a counterpressure on the upstream side of the membrane of the reverse osmosis module 6, which then operates normally again.
A three-way solenoid valve 8 at the outlet of the reverse osmosis module 6:
In the latter case, the water passes successively through a UV radiation oxidation treatment module 9 (wavelength 185 nm), a polishing module 10, a degassing module 11 and, finally, a final filtration element 12 with a mesh size of 0.22 μm. Each of these filtration techniques being known in the art, they are not described in further detail here.
The purified water at the outlet of the filter 12 is directed into a storage tank 14 equipped with a sterilization UV lamp (wavelength 254 nm) to maintain a low level of bacteria therein.
In accordance with the invention, the storage tank 14 is in fluid communication with the inlet of the UV treatment module 9 to cause the water in the final purification section to flow in a loop (the recirculation loop 17 integrates the storage tank 14), thanks in particular to a recirculation pump 13 and a check valve 22. This means that the purified water in the storage tank is constantly renewed and of maximum purity. The pump 13 also provides the vacuum pump function necessary for operation of the degassing module 11.
The points of use of the analyzer system 18 of the analyzer 100 are supplied via a distributor 15 connected to the storage tank 14, which ensures that whenever the device is operating (under steady state conditions) the water distributed to the points of use is of high quality, in practice of Type I purity.
This analysis section 18 includes analysis means generally used in prior art analyzers and for this reason are not described in more detail here. Likewise the electronic control means of the purification system 23 and the analyzer system 18 of the analyzer 100 are not described in more detail here. However, one embodiment of the latter is described next with reference to
As shown by the dashed line arrows in
Furthermore, depending on the chosen embodiment of the invention, the water purification system 223 can have various configurations:
Turning to
As in
It is therefore at the outlet of the unit D that the water has the highest quality that can be obtained in the water treatment system. In practice it is water of Type I.
Note that the above units are also shown in
Note also that there are several possible positions for connecting the points of use. They can be connected directly to the outlet of the unit D (arrows 251) or by a dead arm directly to the outlet of the buffer storage tank E (arrow 252), providing a temporary high flowrate, for example. The latter configuration corresponds to that of
The point(s) of use can also be connected directly to take-off points on the recirculation loop 217 (arrows 253), with no “dead arm”.
It is important to note that in all cases the path between the point(s) of use and the outlet of the unit D is optimized to guarantee the predetermined water quality at the point(s) of use.
The continuous water recirculation loop 217 leading to the module D, into which the storage tank E is integrated in the
In the embodiment shown in
The user can therefore have continuously available on a screen 256 connected to the central unit 255 information on the water quality at the outlet of the unit D and/or the various points of use, together with alarm, breakdown and scheduled maintenance signals.
Moreover, the central unit 255 of the analyzer 200 can operate on the water treatment system 223 via the control unit 254 and modify various parameters thereof to adapt the water at the outlet of the unit D to its requirements in real time.
Note also that, for simplicity, sensors for measuring the conductivity and the temperature of the water functionally connected to the control portion of the unit 254, which determine the purity of the water at predetermined locations, such as the outlet of the unit D, are not shown in
Other optional sensors can also be used (to measure the concentration of dissolved oxygen, of total biological carbon, etc.).
It must be understood that the present invention is in no way limited to the embodiments described hereinabove and that many modifications can be made thereto without departing from the scope of the invention.
In particular, in a different embodiment, water can be sent farther upstream in the purification process (to the inlet of the unit A, B or C), or supplementary purification means can be used, for example ultrafiltration means.
Number | Date | Country | Kind |
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03 08812 | Jul 2003 | FR | national |
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5571419 | Obata et al. | Nov 1996 | A |
5585003 | Van Newenhizen | Dec 1996 | A |
6197255 | Miyake | Mar 2001 | B1 |
6649037 | Liang et al. | Nov 2003 | B2 |
Number | Date | Country |
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06265555 3 | Sep 1994 | JP |
2000266763 | Sep 2000 | JP |
Number | Date | Country | |
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20050013739 A1 | Jan 2005 | US |