SYSTEM FOR ELIMINATING GASES IN A CONTAINER

Abstract: System for eliminating gases from a container which contains bicarbonate powder and water for preparation of a solution containing bicarbonate, particularly a dialysis solution. The system comprises a supply conduit (26) for transportation of substantially water from a water source (1, 2) to the container (21), and a concentrate conduit (29) for transportation of the solution containing bicarbonate from the container, and a pump (17) for transportation of said solution. In addition, an evacuation conduit (41) is provided which connects the negative-pressure side of the pump (17) to the upper end (33) of the container (21), and a valve (40) arranged in said evacuation conduit (41). An activation device controls the valve (40) for connecting the upper end of the container (21) to the negative-pressure side of the pump (17) via the evacuation conduit (41) for elimination of said gases.

Description: TITLE SYSTEM FOR ELIMINATING GASES IN A CONTAINER TECHNICAL FIELD The present invention relates to an improvement to a dialysis machine of the type which is described in EP-B1- 278 100 corresponding essentially to the dialysis machine GAMBRO AK 100. BACKGROUND OF THE INVENTION In a dialysis machine of the above-mentioned type, one or more cartridges containing powder of sodium bicarbonate, sodium chloride or other salts are used. The salt is dissolved by the introduction of water into the cartridge and removal of concentrate from the cartridge. The concentrate is used to prepare the intended dialysis solution. The composition of the dialysis solution is determined by the dialysis machine by measuring the conductivity of the prepared solution and regulating dosage pumps for the various concentrates. Nowadays, it is common to use two different concentrates; a B-concentrate comprising only bicarbonate from the above-mentioned bicarbonate cartridge, and an A-concentrate comprising remaining components in concentrated form, for example to a concentration of 37 times. Other combinations of concentrates also exist, such as the B-concentrate, which besides bicarbonate, may also comprise sodium chloride. Alternatively, the B-concentrate can be divided into two parts comprising bicarbonate and sodium chloride respectively, whereby the A-concentrate comprises remaining components in a more concentrated form. By preparing the bicarbonate concentrate and, where appropriate, the sodium chloride concentrate on demand in the dialysis machine, the advantage is attained that bicarbonate concentrate remains stable up to its use in a dialyser connected to the dialysis machine. If a dialysis solution is prepared in advance, which is also common nowadays, the risk exists that bicarbonate can decompose to carbon dioxide and carbonate. This implies that the pH value for the solution rises and the risk of precipitation of the calcium carbonate during mixing to the prepared dialysis solution arises. This can affect the final composition of the dialysis solution (reduction of the calcium ion concentrate) as well as creating problems of silting up of conduits and components in the dialysis machine due to deposition of calcium carbonate. For these reasons, the bicarbonate cartridge as described above has attained widespread use. As mentioned above, the dialysis solution is prepared by mixing the said two concentrates with water. The mixing is regulated by conductivity meters which control dosage pumps. Conductivity meters are, however, sensitive to possible incorporation of gas bubbles in the solution. Thus, the conductivity meters are generally preceded by gas separators whereby more accurate, less fluctuating measuring values can be obtained. The dialysis machine is provided with a monitoring system which is separated from the regulating system and serves to emit alarm signals should error situations arise. In the above-mentioned dialysis machine, GAMBRO AK 100, the monitoring of the dosage of concentrate occurs by monitoring the number of revolutions of the dosage pumps. If the number of revolutions differs too greatly from an expected value, an alarm signal is emitted. When using the above-mentioned bicarbonate cartridge containing dry bicarbonate powder, it is necessary that the powder be wetted with water prior to use. This takes place in a particular "priming step" . Water is introduced into the cartridge at its upper end at the same time that a substantial vacuum is applied to the lower end of the cartridge. Water fills substantially the entire cartridge in less than a minute. When a sensor positioned downstream of the bicarbonate cartridge detects that primarily concentrate flows from the cartridge, the sensor indicates that the priming step is complete. A valve switches over the machine so that the substantial vacuum is cut out. This sensor can be the above-mentioned conductivity meter. During the priming step, a small quantity of air or gas is trapped at the upper end of the cartridge. This quantity of gas does not, however, normally affect the functioning of the cartridge. In the above-mentioned EP-B1-278 100, various methods are described for removing this quantity of gas before the dialysis treatment commences, i.e. during the priming step. However, it sometimes occurs that the trapped gas in the upper region of the cartridge increases in volume during the dialysis treatment. If the trapped volume of gas becomes so great that a considerable quantity of gas passes out through the outlet of the cartridge and reaches the conductivity meter, an alarm is raised. Furthermore, it will be appreciated that the normal functioning of the cartridge is greatly affected if far too great a volume of gas is present in the cartridge. Normally, it is preferred that the water level always remains above the salt particle level in the cartridge. The above-mentioned condition with increasing volume of gas can be attributed to several causes. One possible cause is leakage in the connection between the upper or lower ends of the cartridge and the dialysis machine. The dialysis machine normally maintains a small vacuum in the cartridge. Other causes can be that gas bubbles accompany the water which enters the cartridge and thereafter become separated in the cartridge. The main cause would seem, however, to be gas formation in the cartridge, such as formation of carbon dioxide gas. It has been observed that the above-mentioned problem is exacerbated at higher ambient temperatures, which is probably due to the decomposition of bicarbonate to carbon dioxide and carbonate. Since the cartridge circuit is closed, there is no other route for the gas to flow than through the outlet from the cartridge, something which can activate the above-mentioned conductivity alarm. In order to deal with such an alarm situation, it is necessary to remove the bicarbonate cartridge and to insert an new cartridge in the system, whereafter the machine has to be restarted with a priming step and subsequent stabilising steps, something which can take a long time. During this time, the dialysis treatment has to be interrupted. It has also been observed that the conductivity signal from the conductivity meter, despite the preceding gas situation, fluctuates greatly, particularly at high ambient temperatures. In extreme cases, such as at high temperatures, these fluctuations are so great that the alarm limit is exceeded. It is noted that JP 55115819 describes a method of degassing the water and optionally the concentrates prior to mixing at volumetric dilution for avoiding problems relating from air bubbles formed during heating. SUMMARY OF THE INVENTION The object of the present invention is to provide a system which overcomes the above-mentioned problems with gas- filling in a bicarbonate cartridge. Another object of the invention is to provide an indicating arrangement for indicating when a dialysis cartridge runs the risk of becoming full of gas and measures are needed to remove this gas. A further object of the present invention is to improve the priming of a dialysis cartridge. The above-mentioned objects are achieved by a system and an arrangement which are defined in the subsequent claims. BRIEF DESCRIPTION OF THE DRAWINGS The invention will be described below in greater detail with reference to preferred embodiments of the invention depicted in the attached drawings. Fig. 1 is a schematic diagram of a dialysis machine according to the prior art, corresponding essentially to the dialysis machine GAMBRO AK 100. Fig. 2 is a schematic diagram corresponding to Fig. 1 with a deaeration device according to the invention. Fig. 3 is a schematic diagram corresponding to Fig. 1 showing an alternative embodiment of the deaeration device according to the invention. Fig. 4 is a schematic diagram corresponding to Fig. 1 showing a variant of the embodiment according to Fig. 3. Fig. 5 is a schematic diagram corresponding to Fig. 3 or 4, provided with an indicator. Fig. 6 is a schematic diagram corresponding to Fig. 5 showing an alternative embodiment. Fig. 7 is a schematic diagram corresponding to Fig. 6 but with an alternative valve arrangement. DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS A dialysis machine is shown schematically in Fig. 1, corresponding substantially to GAMBRO AK 100. The dialysis machine comprises a water reservoir 1 with inlet 2 for water which is normally received from a water purification plant (RO-unit, reverse osmosis) . The water reservoir 1 contains a heating coil 3 which warms the water to a suitable temperature, usually about 37°C. An outlet 4 is connected via a particle filter 5 to a primary conduit 6 for preparation of the dialysis solution. A first branch conduit 7 supplies A-concentrate from a container 8 via a suction nozzle 9 inserted in the container, a conduit 10 and a dosage pump 11. The A- concentrate is mixed with the water in the conduit 6 and is supplied to a mixing chamber 12 where homogenisation of the mixture takes place. Thereafter, the mixture passes a conductivity meter 13 where the conductivity of the mixture is determined. The conductivity meter 13 controls the dosage pump 11 so that a predetermined conductivity is attained. Normally, the A-concentrate is diluted approximately in the proportion 1:34. A second branch conduit 14 is located downstream of the conductivity meter 13, which conduit supplies concentrated bicarbonate or B-concentrate. The thus obtained dialysis solution passes through a throttle valve 15 and further to an expansion chamber 16 and a powerful pump 17. The dialysis solution is fed from the pump 17 to a bubble chamber 18 and a second conductivity meter 19. The increase of the conductivity with respect to the conductivity meter 13 is determined by the conductivity meter 19 and the difference signal regulates a dosage pump 20 for bicarbonate concentrate. The throttle arrangement 15 and the pump 17, together with the expansion chamber 16, form a gas eliminator. After the throttle arrangement 15, the pressure is relatively low, around -600 mmHg, and any gas in the solution is released, something which is assisted by the expansion chamber 16. The released gas collects in bubbles and passes via the pump 17 to the bubble chamber 18. The received bubbles rise to the upper part of the chamber 18 and are removed at approximately atmospheric pressure. Bicarbonate concentrate is prepared in the above-depicted dialysis machine in situ by use of a cartridge containing bicarbonate powder. The cartridge 21 is connected to a particular cartridge holder 22 equipped with swinging arms 23 and 24, as is described in greater detail in EP-B1-278 100. The cartridge 21 is connected in a circuit which runs from the water reservoir 1 via a suction nozzle 25 inserted in the water reservoir, a conduit 26 and a throttle arrangement 27 to the upper arm 23 of the cartridge holder 22. The upper arm 23 is connected to the upper end of the cartridge 21 via a spike. The lower end of the cartridge is, in a similar manner, connected to the lower arm 24 and communicates further via a particle filter 28 and a conduit 29 with the dosage pump 20 for bicarbonate concentrate. The dialysis machine can also be used for B-concentrate in liquid form by swinging the arms 23 and 24 to a shunt conduit 30, with the suction nozzle 25 being placed in a container for B-concentrate in a manner similar to that of the suction nozzle 9. In order to initially wet the powder in the cartridge 21, the dialysis machine is provided with a priming arrangement in the form of a conduit 32 and a valve 31. The conduit 32 is connected between the lower end of the cartridge, preferably between the filter 28 and the pump 20, and the primary conduit 6 downstream of the throttle arrangement 15 where a substantial vacuum is present (-600 mmHg) . Priming takes place by placing a bicarbonate cartridge 21 in the holder 23, 24, 22, as shown in Fig. 1, and opening the valve 31. In this manner, a substantial vacuum is applied to the cartridge 21 which draws air out of the lower end of the cartridge until the pressure in the cartridge is in the order of -600 mmHg. At the same time, water is drawn from the water reservoir 1 via the conduit 26 and the throttle arrangement 27 into the upper end of the cartridge. By means of the throttle arrangement 27, it is ensured that low pressure is able to have been established in the cartridge before water flows in via the arm 23. Thereafter, the cartridge is filled from above with water which is drawn through the powder in the cartridge 21 and eventually reaches the outlet in the arm 24. This condition is detected by the conductivity meter 19, whereupon the valve 31 is closed. The concentrate pump 20 is operated during the entire process. The concentrate pump 20 now receives liquid-based concentrate from the cartridge 21. A closed circuit has thus been created from the water reservoir 1 via the conduit 26, the cartridge 21 and the conduit 29 to the pump 20. During the above-mentioned process, a certain quantity of air will have become trapped in the upper end of the cartridge in a space 33. However, the water level is above the level of the bicarbonate powder 34 so that the powder is constantly wet. During operation, bicarbonate concentrate is removed via the concentrate pump 20. Due to the closed circuit, as much water is supplied to the upper end of the cartridge as is removed from its lower end. The supplied water dissolves the bicarbonate powder and a substantially saturated solution is formed in the cartridge. When the solution is saturated, dissolving ceases automatically. Since the cartridge 21 is included in a closed circuit, the gas in the space 33 remains entrapped and cannot migrate anywhere. This is not a disadvantage and does not lead to any damage. In the event that a slight vacuum be present in the cartridge 21, any leak in the connection between the cartridge 21 and the upper arm 23 can result in an increase in the gas volume in the space 33. The gas volume can also increase by means of gas accompanying the water from the water reservoir 1 via the conduit 26 to enter the cartridge 21. At high ambient temperatures it may occur that the sodium bicarbonate solution in the cartridge to a certain extent decomposes to carbon dioxide and sodium carbonate (soda) . Such carbon dioxide gas can collect in the space 33 and increase the confined gas volume. The gas volume in the space 33 is only harmful if it becomes too great and forces the water level below the level of the powder 34. In such a case there is the risk that the concentrated, substantially saturated solution which is removed via the outlet in the arm 24 can contain a certain quantity of gas. It may even happen that the cartridge runs dry, whereby a large quantity of gas will exit via the outlet 24. This condition can create an alarm. If the cartridge runs dry, it must normally be replaced, something which causes an interruption of operation. In accordance with the present invention, it is proposed to provide the dialysis machine with a valve with which the gas volume in the space 33 can be reduced, particularly if it shows a tendency to increase and to become far too great, i.e. reach below the level of the powder concentrate 34. A first embodiment of the present invention is shown in Fig. 2. A three-way valve 40 which normally connects the upper end of the cartridge 21 to the water reservoir 1 is placed in the conduit 26. In its second, activated position, however, the valve 40 connects the upper end of the cartridge 21 to a conduit 41 which leads to a substantial vacuum after the throttle arrangement 15, i.e. to the conduit 32. When the valve 40 is switched over, the air in the upper end of the cartridge 21 is drawn via the valve 40, the conduit 41 and the conduit 42 to the pump 17 and is separated in the subsequent bubble chamber 18 (see Fig. 1) . By arranging the valve 40 as close as possible to the cartridge 21, only a small quantity of water has first to flow via the conduit 41 and 32 before the air is drawn out. In this manner, a substantial vacuum is established in the cartridge 21. When the valve 40 is returned to its initial position, the vacuum in the upper end of the cartridge 21 will result in water being drawn in via the conduit 26 from the water reservoir 1 and partially filling the space 33 in order to equalise the vacuum. In this manner, the air-filled space 33 can be substantially halved with the help of a vacuum of about a half atmosphere. Since the valve 40 is located close to the inlet of the cartridge, the effect of the pressure reduction and subsequent pressure equalisation with water will be as great as possible. It is possible to repeat said process several times, for example 3 times in the course of one minute. This deaeration of the cartridge 21 can occur at repeating time intervals during dialysis treatment, for example in connection with a regularly repeating calibration of the ultrafiltration sensor in the dialysis machine, something which normally occurs at 30-minute intervals. The deaeration may result in a conductivity alarm since the large quantity of gas which flows via the conduit 32 and pump 17 can result in the flow in the primary conduit 6 being affected to such a degree that the alarm limits are exceeded. Should the machine be in its calibration mode, however, the alarm can be suppressed. The embodiment shown in Fig. 2 has a minor drawback in that any leakage in the valve 40 between the conduit 26 and the conduit 41 can disrupt the functioning of the dialysis machine. One embodiment of the present invention in which this drawback is overcome is shown in Fig. 3. In this embodiment the three-way valve 50, which corresponds to the three-way valve 40 in the embodiment according to Fig. 2, is placed in the conduit 32 between the priming valve 31 and the connection to the conduit 29. The deaeration valve 50 is thus connected to the valve 31 via a conduit 51 and to the conduit 29 via a conduit 52. The valve 50 connects the conduit 51 to the conduit 52 in its normal position. In its activated position the valve 50 connects the conduit 51 to a deaeration conduit 53 which is connected in the conduit 26 between the throttle arrangement 27 and the inlet to the cartridge 21. By means of this connection, it is ensured that no substantial pressures are present across the deaeration valve 50 during normal operation. The valve 31 isolates the system from the substantial vacuum in the conduit 32. The deaeration takes place by switching the deaeration valve 50 to its activated position, whereafter the valve 31 is opened. In this manner, a substantial vacuum arises in the conduit 53 via the valve 50, the conduit 51, the valve 31 and the conduit 32. A suction pressure thus arises in the conduit 26 at the connection to the conduit 53. Air will thus be drawn from the upper end of the cartridge 21. At the same time, water flows from the water reservoir 1 via the conduit 26 and the throttle arrangement 27 to the conduit 53. Due to the throttle arrangement 27, there is still, however, a substantial vacuum in the upper end of the cartridge 21. Thereafter, the valve 31 is closed whereby water flows from the water reservoir 1 via the conduit 26, the throttle arrangement 27 and to the upper end of the cartridge 21 to equalise the vacuum therein. The valve 31 can thereafter be opened for a second deaeration cycle if so desired. An alternative manner to operate the deaeration arrangement according to Fig. 3 is the following. Firstly, the valve 50 is switched to its activated position, whereafter the valve 31 is opened and a substantial vacuum is established in the upper end of the cartridge 21. Thereafter, the valve 50 is switched to its normal position whereby the substantial vacuum is diverted to the conduit 29 which is connected to the lower end of the cartridge 21. In this manner, water flows from the water reservoir 1 via the conduit 26, the throttle arrangement 27 and into the upper end of the cartridge 21. The valve 50 is thereafter switched back to its activated position and further gas is withdrawn from the upper end of the cartridge 21 via the conduit 53. This process is repeated one or more times. Finally, normal operation is resumed by switching the valve 50 to its normal position and closing the valve 31. The advantage of this method is that the powder in the cartridge 21 is agitated and any gas bubbles which adhere to the powder are loosened and rise to the upper end of the cartridge 21. At the same time, any channel formations in the powder in the cartridge can be avoided. A combination of the two above-described methods can also be used in which the valve 13 is closed between each switching action of the valve 50 to permit equalisation of the pressure in the cartridge 21 via the conduit 26 before the vacuum is applied to the lower end of the cartridge via the conduit 29. An alternative embodiment to Fig. 3 is shown in Fig. 4. Since the throttle arrangement 27 is normally positioned very close to the inlet to the cartridge 21, it can be difficult to connect the conduit 53 after the throttle arrangement 27. In the embodiment which is shown in Fig. 4, the conduit 63 from the valve 60 has been connected to the conduit 26 and the throttle arrangement 27 has beem removed. A normally open valve 64 is connected in the conduit 26 between the water reservoir 1 and the connection to the conduit 63. The valve 60 is connected to the valve 31 via a conduit 61 and is connected to the conduit 29 via a conduit 62. During the connection of the valve 60, the valve 64 is closed, whereby it is prevented that water is drawn from the water reservoir via the conduit 26 to the conduit 63. Otherwise, the operation is the same as for the operation according to the embodiment of Fig. 3. In the embodiment of Fig. 4, the operation of the throttle arrangement 27 is replaced by the operation of valve 60. As has been stated above, the deaeration valves 40, 50, 60 can be activated on suitable occasions when it is desired to deaerate the bicarbonate cartridge 21. Such deaeration can take place regularly with 30-minute intervals during the dialysis treatment when the normal dialysis treatment is interrupted for a calibration step. It is also possible to provide the dialysis machine with a possibility to manually initiate a deaeration. This can occur should a nurse or a user discover that the water level has dropped below the level of the powder 34 in the cartridge 21 or when the trapped volume of gas becomes too great. It is also feasible to provide the holder 22 with an indication arrangement which senses if the water level drops below the level of the indication arrangement. Such an indicator could be a load-cell 65 as illustrated in Fig. 4. In Fig. 4 there is additionally shown an electronic device 66 or microprocessor which controls the function of the valves, as indicated by dashed lines in Fig. 4. Device 66 can be adapted to control or indicate when deaeration is required, for example at regular time intervals or according to signals from an indication device or at demand from a user. A further indication arrangement is shown in Fig. 5. The embodiment according to Fig. 5 is provided with the same valves and conduits as the embodiment according to Fig. 4. In addition, the conduit 29 which connects the outlet of the cartridge 21 to the dosage pump 20 is provided with a deaeration indicator 70 in the form of a gas separation chamber 71. The chamber 71 is provided with an inlet 72 connected to the outlet from the cartridge 21 via a conduit 73, and to an outlet 74 connected to the conduit 29 and further to the pump 20. The chamber 71 may be positioned anywhere along the conduit 29 between the outlet from the cartridge 21 and the dosage pump 20. The bicarbonate concentrate from the cartridge 21 thus flows to the chamber 71 which has a relatively large cross section. Due to the low flow velocity in the chamber 71, any gas bubbles in the concentrate are separated and rise to the upper end of the chamber 71. If the bicarbonate concentrate should contain a large quantity of small gas bubbles, such as can be the case at high ambient temperatures, the confined gas volume in the chamber will increase. When the gas volume or the water level in the chamber 71 reaches an indicator 75, a signal is emitted which indicates that deaeration is required. If the cartridge 21 runs dry so that the space 33 increases greatly in volume and the risk arises that gas will be drawn out together with the concentrate, the gas which accompanies the concentrate will quickly fill the chamber 71 so that the level indicator 75 is activated. The chamber 71 preferably has such a large volume that the quantity of concentrate which is accommodated beneath the indicator 75 is sufficient for, for example, several minutes' treatment, i.e. ca. 50 ml. If the cartridge has run dry, the dialysis treatment can thus continue for several minutes in anticipation of a suitable occasion for deaeration. When the level indicator 75 registers that deaeration is required, the valves 60, 31 and 64 are activated as described above in connection with the embodiment according to Fig. 4. In addition, the chamber 71 is provided with a conduit 76 which connects the upper gas-filled end of the chamber with the conduit 61 between the valve 60 and the valve 31. Furthermore, the conduit 66 is provided with a throttle arrangement 77. When the deaeration cycle is activated by activating the valve 60 and the valve 31 is opened, the upper end of the chamber 71 will thus be evacuated by the conduit 76, conduit 61, the valve 31 to the conduit 32. When the water level in the chamber 71 has risen such that water fills the conduit 76 and reaches the throttle arrangement 77, the flow through the conduit 76 will be very small. At the termination of the deaeration cycle, the chamber 71 will therefore be substantially full of liquid and a new monitoring cycle can be initiated by means of the chamber 71. During normal operation, bicarbonate concentrate flows from the cartridge 21 via the conduit 73 and the chamber 71 to the conduit 29 and the concentrate pump 20. It has been shown that the conductivity measurement in the conductivity meter 19 attains considerably smaller fluctuations after the connection of the chamber 71. The reduction of the fluctuations is already noticeable at a room temperature of 20°C and becomes marked at room temperatures in the order of 30°C, something which can arise in warm countries. One explanation for the above-mentioned fluctuations and the decrease when the chamber 71 is connected in can be the following. At higher ambient temperatures, carbon dioxide gas is formed in the cartridge 21 at the same time as the dissolving of the powder or during the period substantially saturated concentrate is in the cartridge 21 before being fed through the outlet to the conduit 29. As the concentrate is fed out, the smallest bubbles, which do not adhere to adjacent salt particles, accompany the concentrate. The quantity of gas bubbles in the exiting concentrate varies stochastically. At higher temperatures, the mixture is greater and, as a result, so too is the variation of the mixed gas bubbles. The pump 20 is a metering pump which pumps a predetermined quantity of concentrate per revolution or fraction of a revolution. Since the concentrate is, however, diluted with gas bubbles, different quantities of sodium bicarbonate will pass through the pump depending on the intermixed quantity of gas. The intermixed quantity of gas is thereafter effectively separated in the bubble chamber 18. The conductivity meter 19 is thus subjected to a varying concentration where the variation depends on the quantity of intermixed gas bubbles during the passage of the pump 20. The more gas bubbles which are intermixed, the lower the concentration of the bicarbonate becomes. By introducing a bubble separator or gas separator 71 before the metering pump 20, it is ensured that the pump 20 always pumps saturated concentrate which is not diluted with gas bubbles. Consequently, the feeding of bicarbonate to the primary conduit 60 will be very consistent and without fluctuations, and as such the conductivity meter 19 emits a very constant signal. A further embodiment of the invention is shown in Fig. 6 which is a variation of the embodiment according to Fig. 5. The switching valve 60 has in this case been replaced by a simple valve 80 and the conduit 62 has been omitted. In this embodiment, priming of the cartridge 21 takes place by opening the valve 31 whilst the valve 80 is closed and the valve 64 is in its normal open position. In this manner, a substantial vacuum is obtained in the cartridge 21 via the conduit 73, the chamber 71, the conduit 76, the throttle arrangement 77, the conduit 81, the valve 31 and the conduit 32. Water flows from the water reservoir 1 via the valve 64 and the conduit 26 and the throttle arrangement 27 to the upper end of the cartridge 21. Water is thus introduced into the upper portion of the cartridge 21 and is withdrawn via the lower portion and the conduit 73 and fills the chamber 71. At the same time, the pump 20 is running, thus causing the liquid to flow through the outlet 74 to the conduit 29 and the pump 20. Simultaneously, the air in the upper end of the chamber 71 is withdrawn via the conduit 76 and 81. When the entire chamber 71 is filled with concentrate, the conduit 76 is filled up to the throttle arrangement 77 with concentrate. When liquid reaches the throttle arrangement 77, the pressure drop over the throttle arrangement falls greatly, which is sensed by a pressure sensor 84 arranged in connection with the conduit 76. The pressure sensor 84 indicates that the priming has been achieved and the valve 31 is closed. The cartridge 21 is thereafter refilled from the water reservoir 1 via the conduit 26 and the throttle arrangement 27 until approximately atmospheric pressure is attained in the cartridge 21, (a slight vacuum is normally present in the cartridge 21) . When the level indicator 75 registers that deaeration is necessary, this is attained by opening the valves 80 and 31 at the same time that the valve 64 is closed. Otherwise, the function is identical to that which has been described in connection with Fig. 5. In Fig. 6 it is shown that the separation chamber has been provided with a particular conical inlet 85 which faces upwardly. The concentrate thus flows upwardly through the inlet 85 with continuously diminishing velocity. The surface at the upper end of the inlet 85 is as large as the ring surface exterior of the upper end of the outlet so that the concentrate flows around the edge and continues downwardly without increasing the flow velocity. The flow velocity decreases further during the transport downwardly to the outlet 74. This flow pattern is favourable for separating gas bubbles in the flowing liquid. An alternative embodiment is shown in Fig. 7 in which the valve 80 is connected directly to the conduit 32 instead of via the valve 31. An evacuation conduit 86 connects the conduit 32 to the valve 80 and further to the conduit 63. In this manner, the valves 80 and 31 can be controlled totally independently of each other. During the normal priming in the embodiment according to Fig. 7, the valve 64 is firstly closed whilst the valve 31 is open. In this manner, it is ensured that a substantial vacuum is attained in the cartridge 21 before water is supplied via the opening of the valve 64. In this manner, an improved filling of the cartridge during the priming is attained. The invention has been described above in connection with preferred embodiments of the invention, suitable for use in the dialysis machine GAMBRO AK 100. The invention can, of course, be adapted to other types of dialysis machine, for example where an overpressure is present in the bicarbonate cartridge 21. The invention has also been described in connection with use of the internal feed pump for the elimination of the gases. Naturally, a separate pump can be used if this should be desired. The gas separation chamber performs two functions; on the one hand it serves as an indication arrangement for when the cartridge requires gas elimination and, on the other hand, it performs a deaeration of the concentrate which is obtained from the cartridge so that a more accurate dosage can be obtained in the dosage pump and noise can be eliminated in the conductivity meter. The latter-mentioned property can also be performed separately without the chamber being used for indication, for example by elimination of gases occurring time-dependently, for example every half hour. Further modifications which are apparent to the skilled man are intended to fall within the scope of the invention as defined by the appended claims.

Claims: CLAIMS 1. System for eliminating gases from a container which contains bicarbonate powder and water for preparation of a solution containing bicarbonate, particularly a dialysis solution, whereby the system comprises a supply conduit (26) for transportation of essentially water from a water source (1, 2) to the container (21) , and a concentrate conduit (29) for transportation of the solution containing bicarbonate from the container, characterized by a pump (17) ; an evacuation conduit (41) which connects the negative pressure side of the pump (17) to the container (21) ; a valve (40) located in said evacuation conduit (41); an arrangement (66) to activate the valve (40) to connect the container (21) to the negative pressure side of the pump (17) via said evacuation conduit (41) for elimination of said gases; and an indication device (65,66,70) arranged to control or indicate that the container requires elimination of said gases. 2. System according to claim 1, characterized in that the supply conduit (26) is provided with a three-way valve (40) which normally connects the upper end of the container to the supply conduit (26) and which, when activated, connects the upper end of the container to said evacuation conduit (41) . 3. System according to claim 2, characterized in that said three-way valve (40) is arranged in the vicinity of the upper end of the container. 4. System according to claim 1, characterized by a first evacuation conduit (53) which connects the upper end of the container to a first connection to said valve (50) , and a second evacuation conduit (52) which connects the concentrate conduit (29) to a second connection to said valve (50) , and a third evacuation conduit (51) which connects a third connection to said valve (50) to a conduit (32) which leads to the negative pressure side of the pump, whereby the valve is arranged to normally connect the third evacuation conduit (51) to the second evacuation conduit (52) and, when activated, is arranged to connect the third evacuation conduit (51) to the first evacuation conduit (53) for elimination of said gases. 5. System according to claim 4, characterized in that the supply conduit (26) is provided with a constriction (27) arranged between the water source (1, 2) and the connection of the first evacuation conduit (53) to the supply conduit (26) . 6. System according to claim 4, characterized in that the supply conduit (26) is provided with a valve (64) arranged between the water source (1, 2) and the connection of the first evacuation conduit (53) to the supply conduit (26) , which valve is normally open and which is closed during said elimination. 7. System according to any one of the previous claims, characterized by a gas separator (70) arranged in said concentrate conduit (29) , which gas separator comprises an indicator (75) which indicates when a gas level in the gas separator is below a predetermined level. 8. System according to claim 7, characterized in that the gas separator (70) comprises a chamber (71) with an inlet (72) connected via a conduit (73) to the lower end of the chamber and an outlet (74) connected to said concentrate conduit (29) , whereby the chamber has a surface cross-section which is substantially greater than the surface cross-section of said inlet (72) , whereby the flow velocity through the chamber is low and gas separation takes place and the separated gas is collected in the upper end of the chamber. 9. System according to claim 7 or 8, characterized in that the gas separator (70) is positioned in the concentrate conduit (29) between the lower end of the container and a concentrate dosage pump (20) . 10. System according to any one of the previous claims, characterized in that the system is adapted to produce a dialysis fluid.

Inventors: ERICSON BJOERN, FANG JI JUN, HOBRO STURE, LINDERUP ERIK, ERICSON, BJOERN, FANG, JI, JUN, HOBRO, STURE, LINDERUP, ERIK
Applicants: ERICSON BJOERN, FANG JI JUN, GAMBRO AB, HOBRO STURE, LINDERUP ERIK, ERICSON, BJOERN, FANG, JI, JUN, HOBRO, STURE, LINDERUP, ERIK
Application year: 1997
Main classification: A61M1
IPC codes: A61M1