Patent Application
20110000902
The invention relates to a method for the heating of solutions preferably dialysis solutions, in accordance with the preamble of claim 1.
The dialysis solutions preferably treated in accordance with the invention are used, for example, in the field of peritoneal dialysis. In peritoneal dialysis, the dialysis solution to be infused into the abdominal cavity should be approximately at body temperature. On the one hand, this is perceived as pleasant by the patient and, on the other hand, is beneficial to the health. Another application is in the area of infusion technology, blood transfusion technology or other similar areas in which the liquids have to be heated.
The invention equally relates to an apparatus, in particular in a peritoneal dialysis device, for the heating of solutions, preferably dialysis solutions, in accordance with the preamble of claim 10.
It is already known to achieve the temperature of dialysis solutions to be used in peritoneal dialysis before the infusion. EP 0 956 876 B1, for example, describes a cassette for the conveying of dialysis liquids in which the dialysis liquid is heated before the infusion. For this purpose, the lines conducting the dialysis liquid are arranged in spiral manner in a heatable region of the cassette.
In accordance with WO 88/09186 A1 and WO 97/09074 A2, the dialysis solution to be heated is presented in a bag and is heated in this form. In this connection, a heater serves the heating of the bag in WO 97/09074 A2.
The heating time should be minimized as much as possible during the heating of the dialysis solution. However, the starting temperature of the heater for the heating of the dialysis solution having ambient temperature cannot be selected to be at any desired level. In the case a heater is used, on the one hand, the heat stability of the dialysis solution itself and, on the other hand, the heat stability of the bag material must be taken into consideration. Furthermore, particularly for the case that the heater system is accessible to the operator, it must be configured such that a risk of injury due to burns at a correspondingly hot heater can reliably be precluded.
There is a further problem in the so-called overshooting of the heating temperature which results as follows. To achieve the fastest possible heating of the bag contents, the heating device could preferably be operated at a maximum limit temperature which takes account of the previously mentioned conditions. If, however, the bag is removed from the heater during the heating of the heater or after a corresponding reaching of the wanted desired temperature of the bag, accumulated heat arises on the heater and thereby a heat accumulation which allows the temperature to rise briefly above the permitted limit temperature. This exceeding of the limit temperature can be called overshooting. On this uncontrolled exceeding of the limit temperature, there is an acute risk of burning for the user.
It is therefore the object of the present invention to further develop a generic method and an apparatus for the heating of solutions such that a bag containing the solution can be heated to the desired end temperature as fast as possible without there being any risk of temperature overshoots on the heating of the heater.
This object is solved in accordance with the invention by the method in accordance with the feature combination in accordance with claim 1. A method is accordingly proposed for the heating of solutions, preferably dialysis solutions, to a wanted desired temperature, wherein a solution presented in a bag is heated on a heater system including a heater by means of a two-step control. In accordance with the present invention, the temperature forming the lower switch-on threshold of the heater and the temperature forming the upper switch-off threshold of the heater vary. The unwanted overshooting of the temperature of the heater in the heating procedure can be reliably prevented by this.
Preferred embodiments of the invention result from the dependent claims following on from the main claim.
In accordance with a first advantageous embodiment of the invention, the temperature T of the bag containing the solution is measured by means of a first temperature sensor, whereas the temperature T2 of a heating element arranged in the heater system is measured via a second temperature sensor.
A previously fixed precontrol temperature TV is advantageously used as the temperature T2 forming the upper switch-off threshold. This pre-control temperature TV is determined in advance for discrete bag temperatures T1.
The method in accordance with the invention is particularly advantageously carried out by means of a two-step control in which the following steps run iteratively:
This method is repeated for so long until the bag has the desired temperature, with the heating element cooling down after the heating of the heating element up to the reaching of the precontrol temperature TV until it has reached the temperature the solution bag T1 has reached in the meantime. Subsequently, it is heated again in each case in the following iteration steps until the reaching of the precontrol temperature TV.
The precontrol temperature is preferably selected such that an overshooting of the temperature beyond the maximum heater temperature Tmax is not possible.
In accordance with a particularly advantageous embodiment of the invention, the switch-on point for the switching on of the heating element is determined in that a predetermined ratio of the temperature T2 forming the upper switch-off threshold to the temperature T1 of the bag containing the solution is reached.
It is in turn of particular advantage if the temperature T1 of the bag containing the solution is determined when the influence of the heating element on the sensor measuring the temperature T1 of the bag containing the solution has fallen below a limit value. The following phenomenon can hereby be taken into account. Since the temperature sensor for the measurement of the temperature T1 is not completely thermally decoupled due to the design of the heater, the measured temperature at this sensor cannot be directly associated with the solution temperature. At the end of the heating process, the sensor for the measurement of the temperature T2 adopts the temperature of the heating element, the sensor for the measurement of the temperature T1 adopts a temperature which lies between the actual solution temperature and that of the heating element. In accordance with the aforesaid advantageous embodiment of the method in accordance with the invention, it is now waited until the influence of the heating element on the sensor measuring the temperature T1 of the solution has fallen below a predetermined limit value. It is hereby ensured that the heat energy created is removed and has transferred into the solution so that the influence of the heating element on the sensor measuring the temperature T1 is minimized and the solution temperature can now be determined with greater precision.
The aforesaid limit value can advantageously be determined in that the temperature T1 of the bag containing the solution is determined from the gradient of the sensors measuring the temperatures. The gradient of the temperature changes T1 and T2, the gradient of the temperature change T1 to T2 or the temperature difference of T1 and T2 can advantageously be determined here.
The aforesaid object is also solved by an apparatus in accordance with claim 10. Preferred embodiments of this apparatus result from the dependent claims following on from claim 10.
The aforesaid method and/or the aforesaid apparatus can be used in a device for peritoneal dialysis in accordance with US 2006/0195064 A1 and US 2007/0112297 A1. Reference is made to the content of US 2006/0195064 A1 and US 2007/0112297 A1 and the description of the subject matter of these documents is made the subject of the present application by reference.
Further features, details and advantages of the invention will be explained in more detail in the following with reference to an embodiment shown in the drawing. There are shown:
A heater system 10 is shown in its schematic design in
The dialysis solution 20 in the bag 22 should be heated to 37° C. in as short a time as possible. To enable setup times for the peritoneal dialysis in which the dialysis liquid should be used which are as short as possible, this time period should be, for example, 45 minutes. It must now be taken into account that the filling volume 22 varies during the treatment since this bag is used for the start-up phase in the peritoneal dialysis.
The shortest possible time for the heating up to 37° C. must be achieved by means of a maximum heater temperature Tmax of 55° C. This maximum heater temperature is predetermined in that a higher temperature could result in a possible injury to the patient if he touches the heater during operation.
Due to the aforesaid properties, the exact volume of the dialysis solution bag 20 is not known as a rule. The starting temperature of the dialysis solution in the solution bag is not known as a rule, either. It must also be taken into account that the temperature sensor 18 of the bag can be influenced by the temperature of the heater carrier or of the heating element.
The aforesaid demands can be achieved by means of the method management in accordance with the invention in that only so much heat energy is always fed into the heater carrier that an overshooting beyond the maximum temperature Tmax is reliably prevented. The heating procedure of the heater 14 via the heating element 12 of the heater system 10 takes place by means of a two-step controller not shown in any more detail here, but widely known in the prior art. In accordance with the invention, in contrast to the known two-step controllers in accordance with the prior art, however, the upper switch-off threshold and also the lower switch-on threshold are varied over time. In this connection, the upper switch-off threshold is limited by a previously fixed precontrol temperature TV.
The switch-on point can, in contrast, be determined in that the temperature measured using the sensor 18, namely the temperature T1, is in the correct ratio with the temperature of the heating element 12 measured using the sensor 16, namely the temperature T2.
The precontrol temperature is determined as follows in accordance with the embodiment shown here. To meter the amount of energy of the heating element such that no overshooting of the temperature beyond the maximum temperature Tmax arises, the precontrol temperature TV is determined in dependence on the heater temperature. It is the aim in this connection to select a precontrol temperature which allows a cold bag 20 with dialysis solution 20, containing 5 liters for example, to be removed from a still heating heater 14 without an overshooting beyond the maximum temperature Tmax taking place.
In this context, it is very easy for the heating element to give off heat energy into the solution 20 due to the large temperature drop between the heating element 14 and the bag 22. However, at that moment at which the bag is removed from the heater 14, accumulated heat arises here which can no longer be dissipated so fast to the environment. This results in the previously described overheating of the heater system 10.
To prevent this above-described heating, the precontrol temperature TV must be selected to be relatively low, on the one hand, but so high to ensure a fast heating of the solution.
In accordance with the invention, the measured solution bag temperature T1 is put into a fixed ratio to the precontrol temperature TV. This relationship is shown with reference to the embodiment reproduced in the following table:
The association of the values in the aforesaid table signifies that, for example on the measurement of a temperature value T1 of 15° C., the predetermined precontrol temperature value TV is set to 39° C. as the upper switch-off threshold.
The course of the method in accordance with the invention can now be explained with the temperature curve shown in
In a first step, the solvent temperature T1 is determined by the sensor 18. The precontrol temperature TV is selected from the above table in dependence on this measured temperature T1. The heater system 10 is now heated until the heating element 12 has reached the precontrol temperature TV. It is monitored via the sensor 16 and the temperature curve T2 of the heating element 12.
In the next step, the solution temperature of the heated part of the solution 20 is measured and the aforesaid course of the method is repeated until the desired solvent temperature is reached.
It is not necessary in the method in accordance with the invention for the heating transition resistance between the heating element 14 and the bag 22 with the contained solution 20 to be known. Different materials can be used here, for example aluminum for the heater carrier and for example PVC for the solvent bag 22.
The contact surface of the bag on the heater carrier can vary in dependence on the bag size and the bag volume; nor does it have to be known to the system to carry out the method in accordance with the invention.
In accordance with the method in accordance with the invention, the dead time in which the generated heat energy from the heating element 12 is transferred into the solution bag 22 and has heated the solution there can also be taken into account.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2008 011 828.1 | Feb 2008 | DE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2009/001435 | 2/27/2009 | WO | 00 | 8/24/2010 |
