The present invention relates to a dishwasher, in particular a commercial single-tank dishwasher or commercial multi-tank dishwasher, for washing washware.
In the field of commercial dishwashers—be they conveyor-type dishwashers having several liquid tanks or hood-type dishwashers or other stationery machines with only one liquid tank—it is necessary for fresh water to be introduced into the system at least at one point and for used washing water to be discharged from the system at least at one point. Since the fresh water is usually drawn from the public drinking water system or the like, it is at a comparatively low temperature which is not suitable for all dishwashing zones or dishwashing processes. Therefore, final rinsing can of course be performed with comparatively cold fresh water; however, at the latest when the water is intended to be used as cleaning water, for example, in the next dishwashing section of the washing water cascade in the case of a conveyor-type dishwasher or at a corresponding program point in the case of a batch dishwasher and, for example, with a detergent or the like admixed, low washing water temperatures of this kind are no longer sufficient.
If the washing water is now heated to the required temperature as is customary, the question arises of whether the heat remaining in the washing water after said washing water is used, for example by partial or complete replacement of the used washing water with fresh water, can be used.
In the case of commercial hood-type dishwashers, approximately 50% of the supplied thermal energy is discharged as lost heat in the form of heated waste water.
The remainder of the supplied thermal energy remains in the washware or is lost as a result of vapor discharge or the like.
It is known in the art to use the thermal energy in the waste water, before said waste water is discharged to the waste water system, by means of a heat exchanger in such a way that this heat in the outflowing waste water—physically separately from the fresh water—is at least partially transmitted to the supplied fresh water by means of a heat exchanger. The conventional solutions now have the disadvantage that they sometimes do not function reliably enough and, in particular, the waste water remains at a comparatively high temperature when introduced into the waste water system, as a result of which less thermal energy is emitted to the supplied fresh water. This is the result of, for example, heat exchangers which are composed of plastic materials often being used, these having a low thermal conductivity on account of the material used. In addition, plate-type heat exchangers or the like which are used can become clogged if the washing water is heavily soiled (food residues), wherein these food residues collect between the plates of the plate-type heat exchanger and block the liquid channel.
An excessively high waste water temperature is also disadvantageous in that it is not possible to comply with any existing local standards. For example, the US “Uniform Plumbing Code” specifies a maximum waste water temperature of 140° Fahrenheit (60° C.) wherein, if this auxiliary limit cannot be complied with, cold fresh water is often supplied to the waste water in order to comply with the required maximum waste water value.
The invention is therefore based on the object of specifying a dishwasher having a corresponding heat recovery device which operates more reliably than conventional solutions and at the same time has a good energy yield and can be produced in a cost-effective manner.
The object is achieved, in particular, by a dishwasher for washing washware, wherein the dishwasher has a liquid transportation line comprising at least one supply line for supplying liquid at a first temperature and comprising at least one discharge line for discharging liquid at a second temperature, wherein the supply line and the discharge line run coaxially in relation to one another, so that either the supply line or the discharge line forms an internal line which runs in the direction of extent of the liquid transportation line within the respectively other supply line or discharge line which for its part forms an external line, and thereby form a countercurrent heat exchanger.
In this case, the direction of extent of the liquid transportation line is defined by the flow path of the fluid which is to be supplied or to be discharged and does not necessarily have to run in a straight line.
The fact that the supply line and the discharge line run coaxially in relation to one another results in the particular advantage that, by forming a countercurrent heat exchanger, heat can be transferred in a reliable and efficient manner in such a way that the waste water, which is intended to be discharged by means of the discharge line, is then at a sufficiently low temperature. At the same time, the solution of forming the heat exchanger by coaxial construction from the supply line and the discharge line and realizing said heat exchanger in countercurrent form is very cost-effective.
Advantageous developments of the solution can be implemented.
For example, it is provided that the internal line has a wall which is formed from a material which has a high specific thermal conductivity, and that the external line has a wall which is formed from a material which has a low specific thermal conductivity.
This has the result that good heat exchange can take place between the two fluids (fresh water and waste water) which flow in countercurrent in the interior of the liquid transportation line, wherein undesired emission of heat to the outside is suppressed at the same time. In this connection, it is preferably provided that the material of the wall of the internal line is copper. Copper has a high specific thermal conductivity in the range of from approximately 240 to 400 W/(m2·K). In this connection, it can be provided, as an alternative or in addition, that the material of the wall of the external line is a plastic material. The specific thermal conductivity of additive-free plastics lies, for example, in the range of between 0.1 and 0.6 W/(m2·K), while plastics with additives have, for example, a specific thermal conductivity of approximately 1 to 10 W/(m2·K).
According to a further aspect, it is provided that the liquid which can be discharged by means of the discharge line is waste water and is preferably supplied directly to the waste water system. Since, owing to the solution provided herein, this waste water is at a temperature which is suitable for direct introduction in accordance with strict standards such as, for example, the US “Uniform Plumbing Code” and is generally less than 60° C., it is, owing to the solution provided herein, no longer necessary to supply fresh water to the waste water for cooling purposes in order to comply with this maximum temperature. According to a further aspect, it is provided that the liquid which can be supplied by means of the supply line is fresh water and is preferably drawn directly from the drinking water system.
This results in the particular advantage of the solution provided herein that this fresh water which is drawn directly from the drinking water system and is usually at a relatively low temperature of, for example, 15° C. or the like does not first have to be reheated, but rather can be efficiently heated by the transfer of heat in the countercurrent heat exchanger.
According to a further aspect, the external line is the supply line, and accordingly the internal line is the discharge line. In other words: the hot water is conducted through the internal line of the two lines, while the cool fresh water is introduced into the dishwashing system by means of the external line. This ensures, in particular in combination with a corresponding material selection, optimum transfer of heat from the hot waste water flowing on the inside to the cold fresh water flowing in the opposite direction on the outside, wherein an insulating effect is ensured toward the outside, that is to say in relation to the liquid transportation line toward the outside, at the same time.
In this case, it is particularly provided that the first temperature is lower than the second temperature, and is preferably 30 to 40 K lower, and particularly preferably approximately 45 K lower, than the second temperature.
According to a further aspect, it is provided that a continuous intermediate wall is provided between the wall of the internal line and the wall of the external line. In this case, it is preferably provided that the intermediate wall bears against the internal line at least in regions and preferably by way of more than half of its surface. In this connection, “continuous” means that said intermediate wall runs in the direction of extent of the liquid transportation line substantially as far as the line end, but there can be correspondingly shortened or lengthened in order to be able to create a possible connection.
Sufficiently good heat transfer between the medium flowing through the internal line and the medium flowing through the external line is further possible particularly when the intermediate wall bears against the internal line by way of more than half of its surface; at the same time however the intermediate wall provides additional protection to the effect that unintentional mixing of waste water and fresh water and/or waste water affecting the fresh water system or the like can be effectively prevented.
In this case, it is particularly preferably provided that at least one channel which runs in the direction of extent of the liquid transportation direction is formed between the intermediate wall and the internal line. This at least one channel is connected to the surrounding atmosphere in a pressure-related manner at at least one of the line ends of the liquid transportation line. In other words: this at least one channel forms a leakage gap and, in the event of a leakage, conducts the escaping liquid to at least one of the line ends of the liquid transportation line. In this case, said liquid can be accordingly discharged without there being any risk of it affecting the fresh water system and as a result possibly contaminating the fresh water or drinking water system.
According to an advantageous development of this aspect, the at least one channel is connected to a sensor device in order to identify liquid escaping from the internal line into the channel. In this case, the sensor device can be in the form of a pressure sensor. However, at the same time, it is also possible for the sensor device to be in the form of an optical sensor. An optical sensor of this kind is preferably arranged at at least one of the line ends of the liquid transportation line and serves to identify liquid escaping from the at least one channel.
Both the pressure sensor and an optical sensor of this kind enables simple and reliable identification of a leakage of this kind, wherein, in the event of identification in this way, a liquid blocking device which separates the fresh water-carrying line (external line or internal line) from the fresh water system as soon as a leakage of this kind is identified by means of the sensor. A blocking device of this kind can be, for example, a controllable solenoid valve or the like. As a result, it is possible to reliably suppress an undesired effect (contamination or the like) on the fresh water system, specifically at an early stage when a possible leakage is first identified.
According to a further development, a connection device, in particular a T-shaped connection piece which is composed of plastic, is provided at at least one of the line ends of the liquid transportation line. This connection device has a connection for the external line and a connection for the internal line. When a channel is provided in an intermediate wall, a connection for this at least one channel can preferably additionally be provided. Simple connection of the coaxial liquid transportation line is possible by means of a connection piece, in particular T-shaped connection piece, of this kind.
Exemplary embodiments will be explained in greater detail below with reference to the drawings, in which:
As is clear from the sectional side view in
Therefore, the structure shown in side view in
Analogously to the illustration in
As is clear from the enlarged perspective illustration in
In other words: adjacent regions 32 of the intermediate wall 30 are provided on the internal line 10, wherein channels 31 which each run in the direction of extent of the liquid transportation line 100 are provided between these adjacent regions 32. These channels 31 are connected to the surrounding atmosphere in a pressure-related manner at at least one of the line ends 101 and/or 102 of the liquid transportation line 100 in the dishwasher in line with the second embodiment.
A sensor device, for example an optical sensor (103), which serves to identify undesired leakages and the like, is provided at the respective line end 101 or 102. It goes without saying that it is equally possible to provide a plurality of intermediate walls 30. In the event of a leakage, in particular a leakage in the internal line 10 which transports the hot waste water in line with the embodiments 1 and 2, the escaping liquid is, in the case of this leakage, therefore conducted to the line end 101 or 102 where it can be collected without the possibility of contamination due to said escaping liquid affecting the fresh water system or the like. At the same time, a signal can be triggered by means of the sensor (not illustrated) by way of a corresponding control device or the like, said signal closing a solenoid valve (likewise not illustrated) or the like as soon as a leakage is identified. In this case, this solenoid valve is provided between the connection 51 for the external line 20 and the fresh water system.
Owing to the solution provided herein, it is possible to provide an effective and low-cost possible way of ensuring heat recovery in a dishwasher, in particular a commercial single-tank dishwasher or commercial multi-tank dishwasher, wherein the waste water temperature of the waste water which is to be introduced is low enough to be able to meet strict standards, such as the US “Uniform Plumbing Code” for example, at the same time. At the same time, in particular when an intermediate wall 30 is provided, pressure-related compensation of the channels 31 which are arranged therebetween is provided at the same time, as is likewise required, for example, by the “Uniform Plumbing Code”.
However, owing to the particular construction, in particular owing to the adjacent regions 32, effective heat transfer between the medium flowing in the internal line and the medium routed in countercurrent in the external line is then possible with the proposed coaxial construction. As a result, hot waste water which is at, for example, 60° C. is cooled to below 50° C. in said countercurrent heat exchanger during a normal dishwashing cycle, as a result of which an otherwise usually elevated consumption of fresh water on account of cold water being admixed with said hot waste water before it is introduced into the waste water system is dispensed with.
It should be noted here that all described features of the embodiments have value in combination or on their own. It is to be clearly understood that the above description is intended by way of illustration and example only, is not intended to be taken by way of limitation, and that other changes and modifications are possible.
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10 2014 217 503 | Sep 2014 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/US2015/047093 | 8/27/2015 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2016/036568 | 3/10/2016 | WO | A |
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Number | Date | Country | |
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20170209020 A1 | Jul 2017 | US |