Apparatus for generating steam
09719675 · 2017-08-01
Assignee
Inventors
Cpc classification
D06F75/10
TEXTILES; PAPER
F22B37/48
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F22B1/288
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F22B1/284
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F22B1/287
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
D06F75/18
TEXTILES; PAPER
International classification
F22B1/28
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F22B37/48
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
D06F75/18
TEXTILES; PAPER
Abstract
The present application relates to apparatus for generating steam. It comprises a water inlet (19), a evaporation surface (24), and a heater (26) disposed adjacent to the evaporation surface (24) to heat the evaporation surface (24) to a predetermined temperature such that water fed onto the evaporation surface (24) via the water inlet (19) forms a film on the evaporation surface (24) and is evaporated. The apparatus is configured so that water is fed to one or more regions of the evaporation surface (24), and the temperature of the water fed onto the evaporation surface (24) is lower than the predetermined temperature, so that scale on the or each region of the evaporation surface (24) to which water is fed cools at a different rate at which water on a remainder of the evaporation surface (24) cools. This causes scale on the evaporation surface (24) to break apart and be dislodged from the evaporation surface (24).
Claims
1. An apparatus configured to generate steam comprising: at least one water inlet, an evaporation surface, a heater, disposed adjacent to the evaporation surface and configured to; heat said evaporation surface to a predetermined temperature, and a controller configured to direct a flow of water through the at least one water inlet onto multiple spaced regions of the evaporation surface, wherein a temperature of the water fed onto the evaporation surface is lower than the predetermined temperature, so that a scale formed on the evaporation surface, caused by an evaporation of the water in contact with the evaporation surface, to which water is fed cools at a different rate than a scale, formed on a remainder of the evaporation surface, cools, thereby causing the scale formed on the multiple spaced regions on the evaporation region and on said remainder of the evaporation surface to break apart and be dislodged from said evaporation surface.
2. The apparatus of claim 1, wherein the heater and the at least one water inlet are configured to: heat the evaporation surface and feed water to the evaporation surface, respectively, so that the scale is dislodged from the evaporation surface once it reaches a predetermined minimum thickness and before it reaches a predetermined maximum thickness.
3. The apparatus according to claim 1, wherein the controller is configured to: control the flow of water onto the evaporation surface based on the temperature of said evaporation surface.
4. The apparatus of claim 1, wherein the controller is configured to: control the rate of flow of water through the at least one water inlet onto the evaporation surface.
5. The apparatus of claim 3, wherein the controller is configured to: control the rate of flow of water through the at least one water inlet, wherein substantially all the water fed onto the evaporation surface is evaporated from said evaporation surface.
6. The apparatus of claim 5, wherein the controller is configured to: direct the flow of water through the at least one water inlet onto separate regions of the multiple regions of the evaporation surface alternately.
7. The apparatus of claim 1, comprising: a scale collection region remote from said evaporation surface, said scale collection region configured to: collect dislodged scale from said evaporation surface.
8. The apparatus of claim 7, further comprising: a casing configured to: define a steam chamber, wherein the evaporation surface being formed on an evaporation element that extends into the steam chamber from one side of the casing; and the scale collection region being formed within the steam chamber, adjacent to the evaporation element.
9. The apparatus of claim 8, wherein the evaporation surface comprises a dome shaped profile.
10. The apparatus of claim 7, wherein the evaporation surface comprises one or more regions with recessed features.
11. The apparatus of claim 7, further comprising: a scale collection chamber; and a channel configured to collect the scale dislodged from the evaporation surface, wherein the discharged scale passes along said channel into said scale collection chamber.
12. A steam iron comprising; an apparatus configured to generate steam, said apparatus comprising: at least one water inlet, an evaporation surface, a heater, disposed adjacent to the evaporation surface, configured to: heat said evaporation surface to a predetermined temperature wherein the water fed onto the evaporation surface is evaporated; and a controller configured to: direct a flow of water through the at least one water inlet onto multiple spaced regions of the evaporation surface, wherein a temperature of the water fed onto the evaporation surface is lower than the predetermined temperature, so that a scale formed on the evaporation surface, caused by an evaporation of the water in contact with the evaporation surface, to which water is fed cools at a different rate than a scale, formed on a remainder of the evaporation surface, cools, thereby causing the scale formed on the multiple spaced regions on the evaporation region and on said remainder of the evaporation surface to break apart and be dislodged from said evaporation surface.
13. A method for dislodging scale from an evaporation surface in an apparatus for generating steam that comprises a water inlet, an evaporation surface, a heater disposed adjacent to the evaporation surface, wherein the method including the steps of: heating said evaporation surface to a predetermined temperature, and feeding water having a temperature lower than said predetermined temperature onto separate regions of the evaporation surface, alternately so that scale on the separate regions of said evaporation surface to which water is fed cools at a different rate than a rate at which scale on a remainder of the evaporation surface cools, thereby inducing thermal stress and/or strain in scale present on said separate regions and on said remainder of said evaporation surface that causes the scale to break apart and be dislodged from said evaporation surface.
14. A method for dislodging scale from an evaporation surface in an apparatus for generating steam that comprises a water inlet, an evaporation surface, a heater disposed adjacent to the evaporation surface, wherein the method including the steps of: heating said evaporation surface to a predetermined temperature, and feeding water having a temperature lower than said predetermined temperature onto multiple spaced regions of the evaporation surface, so that scale on the multiple spaced regions of said evaporation surface to which water is fed cools at a different rate than a rate at which scale on a remainder of the evaporation surface cools, thereby inducing thermal stress and/or strain in scale present on said evaporation surface that causes the scale to be dislodged from said evaporation surface.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Embodiments of the invention will now be described, by way of example only, with reference to the accompanying drawings, in which:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF THE EMBODIMENTS
(9)
(10) The steam generating chamber 4 comprises a water drop dispensing device 8 that feeds water droplets from a water reservoir into the steam generating chamber 4 where the water is evaporated. The steam generating chamber 4 also includes a baffle device 9, which, for clarity, is shown positioned within the steam generating chamber 4 and also removed from the steam iron 1. The baffle device 9 has two opposing inclined evaporation surfaces 10, 11 joined at a ridge 12 which is positioned below the water drop dispensing device 8. The baffle device 9 acts to separate the water droplets substantially evenly so that water flows down both inclined evaporation surfaces 10, 11 of the baffle device 9 and accumulates within the steam generating chamber 4 at the bottom of the baffle device 9, against the side edge 7 of the steam generating chamber 4 where the heater 6 is positioned. Therefore, the water is evaporated into steam on the inclined evaporation surfaces 10, 11 of the baffle device 9 and from pools formed at the bottom of the inclined evaporation surfaces 10,11, against the side edge 7 of the chamber 4 and the heating element 6.
(11) However, because the water is evaporated on the inclined evaporation surfaces 10, 11 of the baffle device 9 and in pools formed in the bottom of the steam generating chamber 4, against the heating element 6, scale will form and accumulate in these regions. As scale accumulates the evaporation rate of the device will fall as scale acts to insulate the heating element 6 and reduce the heat transfer rate from the heating element 6 to the inclined evaporation surfaces 10,11 and subsequently the water. Eventually, unless cleaned and maintained, the device will stop working as the heating element 6 will overheat or will not be able to transfer enough heat energy to evaporate the water and produce steam. Furthermore, because scale will accumulate in the same location as the water is boiled and evaporated, the evaporated steam will carry particles and foam will be generated by water and steam reacting with the accumulated scale, as previously explained.
(12) The lifetime of the device described with reference to
(13)
(14) As shown in
(15) The steam outlet 21 may be connected to any device, hose, pipe, tube, or other means for applying, using or conveying steam. For example, the steam outlet 21 may convey steam from within the steam chamber 17 to a steam passage of a soleplate of a steam iron similar to that described with reference to
(16) The first part 14 of the casing comprises an evaporation element 22, which acts to heat and evaporate water being fed into the steam chamber 17, and a scale collection region 23, as will be described in more detail below with reference to
(17) As shown in
(18) The evaporation element 22, which protrudes from the first part 14 of the casing into the steam chamber 17, comprises a curved evaporation surface 24 which is directed towards the water inlet 19 such that water 25 being fed into the steam chamber 17 falls onto the evaporation surface 24. In this way, the evaporation surface 24 is arranged at a different level to the scale collection region 23. The evaporation surface 24 is heated and the water 25 forms a film on this heated evaporation surface 24 which is evaporated to produce steam. In particular, the water inlet 19 is positioned directly above the evaporation surface 24 so that water falls, under gravity and/or pressure, from the water inlet 19 onto the evaporation surface 24.
(19) The water inlet 19 may be configured to drip water 25 onto the evaporation surface 24 a regular rate. Alternatively, the water inlet 19 may be configured to feed a constant stream of water 25 onto the evaporation surface 24. Alternatively, the water inlet 19 may be configured to spray the water 25 onto the evaporation surface 24 of the evaporation element 22 so that water 25 is simultaneously provided to the evaporation surface 24 in multiple positions. Alternatively, there may be more than one inlet to introduce water 25 to multiple positions on the evaporation surface 24. Alternatively, there may be one inlet that is moveable such that it can be repositioned to introduce water 25 to different positions on the evaporation surface 24. In any case, the water 25 is provided to the steam chamber 17 in such a way that a film of water is formed on the evaporation surface 24 of the evaporation element 22 and that film of water is heated and evaporated. In this way, substantially all of the water 25 being fed into the steam chamber 17 is evaporated on the evaporation surface 24 of the evaporation element 22 and does not flow into the adjacent scale collection region 23. Therefore, substantially no water enters the scale collection region 23 and so the water cannot react with the accumulated scale to create foam and impure steam.
(20) In some of the above described examples water 25 is provided to the evaporation surface 24 in multiple positions on the evaporation surface 24. That is, multiple water droplets or a multiple streams of water contact the evaporation surface in different positions. This may be achieved by a spraying action or by having multiple water inlets. This may happen simultaneously, for example if the water inlet 19 sprays water onto the evaporation surface 24 then multiple water droplets will simultaneously be provided to the evaporation surface 24. On the other hand, water 25 may be provided to multiple positions on the evaporation surface 24 in a sequential manner. Either way, the water 25 will act to cool different areas of the evaporation surface 24, and scale on the evaporation surface 24, at different rates and by different amounts. That is, areas of the evaporation surface 24 which are directly provided with water will be cooled more rapidly than other areas of the evaporation surface 24, which will cause scale on the evaporation surface 24 to cool at different rates. This differential cooling and heating will result in stresses and strains within the scale which will cause the scale to break apart, come detached from the evaporation surface 24 and fall into the scale collection region 23.
(21) The water inlet 19 is connected to a water reservoir 39 which provides water for generating steam. The water inlet 19 may be formed within the water reservoir 39 which is positioned directly above the second part 15 of the casing. Alternatively, as shown in
(22) According to any embodiment of the invention, the apparatus is provided with a controller 50. The controller 50 may operate the pump 41 and/or the valve so as to control the rate and/or amount of water supplied through the inlet 19 to the evaporation surface in dependence upon the temperature of the evaporation surface, for the purpose of maximising the thermal shock effect. The flow may also be controlled to ensure that all the water that contacts the evaporation surface is evaporated and none of it, or substantially none of it, flows from the evaporation surface 24 into the scale collection region 23. For example, for controlling the thermal shock effect and/or to ensure that all the water is evaporated on the evaporation surface, the valve may be operated by a thermal switch sensitive to the temperature of the evaporation surface and which varies the flow rate through the valve in dependence on the temperature at said evaporation surface. The amount and/or flow rate of water that will be evaporated on the evaporation surface when the evaporation surface is at a given temperature can be predetermined and the valve and thermal switch can be designed accordingly.
(23) The size and area of the evaporation surface 24 on the evaporation element 22 is selected to provide an appropriate steam generation rate. The required steam generation rate will depend on the application of the device, the pressure limitations of the casing, the maximum water feed rate and the size of the device. However, as an indication, experiments have shown that to generate steam from a water feed rate of 30 grams/minute would require a circular evaporation surface having a diameter of 49 millimeters heated to 180 degrees Celsius, or a diameter of 70 mm at 150 degrees Celsius. The evaporation surface 24 has a sufficient size and temperature to evaporate substantially all of the water 25 that is fed onto the evaporation surface 24 so that little or no water enters the scale collection region 23 surrounding the evaporation element 22.
(24) The evaporation element 22, in particular the evaporation surface 24 onto which water 25 is fed by the water inlet 19, is heated by an electric heater. In this example, an electric heating element 26 is embedded into the evaporation element 22 such that the evaporation surface 24 is heated to evaporate water being fed into the steam chamber 17 through the water inlet 19. A temperature sensing device 27 may also be provided to measure the temperature of the evaporation element 22 and in particular the temperature of the evaporation surface 24. The temperature sensing device 27 may be positioned on an outside evaporation surface of the first part 14 of the casing and an allowance made for the decreasing temperature gradient between the evaporation surface 24 and the outside evaporation surface.
(25) Alternatively, the temperature sensing device 27 may be disposed such that it directly senses the temperature of the evaporation element just below the evaporation surface 24 or on the evaporation surface 24 itself. The temperature sensing device 27 can be connected to the controller 50 so that the controller 50 controls the amount and rate of flow of water in dependence on the temperature sensed by the temperature sensing device 27. In one embodiment, a valve controls the flow of water through the inlet 19 onto the evaporation surface 24 and may comprise a rod moveable towards and away from a conical valve seat to control the flow through an orifice in the valve seat. The temperature sensor may comprise a bimetallic strip connected or exposed to the temperature of the evaporation surface and which deforms as a function of the temperature of the evaporation surface to cause the rod to slide in a direction towards, or away from, the valve seat, thereby varying the flow of water through the orifice in dependence on the temperature of the evaporation surface. However, it will be appreciated that other methods of controlling the flow of water to the evaporation surface are possible.
(26) In this way, it is possible to prevent water from reaching the scale collection region 23 around the evaporation element 22 and/or control the thermal shock effect. Moreover, the heating element 26 is disposed proximate to the evaporation surface 24 so that the evaporation surface 24 is heated but the evaporation surface within the scale collection region 23 is not heated. In this way, no water is evaporated from the scale collection region 23 and steam will not be generated in the presence of the accumulated scale. The scale collection region 23 will become warmer than room temperature due to the generation of steam in the steam chamber 17, but the scale collection region 23 is not directly heated by the heating element 26 so that little or no evaporation will occur in the scale collection region 23.
(27) As explained above, as water 25 is fed into the steam chamber 17 via the water inlet 19 it will fall onto the evaporation surface 24 of the heated evaporation element 22 and form a film of water on the evaporation surface 24 which is evaporated into steam. The steam will exit the steam chamber 17 through the steam outlet 21 or other means provided to carry the steam away from the steam chamber 17. If impure water is used in the device of
(28) In the example shown in
(29) Although the above description describes the loose dislodged scale falling from the evaporation surface 24 into the scale collection region 23, it will be appreciated that the scale may be moved from the evaporation surface by being pushed by the water and/or steam, or it may slide over the evaporation surface 24 and into the scale collection region 23. In any case, the loose dislodged scale will fall away from the evaporation surface 24, towards the scale collection region 23.
(30) It will be appreciated the evaporation element 22 may alternatively be provided with an evaporation surface that has a pitched, conical or pyramidal or any other shape. In any case, the evaporation surface 24 should be inclined into the adjacent scale collection region 23 so that dislodged scale moves off of the evaporation surface 24 and into the scale collection region 23.
(31) It will also be appreciated that the apparatus may be configured to hold steam within the chamber at a pressure which is greater than atmospheric pressure so that steam can be released at any time. In this case, the water inlet 19 may be configured to open and allow water into the steam chamber when the pressure within the chamber falls below a certain level. Also, it should be considered that the boiling point of water increases as pressure increases so the heater and other components need to be selected and/or designed according to the required pressure and temperature. It will be appreciated that the maximum steam pressure can be regulated by controlling the temperature of the evaporation surface 24 and the water feed rate through the water inlet 19.
(32) In an alternative example, the water inlet 19 may open whenever the apparatus is in use or when a user opens the water inlet 19 to allow steam to flow out of the steam outlet. In this way, steam is made ‘on demand’ and the user does not need to wait for a required pressure to build up before using the device.
(33) The movement of loose scale from the evaporation surface 24 into the surrounding scale collection region 23 means that accumulation of scale on the evaporation surface 24 is prevented. Instead, scale is collected in the scale collection region 23 which is separate to the heated evaporation surface 24 where the steam is produced and so the water 25 is not evaporated in the presence of an accumulation of scale. Moreover, the disadvantages of the scale acting as an insulating material on the evaporation surface 24 are also avoided and the efficiency and effectiveness of the heating element 26 is not diminished over time.
(34) In the example shown in
(35) Furthermore, the high temperature of the evaporation surface 24 and the consistency of that temperature means that scale is less likely to be retained on the evaporation surface 24 itself and will become dislodged and broken into flakes and powder that will move into the scale collection region 23 surrounding the evaporation element 22. The constant high temperature of the evaporation surface 24 combined with the relatively low temperature of the water 25 being fed onto the evaporation surface 24 means that any scale on the evaporation surface 24 will be subjected to a high thermal shock which will break apart and dislodge any scale. Any scale formed on the evaporation surface 24 will have a different thermal expansion coefficient to the material of the evaporation surface 24 itself. Therefore, as water 25 is provided to the evaporation surface 24 the scale will cool at a different rate to the material of the evaporation surface 24 and then be heated up at a different rate as the heat energy is transferred to the water. This will cause a differential rate of contraction and expansion of the scale compared to the evaporation surface 24, which will induce stresses and strains in the scale, causing it to break apart into particles and detach from the evaporation surface 24, which are then moved into the scale collection region 23 as previously explained. Even if the material of the evaporation surface 24 does not undergo any significant contraction when water is fed onto the evaporation surface 24, any accumulated scale will be cooled by the water and the thermal shock of this differential cooling will break apart the scale and allow it to move into the scale collection region 23.
(36) Moreover, once cracks and gaps are formed in the scale layer on the evaporation surface 24, water 25 being fed onto the evaporation surface 24 will flow through those cracks and into the gaps and onto the evaporation surface 24. As this water contacts the evaporation surface 24 it will be evaporated and undergo an increase in volume as it turns into steam. This will push the scale away from the evaporation surface 24 and provides a further force acting to break apart the scale and push it off the evaporation surface 24 and into the scale collection region 23.
(37) As previously explained, in one example the water inlet 19 or multiple water inlets may be configured to provide water to the evaporation surface 24 in multiple locations. This may be achieved with multiple water inlets, a water inlet which sprays water onto the evaporation surface, or with a moveable water inlet. Providing water to different positions on the evaporation surface will result in differential cooling of the scale layer and evaporation surface 24, differential heating of the water, and uneven steam generation across the evaporation surface 24. This will increase the magnitude of the stresses and strains created in the scale layer, causing the scale to be broken apart such that it falls into the scale collection region 23.
(38) Whilst the generation of thermal shock within the scale is the primary way in which scale is to be removed from the evaporation surface 22, the evaporation element 22, including the evaporation surface 24, may also be configured to alter its shape under thermal heating and cooling. In particular, the evaporation element 22 may be shaped such that when it is heated the thermal expansion of the evaporation element 22 causes the shape of the evaporation surface 24 to change in a regular or irregular manner. In this case, regular shape change will occur if the evaporation surface 24 were to expand by the same amount in every direction, that is, it undergoes regular thermal expansion and/or contraction. On the other hand, irregular shape change will occur if the evaporation element 22 and evaporation surface 24 are configured to expand more in one direction than in another. For example, the walls of the evaporation element 22 and/or evaporation surface 24 may have varying thickness so that some areas will expand more than others when heated, causing the evaporation surface 24 to change shape in an irregular manner. In either case, the thermal expansion and/or contraction will also act to break apart any scale which has formed on the evaporation surface 24 which, in combination with the thermal shock effect described above, will further assist to dislodge scale from the evaporation surface 22 so that it will fall into the scale collection region 23. In addition, the evaporation surface 24 may optionally be provided with some coating or evaporation surface finish that also helps to prevent scale from becoming bonded to the evaporation surface 24 so that the scale is more easily broken apart and dislodged when subjected to thermal shock. For example, a non-stick coating such as PTFE or a ceramic coating, or alternatively a highly polished evaporation surface finish may be provided to make it more difficult for the scale to form into large particles and flakes on the evaporation surface 24. Furthermore, the non-stick coating or evaporation surface finish will allow greater relative movement between the scale and the evaporation surface 24. This will result in higher stresses in the scale which will be broken apart and dislodged from the evaporation surface 24 more quickly.
(39) The evaporation element 22 described above with reference to
(40) The arrangement of the evaporation element 22 and scale collection region 23, as described above with reference to
(41) The arrangement of the evaporation element 22 and scale collection region 23 results in better performance of the steam generating device as the scale does not accumulate and so heat transfer from the evaporation surface 24 to the water is not reduced. This will also increase the longevity of the device and the potential required time between cleaning or servicing to remove scale.
(42)
(43) Also shown in
(44) The size and volume of the scale collection region 23 surrounding the evaporation element 22 can be configured to define how often the scale must be removed from the device to maintain performance. For example, if the product should be designed with a lifetime of 6 years then, based on a 100 liters-per-year usage of water with a calcium carbonate concentration of between 120 and 180 milligrams/liter, the volume of scale generated will be approximately between 195 and 293 cubic centimeters. However, given that the flakes or powder particles of scale will not occupy all the volume in which they are disposed, a scale collection region having a volume of approximately 600 cubic centimeters may be provided so that the device can operate for up to 6 years without the scale detrimentally affecting the performance of the evaporation element.
(45) It will be appreciated that the above description is merely an example of a possible volume of the scale collection region 23 and the scale collection region 23 may HI alternatively be any size. If, for example, a longer or shorter product life is required then the volume can be adjusted accordingly. Also, the scale collection region 23 may have a volume which is smaller than the expected volume of scale over the entire lifetime of the product and the product may be provided with a predetermined service interval or indicator so that the consumer knows when to remove the accumulated scale. Alternatively, as described in more details hereinafter, a device having the apparatus described above may be provided with a way of removing scale.
(46) In another example, the evaporation surface 24 may be provided with one or more recessed regions, for example a groove or a plurality of dimples. The recessed region(s) may be provided to ensure that the film of water being formed on the evaporation surface 24 is substantially evenly distributed and does not always flow in the same direction. The recessed regions will act to disturb any prevailing flow of water and spread the water over a greater part of the evaporation surface 24, resulting in better evaporation.
(47)
(48) As shown in
(49)
(50) The recessed regions 42,43 on the evaporation surface 24, as described with reference to
(51)
(52) As shown in
(53) As previously described, when the device is in use, with the soleplate 32 placed against a substantially horizontal evaporation surface, water from the water storage area 33 flows through the water inlet 19 and into the steam chamber 17. The arrangement of the water inlet 19 and evaporation element 22 means that the water entering the steam chamber 17 is fed onto the heated evaporation surface 24 within the steam chamber 17. Therefore, when the device is placed in an operational position, water is fed onto the evaporation element 22 and steam is produced in the same way as described with reference to the apparatus of
(54) The water inlet 19 may be an opening through which water can pass when the steam iron 30 is placed in an operational position, as shown in
(55) Steam being produced in the steam chamber 17 may be able to flow directly out of openings in the soleplate 32, or it may alternatively be retained within the steam chamber 17 until the user releases the steam by pressing a button or other user interface to create an opening through which the steam can exit the steam chamber 17.
(56) The evaporation element 22 and the scale collection region 23 are configured in the same manner as the apparatus described with reference to
(57) As shown in
(58) As shown in
(59) As shown in
(60) Any scale generated during use of the device 30 described with reference to
(61) The apparatus for generating steam in the device described with reference to
(62) It will be appreciated that the apparatus for generating steam described with reference to
(63) Whilst it is advantageous for the scale dislodged from the evaporation surface to fall into a scale collection region which is remote from the evaporation surface so that water does not collect in, and is not evaporated from, the scale collection region, the thermal shock technique for the dislodgement of scale from an evaporation surface is applicable to apparatus in which the scale is dislodged from the evaporation surface but remains on the evaporation surface until it is removed manually. Alternatively, the apparatus may have a region where scale collects, although water may still be evaporated from said region.
(64) It will be appreciated that the term “comprising” does not exclude other elements or steps and that the indefinite article “a” or “an” does not exclude a plurality. A single processor may fulfil the functions of several items recited in the claims. The mere fact that certain measures are recited in mutually different dependent claims does not indicate that a combination of these measures cannot be used to an advantage. Any reference signs in the claims should not be construed as limiting the scope of the claims.
(65) Although claims have been formulated in this application to particular combinations of features, it should be understood that the scope of the disclosure of the present invention also includes any novel features or any novel combinations of features disclosed herein either explicitly or implicitly or any generalization thereof, whether or not it relates to the same invention as presently claimed in any claim and whether or not it mitigates any or all of the same technical problems as does the parent invention. The applicants hereby give notice that new claims may be formulated to such features and/or combinations of features during the prosecution of the present application or of any further application derived therefrom.