Patent Application
20090255146
The invention relates to a method of supplying steam into a fabrics storage compartment of a laundry treatment device, and a treatment apparatus having a control unit controlling the steam supply to the fabrics storage compartment.
In a conventional condenser dryer as proposed in DE 102 60 151 A1 a steam evaporating device is arranged in an air channel for supplying the circulated air into a drum. In the evaporating device the heat of a heater normally used for heating the circulated air heats and evaporates water which is supplied into a cup located in the air channel. During steam supply into the rotating drum, a fan in the circulation channel is operated such that the steam is blown from the channel into the drum. The efficiency of the steam supply is lowered in that the air is circulated through the drum such that a portion of the steam introduced into the drum is again flown out of the drum into the exit channel where it then may condensate at a condenser and other elements in the air passages. Further, the steam generated in the air channel can condense and inhomogeneously cool down at or close to the channel walls and the backside of the drum wall prior or during inlet into the drum.
It is an object of the invention to provide a steam supplying method for supplying steam to a fabric storage compartment and to provide a treatment apparatus in which at the one side the precision of the steam treatment is improved and on the other hand the risk of damage or negative effects on fabrics from steam treatment are reduced.
The invention is defined in claims 1, 3, 16 and 18, respectively. Particular embodiments are set out in the dependent claims.
It has been observed that when introducing the steam into the storage compartment of a treatment apparatus like a dryer at least a portion of the steam may condensate and form droplets, wherein the droplets formed in cold areas of the delivery path to the fabrics result in low temperature droplets or the condensation in areas of hot temperature steam supply may result in high temperature droplets. In both cases the contact of the fabrics to be treated with the steam droplets may result in adverse effect to the fabrics or to the efficiency of the fabrics treatment. Due to inhomogeneities in temperature and/or dampness at the locations where the droplets hit the fabrics or textiles as compared to areas where the textile is in contact with the hot steam only, significant differences in the steam treatment effect may arise. For example wrinkles may form due to different elasticity of the fabrics being non-uniformly dampened, partially overheating of the fabrics with the hot droplets, decoloration effects, different efficiencies of additives added to the steam treatment and the like may result. To avoid the formation of droplets, the inventors propose two solutions which are fully compatible with each other and which are preferably combined with each other. According to the first approach (claims 1 and 16) and before starting the steam supply into the storage compartment, optimum starting conditions are provided such that when starting the steam supply, the likelihood of droplet formation is significantly reduced. According to the other approach or solution (claims 3 and 18) the processing conditions in the storage compartment are directly or indirectly monitored and the steam supply parameters are adapted in dependency of the monitored internal conditions for droplet prevention.
According to claim 1, a steam supplying method is provided in which the steam is supplied into a fabrics storage compartment of a treatment apparatus. The treatment apparatus is for example a dryer or a washing machine providing refreshment functionality or any other treatment apparatus having a storage compartment through which air, preferably drying air, is ventilated. The steam supplying method can for example be implemented as a subroutine of a refreshment cycle, an anti-crease cycle during a drying procedure, or an anti-crease phase after the drying of the laundry stored in the storage compartment. Preferably the steam is supplied directly into the storage compartment. This means that the steam injection is made at a location having a direct and contact-free path from the point of injection to the storage compartment's inner volume. Alternatively but not preferably the steam may be supplied indirectly into the storage compartment, for example by injecting the steam into an air guiding channel connected to the storage compartment.
For preparing the start of the steam supply into the storage compartment, the air or drying air is blown through the storage compartment until a predefined temperature and/or humidity has been achieved. If for example dry laundry is loaded into the storage compartment, it is not required to dry the laundry by the air (in particular drying air) and instead the temperature of the laundry, the air passed through the storage compartment or circulated through the storage compartment, and elements in contact with the circulated or injected air are heated up to a predefined temperature. As the condensation effect is mainly induced by the contact or mixture of the steam with the air flowing through the storage compartment, of course the air temperature is the most relevant parameter in this case. Preferably, the predefined temperature is somewhat above typical ambient temperatures, for example about 35, 40 or 50° C. If the laundry or fabrics loaded into storage compartment is already wet or damp, for example after a previous washing process, the humidity of the air within the storage compartment and/or the humidity of the laundry is set to a predefined humidity level, for example a residual or relative humidity of 3%, 5% or 10%. Preferably, the predefined temperature and the predefined humidity are both set by the pre-drying process, as the steam condensation behavior depends on the air temperature as well as on the (already existing) air humidity.
The air ventilated through the storing compartment may be heated or cooled or neither nor (air with ambient or internal temperature is ventilated). Air heating is effected by activation of a heating device. Cooling is effected by activating a cooling device like a condenser (e.g. used in a condenser air dryer) and/or cold ambient air from outside the treatment apparatus is sucked into the treatment apparatus—at least partially forming the ventilated air.
According to claim 2 and after the starting phase of supplying steam into the storage compartment, the steam supply is continued wherein the steam flow and/or the temperature of the steam is set in dependency of at least one process parameter. This means that in this embodiment the steam supply is not continued with the predefined flow and/or temperature, but the flow and/or temperature is adjusted according to the current operation process parameters which may vary after having started the steam supply process. For example, the air humidity changes in the storage compartment after the steam supply has been started and at the same time the rate of change of the air humidity depends on the amount of laundry or fabrics loaded in the storage compartment and/or the type of fabrics stored therein. If, for example, the current process parameters change, the steam flow and/or the temperature are correspondingly adapted in reaction thereto such that the effect of avoiding the droplet formation during the steam supply is maintained even over a longer period of steam supply. A steam supply period lasts for example longer than one minute, two minutes, or lies in a range of three to seven minutes.
The subject matter of claim 3 also provides the effects and advantages of claim 2, while according to claim 3 it is not necessary that the steam supply sequence is started at a predefined temperature and/or humidity in the storing compartment. For example, the steam supply may be started with a very low steam supply rate which inherently avoids the risk of forming droplets, and then the steam supply flow rate can be increased in reaction to the detected process parameters allowing a higher steam flow rate. In an alternative embodiment for the starting phase, the steam supply sequence is started at a low level or from a zero steam flow rate and is successively increased to a predefined steam flow rate. Thereafter the steam flow rate is preferably adjusted according to claim 3.
The process parameters relevant for setting the steam flow and/or the temperature of the steam are one or more the following:
According to a preferred embodiment, the approach to the predefined temperature or generally the current air temperature is detected in the storage compartment as the most relevant measurement location having an effect onto the steam condensation. Preferably the air temperature is detected at a surface or a wall of the air guiding and enclosing walls of the apparatus or fabrics storage compartment. For example the air temperature is detected at the storing compartment's surface or wall (e.g. drum wall). In alternative embodiments or in addition thereto the temperature can be measured in an air flow path or in an air circulation path or also preferably at a location close to the injection point for the steam supply.
Alternatively or additionally the air humidity is preferably detected at the same locations as the air temperature detection locations. Preferably the humidity is detected together with the temperature (at the same location), such that there is a direct correlation between the temperature and humidity at one location. Preferably, the humidity of the air is derived from the humidity detection of the laundry which is often implemented by an electrical conductivity measurement at the inner walls of the drum.
The values of the temperature and/or humidity for observing the approach to the predetermined temperature and/or predetermined humidity for adjusting the steam supply in dependency of these process parameters, are preferably detected or monitored periodically, permanently, intermittently or the like, such that the progress or changes in the process parameter conditions (e.g. temperature/humidity) can be steadily used to correct and optimize the steam flow and/or temperature. This is correspondingly valid for the other process parameters, if changing over time, and is considered for determining the steam flow and/or temperature.
Preferably in the method of claim 1 and the apparatus of claim 16 at least the predetermined steam flow rate (preferably also or alternatively the predetermined temperature) is calculated on the basis of the predefined air temperature and the predefined air humidity using the below formula for calculating the dew point. Preferably additional parameters are considered (which can partially be determined by experiments) in calculating or determining the predetermined flow rate (and the predetermined temperature), like the laundry weight, the drum volume, the temperature drop during transport of the steam from the steam supplying device to the injection point, the drum rotation speed and the like.
Correspondingly for the method of claim 3 and the apparatus of claim 18 the steam flow (and preferably also the steam temperature) are calculated on the basis of the detected air temperature and detected air humidity (the most relevant process parameters) the same way as for claims 1 and 16.
For example the following formula is convenient to calculate the dew point in degrees Celsius to within ±0.4° C. It is valid for 0° C.<T<60° C.; 0.01<RH<1.0; and 0° C.<Td<50° C.
where
and a=17.27, b=237.7° C., and in is the natural logarithm.
It is to be noted that the setting of the steam flow and/or the temperature of the steam supplied to the compartment in dependency of the drying process parameter(s) can be used for example for maximizing the steam flow up to a limit below the condensation or droplet forming such that due to the high steam flow rate the time required to supply a predefined steam amount into the compartment is reduced. Alternatively or additionally the temperature of the steam is minimized, for example, to reduce energy consumption during steam generation and/or to treat delicate textiles with steam at as low temperature as possible.
According to a preferred embodiment the steam flow rate and/or the temperature of the steam is adapted or set by setting a supplying flow rate of liquid to a first heating device of the steam generator. Or the heating activity of the steam generator is adapted in dependency of the predefined temperature and/or humidity or the monitored temperature and/or humidity during the steam supply sequence. For example, the liquid flow rate to the steam generator is increased to increase the steam flow rate while at the same time the heating power is increased to maintain the steam supply at a constant steam temperature.
In an embodiment the temperature of the steam can be monitored and the steam temperature signal can be used in a closed-loop configuration to adjust the heating and evaporation of the liquid for steam generation in dependency of the current steam temperature signal. Steam temperature is for example detected within the steam generator (steam supplying unit), at a pipe guiding the steam from the steam generator to the injection location, in or at a nozzle injecting the steam, or a combination of temperatures measured at these temperature detection locations.
In a preferred embodiment the air flow through the storage compartment is reduced or stopped such that the steam is not exhausted out of the storing compartment during air circulation or ventilation. This also avoids steam condensation outside the storage compartment.
In a further embodiment, the duration of steam supply and/or the total amount of steam supplied to the drum is set in dependency or is dependent of the process parameters, preferably the air temperature and/or the air humidity. The duration and/or steam amount may be set at the beginning of the steam supply phase, or preferably it is adjusted under continued monitoring of the process parameters which gives an indication when the steam treatment has reached a predetermined end level. For example the air temperature is allowed only to increase to a predetermined level during steam supply to avoid damages to the fabrics (e.g. the predetermined temperature level itself depends on the fabrics type). And/or a maximum air or laundry humidity represents an end point for steam supply.
The treatment apparatus according to claims 19 or 21 are provided with a control unit which is adapted to control or operate the treatment apparatus such that the effects described above in relation to the method claims are fully applicable also for the operation of the treatment apparatus using the respective functional components of the treatment apparatus.
Reference is made in detail to an exemplary embodiment of the invention, an example of which is illustrated in the accompanying drawings, which show:
When operating in condenser mode, the air from the outlet channel 16 is passed through a condenser 20 from where the circulated air is further guided through a heater 21 and then it is passed to the inlet channel 14. In the present exemplary embodiment the tumble dryer 2 can be switched from a condensation mode, where the air is circulated in channels 14, 16 and drum 6, and an exhaust mode, where fresh air is sucked in through an intake channel 24 and the humidity laden air is exhausted through exhaust channel 22. Switching between condensation mode and exhaust mode is made by switching valve 26 under the control of the control unit 50. Any intermediate position between the two modes of circulation and condensation can also be switched to by correspondingly adjusting the position or alignment of a valve element 28 within the valve body 26. I.e. in the three positions I, II, III shown in
The humidity of the laundry in the drum is detected by a humidity sensor 30 which is formed as a conductivity sensor. The conductivity sensor detects the electrical conductivity of the laundry between two metallic contacts at the drums inside which are spaced from each other. In alternate embodiments or in addition to the conductivity sensor the air humidity of the air flown through the drum 6 can be detected at another position in the air passage, for example at a location close to or at the fluff filter 18. Further, a second temperature sensor 44 is arranged at the loading opening of the drum to detect the temperature of the air within the drum. As shown, the temperature measure point is close to a nozzle 36 of an additive injector 32.
The additive injector 32 generates water steam which is supplied via supply line 34 to the nozzle 36 such that a steam jet 38 is injected into the drums inside. Under the control of the control unit 50, a pump 40 assigned to the additive injector 32 pumps water from a water reservoir (not shown) into the additive injector 32 in which a heating element 42 is arranged to evaporate the water. The power dissipated by heating element 42 is also controlled by control unit 50 such that steam flow rate and/or steam temperature are controlled by correspondingly setting the temperature within the additive injector 32 by heating the heating element 42 and by pumping a controllable flow of water into the additive injector 32 where the water is brought into contact with the heating element 42. The temperature within the additive injector 32 is detected close to the heating element 42 by a first temperature sensor 41.
In an embodiment not shown, the steam temperature is detected with an additional temperature sensor within the steam supply pipe 34 or temperature signal of the sensor 44 is taken as the steam temperature during steam supply phases (while it is e.g. taken as an air temperature signal in non-steam supply phases). The steam temperature signal thus detected is also supplied to the control unit 50 and processed there to adjust the steam temperature either by taking this signal exclusively to control operation the heating element 42 and thereby the steam temperature, or it is taken as a correction signal together with the temperature signal from the first temperature sensor 41 (
As indicated by the arrows, the CPU 50 controls the operation of motor 4, heater 21, valve 26 and additive injector 32. Selected programs and program options can be indicated at the display section 54 under the control of the CPU 50. Also operating states of the dryer are indicated in the display section, for example the remaining time until finishing the program or the like. Via a subunit 56 the CPU 50 received measurement signals from the first temperature sensor 41, the second temperature sensor 44 and the humidity sensor 30. Of course,
For controlling and optimizing the steam supply into the drum during a steam supply phase and in preparation for a steam supply phase, the subunit 56 receives and processes the signals of the first and second temperature sensors and the humidity sensor 30. In a look-up memory 56a connected to the subunit 56 optimization patterns are deposited such that, by using the corresponding signals from sensors 30, 41 and 44, an optimum steam flow rate and temperature for supplying the steam into the drum 6 from the additive injector 32 is calculated. In the shown embodiment the ‘calculation’ means retrieval from look-up memory 56a storing a look-up table. Here the temperature and steam flow rate are adjusted by providing from the subunit 56 to the CPU 50 control signals which are forwarded to the pump 40 and the heating element 42. Thereby, the steam flow rate essentially depends on the heating power developed by heating element 42 and the pumping rate of pumping water by pump 40 to the heating element 42. Correspondingly, the steam temperature is a function of the heating power and the fluid flow rate generated by pump 40.
According to an exemplary embodiment of the invention, the threshold value T1 as well as the lower and the upper limits Tmin, Tmax itself are not fixed, but one, two or all three dependent on the processing conditions for processing the laundry. Together with adapting these (one, two or three) temperatures in dependency of the process parameters, the liquid flow rate generated by pump 40 is adapted such that the formation of droplets in the drum or at the nozzle 36 are avoided when the steam jet 38 is injected into the drum 6. This means that in the present exemplary embodiment dew point conditions are stored in look-up memory 56a, wherein on the basis of the detected air temperature (second temperature sensor 44) and the humidity (humidity sensor 30) an optimized pumping flow rate (pump 40) and heating power or temperature (e.g. temperature limits Tmin, Tmax) of the additive injector 32 (first temperature sensor 41) is adjusted and controlled such that finally an optimized steam temperature and steam flow rate of the steam exiting the nozzle 36 is effected avoiding the formation of droplets.
In another aspect of the invention, the starting conditions for supplying the steam from the additive injector 32 into the drum are selected such that droplet suppression is also achieved from the beginning. According to a first approach this can be made in that, prior to the start of the steam supply, a predefined condition in the drum is effected, for example by heating the air in the drum 6 to a predefined temperature and at the same time by pre-drying the laundry (if damp) to a predefined starting humidity (which can be detected either via the laundry's humidity or the air humidity). As soon as these predefined conditions have been achieved, the steam supply is started. According to a second approach (or additionally), the threshold temperature T1 for starting fluid supply to the heating element 42 is selected in dependency of the current conditions in the drum (air temperature and/or humidity) and also the upper and lower two-point control values Tmax and Tmin are selected in dependency of the initial conditions (temperature and/or humidity) in the drum 6. This means that by either way the risk of droplet forming in the starting phase of steam supply is significantly reduced.
It should be noted that according to an exemplary operation of the dryer 2 the flow of air through the drum 6 is stopped in that the fan 12 is decoupled from the reverse motor rotation via freewheel 10. In this case, the steam 38 injected by nozzle 36 is not blown out of the drum 6 and maximum steam efficiency is achieved at the laundry rotated in the drum via reverse drum rotation.
Of course, the operation conditions for the additive injector 32 are also optimized to avoid condensation within supply pipe 34 or at the nozzle 36 or inside the drum 6 at cold inner walls. The latter is avoided by the above mentioned pre-heating of the air via heater 21 and thereby pre-heating the laundry and also the drum material. Even if the air circulation is maintained during the steam supply phase, the steam parameters (temperature/flow rate) can be selected such that an adverse condensation rate at the condenser or heater 21 is avoided. The adaptation of the steam generation parameter in dependency of the processing conditions also takes into consideration deviations from identical processing runs, if for example an exhaust air mode is selected and ambient air with high humidity and high temperature is sucked and blown through drum 6.
| Number | Date | Country | Kind |
|---|---|---|---|
| 06011420.4 | Jun 2006 | EP | regional |
| 06015884.7 | Jul 2006 | EP | regional |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP07/04852 | 6/1/2007 | WO | 00 | 11/26/2008 |
