1. Field of the Invention
The present invention relates to a method for estimating the moisture content of fabrics in a dyer during the drying cycle and for enabling an automatic cycle termination once a desired moisture level is reached.
As a drier it is here meant any appliance for drying clothes and fabrics and which is preferably for domestic use. The dyer can be either a condensing dyer or an air-vented dyer. Preferably it is a condensing tumble dyer for domestic use. The invention support either the heating system based on “electrical resistance” or systems known as “heat pump” system that makes use of a refrigerant cycle to heat the air.
2. Description of the Related Art
Methods for terminating the drying cycle of a dyer when the desired drying level is achieved are known in the art.
A known simple method is based on the drying time length. The level of the residual moisture is assumed to be directly correlated with the drying time. The control unit counts the drying time and stops the drying cycle after the time manually set by the user has elapsed, leaving a certain level of residual moisture in the fabrics. This method requires the user to estimate the drying time and to set manually the dryer accordingly. As a result, this method does not provide excellent performances but drives to a waste of time and energy.
Another known method uses conductibility sensors in the form of metal stripes placed either in the drum or on the drum lifters. With such sensors it is measured the instantaneous resistance of the clothes contacting the stripes, which is linked with their moisture content: the higher is the resistance the dried are the clothes. The conductibility value read through these sensors is compared to a predefined/selected threshold value stored in the memory of the control unit. In the memory are stored a certain numbers of threshold values, each of them corresponding to a certain dryness level according to the number of drying programs offered by the machine to the user.
This method requires a quite complex manufacturing operation for fixing the conductibility sensors in the drying chamber. This method is particularly efficient when implemented in tumble driers, but it is less efficient when applied in driers wherein fabrics are not agitated/moved during the drying process. The method is however unsatisfactory when drying bulky items, that is items presenting high volume/surface and low mass. In these cases in fact, conductibility sensors do no enter in contact with the interior portion of the items.
Moreover, from EP-A-2034086 filed by the same applicant, the moisture retention of fabric inside the dryer is estimated using two temperature sensors: a first sensor placed nearby the heater at the inlet of the drying chamber, and used to avoid over temperatures; and a second sensor placed the near or at the outlet of the drying chamber used to control the air temperature linked with the clothes. In
The air temperature of the drying chamber is controlled with a closed loop temperature control, as described on
However, more than one temperature sensor is required to estimate the moisture content.
Further known methods use a relative humidity sensor or a weight sensor, and stop the drying cycle when a predefined threshold limit is reached. These methods require an “ad hoc” expensive sensor, while the other described methods use the same temperature sensors used for controlling the heater temperature.
Finally, in the art are also known methods using a single temperature sensor to automatically estimate the mass amount of clothes within the dryer. With this information the duration of the drying cycle is established accordingly. To be reliable this method requires having in input also the type of fabrics to be dried. This information is normally not accurate if automatically calculated, and it is preferably required to be inputted by the user, causing to the process become a manual process.
Aim of the present invention is a method which does not present the drawbacks of the prior art.
The above disadvantages are overcome thanks to the features listed in the appended claims.
Other features and advantages of the present invention will become readily apparent to the skilled artisan from the following detailed description when read in light of the accompanying drawings, in which:
Having regard to the accompanying drawings, the method of the present invention is described with reference to a tumble drier. A tumble dryer implementing the method of the present invention typically includes the following components and functionalities:
a drum aimed at containing a certain amount of laundry articles and optionally rotationally driven with an electric motor;
a heating element to heat the air to be blown inside the drum. The heater is preferably a radiant heater even if other heating systems can be used.
a blower (not shown) forcing the air through the drying chamber.
a temperature sensor to measure the a temperature TOUT linked with the laundry articles temperature within the chamber, for instance the air temperature within or at the outlet of the chamber.
an air channel that conveys the air either outside the appliance (vented dryer) or to a condenser (condensing dryer);
a control unit for:
Since the present invention requires a sensor to measure a temperature linked with the temperature of the laundry items, it follows that several dispositions of the sensor (connected to different parts/component of the dryer), or different types of sensors can be used. For instance it could be used a temperature sensor connected to the temperature of the refrigerant fluid;
The temperature set point TSET value is used by the control unit to as reference value for regulating the air temperature TOUT within the drying chamber. For the sake of simplify the temperature set point TSET is here considered to be constant, even if the profile of the set-point temperature can be changed during the drying cycle for obtaining different drying performances.
According to the invention the method starts when the temperature TOUT linked with the laundry articles reaches a steady state condition.
A steady condition is considered to be reached, when the air temperature TOUT is close to the temperature set point TSET, as described in the flowchart of
In
P=P
EV
+P
LOS. (1)
Power losses PLOS depend on the temperature of clothes and so its magnitude can be considered constant when TOUT is in steady conditions.
During the drying cycle a power PEV is absorbed by the heater for the water evaporation and depends on dryness status of the laundry articles, which is strictly linked with the evaporation rate (dMR %) of the water in the clothes/fabrics.
The power required for the evaporation PEV is a function of the latent heat that is needed for the evaporation of water from clothes. At the beginning of the drying cycle, when the clothes are wet, the power PEV required for the evaporation reaches its maximum value of power absorption max(P) and then decreases till to disappear when the articles are dried, when only PLOS is supplied with the heater in order to compensate the power losses PLOS.
By monitoring the variation of the power required by the system during the cycle it is possible to determine an estimation of the evaporation rate dMR %.
According to the invention the normalization (scaling) of the measured power to the max value of power absorbed max(P) during the drying phase, renders the evaluation independent from the heater nominal power.
P/max(P)≈Pev/max(Pev)≈dMR %/max(dMR %) (2)
When the variation of the evaporation rate becomes lower than a predetermined level (from the customer) the cycle can be terminated.
With reference to
In the first step the Pfilt(t0) is assigned as Pmax. During the drying cycle the maximum Power is memorized in the Pmax variable.
Pmax=max(Pmax,Pfilt(t)) (3)
During the drying phase the ratio between the Pfilt and Pmax is calculated and stored in a temporary register d and multiplied for 100.
When the value of the register d (or the corresponding scaled value d %) reaches a predefined threshold dSET (for instance equals to 60%), which corresponds to certain % MR dryness level (for instance equals to 0%) the heating element is switched off and, and after a predefined cool down period aimed at cooling the clothes, the cycle is stopped. The user can withdraw the fabrics from the dryer, dried at the desired moisture level.
The relationship between d or d % and MR %, represented on
The method according to the present invention estimates the total moisture inside the mass of clothes, and not takes into account the superficial moisture like for the methods that use the conductibility sensors. In this way the algorithm assures the correct drying performance also when bulky items are loaded. In some cases the system could be used together with the stripes in order to obtain a more robust moisture control, and for further improving the performance of the drying cycle.
Moreover the method of the present invention uses the information of just one sensor (in the described example the air temperature TOUT), which can be placed at the outlet of the drum or within the same, This sensor which measures a temperature linked with the temperature of the clothes can be any type of sensor suitable to provide such information, including a CCD or an infrared sensor.
Further, since the method of the present invention uses in input only the control signal (P) for regulating the power which has to be supplied by the heater in the control loop, the drying machine implementing the method of the present invention requires only one sensor for sensing the temperature related to the clothes, and not any additional sensor, in particular temperature sensors for controlling the heater over temperature Additional sensors can be used for further improving the performances of the method, but are not necessary for the present invention.
The verification of the use of the present invention can be simply done by measuring the absorbed power during the drying phase/cycle, using a power meter. In this manner it is possible to verify that the residual moisture estimation and the related automatic cycle termination according to the present invention is achieved when a predetermined relative level (scaled to the maximum power value delivered during the drying phase) of the power absorption of the heater is reached. It follows that different loads for which the same drying level has been selected (automatically or set by the user) will cause the drying phase/cycle to terminate substantially at the same relative power level.
The method of the present invention can be applied on all kind of dryers, especially to condenser dryer presenting a closed loop air circulation path, and air-vented driers discharging the saturated air into the surrounding environment.
The method of the present invention can be applied either when using heat pumps, gas heaters, or systems comprising a refrigerated gas circuit, solar system or any other kind of heating system rather than resistive heating elements.
A drying cycle can finally be implemented using a plurality of drying phases according to the present invention, each phase characterized by a having a predetermined temperature set point TSET, and its relative maximum value of power absorption max(P).
Finally the method of the present invention is applicable both to any tumble drier or to any static drier.
Number | Date | Country | Kind |
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10187667.0 | Oct 2010 | EP | regional |