[0001] This invention relates to tumble dryers and has particular but not exclusive reference
to tumble dryers for domestic use.
[0002] There are many known systems for controlling automatically the drying cycle of a
tumble dryer. In some systems, the "dryness" of articles undergoing tumble drying
is sensed by measuring the electrical resistance of the articles in the drum of the
dryer. However, it is difficult to measure the resistance sufficiently accurately
as it increases towards the value indicating that the articles are dry. It is also
found that there are other factors than the dampness of the articles that affect their
electrical resistance particularly around the "dry" condition of the articles and
the variation produced by these factors is sufficient to make effective sensing impossible.
The systems, therefore, are designed to sense a particular "damp-dry" condition of
the articles after which the drying time is extended by an amount determined by the
user and which is assumed to bring the articles to a "dry" condition. As the added
time depends upon many factors, it is very likely to be incorrect.
[0003] Other systems make use of the observation that the temperature of air leaving the
drum - exhaust air - rises as articles in the drum dry out. Knowledge of factors including
air flow through the drum and heat input enable the system to assume that when a particular
exhaust air temperature is reached, the articles in the drum have reached the "dry"
condition. Variable factors, for example, ambient air temperature affect the exhaust
air temperature but the effect of these variables can be allowed for by the system.
One system of this general type is described in DE-A-2941166. In this system, use
is made of the fact that, as a drying cycle progresses, exhaust air temperature shows
an initial rapid increase followed by a steady condition and then rises again: by
monitoring the exhaust temperature at regular intervals, the systems detects when
a predetermined temperature increase above the "steady condition" has been achieved
and terminates the drying cycle. Systems of this general type are effective when required
to sense the "dry" condition but considerably less effective when required to detect
the "damp-dry" condition suitable for ironing because the difference between the exhaust
air temperature when the articles contain about 25% by weight of moisture and that
when the articles contain say 10% by weight of moisture, is small, although the different
moisture contents are important. In addition, other variable factors not catered for
by the system can affect the exhaust air temperature by that difference or more.
[0004] A combination of the two systems just described has also been proposed but even this
does not produce fully acceptable results.
[0005] Other systems dependent upon monitoring exhaust air temperature have also been proposed
but all suffer from the disadvantage that they are not able to sense sufficiently
accurately the "damp-dry" condition mentioned above.
[0006] It is an object of the present invention to provide a control system for a tumble
dryer that is able to sense to an acceptable degree of accuracy the "damp dry" condition
of articles during a tumble drying operation and able to sense to the same degree
of accuracy the "dry" condition.
[0007] According to the present invention, a tumble dryer includes a control means for controlling
the drying cycle, which comprises a temperature sensor responsive to the temperature
of air exhausted from the drum of the dryer and means for monitoring, at specified
times during the drying cycle, changes in said temperature and translating said changes
into an output to control the duration of the drying cycle, characterized in that
the monitoring means is operable to monitor exhaust air temperature changes during
at least an initial part of the drying cycle and, from said changes, to predetermine
the duration of the drying cycle and to terminate operation of the dryer when the
predetermined time has elapsed.
[0008] The control means may further include means for assessing the rate of flow of air
through the drum and for modifying the effect of the monitored exhaust air temperatures
to take account of the assessed air flow rate.
[0009] The means for assessing the rate of air flow may include an arrangement for measuring
the increase in temperature of air emerging from the air heater of the dryer. Conveniently,
such an arrangement includes a temperature sensor responsive to the temperature of
air entering the
' air heater and another temperature sensor responsive to the temperature of air leaving
the air heater.
[0010] Heat is also imparted to air before it enters the air heater, for example, the air
may pass over hot components. In many cases, air is drawn over the motor driving the
drum before entering the air heater. Means may be provided for taking into account
such extra heat when the control system translates exhaust air temperatures.
[0011] Furthermore, changes in ambient air temperature may increase or decrease the temperature
of air leaving the heater and the drum, and a sensor may be provided for detecting
such ambient air changes. The output of the sensor is fed into the control means where
the effect of the changes on other variables is accommodated.
[0012] Variations in other factors affecting the exhaust air temperature may be taken into
account to modify or adjust the effect of exhaust air temperature readings. For example,
the control means may include means responsive to the existence of changes in exhaust
air temperature which, in the said initial part of the drying cycle, depart from a
pre-set pattern, said responsive means being operable to adjust the predetermined
duration of the drying cycle.
[0013] In addition, the control means may provide a visual indication of the time that must
elapse before the articles reach the predetermined condition of dryness. To this end,
the control means may include an indicator connected to receive an output of the monitoring
means for indicating the said predetermined duration of the drying cycle, the arrangement
including means for setting the indicator.
[0014] In one embodiment, a visual indication is given of the longest time that must elapse
to reach a predetermined degree of dryness, the time being maintained but the heat
input being corrected either by decreasing the time for which heat is supplied or
by decreasing the rating of the heater in terms of kilowatts of heat input, as determined
by the subsequent monitored conditions, should correction be necessary. For example,
the control means may be adapted to set the indicator to show a predetermined cycle
time duration based on a first monitored exhaust air temperature during the initial
part of the drying cycle and to predetermine in accordance with a subsequently monitored
exhaust air temperature at which point in that cycle time duration air heating shall
be terminated. Alternatively, the control means may be adapted to set the indicator
to show a predetermined cycle time duration based on monitored exhaust air temperatures
during the initial part of the drying cycle and to determine, in accordance with monitored
rate of increase of exhaust air temperature, at which point in that cycle time duration
air heating shall be terminated.
[0015] In another embodiment, the control means is adapted to set the indicator to show
a cycle time duration translated from a first monitored exhaust air temperature and
to reset the indicator in accordance with a subsequently assessed exhaust air temperature
during the said initial part of the drying cycle.
[0016] By way of example only, embodiments of the invention will now be described with reference
to the accompanying drawings of which:
Fig. 1 is a block schematic of a control system embodying the invention,
Figs. 2-6 are explanatory graphs, and
Figs. 7A, B, C and 8 are explanatory flow diagrams.
[0017] The tumble dryer to which the control system is fitted may be of any conventional
form. A typical example of dryer to which the system may be fitted is found in GB-A-1,226,951.
[0018] Fig. 1 shows in block schematic form the features of a control system embodying the
invention.
[0019] A microprocessor has a plurality of inputs applied to it via an input interface 2,
the outputs of the microprocessor being applied via an output interface 3.
[0020] Fig. 1 shows a variety of inputs of which some are user-controlled and others are
not. A user- operated control (not shown) inputs to the input interface 2 over leads
4, 5, 6 to indicate the material of which articles to be tumbled are made, for example
Fig. 1 shows a control operable to select cotton or nylon or acrylic materials, the
control could equally well be adapted to select cotton, acrylic or mixed materials.
[0021] Temperature sensors (not shown) are positioned so as to be exposed to air leaving
the drum of the dryer (exhaust air), to ambient air, to air inside the machine before
such air passes over the air heater of the dryer, and to air that has been heated
by the air heater but has not yet entered the drum. The exhaust air sensor inputs
over lead 7, the ambient air sensor inputs over lead 8, the sensor exposed to unheated
air inside the machine inputs over lead 9 whilst the remaining sensor inputs over
lead 9a. Such sensors may be thermistors or thermocouples providing a voltage input
to the interface 2 indicating the sensed value of exhaust air temperature and ambient
air temperature.
[0022] Input 10 is connected to a voltage sensitive device that detects variations in the
voltage of the mains supply to the tumbler dryer.
[0023] A further input 11 indicates the electrical load of the air heater of the tumble
dryer and is normally set during factory testing of the machine. The heater rating
may also be variable by the user on operation of the control indicating the type of
material of which articles to be tumbled are made.
[0024] Input 12 is connected to a control set by the user at the commencement of a drying
cycle and determines the stage to which the cycle is to be taken to ensure articles
reach a required state of dryness. The control may be a multi-position knob settable
to different positions indicating, for example "Dry", "Iron Dry", "Damp 1", "Damp
2 ...", "Extra Dry". "Iron Dry" indicates a condition suitable for ironing, whilst
"Damp 1", "Damp 2 ..." are differing degrees of dampness of the articles. "Extra Dry"
provides a drying cycle of somewhat greater duration than "Dry" and is suitable for
articles with seams or otherwise of uneven thickness and require an extra long cycle
to ensure that such thick parts reach the dry condition.
[0025] Controlled by the microprocessor output via output interface 3 are a digital display
13, a motor (not shown) driving the drum of the dryer and an impeller (not shown)
pumping air through the drum, and an air heater (not shown) of the dryer that heats
air prior to its entry into the drum.
[0026] As is described in the Specification referred to above, air passing over the air
heater of the dryer has been drawn into the casing of the appliance and over the motor
driving the drum.
[0027] The following factors determine the drying cycle required by a particular load of
articles to be tumble dried:
1. The type of material from which the articles are made.
2. The total amount of water in the load.
3. The weight of the load.
4. The rate of flow of air through the drum of the dryer.
5. The total heat input.
6. The basic efficiency of the dryer.
7. The ambient temperature.
8. The humidity of the ambient air.
9. The temperature of the articles when they are loaded into the drum.
[0028] Of these factors, the first is programmed into the microprocessor by the user and
results in an input on one of input leads 4, 5 or 6.
[0029] Factor 2 is the most important single one of the factors which determine the time
that a wet load takes to dry in a particular design of dryer where efficiency and
the heat input remain constant. The weight of clothes involved - factor 3 - is relatively
unimportant in determining the time for a particular total weight of water to be evaporated,
but it does affect the shape of the temperature/time curve. These factors are determined
by the microprocessor in accordance with information received and following procedures
to be described below.
[0030] The rate of flow of air through the drum - factor 4 - has little effect on total
drying time but is important because it influences the shape of the exhaust air temperature/time
relationship which is referred to below. Air flow is difficult to sense directly but
a sufficiently accurate assessment is obtainable indirectly from observations of the
increase in temperature of air flowing over the air heater. Such increase is determined
by sensing the temperature of air entering, and that of air leaving, the air heater.
[0031] The value of factor 5 is determined by ambient air temperature, the extent to which
air picks up heat before entering the air heater, for example from the motor and the
heat imparted to the air by the air heater.
[0032] There are basically two different sets of conditions to be considered in connection
with heat pick-up. The dryer may be totally at ambient air temperature, or it, or
parts of it, may be at a temperature other than that of ambient air. In the latter
two cases, the exhaust air temperature will be initially modified by this factor and
allowance will have to be made for this, and the consequences of the differing initial
temperature conditions of the dryer are discussed later.
[0033] The heater input depends upon the electrical resistance of the heater and the supply
voltage. Resistance could be measured during a final factory test and the control
system calibrated to respond to the time/temperature curve given by a specific heater
resistance by means of an adjustable potentiometer and subsequently regarded as pre-set.
In Fig. 1, the setting of the potentiometer forms input 11.
[0034] Alternatively, the resistance of the heater could be sensed at the commencement of
a drying cycle and the value indicated over input 11.
[0035] Changes in supply voltage are sensed and indicated over input 10.
[0036] The basic efficiency of the dryer - factor 6 - can be determined during the course
of development and can, thereafter, be regarded as constant.
[0037] In practice, the humidity of ambient air can be ignored as it has very little significant
effect on the drying cycle within the range associated with normal dryer use.
[0038] The temperature of the articles loaded into the drum of the dryer will be determined
to a very large extent by the temperature of water used for a final rinse during a
washing process to which the articles are subjected before they are to be tumble dried
in the case in which the user takes the articles directly from the washing machine
and loads them into the tumble dryer.
[0039] If there is a delay between extracting the articles from the washing machine and
loading them into the tumble dryer, the temperature of the articles may vary from
that of ambient air to the rinse water temperature.
[0040] The way in which such conditions are dealt with is described below.
[0041] In order to explain the evaluation of factor 2, it is now proposed to detail the
basic drying cycle of the tumble dryer.
[0042] Fig. 2 shows the way in which exhaust air temperature increases with time in the
case in which the dryer is empty. Air incoming to the drum from the air heater merely
heats up the drum and adjacent components of the dryer and consequently the exhaust
air temperature shows an initial rapid increase followed by a steady condition.
[0043] Fig. 3 shows the relationship with time of changes in the exhaust air temperature
for several different loads of articles made of cotton.
[0044] Of the curves shown in Fig. 3, that numbered 14 shows the relationship for a 4 kg
(dry weight) load of cotton articles with, initially, a 100% (by weight) water content.
Curves 15, 16 and 17 show respectively the relationship for a 4 kg (dry weight) load
of cotton articles with, initially, a 50% (by weight) water content, a 2 kg (dry weight)
load of cotton articles with, initially, a 100% (by weight) water content, and, a
2 kg (by weight) load of cotton articles with, initially, a 50% (by weight) water
content.
[0045] The relationships are of the same general pattern. There is an initial fairly rapid
increase in the temperature of the exhaust air - time period A - after which that
temperature stabilises at an intermediate plateau temperature during which evaporation
from articles in the drum takes place at a steady state. When the bulk of the water
in the articles has been driven off, the exhaust air temperature starts to rise again
and, when the articles are completely dry, stablises once again.
[0046] From Fig. 3, it can be seen that, for the same dry weight of articles, the rate of
increase in exhaust air temperature during time period A varies primarily with the
amount of water in the load. Thus, in general, a large rate of increase in exhaust
air temperature is an indication of a small weight of water requiring a shorter time
to dry the load, the converse also being true.
[0047] However, it will be seen that although curve 16 rises initially at a larger rate
of increase than curve 15, both having the same 2 kg content of water to be evaporated,
in fact a slightly longer, nor shorter, drying time is required for the smaller dry
weight of articles. This is because the smaller weight of articles makes less efficient
use of the hot air passing through the drum of the dryer, and consequently the drop
in temperature from the temperature at which the air enters the drum is less and the
plateau temperature is slightly higher.
[0048] Thus, other factors, for example voltage, heater loading, air flow, type of material
and ambient temperature, being equal, a) the larger the rate of increase in exhaust
air temperature during the initial period the shorter the drying time, and b) the
higher the plateau temperature for a particular rate of increase in exhaust air temperature
the longer the drying time. If the temperature is ultimately going to be slightly
higher during the plateau period other factors, such as those mentioned above and
also the amount of water in the articles, being constant, the initial rate of increase
will be greater. This initial larger rate of increase would cause the microprocessor
to miscalculate the time required to evaporate the water contained in the articles,
as the microcompressor would assume less water in the load than was actually the case
unless some compensations were made. This compensation can be made by the microprocessor
when it sees what the plateau temperature is. The microprocessor will endeavour to
anticipate the plateau temperature from the initial shape of the temperature/time
curve, an early large rate of increase in exhaust air temperature followed by a more
rapid decline in the rate of increase will indicate a lower plateau temperature than
the same early rate of increase followed by a less rapid decline in the rate of increase.
The more time and temperature reference positions that are taken and the longer they
continue to be taken, the more accurate the assessment will be. For any particular
initial rate of increase in exhaust air temperature, time will have to subsequently
be detracted by the control from the time first calculated to switch off the heater,
should the plasteau temperature be less than the assumed temperature programmed into
the microprocessor for any given heat input, air throughput, ambient temperature and
so on.
[0049] This is illustrated in Fig. 3, the "dry" condition for each load being indicated
by the points X on the curves. Point X on curve 16 occurs later in the drying cycle
than does point X on curve 15.
[0050] Generally similar curves apply to other different materials: Fig. 4 shows the exhaust
air temperature/time relationship for 2 kg (dry) weight with 100% (by weight) initial
water content of articles made of nylon - curve 21, and of acrylic fibers - curve
22. In each case, the points X on the curves indicate the dry condition and it will
be noted that the time to reach that condition is different for the different materials.
[0051] Thus, it will be appreciated that, in general, the less weight of water initially
present in the articles, the greater is the initial rate of increase in exhaust air
temperature and the smaller the weight of articles the higher is the exhaust air temperature
that is reached after the initial heat up over time period A, additionally.
[0052] The relationship between exhaust air temperature and time over the initial part of
a drying cycle will depend upon the dryer temperature at the commencement of the cycle,
all other variables being the same.
[0053] Fig. 5 illustrates the dependence. If the dryer is "hot" at the commencement of a
drying cycle, the exhaust air temperature will start from a higher value but will
in due course, rise to the said final temperature as if the starting temperature was
that of ambient air.
[0054] In Fig. 5, curve 23 relates exhaust air temperature and time for the case in which
the starting exhaust air temperature is 30°C. Curve 23 can be compared with curve
24 which relates exhaust air temperature and time for the case in which the starting
exhaust air temperature is 10°C. The curve 23 condition must be recognised by the
microprocessor so that the latter can apply a correction to the sensing base from
which the microprocessor calculates the heating time and the overall cycle duration
of the dryer which may take the form of a decreasing deduction from the sensed value
of the exhaust air temperature as indicated by curve 25, the deduction being the curve
23 value minus the curve 24 value.
[0055] A somewhat similar situation arises in the case of articles to be dried and which
are loaded into the dryer when their temperature is below that of ambient air and
of the dryer. In this case, the first effect on exhaust air temperature is to depress
it below ambient. After a while, the exhaust air temperature will increase and will
eventually reach the same final temperature referred to above. This is illustrated
in Fig. 6 whose curve 26 relates exhaust air temperature and time for the case in
which articles at a temperature of 5°C are loaded into the dryer. For comparison purposes,
curve 27 relates exhaust air temperature and time for the case in which the articles
are at a temperature of 10°C when loaded into the drum.
[0056] The correct time to reach dryness must be based on the curve from the point at which
the exhaust temperature has risen to the ambient value, thereafter the curve will
be identical with that of articles loaded whilst at ambient temperature. Thus, the
microprocessor must respond to the drop in sensed exhaust air temperature and make
the appropriate correction.
[0057] The microprocessor is programmed to scan or otherwise monitor the rate of increase
in exhaust air temperature at specified intervals of time during the initial heat
up period - time period A.
[0058] The microprocessor is also programmed with a series of cycle durations corresponding
with a variety of different exhaust air temperatures and times of occurrence of such
temperatures. These cycle durations will be not only those required to bring the articles
to a "dry" condition but will also include cycle durations to reach various conditions
of damp dry.
[0059] The exhaust air temperature is checked at specified intervals of 0.5 sec for the
first 5 sec after the start of a drying cycle. Thus, at the end of the first 5 sec
of the drying cycle, the microprocessor will deduce from the averaged or aggregated
exhaust temperature readings that the cycle duration is, say 2 hours. That duration
is displayed in a mode characterizing an unconfirmed time because the time is likely
to be an approximation only, because at the commencement of a cycle, the exhaust air
temperature/time curves, as can be seen from Fig. 3, are very close together. However,
as more readings become available greater certainty is possible and after about 60
seconds a reasonably accurate cycle duration is available. The displayed time includes
"cold" run of 10 min.
[0060] Typically, checking continues every 0.5 sector a further period of 10 sec (15 sec
runs time). At the end of that further period, the microprocessor determines and stores
the average value of the temperatures at each 0.5 sec interval, or aggregates those
temperatures. The microprocessor will then up-date the first assessed cycle duration
time and display, in the unconfirmed mode, the up-dated time including the 10 min
"cold" run.
[0061] Monitoring of exhaust air temperature is then continued for a further 45 sec (60
sec run time) during which time the temperature is checked every 0.5 sec to give,
at the end of the 60 sec run time, an averaged value or an aggregated value which
is related to the averaged or aggregated value obtained at the end of the 15 sec period
to enable the microprocessor to make a final estimate of the cycle duration time (T)
which will include a 10 minute period of "cold" run after the air heater has been
de-energised.
[0062] In practice, the initial duration deduced would be programmed to be the longest that
would be required, to be corrected at a later stage. The correction made might be
of the order of a 5 minute reduction in the time during which the heater is energized,
but no reduction will be made in the total time to run of the dryer.
[0063] Monitoring of exhaust air temperature may cease after a predetermined time programmed
into the microprocessor or it may continue as will be described below.
[0064] The deduced cycle time is also displayed on the display 13 - preferably a digital
display showing minutes only or hours and minutes.
[0065] Thus, in the example just described, the display would be energised after 5 sec to
show 2:00 hours. To indicate to a user that the displayed time may be an unconfirmed
time only, an additional symbol is energized, for example the colon separating the
hours and minutes in the display is caused to flash - this is referred to as the "unconformed
mode".
[0066] As monitoring of the exhaust temperature continues, the deduced duration may change
and this can be indicated to the user as such changes take place, i.e. by a constantly
changing display or by one single change at the end of the 60 sec period. The colons
would cease flashing at the end of that period - the display then being in the confirmed
mode.
[0067] Once the cycle duration has stabilised, its value is stored to allow the microprocessor
to produce, at the approximate time, outputs to terminate the drying cycle. Two outputs
are normally required because the air heater is de-energised before the drying cycle
ends, the remainder of the cycle being simply the conventional "cool-down" period
during which cool air is circulated through the drum to cool articles therein.
[0068] It is, of course, possible to so program the microprocessor that monitoring of exhaust
air temperature continues after the 60 sec period referred to above. This continued
monitoring enables a more accurate deduction to be made of the cycle duration. Thus,
at the end of, say, 5 min from start a very accurate duration time is available. The
displayed time is not changed and the more accurate duration is used to cause de-
energisation of the heater earlier or later within the cycle time, the "cool-down"
period being lengthened or shortened as a result and the total duration of the cycle
remains unchanged.
[0069] Operation of the "materials" control inputting over leads 4, 5 and 6 sets the microprocessor
to approximate cycle duration times appropriate to the selected material. If "acrylic"
is selected, the microprocessor may also be programmed to reduce the heater to a half-heat
condition at an appropriate point in the cycle. This will reduce the possibility of
overheating articles made from that material.
[0070] Changes in ambient temperature and any other changes, for example supply voltage,
may be caused to adjust the effect of exhaust air temperature readings either before
such readings are inputted to the microprocessor or within the latter. Inputs 9, 9a,
10 and 11 may operate in a similar fashion.
[0071] Adjustment of input 12 makes an appropriate adjustment to the time within a cycle
that the air heater is energised, the microprocessor having been programmed to terminate
energisation in accordance with the adjustment of the input 12 and the state of dryness
indicated thereby.
[0072] To use a tumble dryer incorporating the features described above, a user first loads
the machine with articles to be tumble dried and then sets the control in accordance
with the nature of the material from which the articles are made. Control 12 is then
set in accordance with the state of dryness required. Once the door giving access
to the drum is closed, the machine may be energised and may commence the tumble dry
cycle.
[0073] By observation of the display 13, the user will, after 60 sec running time or when
the colons are "steady", be able to read the exact time that must elapse before the
cycle finishes.
[0074] It will, of course, be understood that the machine may incorporate some only of the
features mentioned above. For example, only exhaust air temperature may be monitored,
fixed values being assumed for ambient air temperature, inlet air temperature supply
voltage and element loading. In addition, it may be possible to distinguish between
acrylic and other materials only.
[0075] As an alternative to relating the increase in exhaust air temperature to ambient
or to a given datum, it could be related to the temperature of air entering the drum
after passing over the heater.
[0076] Figs. 7A, B, C and 8 are flow diagrams showing in more detail the procedure described
above. The convention adopted employs blocks with round ends to designate inputs to
and outputs from the microprocessor, rectangular blocks to designate non-decision
operations which are carried out and diamond-shaped blocks to represent interrogations.
[0077] Step 1 in the diagram of Fig. 7 is normally affected during factory testing of the
dryer but steps 2 and 3 are carried out by the user as explained above.
[0078] Rectangular blocks carrying the text "adjust sensing base" indicate that a sensed
variation from standard of the parameter is used to adjust the value to be used in
step 11.
[0079] Fig. 8 is an alternative to the automatic de- energisation of the air heater attime
T-10 min, it is possible to employ a microprocessor programmed to terminate air heating
when the rise in exhaust air temperature exceeds a predetermined value and to monitor
exhaust air temperature throughout the drying cycle or at least for that part thereof
during which the air heater is energised.
[0080] For example, monitoring of exhaust air temperature is continued after the 5 min period
mentioned above, checks on the temperature occurring ever 5 sec. By averaging exhaust
air temperatures over a selected period, a temperature trend can be established and
when this indicates an increase of a preselected value, the air heater is de-energised.
Tumbling then continues under "cool" incoming air conditions until time T is reached
when the drum motor is switched off.
[0081] Such a technique is the subject of the flow diagram of Fig. 8.
[0082] It will, of course, be understood that the tumble dryer may be embodied as a combined
washing machine and tumble dryer.
1. A tumble dryer including a control means for controlling the drying cycle of the
dryer, the control means comprising a temperature sensor responsive to the temperature
of air exhausted from the drum of the dryer and means (1, 7) for monitoring, at specified
times during the drying cycle, changes in said temperature and translating said changes
into an output to control the duration of the drying cycle, characterised in that
the monitoring means (1, 7) is operable to monitor exhaust air temperature changes
during at least an initial part (A, Fig. 3) of the drying cycle and, from said changes,
to predetermine the duration (T1) of the drying cycle (step 23, Fig. 7C) and to terminate operation of the dryer when
the predetermined time has elapsed (step 27, Fig. 7C).
2. A tumble dryer as claimed in claim 1 in which the control means also includes means
(9, 9a for assessing the rate of flow of air through the drum and for modifying the
effect of monitored exhaust air. temperature to take account of the assessed air flow
rate.
3. A tumble dryer as claimed in claim 2 in which the means for assessing the rate
of air flow includes an arrangement (9,9a) for measuring the increase in temperature
of air emerging from the air heater.
4. A tumble dryer as claimed in claim 1, or 3 in which the control means further includes
a temperature sensor (8) exposed to ambient air temperature and means for modifying
the effect of monitored exhaust air temperature to take account of changes in ambient
air temperature.
5. A tumble dryer as claimed in any one of claims 1-4, in which the control means
includes means responsive to the existence of changes in exhaust air temperature which,
in the said initial part of the drying cycle, depart from a pre-set pattern (curve
23, Fig. 5 and curve 26, Fig. 6); said responsive means being operable to adjust the
predetermined duration of the drying cycle.
6. A tumble dryer as claimed in any one of claims 1-5 in which the control means includes
an indicator (13) connected to receive an output of the monitoring means (1) for indicating
the said predetermined duration of the drying cycle, and including means for setting
the indicator.
7. A tumble dryer as claimed in claim 6 in which the control means is adapted to set
the indicator to show a cycle time duration translated from a first monitored exhaust
air temperature (step 20, Fig. 7B) and to reset the indicator in accordance with a
subsequently assessed exhaust air temperature during the said initial part of the
drying cycle (steps 22, 24 Fig. 7C).
8. A tumble dryer as claimed in claim 6 or claim 7, in which the control means is
adapted to set the indicator to show a predetermined cycle time duration based on
a first monitored exhaust air temperature during the initial part of the drying cycle
(step 2, Fig. 7B) and to predetermine in accordance with subsequently monitored predetermined
exhaust air temperature at what point in that cycle time duration air heating shall
be terminated (step 25, Fig. 7C).
9. A tumble dryer as claimed in claim 6 or claim 7, in which the control means is
adapted to set the indicator to show a predetermined cycle duration based on monitored
exhaust air temperatures during the initial part of the drying cycle (step 20, Fig.
7B) and to determine, in accordance with monitored rate of increase of exhaust air
temperature at what point in that cycle time duration air heating shall be terminated
(step 26, Fig. 8)..
1. Ein Trommeltrockner mit einer Steuereinrichtung für die Steuerung des Trocknungszyklus
des Trockners, welche Steuereinrichtung einen Temperatursensor umfaßt, ansprechend
auf die Temperatur von Abluft aus der Trommel des Trockners und einer Einrichtung
(1, 7) für die Überwachung zu spezifizierten Zeiten während des Trocknungszyklus von
Änderungen in der genannten Temperatur und die Umsetzung der genannten Änderungen
in einen Ausgang zum Steuern der Dauer des Trocknungszyklus, dadurch gekennzeichnet,
daß die Überwachungseinrichtung (1, 7) betätigbar ist zum Überwachen von Ablufttemperaturanderungen
während zumindest des anfänglichen Teils (A, Fig. 3) des Trocknungszyklus und, aus
den genannten Änderungen, die Dauer (T1) des Trocknungszyklus (Schritt 23, Fig. 7C) zu bestimmen und den Betrieb des Trockners
zu beenden, wenn die vorbestimmte Zeit verstrichen ist (Schritt 27, Fig. 7C).
2. Ein Trommeltrockner nach Anspruch 1, bei dem die Steuereinrichtung ferner eine
Einrichtung (9, 9a) umfaßt für die Abschätzung der Luftdurchströmungsrate durch die
Trommel und für die Modifizierung des Effekts der überwachten Ablufttemperatur zur
Berücksichtigung der abgeschätzten Luftströmungsrate.
3. Ein Trommeltrockner nach Anspruch 2, bei dem die Einrichtung für die Abschätzung
der Luftströmungsrate eine Anordnung (9, 9a) umfaßt für die Messung der Temperaturzunahme
von aus dem Lufterhitzer austretender Luft.
4. Ein Trommeltrockner nach Anspruch 1, 2 oder 3, bei dem die Steuereinrichtung ferner
einen Temperatursensor (8) umfaßt, der der Umgebungslufttemperatur ausgesetzt ist,
und eine Einrichtung für die Modifikation des Effektes der überwachten Ablufttemperatur
zur Berücksichtigung von Änderungen der Umgebungslufttemperatur.
5. Ein Trommeltrockner nach einem der Ansprüche 1 bis 4, bei dem die Steuereinrichtung
eine Einrichtung umfaßt, ansprechend auf das Vorliegen von Änderungen in der Ablufttemperatur
die, in den genannten Anfangsteil des Trocknungszyklus, von einem voreingestellten
Muster (Kurve 23, Fig. 5 und Kurve 26, Fig. 6) abweicht, welche Einrichtung betätigbar
ist zum Einstellen der vorbestimmten Dauer des Trocknungszyklus.
6. Ein Trommeltrockner nach einem der Ansprüche 1 bis 5, bei dem die Steuereinrichtung
einen Indikator (13) umfaßt, angeschlossen zum Empfang eines Ausgangs der Überwachungseinrichtung
(1) für die Anzeige der genannten vorbestimmten Dauer des Trocknungszyklus, einschließlich
einer Einrichtung für das Setzen des Indikators.
7. Ein Trommeltrockner nach Anspruch 6, bei dem die Steuereinrichtung ausgebildet
ist zum Setzen des Indikators zum Anzeigen einer Zykluszeitdauer, umgesetzt von einer
ersten überwachten Ablufttemperatur (Schritt 20, Fig. 7B) und zum Rücksetzen des Indikators
in Übereinstimmung mit einer nachfolgend zugeordneten Ablufttemperatur während des
genannten Anfangsteils des Trocknungszyklus (Schritte 22, 24, Fig. 7C).
8. Ein Trommeltrockner nach Anspruch 6 oder 7, bei dem die Steuereinrichtung ausgebildet
ist zum Setzen des Indikators zum Anzeigen einer vorbestimmten Zykluszeitdauer, basierend
auf einer ersten überwachten Ablufttemperatur während des Anfangsteils des Trocknungszyklus
(Schritt 20, Fig. 7B) und zum Vorbestimmen, in Übereinstimmung mit einer nachfolgend
überwachten vorbestimmten Ablufttemperatur, an welchem Punkt in dieser Zykluszeitdauer
die Lufthitzung beendet werden soll (Schritt 25, Fig. 7C).
9. Ein Trommeltrockner nach Anspruch 6 oder 7, bei dem die Steuereinrichtung ausgebildet
ist zum Setzen des Indikators zum Anzeigen einer vorbestimmten Zykluszeitdauer, basierend
aus überwachten Ablufttemperaturen während des Anfangsteils des Trocknungszyklus (Schritt
20, Fig. 7B) und zum Bestimmen, in Übereinstimmung mit der überwachten Rate der Zunahme
der Ablufttemperatur, an welchem Punkt in dieser Zykluszeitdauer die Lufterhitzung
beendet werden soll (Schritt 26, Fig. 8).
1. Sécheur à agitation comportant un dispositif de commande servant à commander le
cycle de séchage du sécheur, le dispositif de commande comprenant un capteur de température
réagissant à la température de l'air déchargé du tambour du sécheur et un moyen (1,
7) pour contrôler, à des instants spécifiés pendant le cycle de séchage, des variations
de ladite température et pour convertir lesdites variations en un signal de sortie
servant à commander la durée du cycle de séchage, caractérisé en ce que le moyen de
contrôle (1, 7) peut agir pour contrôler des variations de la température de l'air
sortant pendant au moins une partie initiale (A, figure 3) du cycle de séchage et
pour prédéterminer, à partir desdites variations, la durée (T1) du cycle de séchage (étape 23, figure 7c), et pour faire cesser le fonctionnement
du sécheur quand le temps prédéterminé s'est écoulé (étape 27, figure 7C).
2. Un sécheur à agitation tel que revendiqué dans la revendication 1, dans lequel
le dispositif de commande comprend également un moyen (9, 9a) pour déterminer le débit
d'écoulement de l'air au travers du tambour et pour modifier l'effet de la température
d'air sortant contrôlée afin de tenir compte du débit d'écoulement d'air ainsi déterminé.
3. Un sécheur à agitation tel que revendique dans la revendication 2, dans lequel
le moyen de détermination du débit d'écoulement d'air comprend un agencement (9, 9a)
pour mesurer l'augmentation de la température de l'air sortant du réchauffeur d'air.
4. Un sécheur à agitation tel que revendiqué dans la revendication 1, 2 ou 3, dans
lequel le dispositif de commande comprend en outre un capteur de température (8) exposé
à la température de l'air ambiant et un moyen pour modifier l'effet de la température
d'air sortant contrôlée pour tenir compte de variations de la température d'air ambiant.
5. Un sécheur à agitation tel que revendiqué dans une quelconque des revendications
1 à 4, dans lequel le dispositif de commande un moyen réagissant à l'existence de
variations dans la température d'air sortant qui, dans ladite partie initiale du cycle
de séchage, s'écarte d'une relation prédéterminée (courbe 23, figure 5 et courbe 26,
figure 6); ledit moyen de réaction pouvant opérer pour régler la durée prédéterminée
du cycle de séchage.
6. Un sécheur à agitation tel que revendiqué dans une quelconque des revendications
1 à 5, dans lequel le dispositif de commande comporte un indicateur (13) connecté
de manière à recevoir un signal de sortie du moyen de contrôle (1) pour indiquer ladite
durée prédéterminée du cycle de séchage, et comportant un moyen de réglage de l'indicateur.
7. Un sécheur à agitation tel que revendiqué dans la revendication 6, dans lequel
le dispositif de commande est adapté pour régler l'indicateur de façon à indiquer
une durée temporelle de cycle établie à partir d'une première température d'air sortant
contrôlée (étape 20, figure 7B) et à ramener l'indicateur dans la condition initiale
en concordance avec une température d'air sortant déterminée ultérieurement pendant
ladite partie initiale du cycle de séchage (étapes 22, 24, figure 7C).
8. Un sécheur à agitation tel que revendiqué dans la revendication 6 ou la revendication
7, dans lequel le dispositif de commande est adapté pour régler l'indicateur de manière
à indiquer une durée temporelle de cycle prédéterminée, basée sur une première température
d'air sortant contrôlée pendant la partie initiale du cycle de séchage (étape 20,
figure 7b) et pour prédéterminer, en concordance avec une température d'air sortant
prédéterminée et contrôlée ultérieurement, à quel moment de cette durée temporelle
de cycle le chauffage de l'air doit être terminé (étape 25, figure 7C).
9. Un sécheur à agitation tel que revendiqué dans la revendication 6 ou la revendication
7, dans lequel le dispositif de commande est adapté pour régler l'indicateur de façon
à indiquer une durée temporelle de cycle prédéterminée basée sur des températures
d'air sortant contrôlées pendant la partie initiale du cycle de séchage (étape 20,
figure 7B) et pour déterminer, en concordance avec l'allure d'augmentation contrôlée
de la température d'air sortant, à quel moment de cette durée temporelle de cycle
le chauffage de l'air doit être terminé (étape 26, figure 8).