[0001] This invention relates to controlling compressor driven vapour compression heat movement
systems as used for example in refrigeration and air conditioning for cooling and
in heat pump arrangements for heating. Reference will be made primarily to refrigeration
systems for explaining the invention in detail.
[0002] Figure 1, which will be described in more detail below, shows a typical refrigeration
system in which there are three refrigerated food cabinets. Two graphs in Figure 2
illustrate two alternative known modes of controlling such a system. As will also
be explained in more detail below, the mode illustrated in the left-hand graph permits
the compressor inlet pressure to fall to extremely low values on occasions, and on
these occasions the system is operating very inefficiently (consuming excessive power)
and removing moisture excessively from food stored in the cabinets. The mode shown
in the right-hand graph avoids these problems but on occasions may result in the compressor
being switched on and off unacceptably often. It is of course desirable that the system
should run as efficiently as possible so as to minimise its power consumption, due
to limitations in the physical design of compressors, they are given by the manufacturers
a rating as to the maximum frequency with which they can be turned on without unacceptably
shortening their requirements for servicing and repair. Typical ratings would lie
between about six and ten starts per hour.
[0003] The invention aims to provide an improved method of controlling a compressor driven
heat movement system which enables the system to be run particularly efficiently,
while rarely if ever exceeding the starts per hour rating of the compressor.
[0004] More particularly, the invention provides a method of controlling a compressor driven
vapour compression heat movement system in which a common compressor system heats
or cools a plurality of load units (e.g. refrigerated cabinets, air-conditioning units
or heat pump output units) and is operated in cycles each of which include a compressor
system higher capacity period and a compressor system lower capacity period, characterised
in that the lower capacity period is made sufficiently long that when the compressor
system is switched to the higher capacity a majority of the load units are demanding
heating or cooling and that the higher capacity period is made sufficiently long that
when the compressor system is switched to lower capacity one or more of the load units
have had their heating or cooling demand satisfied.
[0005] The compressor system involved can be a single compressor as in the embodiment which
will be described in detail below. In that event its higher capacity mode will be
when the compressor is running and its lower capacity mode will be when it is not
running during which period of course its capacity is actually zero. However, the
invention can also be applied where the compressor system includes a plurality of
compressors. Then, in the higher capacity mode some of the compressors are running
and in the lower capacity mode a lesser fixed number, which may be zero, are running.
For example, it may be desirable to have one compressor, which may be relatively small,
which always runs so as to prevent liquid refrigerant accumulating in the inlet route
to a main compressor, which is switched on and off.
[0006] The low capacity period may be controlled so as to be sufficiently long that when
the compressor system is switched to higher capacity a majority of the load units
are demanding heating or cooling or, where the operating conditions are sufficiently
predictable, the low capacity period may be fixed at a sufficiently long value to
ensure that the same condition is met. In the case where the low capacity period is
controlled, the control may be exercised in response to various different sensed characteristics
and these will be referred to in more detail below.
[0007] In one embodiment, the length of the lower capacity period is controlled in dependence
upon the length of the preceding higher capacity period.
[0008] So far as concerns making the higher capacity period sufficiently long that when
the compressor is switched to low capacity at least some of the load units have had
their demand satisfied, preferably this will comprise sensing a variable which represents
the load on the compressor system and terminating the higher capacity period when
the sensed variable indicates that the load on the compressor system is falling.
[0009] Generally, in operating a control method in accordance with the invention for a cooling
system, because a majority of the load units are demanding cooling when the compressor
is brought on, there will be a substantial period of time during which the majority
of the load units will continue to require cooling and therefore there will be a substantial
flow of refrigerant through the system and the inlet pressure of the compressor system,
and hence the temperature in the evaporators of the load units, will remain at a reasonably
constant level so long as this situation prevails. This may conveniently be referred
to as a plateau in the load on the compressor system and also in the inlet pressure
against time curve. Furthermore, the method of the invention involves turning the
compressor system off when one or more of the load units have had their cooling demand
satisified i.e. not very long after the pressure has started to fall from the plateau
following one or more of the load units ceasing to take refrigerant flow because it
is no longer demanding cooling.
[0010] Consequently, when a method in accordance with the invention is used, most of the
heat transfer from the load units occurs in the vicinity of the plateau level of inlet
pressure and evaporator temperature and it will become apparent that this means the
system is operating primarily above the band P
off-P
on of the prior art system of the left hand side of Figure 2, and hence is operating
more efficiently in terms of energy consumed per unit of refrigeration or cooling
achieved.
[0011] Various variables may be sensed to indicate the load on the compressor system and
these will be described in more detail below. The higher capacity period may be terminated
when the sensed variable reaches a set point value.
[0012] It has previously been mentioned that when operating a control method in accordance
with the invention the compressor inlet (or in the case of a heat pump system, the
outlet) pressure variation wil exhibit a plateau during the higher capacity period.
Preferably, the invention further comprises sensing the occurrence of a substantially
constant level (or "plateau") of load on the compressor system during its higher capacity
period and automatically adjusting the set point value to a value which would represent
a load level below said substantially constant level.
[0013] For example, in a cooling system the set point value may be automatically adjusted
during each cycle to lie at 80% of the plateau level measured in terms of absolute
value of the compressor inlet pressure, though values between 60% and 90% may be employed
depending on the circumstances. A "substantially constant level" may be defined for
the above purpose as the pressure varying by less than 10% over a significant period
(e.g. between 30 and 60 seconds) of time. Also, if a variable other than pressure
is sensed, its set point value may need to be set at a different percentage of the
plateau value in order to achieved the desired percentage for the pressure level itself.
[0014] This preferred feature prevents the occurrence of problems which may otherwise arise
as a consequence of the fact that the level of the plateau will not necessarily be
the same during each higher capacity period, but may vary from cycle to cycle or drift
over a substantial period of time due to various types of change in operating conditions.
For example, in a single compressor system where the load units are refrigerated cabinets,
the plateau will occur at a lower value when a number of cabinets are taken out of
service, as sometimes happens in practice. If the set point were fixed, this could
result in the compressor being switched off before the plateau level is reached in
which case adequate cooling of the remaining cabinets would not be achieved. Inaccurate
manual setting of the set point pressure could have the same effect. Drift may also
occur in the characteristics of pressure transducers and this could result in undesirable
shift of the effective set point in a system where the set point is ostensibly fixed.
Also, the different operating conditions encountered in winter as compared with summer,
the natural plateau level being higher in summer than it would be in winter, means
that for uniform operation throughout the seasons a lower set point level should be
used in winter than in summer. The preferred feature of automatic adjustment of set
point level in response to plateau level mitigates the problems just referred to.
[0015] In order than the invention may be more clearly understood, embodiments thereof
will now be described with reference to the accompanying diagrammatic drawings in
which:
Figure 1 is a simplified illustration of a typical compressor driven refrigeration
system;
Figure 2 shows in a simplified form the relationship between compressor inlet pressure
and time for two different known methods of controlling such a system;
Figures 3 shows in detail a control cycle in accordance with the invention plus other
information useful in understanding the invention;
Figure 4 shows diagrammatically several cycles of a method of control in accordance
with the invention;
Figures 5 shows the components for carrying out the method of Figures 3 and 4;
Figure 6 is a flow chart showing the steps of a control method according to Figures
3 and 4; and
Figure 7 shows the form of a compressor outlet pressure cycle in a heat pump heating
system.
[0016] The refrigeration system of Figure 1 is typical of systems that might be found in,
for example, supermarkets, where a numbr of refrigeration cabinets need to be kept
cold and have their temperatures controlled. There may be any number of cabinets,
six or more being typical, but for simplicity the Figure 1 system is shown with three.
A compressor 2 feeds compressed gaseous refrigerant to condenser 4 where it is condensed
to liquid which flows to a receiver or reservoir 6. From the receiver it flows on
three parallel paths through three evaporators (one per cabinet) indicated at 8 and
from the evaporators back to the compressor 2 in gaseous form, the liquid refrigerant
having evaporated within the evaporators to produce the cooling effect. In standard
manner, expansion valves 10 precede the evaporators 8 and are automatically controlled
in known manner so as to maintain correct conditions within the evaporators. Each
cabinet is provided with a temperature sensor 12 which exercises thermostatic control
over an on/off value 14 for that particular cabinet. Thus, each evaporator only takes
liquid refrigerant from the receiver when the temperature of its associated cabinet
has risen to such a level that it requires further cooling.
[0017] The left-hand graph in Figure 2 illustrates the use of a control method in which
the compressor inlet pressure (which is related to the evaporator temperature when
refrigerant is boiling in the evaporator) is measured and compared with a set point
value P
off which is set so low that the pressure will fall below it only when all three evaporators
have been turned off by their own thermostatic temperature conrol systems. Consequently,
so long as any one of the evaporators is working, the compressor will be running,
but with its inlet pressure varying according to how many evaporators are on. The
compressor inlet pressure would be approximately at either level 3, 2 or 1 illu strated
in Figure 2 according to whether three, two or one evaporators are operating, and
would fall to the level 0 only when all the evaporators were turned off, so that it
is only in this condition that the compressor itself would be turned off. Pressure
then rises until P
on is reached, when the compressor is re-started. With such a system, at times when
the demand for refrigeration is low, then the compressor inlet pressure is permitted
to become very low, and the evaporator temperatures will be correspondingly low, and
in these conditions the efficiency of the system is very poor in terms of heat removal
per unit of energy input. A further and substantial disadvantage of this method of
control is that the very low evaporator temperature causes excessive icing with the
attendant inconvenience and cost of having to defrost the cabinets more often whilst,
undesirably, the product in them warms up. Another is that certain food products will
have moisture removed from them excessively.
[0018] These problems are avoided by using a control system which as illustrated in the
right-hand graph of Figure 2 has two set point values P
on and P
off which are set relatively close together and are both quite high. This necessarily
prevents the compressor inlet pressure from ever falling to low values but at the
same time, when the demand for refrigeration is low, so that the compressor inlet
pressure falls very rapidly when the compressor is on, the operating cycles of the
compressor become very short and the start per hour rating of the compressor will
be exceeded so that the compressor will be subject to excessive wear and its servicing
and repair costs, and the frequent inconvenience of servicing, will be unacceptable.
[0019] Reference will now be made to the full line curve in Figure 3 to explain the type
of cycle that is repeatedly produced by using a control method in accordance with
the invention to control a cooling or refrigeration system such as that shown in Figure
1. At the beginning 16 of the compressor on period of the cycle, the compressor will
have been off for some while, any liquid refrigerant in the evaporators of the cabinets
will have evaporated to gas and the gas will have warmed up to a greater or lesser
degree. In this condition, the compressor inlet pressure bears no particular relationship
to the gas temperature. Also at the beginning of the on period, and for reasons described
below a majority of the cabinets (preferably at least 75%, for example 5 out of 6)
will have their thermostatically controlled valves 14 open i.e. they are demanding
cooling. When the compressor is switched on, the pressure initially falls very rapidly
as the gas is pumped out of the evaporators. This is indicated by the steeply falling
part 18 of the curve in Figure 6. At the point indicated at 20, the expansion valves
of the cabinets open and liquid refrigerant starts to flow into the evaporators and
to evaporate in them. When the expansion valves have been open for a little while,
the rate of evaporation of refrigerant liquid in the evaporators reaches a relatively
high level such that the pressure stops falling or falls only gradually, in part 22
of the curve. Because the demand for cooling is high, there will be a total flow of
refrigerant through the individual cabinet cooling systems which approaches the maximum
amount of flow possible, and consequently the plateau 22 in the compressor inlet pressure
will occur at a relatively high level e.g., with refrigerant R502, and with chill
(produce temperature +4°C) cabinets as a load, at about 2.8 bar gauge pressure. A
major part of the refrigeration of the cabinets will occur during this phase of the
cycle, and therefore at relatively high efficiency. In contrast, a pump-down control
system as illustrated on the left in Figure 2 would typically operate at an average
pressure of about 1.8 bar gauge under the same conditions. When using the invention,
the plateau would occur at the three-cabinet running level of Figure 2, i.e. at a
higher pressure (above say 2.1 bar) than is ever reached by the pump-down system when
the latter is running between its P
on and P
off values. As individual cabinets reach the temperatures set on their thermostats, their
thermostatic valves 14 start to close off, thus limiting the total refrigerant flow
in the system, and the pressure starts to fall again as indicated at part 24 of the
curve. When the pressure reaches P
set, the compressor is turned off at point 26. P
set is set (by empirically establishing the typical level of the plateau in a given system,
and putting P
set to a value slightly lower than that) at such a level that the pressure will not have
to drop very far from the plateau before the compressor system is switched off at
point 26. Hence only a minority, for example one or two out of six, of the cabinets
will have had their cooling demand satisfied at switch-off.
[0020] Figure 3 shows a downward continuation of part 24 of the pressure curve to illustrate
in more detail how a system operating in accordance with the left-hand side of Figure
2 performs. Typically, P
off is set at a relatively low value and the pressure continues to fall to that value
along the broken-line part 28 of the curve. P
off is set so low that it will not be reached until the thermostatic valves of all the
cabinets have closed i.e. the demand for cooling has become zero. The compressor system
is then switched off and the pressure rises along part 30 of the curve until a pre-set
value P
on is reached at which time the pressure starts to fall again as the compressor system
comes into operation, this being along the broken line 32. The result is that the
system cycles in the band between P
off and P
on which lies in a relatively low pressure range and so the system is operating at a
correspondingly low average efficiency.
[0021] The invention achieves greater efficiency because of the high level of plateau 22.
[0022] With the compressor off, the compressor inlet pressure initially rises very rapidly
because the expansion valves are open, some of the thermostatic valves are open, and
so liquid is entering the evaporators and boiling in them. This is shown at part 34
of the curve and during this phase open thermostatic valves may or may not close.
When the pressure reaches a certain value, to which the expansion valve controls have
been set, the expansion valves close and the remaining refigerant in the evaporators
boils off during part 36 of the curve. When all the liquid has boiled off, the pressure
at the compressor inlet rises only slowly and at a decreasing rate as the gas at that
point becomes gradually warmer, this happening along part 38 of the curve.
[0023] The off period is controlled as will be described so as to be sufficiently long that
at the end of it a majority of the cabinets will once again be demanding cooling.
[0024] Before referring to Figure 4 it should be mentioned that, for control purposes, the
pressure at the inlet of the compressor only has significance when it is fairly close
to the pressure at which refrigerant is boiling in one or more of the evaporators
of the system. For this reason, any pressure measurements made at the peak of part
18 of the Figure 3 curve would not be significant. They only become significant at
a point shortly after (perhaps five seconds after) the compressor has been switched
on, as indicated at 40 in Figure 3, at which time it will be certain that liquid has
entered one or more of the evaporators, and that therefore the compressor inlet is
approximately at the pressure under which that liquid is boiling therein.
[0025] Figure 4 shows the variation of the on and off periods of a compressor controlled
by the method of the invention over several cycles. For simplicity only, the pressure
rises and falls are shown as straight lines (though in reality they would be Figure
3-type curves), and the pressures at which the compressor is shown being switched
on and off in Figure 4 actually represent the points 40 and 26 in Figure 3, in accordance
with the explanation just given.
[0026] In Figure 4, the compressor is run for a period T
on which is terminated when the compressor inlet pressure reaches the set point P
set. The compressor is then turned off for a calculated period of time T
off which may be equal for example to four minutes. After the off period, the compressor
is turned on again until the inlet pressure has again fallen to P
set. The off period of the compressor is derived (as explained below with reference to
Figure 6) with reference to the time that it takes for compressor inlet pressure to
fall to P
set after the compressor has been turned on, this time being taken as a characteristic
indicative of the load on the compressor system. If the on period become undesirably
short (for example less than two minutes) due to low load, then the subsequent period
T
off is extended so as to increase the length of the subsequent period T
on and hence the length of the next cycle. As well as achieving high efficiency, this
also tends to ensure that the total cycle time will be long enough for the number
of starts per hour of the compressor rarely if ever to exceed its rated value.
[0027] From the above, it can be seen that in accordance with the invention insofar as a
fixed set point value is used, only a single set point pressure value has to be set
when the system is being installed, and consequently only a singel value has to be
adjusted in order to adjust the operation of the system.
[0028] Figure 5 shows hardware required to operate the control method of Figures 3 and 4,
including a compressor inlet pressure sensor 42, an inlet pressure set point device
44, and a source of time pulses 46 all of which feed their outputs to a controller
48. The controller may be a digital controller which operates in accordance with the
flow chart shown in Figure 6 and provides an output signal on line 50 which opens
and closes a contactor 52 to switch the compressor 2 off and on. The time factor used
in controlling the compressor cycles is derived with reference to the time pulses
produced by the source 46.
[0029] Figure 6 is a flow chart showing the operation of the controller 48 in order to perform
the control method of Figures 3 and 4. Initially T
off/set is set to four minutes, the compressor is then started, compressor inlet pressure
is compared with P
set until they are equal at which point the compressor is stopped, T
on is recorded and the compressor off period T
off/set starts to run.
[0030] If the read value of T
on is greater than two minutes and less than fifteen minutes, the compressor is switched
on again when it has been off for four minutes.
[0031] If T
on is less than the minimum desired value of two minutes, then T
off/set is increased in inverse proportion to the read value of T
on, but subject to a maximum of twelve minutes, and during the next operating cycle
the compressor is held off for the new increased period of T
off/set. If T
on shoud become greater than fifteen minutes, then T
off/set is reduced in inverse proportion to T
on, but subject to a minimum of four minutes, for the next cycle. The programming of
the controller 22 (Figure 5) will be arranged, empirically if necessary, such that
in the particular system the relationship betwen the current demand for cooling as
indicated by the length of the on period T
on in each cyle, and the length of the off period T
off/set as calculated by the algorithm, will result in the majority of the cabinets demanding
cooling at the end of the off period.
[0032] The lower limit value, in this instance four minutes, for T
off/set sets a lower limit on the frequency with which the compressor can be started and
hence protects it against being started at rates beyond its starts per hour rating.
The upper limit of twelve minutes on T
off/set avoids the temperatures in the cabinets becoming too high.
[0033] Alternatively, instead of the length of the off period being determined by the programming
of the controller, the off period may be terminated in response to a sensed characteristics
of the load units. When each of the load units includes a thermostat system, the sensed
characteristics may be the condition of the thermostat systems and, for example, the
off period may then be terminated when a majority of the load units are demanding
cooling as indicated by the conditions of their thermostat systems. Figure 5 shows
in chain-dotted lines 56 connections from the three thermostat switches 12 of Figure
1 by means of which the controller is informed of the conditions of the thermostatic
switches and hence can be programmed to detect the closure of a majority of them and
in response switch on the compressor system via line 24.
[0034] In a system which is not subject to major variations in load, it is possible for
the off period actually to be fixed at length which can be relied on to allow the
majority of the load units to be demanding cooling when the compressor system is switched
on, though provision may be made for manual adjustment of the length of the off period
in the event that monitoring of the system indicates that the desired pattern of operation
is not in practice being achieved.
[0035] So far as the on period is concerned, this is simply terminated when one or more
of the load units have ceased to demand cooling, i.e. not very long after the compressor
system inlet pressure has dropped from the plateau 22, by appropriately setting the
value P
set.
[0036] However, other variables may be sensed in order to detect the falling load on the
compressor system which is indicative of the plateau region having been passed. When
the compressor system is electrically powered, the current consumption, power consumption
and power factor of the motor or motors will all be reduced as the load on the system
falls from the plateau and hence, as illustrated in Figure 5, a sensing unit 58 may
be associated with the power supply to the compressor motor to sense current consumption,
power consumption, or power factor. Suitable sensing units are readily available and
therefore need not be further described. The output from sensing unit 58 is sent by
line 60 to the controller 48, where it will be compared with the output of the set
point device 44 to detect when the load, falling from its plateau level, reaches the
set point value. Of course, the set point device 44 will be arranged to deliver a
set point signal indicative not of a set point pressure, but of a set point current
consumption, power consumption or power factor value.
[0037] It will be evident that the lengths of the on period and the off period may be determined
independently of each other by separate systems so long as those systems are compatible
with each other.
[0038] It has been mentioned that it is advantageous to vary P
set, or whatever alternative set point value may be employed, automatically in response
to the level at which the plateau 22 occurs, because although the plateau 22 will
necessarily occur at a relatively high level owing to the high load existing at the
beginning of the on period, its exact level will vary according to operating conditions
at the time. To achieve this, the controller 48 may be programmed so as to monitor
a variable indicative of load, for example compressor inlet pressure from pressure
sensor 42, the number of thermostatic valves open as indicated on lines 56, or one
of the electrical parameters of the power supply as indicated by unit 58, to recognise
when that measrued variable does not change by more than 10%, or preferably 5%, during
a predetermined period of time, and to treat the detetion of that occurrence as an
indication that the plateau level 22 is then occurring. It can further be programmed
to then provide on line 62 a signal effective to adjust the set point device 18 so
that it will give a set point output value to the controller equal to, for example,
80% of the measured value in absolute units of the plateau level.
[0039] In certain installations, there may be a small minority of load units which warm
up more quickly, or cool more slowly, than the rest. In that event, the controller
48 may be programmed to operate a modified control method in which, instead of turning
the compressor off as soon as the 80% (of plateau) level is reached, the compressor
is held on until either a lower, e.g. 50%, level is reached or until a further predetermined
time (e.g. one minute) has elapsed, whichever occurs sooner. On occasions, when the
unit or units which tend to run warmer do not need extra cooling, they will hardly
get any because the pressure will fall rapidly from the 80% level to the 50% level,
but when they do need extra cooling the fall will be slower and they will receive
cooling for up to a further minute. When using the Figure 6 algorithm, it may be modified
so that T
on is the time to reach set point rather than the complete period up until actual switch-off.
The requirement that a majority of the cabinets demand cooling at the start of the
next on period is not disturbed.
[0040] It should be appreciated that a method according to the invention can be applied
to a multiple-capacity compressor system which runs at more than one different level
of capacity during a compressor on period, but not at all during the off period. In
that event, steps may occur in the plateau level when an additional capacity stage
is switched in but nevertheless it is possible to detect the fall in load from the
end of the plateau by any of the techniques referred to above.
[0041] It has previously been mentioned that the method of the invetnion may be applied
to a compressor system which includes one, preferably relatively low capacity, compressor
which runs all the time, and a main compressor which is operated in cycles, the purpose
of the small compressor being to ensure that liquid refrigerant does not accumulate
on the outlet sides of the evaporators which will be capable of damaging the main
compressor when it is switched on. In such a system, the continuous running of the
small compressor would depress the level of the maximum pressure reached at the inlet
of the main compressor as indicated by the broken line curve parts 18ʹ and 38ʹ shown
in Figure 3. The pressure reduction may be even greater than is illustrated.
[0042] A control method in accordance with the invention can be applied to air conditioning,
where the principles involved are the same as those in refrigeration. Furthermore,
it can be applied to heat pumps. Heat pump systems are equivalent to refrigeration
systems except that the purpose is to deliver heat in the condenser rather than remove
it in the evaporator. Consequently, in applying the invention to heat pumps, it would
be the compressor outlet pressure that is measured rather than its inlet pressure,
this being an indication of the variable which it is intended to control, namely the
temperature at which refrigerant is condensing in the condenser.
[0043] Figure 7 shows how this outlet pressure varies throughout a cycle in a manner opposite
to that of the inlet pressure. The outlet pressure rises whilst the compressor is
on and, provided that a majority of the heat pump output units are demanding heating
at the time when the compressor is switched on, there is a plateau as shown at 22ʹ
at a relatively low pressure level, which represents efficient operation of the heat
pump system. Following the plateau, the compressor outlet pressure starts rising again
as the heating demand from the output units falls, and the on period is then terminated
in a similar manner to that used in the refrigeration system described in more detail.
For example, the level of the plateau may be sensed, and a set point value may be
set in response to that sensing at a level which is a desired percentage higher than
the plateau level so as to ensure that the compressor is switched off relatively soon
after the demand from the output units starts to fall. The compressor is then held
off, for example in the ways already described in relation to a refrigeration system,
for a sufficient period that when it comes on again at least a majority of the output
units are again demanding heating.
[0044] Other attempts have been made to achieve the benefits of the present invention. For
example, a rectifier/inverter has been used to convert the mains frequency to a variable
frequency so as to run the compressor at a variable speed to match the refrigeration
demand, but this is complex and expensive.
[0045] Other arrangements for seeking to match capacity to demand include mechanical arrangements
for shutting off a number of the cylinders of a compressor to reduce its capacity,
over re-expansion compressors in which the com pression ratio can be changed to alter
the capacity, and multiple compressors which can be switched on in varying numbers.
In some applications, a control method of the present invention applied to a simple
single compressor may achieved similar results to these more complex systems. However,
the invention can also be applied to the control of such systems to improve their
efficiency.
1. A method of controlling a compressor driven vapour compression heat movement system
in which a common compressor system heats or cools a plurality of load units and is
operated in cycles each of which include a compressor system higher capacity period
and compressor system lower capacity period, characterised in that the lower capacity
period is made sufficiently long that when the compressor system is switched to the
higher capacity a majority of the load units are demanding heating or cooling and
that the higher capacity period is made sufficiently long that when the compressor
system is switched to lower capacity one or more of the load units have had their
heating or cooling demand satisfied.
2. A method as claimed in a claim 1, wherein the lower capacity period is controlled
so as to be sufficiently long.
3. A method as claimed in claim 2, wherein the length of the lower capacity period
is controlled in dependence upon the length of the preceding higher capacity period.
4. A method as claimed in claim 2, wherein the lower capacity period is terminated
in response to a sensed characteristic of the load units.
5. A method as claimed in claim 4, wherein the load units each include a thermostat
system, and the sensed characteristic is the condition of the thermostat systems.
6. A method as claimed in claim 11, wherein the length of the lower capacity period
is fixed at a sufficiently long value.
7. A method as claimed in any preceding claim, wherein said majority is at least 75%.
8. A method as claimed in any preceding claim, comprising sensing a variable which
represents the load on the compressor system and utilising the value of the sensed
variable in terminating the higher capacity period.
9. A method as claimed in claim 8, comprising terminating the higher capacity period
when the sensed variable indicates that the load on the compressor system has fallen
from a substantially constant load level.
10. A method as claimed in claim 8 or claim 9, wherein the system is a cooling system
and the sensed variable is the compressor system inlet pressure.
11. A method as claimed in claim 8 or claim 9, wherein the system is a heating system
and the sensed variable is the compressor system outlet pressure.
12. A method as claimed in claim 8 or claim 9, wherein the compressor system is electrically
powered and the sensed variable is its current consumption.
13. A method as claimed in claim 8 or claim 9, wherein the compressor system is electrically
powered and the sensed variable is its power consumption.
14. A method as claimed in claim 8 or claim 9, wherein the compressor system is electrically
powered and the sensed variable is its power factor.
15. A method as claimed in claim 8 or claim 9, wherein the load units each include
a thermostat system and the sensed variable is the number of thermostat systems demanding
heating or cooling.
16. A method as claimed in any one of Claims 8 to 15, comprising terminating the higher
capacity period when the sensed variable reaches a set point value.
17. A method as claimed in any one of Claims 8 to 15 comprising establishing a set
point value for the sensed variable and terminating the higher capacity period either
when a predetermined period has elapsed after the sensed variable reaches the set
point value, or when the sensed variable reaches a predetermined value different from
the set point value, whichever is the sooner.
18. A method as claimed in Claim 16 or Claim 17, comprising sensing the occurrence
of a substantially constant level of load on the compressor system during its higher
capacity period and automatically adjusting the set point value to a value which would
represent a load level lower than said substantially constant value.
19. A method as claimed in Claim 18, wherein the system is a cooling system and the
set point value is set such that when the sensed variable reaches the set point value
the compressor inlet pressure is between 60% and 90% of the absolute value which it
has when the load is at said substantially constant level.
20. A method as claimed in any preceding claim, wherein the compressor system consists
of a compressor and the higher capacity mode is when the compressor is on and the
lower capacity mode is when the compressor is off.
21. A method as claimed in any one of Claims 1 to 19, wherein the compressor system
includes a plurality of compressors, and in the higher capacity mode at least some
of the compressors are running and in the lower capacity mode a lesser, fixed number
which may be zero, are running.
22. A method of controlling a compressor driven vapour compression heat movement system
in which a common compressor system heats or cools a plurality of load units and is
operated in cycles each of which include a compressor system higher capacity period
and a compressor system lower capacity period, characterised in that the lower capacity
period is made sufficiently long that when the compressor is switched to the higher
capacity a majority of the load units are demanding heating or cooling and that the
duration of the higher capacity period is controlled by monitoring a variable which
represents the load on the compressor system and terminating the higher capacity period
when the sensed variable indicates that the load on the compressor system has fallen
from a substantially constant level.
23. A method as claimed in Claim 22 including the further features specified in any
of Claims 2 to 7 or 10 to 21.
24. A compressor driven vapour compression heat movement system in which a common
compressor system heats or cools a plurality of load units, and comprising control
means which controls the compressor system to operate in cycles each of which include
a compressor system higher capacity period and a compressor system lower capacity
period, the control means being adapted to make the lower capacity period sufficiently
long that when the compressor system is switched to the higher capacity a majority
of the load units are demanding heating or cooling and to make the higher capacity
period sufficiently long that when the compressor system is switched to lower capacity
one or more of the load units have had their heating or cooling demand satisfied.
25. A system as claimed in Claim 24, wherein the control means is adapted to control
the lower capacity period so as to be sufficiently long.
26. A system as claimed in Claim 25, wherein the contol means is adapted to sense
the length of the higher capacity period and to control the length of the lower capacity
period in dependence thereon.
27. A system as claimed in Claim 25, comprising means for sensing a characteristic
of the load units, wherein the control means is adapted to terminate the lower capacity
period in response to the sensing means.
28. A system as claimed in Claim 27, wherein the load units each include a thermostat
system, and the sensing means senses of the condition of the thermostat system.
29. A system as claimed in Claim 24, wherein the control means is adapted to fix the
length of the lower capacity period at a sufficiently long value.
30. A system as claimed in any of Claims 24 to 29, wherein said majority is at least
75%.
31. A system as claimed in any of Claims 24 to 30, comprising means for sensing a
variable which represents the load on the compressor system, the control means being
adapted to utilise the value of the sensed variable in terminating the higher capacity
period.
32. A system as claimed in Claim 31, wherein the control means is adapted to terminate
the higher capacity period when the sensed variable indicates that the load on the
compressor system has fallen from a substantially constant and level.
3. A system as claimed in Claim 31 or Claim 32, which is a cooling system and wherein
the sensed variable is the compressor system inlet pressure.
34. A system as claimed in Claim 31 or Claim 32, which is a heating system and wherein
the sensed variable is the compressor system outlet pressure.
35. A system as claimed in Claim 31 or Claim 32, wherein the compressor system is
electrically powered and the variable sensed by the sensing means is its current consumption.
36. A system as claimed in Claim 31 or Claim 32, wherein the compressor system is
electrically powered and the variable sensed by the sensing means is its power consumption.
37. A system as claimed in Claim 31 or Claim 32, wherein the compressor system is
electrically powered and the variable sensed by the sensing means is its power factor.
38. A system as claimed in Claim 31 or Claim 32, wherein the load units each include
a thermostat system and the variable sensed by the sensing means is the number of
thermostat systems demanding heating or cooling.
39. A system as claimed in any one of Claims 31 to 38, wherein the control means is
adapted to terminate the higher capacity period when the sensed variable reaches a
set point value.
40. A system as claimed in any one of Claims 31 to 38 wherein the control means is
adapted to establish a set point value, and includes means for detecting when the
sensed variable reaches the set point value, timing means for defining a predetermined
period following said detection, means for terminating the on period, and means for
activating said terminating means either at the expiry of the predetermined period
or when the sensed variable reaches a predetermined value different from the set point
value, whichever is the sooner.
41. A system as claimed in Claim 39 or 40, wherein the control means is adapted to
sense the occurrence of a substantially constant level of load on the compressor system
during its higher capacity period and to automatically adjust the set point value
to a value which would represent a load level lower than said substantially constant
value.
42. A system as claimed in Claim 41, which is a cooling system and wherein the control
means is adapted to set the set point value such that when the sensed variable reaches
the set point value the compressor inlet pressure is between 60% and 90% of the absolute
value which it has when then load is at said substantially constant level.
43. A system as claimed in any one of Claims 24 to 42, wherein the compressor system
consists of a compressor and the higher capacity mode is when the compressor is on
and the lower capacity mode is when the compressor is off.
44. A system as claimed in any one of Claims 24 to 42, wherein the compressor system
includes a plurality of compressors, and in the higher capacity mode at least some
of the compressors are running and in the lower capacity mode a lesser, fixed number
which may be zero, are running.
45. A compressor driven vapour compression heat movement system in which a common
compressor system heats or cools a plurality of load units, comprising control means
which controls the system to operate in cycles each of which include a compressor
system higher capacity period and a compressor system lower capacity period, the control
means being adapted to make the lower capacity period sufficiently long that when
the compressor system is switched to the higher capacity a majority of the load units
are demanding heating or cooling and to control the duration of the higher capacity
period by monitoring a variable which represents the load on the compressor system
and terminating the higher capacity period when the sensed variable indicates that
the load on the compressor system has fallen from a substantially constant level.
46. A system as claimed in Claim 45, including the further features specified in any
of Claims 26 to 31 or 34 to 44.
47. A control means for controlling a compressor driven vapour compression heat movement
system in which a common compressor heats or cools a plurality of load units, the
control means comprising an input for receiving a signal representing the load on
the compressor system, means for detecting when the signal represents a substantially
constant level of load, and means for utilising said detection in generating a control
signal usable to switch the compressor system to a lower capacity mode.
48. A control means as claimed in Claim 47 wherein the means for utilising said detection
in generating a control signal includes means for providing a set point signal representing
a predetermined fraction of the substantially constant load level, means for detecting
when the signal representing load reaches the value of the set point signal, and means
for generating said control signal in dependance upon said detection.
49. A control means as claimed in Claim 48 wherein the means for generating said control
signal is immediately responsive to said detection.
50. A control means as claimed in Claim 48 wherein the means for generating said control
signal includes timing means for defining a predetermined period following said detection,
means for defining a value different from the set point value, and means for producing
said control signal when the predetermined period has expired or the signal representing
load has reached said different value, whichever is the sooner.