Method for controlling a supply of refrigerant to an evaporator in contingency mode

Abstract

A method for controlling a supply of refrigerant to an evaporator of a vapour compression system, such as a refrigeration system, an air condition system or a heat pump. During normal operation, the opening degree of the expansion valve is controlled on the basis of an air temperature, T.sub.air, of air flowing across the evaporator and/or on the basis of superheat of refrigerant leaving the evaporator. If at least one sensor used for obtaining T.sub.air or the superheat is malfunctioning, operation of the vapour compression system is switched to a contingency mode. A reference temperature, T.sub.out, ref, is calculated, based on previously obtained values of a temperature, T.sub.out, of refrigerant leaving the evaporator, during a predefined previous time interval, and subsequently the opening degree of the expansion valve is controlled on the basis of the obtained temperature, T.sub.out, in order to reach the calculated reference temperature, T.sub.out, ref.

Claims

1. A method for controlling a supply of refrigerant to an evaporator of a vapour compression system, the vapour compression system comprising at least one evaporator, at least one compressor, at least one condenser and at least one expansion valve arranged in a refrigerant circuit, the method comprising the steps of: obtaining a temperature, T.sub.out, of refrigerant leaving the evaporator, obtaining, by at least one sensor, a control parameter value relating to the vapour compression system, controlling an opening degree of the expansion valve, on the basis of the obtained control parameter, and in order to reach a reference value for the control parameter, detecting that the at least one sensor used for obtaining the control parameter is malfunctioning, calculating a reference temperature, T.sub.out, ref, based on previously obtained values of the temperature, T.sub.out, during a predefined previous time interval, and subsequently controlling the opening degree of the expansion valve, on the basis of the obtained temperature, T.sub.out, and in order to reach the calculated reference temperature, T.sub.out, ref, of the refrigerant leaving the evaporator.

2. The method according to claim 1, wherein the step of controlling a control parameter value comprises obtaining a temperature, T.sub.air, of air flowing across the evaporator; the step of controlling an opening degree comprises controlling the opening degree of the expansion valve, on the basis of the obtained air temperature, T.sub.air, and in order to reach a reference air temperature, T.sub.air, ref, of the air flowing across the evaporator; and the step of detecting that at least one sensor is malfunctioning comprises detecting that at least one sensor used for obtaining the air temperature, T.sub.air, is malfunctioning.

3. The method according to claim 1, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating an average value of obtained values of the temperature, T.sub.out, of refrigerant leaving the evaporator during the predefined previous time interval.

4. The method according to claim 1, wherein the step of subsequently controlling the opening degree of the expansion valve comprises the steps of: providing a perturbation signal, and setting the opening degree of the expansion valve to the controlled opening degree, overlaid with the perturbation signal, monitoring the temperature, T.sub.out, of refrigerant leaving the evaporator, analysing a signal representing the monitored temperature, T.sub.out, and increasing the opening degree of the expansion valve in the case that said analysis reveals that T.sub.out>T.sub.out, ref.

5. The method according to claim 1, wherein the step of controlling the opening degree of the expansion valve, on the basis of the obtained temperature, T.sub.out, and in order to reach the calculated reference temperature, T.sub.out, ref, of the refrigerant leaving the evaporator is continued until the malfunctioning sensor(s) has/have been replaced or repaired.

6. The method according to claim 1, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating a first reference temperature, T.sub.out, ref, day, based on values of T.sub.out obtained during daytime, and calculating a second reference temperature, T.sub.out, ref, night, based on values of T.sub.out obtained during nighttime.

7. The method according to claim 2, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating an average value of obtained values of the temperature, T.sub.out, of refrigerant leaving the evaporator during the predefined previous time interval.

8. The method according to claim 2, wherein the step of subsequently controlling the opening degree of the expansion valve comprises the steps of: providing a perturbation signal, and setting the opening degree of the expansion valve to the controlled opening degree, overlaid with the perturbation signal, monitoring the temperature, T.sub.out, of refrigerant leaving the evaporator, analysing a signal representing the monitored temperature, T.sub.out, and increasing the opening degree of the expansion valve in the case that said analysis reveals that T.sub.out>T.sub.out, ref.

9. The method according to claim 3, wherein the step of subsequently controlling the opening degree of the expansion valve comprises the steps of: providing a perturbation signal, and setting the opening degree of the expansion valve to the controlled opening degree, overlaid with the perturbation signal, monitoring the temperature, T.sub.out, of refrigerant leaving the evaporator, analysing a signal representing the monitored temperature, T.sub.out, and increasing the opening degree of the expansion valve in the case that said analysis reveals that T.sub.out>T.sub.out, ref.

10. The method according to claim 2, wherein the step of controlling the opening degree of the expansion valve, on the basis of the obtained temperature, T.sub.out, and in order to reach the calculated reference temperature, T.sub.out, ref, of the refrigerant leaving the evaporator is continued until the malfunctioning sensor(s) has/have been replaced or repaired.

11. The method according to claim 3, wherein the step of controlling the opening degree of the expansion valve, on the basis of the obtained temperature, T.sub.out, and in order to reach the calculated reference temperature, T.sub.out, ref, of the refrigerant leaving the evaporator is continued until the malfunctioning sensor(s) has/have been replaced or repaired.

12. The method according to claim 4, wherein the step of controlling the opening degree of the expansion valve, on the basis of the obtained temperature, T.sub.out, and in order to reach the calculated reference temperature, T.sub.out, ref, of the refrigerant leaving the evaporator is continued until the malfunctioning sensor(s) has/have been replaced or repaired.

13. The method according to claim 2, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating a first reference temperature, T.sub.out, ref, day, based on values of T.sub.out obtained during daytime, and calculating a second reference temperature, T.sub.out, ref, night, based on values of T.sub.out obtained during nighttime.

14. The method according to claim 3, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating a first reference temperature, T.sub.out, ref, day, based on values of T.sub.out obtained during daytime, and calculating a second reference temperature, T.sub.out, ref, night, based on values of T.sub.out obtained during nighttime.

15. The method according to claim 4, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating a first reference temperature, T.sub.out, ref, day, based on values of T.sub.out obtained during daytime, and calculating a second reference temperature, T.sub.out, ref, night, based on values of T.sub.out obtained during nighttime.

16. The method according to claim 5, wherein the step of calculating a reference temperature, T.sub.out, ref, comprises calculating a first reference temperature, T.sub.out, ref, day, based on values of T.sub.out obtained during daytime, and calculating a second reference temperature, T.sub.out, ref, night, based on values of T.sub.out obtained during nighttime.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The invention will now be described in further detail with reference to the accompanying drawings, in which

(2) FIG. 1 is a diagrammatic view of a part of a vapour compression system being controlled during normal operation,

(3) FIG. 2 is a diagrammatic view of a part of a vapour compression system being controlled in a contingency mode, in accordance with an embodiment of the invention,

(4) FIG. 3 is a flow chart illustrating a method according to an embodiment of the invention, and

(5) FIGS. 4 and 5 are diagrammatic views of a part of a vapour compression system being controlled in accordance with alternative embodiments of the invention.

DETAILED DESCRIPTION

(6) FIG. 1 is a diagrammatic view of a part of a vapour compression system 1 being controlled during normal operation. The vapour compression system 1 comprises an evaporator 2 arranged in a refrigerant circuit along with one or more compressors (not shown) and one or more condensers (not shown). An expansion valve 3 is also arranged in the refrigerant circuit for controlling the supply of refrigerant to the evaporator 2.

(7) The vapour compression system 1 further comprises a number of temperature sensors. A first temperature sensor 4 is arranged in the refrigerant circuit after the outlet of the evaporator 2. Accordingly, the first temperature sensor 4 measures a temperature signal, S.sub.2, which represents the temperature of refrigerant leaving the evaporator 2.

(8) A second temperature sensor 5 is arranged in a secondary air flow across the evaporator 2, at a position before the air reaches the evaporator 2. Accordingly, the second temperature sensor 5 measures a temperature signal, S.sub.3, which represents the temperature of air flowing towards the evaporator 2.

(9) A third temperature sensor 6 is arranged in the secondary air flow across the evaporator 2, at a position after the air has passed the evaporator 2. Accordingly, the third temperature sensor 6 measures a temperature signal, S.sub.4, which represents the temperature of air flowing away from the evaporator 2.

(10) The temperature signals, S.sub.3 and S.sub.4, measured by the second temperature sensor 5 and the third temperature sensor 6, are supplied to a sensor selection unit 7. The sensor selection unit 7 selects whether to apply one of the temperature signals, S.sub.3 and S.sub.4, when controlling the expansion valve 3, or to apply a weighted value of the two temperature signals, S.sub.3 and S.sub.4. The selection may, e.g., be based on the availability of the sensors 5 and 6, or on the choice of the installer. Based on the selection, a temperature signal, T.sub.air, is generated, and T.sub.air represents an air temperature, corresponding to the selection performed by the selection unit 7. The temperature signal, T.sub.air, is supplied to a control unit 8, which is arranged to control an opening degree of the expansion valve 3.

(11) A reference air temperature, T.sub.air, ref, is also supplied to the control unit 8. The reference air temperature, T.sub.air, ref, represents a reference or target temperature which is desired in the air flowing across the evaporator 2.

(12) The control unit 8 compares the temperature signal, T.sub.air, to the reference air temperature, T.sub.air, ref, and calculates an opening degree of the expansion valve 3, based on this comparison. The opening degree of the expansion valve 3 is selected in such a manner that the opening degree ensures a supply of refrigerant to the evaporator 2, which causes the air temperature, T.sub.air, to approach the reference air temperature, T.sub.air, ref. Thus, during normal operation, the control unit 8 controls the opening degree of the expansion valve 3 on the basis of the selected air temperature, T.sub.air, i.e. using the second 5 and/or third 6 temperature sensor, and in order to reach the reference temperature, T.sub.air, ref. Accordingly, the normal operation of the vapour compression system 1 depends on reliable temperature measurement signals from the second 5 and/or the third 6 temperature sensor.

(13) The temperature signal, S.sub.2, measured by the first temperature sensor 4 is also supplied to the control unit 8. Thereby, the temperature of refrigerant leaving the evaporator 2 may also be taken into account when the opening degree of the expansion valve 3 is calculated by the control unit 8.

(14) When the control unit 8 has calculated an opening degree of the expansion valve 3 as described above, the control unit 8 may apply a perturbation signal to the calculated opening degree. In FIG. 1, the perturbation signal is shown as a relay like perturbation signal. In this case, the resulting signal is supplied to the expansion valve 3, and the opening degree of the expansion valve 3 is controlled to be the calculated opening degree, overlaid with the perturbation signal.

(15) In the case that the opening degree of the expansion valve 3 is controlled on the basis of the calculated opening degree and the overlaid perturbation signal, the temperature signal, S.sub.2, measured by the first temperature sensor 4, is also supplied to an analysing unit 9. The analysing unit 9 analyses the temperature signal, S.sub.2, e.g. with respect to a rate of change of the temperature signal, S.sub.2. The result of the analysis is supplied to a safety logic unit 10. The safety logic unit 10 monitors the result of the analysis, e.g. the rate of change of the temperature signal, S.sub.2. In the case that the analysis reveals that a dry zone of the evaporator is approaching a minimum length, the safety logic unit 10 sends a signal to the control unit 8, requesting that the opening degree of the expansion valve 3 is decreased. In response to this signal, the control unit 8 decreases the opening degree of the expansion valve 3. For instance, the safety logic unit 10 may conclude that the dry zone of the evaporator 2 is approaching a minimum length if an absolute value of the rate of change of the temperature signal, S.sub.2, reaches a maximum value.

(16) FIG. 2 is a diagrammatic view of a part of a vapour compression system 1 being controlled in a contingency mode, in accordance with an embodiment of the invention. The vapour compression system 1 of FIG. 2 is very similar to the vapour compression system 1 of FIG. 1, and it will therefore not be described in detail here.

(17) However, in the vapour compression system 1 of FIG. 2, the second temperature sensor 5 and/or the third temperature sensor 6 is/are unavailable or unreliable. Therefore the signal from the sensor selection unit 7 to the control unit 8 is blocked, and the control unit 8 thereby receives no air temperature measurements. Accordingly, the control unit 8 is not able to calculate the opening degree of the expansion valve 3, in the manner described above, and on the basis of the air temperature, T.sub.air.

(18) In order to allow the vapour compression system 1 to continue operating, despite the unavailable or unreliable temperature sensor(s) 5, 6, a reference temperature, T.sub.out, ref, is calculated, based on previous measurements of the temperature, T.sub.out, of refrigerant leaving the evaporator 2, performed by the first temperature sensor 4. The previously obtained values of the temperature, T.sub.out, were obtained during a predefined previous time interval, e.g. the four hours preceding the point in time where it was detected that the temperature sensor(s) 5, 6 was/were unavailable or unreliable. The calculated reference temperature, T.sub.out, ref, may, e.g., be an average of the temperature values, T.sub.out, obtained by the first temperature sensor 4 during the predefined previous time interval.

(19) The calculated reference temperature, T.sub.out, ref, is supplied to the control unit 8. Furthermore, the temperature, T.sub.out, of refrigerant leaving the evaporator 2 is still measured by means of the first temperature sensor 4, and the temperature signal, T.sub.out, is supplied to the control unit 8. The control unit 8 compares the temperature signal, T.sub.out, to the calculated reference temperature, T.sub.out, ref, and calculates an opening degree of the expansion valve 3, based on this comparison. The opening degree of the expansion valve 3 is selected in such a manner that the opening degree ensures a supply of refrigerant to the evaporator 2, which cause the temperature, T.sub.out, of refrigerant leaving the evaporator 2 to approach the reference temperature, T.sub.out, ref.

(20) In centralised vapour compression systems, where the suction pressure is controlled by a compressor rack controller, it may be assumed that the suction pressure, i.e. the pressure prevailing in the suction line interconnecting the outlet of the evaporator 2 and the inlet of the compressor rack, is substantially constant, at least on a short timescale. During steady state operation of the vapour compression system 1, the superheat, SH, is kept substantially constant. The superheat, SH, is defined as
SH=T.sub.outT.sub.e,
where T.sub.e is the bubble temperature or the dew point of refrigerant leaving the evaporator 2. Accordingly, the superheat, SH, represents the difference between the actual temperature, T.sub.out, of refrigerant leaving the evaporator 2 and the dew point, T.sub.e, of the refrigerant leaving the evaporator 2. It is desirable to control the vapour compression system 1 in such a manner that the superheat, SH, is kept at a small, positive value, because thereby it is ensured that the refrigerant contained in the evaporator 2 is a mixture of gaseous and liquid refrigerant, along a substantial part of the evaporator 2. This ensures that the potential refrigerating capacity of the evaporator 2 is utilised to the greatest possible extent, without risking that liquid refrigerant passes through the evaporator 2 and into the suction line.

(21) The dew point, T.sub.e, of the refrigerant leaving the evaporator 2 depends on the pressure of the refrigerant leaving the evaporator 2. Since this pressure can be assumed to be substantially constant when the suction pressure is controlled by the compressor rack controller, as described above, T.sub.e can also be assumed to be substantially constant. Furthermore, since the superheat, SH, is kept substantially constant during steady state operation of the vapour compression system 1, it can be concluded that T.sub.out is also substantially constant. Accordingly, maintaining the temperature, T.sub.out, of refrigerant leaving the evaporator at a level which corresponds to an average level of T.sub.out during a predefined time interval, will ensure that the superheat, SH, of refrigerant leaving the evaporator 2 is kept at a suitable level. When the second temperature sensor 5 and/or the third temperature sensor 6 is/are unavailable or unreliable, it is therefore suitable to control the opening degree of the expansion valve 3, and thereby the supply of refrigerant to the evaporator 2, based on the temperature, T.sub.out, of refrigerant leaving the evaporator 2, and in such a manner that the calculated reference temperature, T.sub.out, ref, is reached.

(22) Thus, according to the embodiment of the invention illustrated in FIG. 2, the supply of refrigerant to the evaporator 2 is controlled, based on the temperature measurements performed by the first temperature sensor 4, when the second temperature sensor 5 and/or the third temperature sensor 6 is/are unavailable or unreliable. This is an advantage as compared to prior art contingency mode control, because it allows the supply of refrigerant to the evaporator 2 to be controlled in a manner which optimises the efficiency of the vapour compression system, including utilising the potential refrigeration capacity of the evaporator 2 to the greatest possible extent. Furthermore, it allows the system to react on changes in refrigeration load, e.g. in the case that new products are positioned in a display case of the vapour compression system.

(23) The vapour compression system 1 may be operated as described above, i.e. on the basis of the temperature, T.sub.out, of refrigerant leaving the evaporator 2, until the unavailable or unreliable temperature sensor(s) 5, 6 has/have been replaced or repaired.

(24) FIG. 3 is a flow chart illustrating a method according to an embodiment of the invention. The method illustrated in FIG. 3 may, e.g., be used for controlling the vapour compression system 1 of FIG. 1 or FIG. 2. The process is started at step 11. At step 12, a temperature, T.sub.air, of air flowing across the evaporator, and a temperature, T.sub.out, of refrigerant leaving the evaporator are measured.

(25) At step 13 it is investigated whether or not the temperature sensor used for measuring the temperature, T.sub.air, of air flowing across the evaporator is malfunctioning. If this is not the case, i.e. of the temperature sensor is available an operating reliably, the process is forwarded to step 14.

(26) At step 14 the measured air temperature, T.sub.air, is compared to a reference air temperature, T.sub.air, ref. It is further ensured that the evaporator is filled without being flooded. This may, e.g., include monitoring a superheat value of refrigerant leaving the evaporator, or investigating a behaviour of a temperature signal of refrigerant leaving the evaporator. At step 15 an opening degree of the expansion valve is calculated, based on the comparison performed in step 14. The calculation of the opening degree is performed in such a manner that setting the opening degree of the expansion valve to the calculated opening degree will result in the air temperature, T.sub.air, approaching the reference air temperature, T.sub.air, ref. The calculation of the opening degree may further be based on a comparison of a measured superheat value and a reference superheat value. At step 16 the opening degree of the expansion valve is set to the calculated opening degree, before the process is returned to step 12 for continued measurements of the air temperature, T.sub.air, and the temperature, T.sub.out, of refrigerant leaving the evaporator.

(27) Thus, if step 13 reveals that the air temperature sensor is not malfunctioning, and reliable measurements of the air temperature, T.sub.air, are therefore available, the opening degree of the expansion valve, and thereby the supply of refrigerant to the evaporator, is controlled on the basis of the measured air temperature, T.sub.air, and in order to obtain a temperature, T.sub.air, of air flowing across the evaporator, which is equal to the reference air temperature, T.sub.air, ref.

(28) On the other hand, if step 13 reveals that the air temperature sensor is malfunctioning, it is not possible to control the opening degree of the expansion valve in the manner described above, since reliable measurements of the air temperature, T.sub.air, are not available in this case. It is therefore necessary to apply another control strategy, allowing the vapour compression system to continue operating until the malfunctioning sensor has been replaced or repaired.

(29) To this end a reference temperature, T.sub.out, ref, is calculated at step 17. The reference temperature, T.sub.out, ref, is calculated on the basis of previously obtained values of the temperature, T.sub.out, during a predefined previous time interval, such as a 2-4 hours interval immediately preceding the malfunction of the temperature sensor used for measuring the air temperature, T.sub.air. The reference temperature, T.sub.out, ref, may, e.g., be calculated as an average of measured values of T.sub.out during the predefined time interval. In any event, the reference temperature, T.sub.out, ref, is calculated based on measurements which are performed during normal operation of the vapour compression system, i.e. while the opening degree of the expansion valve is controlled in the manner described above, based on the measured air temperature, T.sub.air. Accordingly, the calculated reference temperature, T.sub.out, ref, represents a typical level of the temperature, T.sub.out, of refrigerant leaving the evaporator, during normal operation of the vapour compression system.

(30) At step 18 the measured temperature, T.sub.out, of refrigerant leaving the evaporator is compared to the calculated reference temperature, T.sub.out, ref, and at step 19 an opening degree of the expansion valve is calculated, based on the comparison performed in step 18. Similarly to the situation described above with reference to step 15, the calculation of the opening degree performed in step 19, is performed in such a manner that setting the opening degree of the expansion valve to the calculated opening degree will result in the temperature, T.sub.out, of refrigerant leaving the evaporator approaching the reference temperature, T.sub.out, ref. At step 20 the opening degree of the expansion valve is set to the calculated opening degree.

(31) Thus, if step 13 reveals that the air temperature sensor is in fact malfunctioning, and reliable measurements of the air temperature, T.sub.air, are therefore unavailable, the opening degree of the expansion valve, and thereby the supply of refrigerant to the evaporator, is controlled on the basis of the measured temperature, T.sub.out, of refrigerant leaving the evaporator, and in order to obtain a temperature, T.sub.out, of refrigerant leaving the evaporator, which is equal to the calculated reference temperature, T.sub.out, ref.

(32) The process is then forwarded to step 21, where it is investigated whether or not the air temperature sensor is still malfunctioning, and thereby whether or not reliable measurements of the air temperature, T.sub.air, are still unavailable. If this is the case, it is still necessary to control the opening degree of the expansion valve, and thereby the supply of refrigerant to the evaporator, on the basis of measured values of the temperature, T.sub.out, of refrigerant leaving the evaporator. The process is therefore forwarded to step 22, where the temperature, T.sub.out, of refrigerant leaving the evaporator is measured. The process is then returned to step 18, where the new measured value of the temperature, T.sub.out, is compared to the calculated reference temperature, T.sub.out, ref.

(33) In the case that step 21 reveals that the air temperature sensor is no longer malfunctioning, reliable measurements of the air temperature, T.sub.air, are once again available, and the opening degree of the expansion valve can therefore once again be controlled according to the normal control strategy. Accordingly, the process is, in this case, returned to step 12 for continued measurements of the air temperature, T.sub.air, and the temperature, T.sub.out, of refrigerant leaving the evaporator.

(34) FIG. 4 is a diagrammatic view of a part of a vapour compression system 1 being controlled in accordance with an alternative embodiment of the invention. The vapour compression system 1 of FIG. 4 is very similar to the vapour compression systems 1 of FIGS. 1 and 2, and it will therefore not be described in further detail here.

(35) In the vapour compression system 1 of FIG. 4, the opening degree of the expansion valve 3 is controlled on the basis of the air temperature, as well as on the basis of the superheat of refrigerant leaving the evaporator 2. The superheat of the refrigerant leaving the evaporator 2 is obtained by measuring the temperature of refrigerant leaving the evaporator 2, by means of the first temperature sensor 4, and the temperature of refrigerant entering the evaporator 2, by means of a fourth temperature sensor 23.

(36) In the case that the fourth temperature sensor 23 malfunctions, i.e. becomes unavailable and/or unreliable, the superheat control of the opening degree of the expansion valve 3 is no longer possible. Therefore the superheat control is replaced by a contingency control strategy identical to the one described above with reference to FIG. 2.

(37) FIG. 5 is a diagrammatic view of a part of a vapour compression system 1 being controlled in accordance with another alternative embodiment of the invention. The vapour compression system 1 of FIG. 5 is very similar to the vapour compression systems 1 of FIGS. 1, 2 and 4, and it will therefore not be described in detail here.

(38) In the vapour compression system 1 of FIG. 5, the opening degree of the expansion valve 3 is also controlled on the basis of the air temperature, as well as on the basis of the superheat of refrigerant leaving the evaporator 2, similar to the embodiment described above with reference to FIG. 4. However, in the vapour compression system 1 of FIG. 5, the superheat of refrigerant is obtained by measuring the temperature of refrigerant leaving the evaporator 2, by means of the first temperature sensor 4, and the pressure of refrigerant leaving the evaporator 2, by means of a pressure sensor 24.

(39) In the case that the pressure sensor 24 malfunctions, i.e. becomes unavailable and/or unreliable, the superheat control of the opening degree of the expansion valve 3 is no longer possible. Therefore the superheat control is replaced by a contingency control strategy identical to the one described above with reference to FIG. 2.

(40) While the present disclosure has been illustrated and described with respect to a particular embodiment thereof, it should be appreciated by those of ordinary skill in the art that various modifications to this disclosure may be made without departing from the spirit and scope of the present disclosure.