Patent Application
20230258380
This teaching concerns a refrigeration plant with a cooling circuit.
In particular, this teaching relates to controlling the temperature of the fluid of a cooling circuit serving a plurality of refrigeration machines of a refrigeration plant, wherein this circuit is apt to absorb the condensation heat of such refrigeration machines.
It is currently known to this Applicant that supermarkets are the most electricity-consuming entities in the commercial sector.
A supermarket may consume on average more than one million kWh per year.
Most of this energy consumption is attributable to the refrigeration of perishable goods that are housed in what are referred to below as peripheral units, i.e. in cold rooms or in display units such as tubs, showcases or displays of various types, which may take up to half the size of the shop.
Conventional refrigeration plants generally use a system known as “multiplexed”, whereby the refrigerant fluid is distributed and evaporated in heat exchangers (evaporators) installed in the peripheral units, thus maintaining the desired temperature inside the latter for product preservation.
A centralised compressor rack sucks the vapour from the evaporation of the refrigerant in the various services by means of a compressor unit which raises the pressure and sends it to the condenser where the fluid is returned to a liquid state and finally redistributed again to the peripheral units, repeating the cycle.
The compressor unit is installed in a dedicated room, which is usually located in a room in the shop or on the roof of the shop.
The nature of the food available in a supermarket is such that there are at least two levels of storage temperature in the peripheral units: medium temperature “MT” (where products are stored between approximately +1° C. and 3° C.) for fresh food, and low temperature “LT” (where products are stored between approximately -20° C. and -28° C.) for frozen or deep-frozen food. Different temperatures may be required for specific cases.
For this reason, the compressor units in supermarkets usually have two compressors racks with very different saturated suction temperatures; in fact on average, the compressor racks serving the MT peripheral units and those serving the LT peripheral units suck in the refrigerant fluid at a saturated temperature of approximately -10° C. and from -30° C. to -35° C., respectively.
Obviously, this type of plant comprises an often very complex network of pipes for conveying the refrigerant.
While the same condensed liquid from the compressor racks may be distributed to both categories of services, i.e. MT and LT peripheral units, the suction pipes are necessarily different between MT and LT services.
Due to the distance between the compressor/condenser units and the peripheral services and the consequent extension required by the piping, large quantities of refrigerant are required, which may exceed one thousand kilograms.
The length of the path of the piping between the peripheral services and the centralised unit, which comprises the compressor units and condensers, also results in significant pressure losses, which translate into significant decreases in the overall efficiency of the plant.
In addition, this conventional layout - consisting of multiple sections of piping and welded connections - implies a significant risk of leakage which, on a statistical basis, varies on average from 10% to 25% of the total refrigerant charge, on an annual basis.
In this context, the so-called “water loop self-contained system” (WLSC in short) is increasingly now being used to reduce both the annual energy consumption and the total warming impact (TEWI).
This type of plant requires each peripheral unit (or small groups of peripheral units) to be equipped with its own autonomous refrigeration unit, preferably provided with a variable speed compressor (normally with a BLDC brushless motor driven by an inverter), water condenser and expansion valve; this unit, which is connected to the evaporator, makes each unit self-sufficient and independent from the others.
Each of these peripheral units is connected to a closed hydraulic circuit crossed by a liquid (generally water with antifreeze added) and supplied by it so that its condenser is cooled by heat exchange with the liquid itself, which absorbs the condensation heat of the various connected peripheral units and disperses it through a heat sink consisting of an exchanger outside the supermarket premises.
Solutions aimed at optimising energy consumption may involve not dispersing the heat completely to the outside but recovering some of it for other uses, for example to obtain hot water, obviously with complications of the circuit.
The most commonly used heat sink is the type generally known as a dry cooler consisting of a fan-forced convection heat exchanger.
Example diagrams of conventional plants are shown in accompanying
In particular,
Evidently, the temperature of the water cooled by the dry cooler is closely linked to the outside ambient temperature, where obviously as the latter rises, the temperature of the water supplying the refrigeration units of the peripheral units 1003 and 1004 rises accordingly.
The physical quantities that have the greatest influence on the cooling capacity and efficiency of a compressor are the saturated condensing pressure and the saturated evaporating pressure, which in the case of food storage is not subject to significant variations. The ratio of the saturated condensing pressure to the saturated evaporating pressure constitutes the compression ratio.
It is well known that every 1° C. increase in the saturated condensing temperature - which here is due to the increase in the external temperature - causes a decrease in both the cooling capacity and the energy efficiency of the compressor of approximately 2.5%-3%.
In addition, there is a limit value for the compression ratio declared by compressor manufacturers beyond which serious damage may occur.
The problem at the heart of this teaching is to improve the constructive simplicity of conventional plants.
The task of this teaching is therefore to solve this problem by making available a refrigeration plant with a cooling circuit that can maintain satisfactory operating efficiency even at high ambient temperatures, while at the same time being suitable for operating in a wide range of cooling capacities depending on the pressure required in relation to the seasonality and the number of peripheral units in operation.
In the context of this task, it is the aim of this teaching to propose a refrigeration plant with a cooling circuit that is easy to install and regulate.
This task, as well as these and other purposes which will appear more clearly below, are achieved by a refrigeration plant with a cooling circuit according to the attached independent claims.
Detailed characteristics of a refrigeration plant with a cooling circuit according to this teaching are given in the dependent claims.
Further features and advantages of the teaching will emerge more fully from the description of a preferred, but not exclusive, embodiment of a refrigeration plant with a cooling circuit, according to this teaching, illustrated by way of non-limiting example in the accompanying drawings tables, in which:
With particular reference to the above-mentionedfigures, a refrigeration plant with a cooling circuit 101 is indicated as a whole by 100, and comprises:
In other words, the control device 105 may be configured to operate the cooling apparatus 104 so as to modulate, by operating the latter, the operating temperature of the secondary fluid so as to maintain the latter within the reference range and causing it to pursue the target or set-point value.
The operating temperature according to this teaching may be a value calculated from measured or derived temperatures taken on by the secondary fluid in a plurality of sections of the cooling circuit.
The operating temperature in particular may be measured upstream or downstream of the cooling apparatus.
In a possible embodiment of this teaching particularly suitable for providing a refrigeration plant 100 for a supermarket, there are provided a plurality of peripheral units 102, 103 which are divided into medium temperature units 102 and low temperature units 103.
The medium temperature units 102 may be configured to maintain the respective storage compartment at a temperature indicatively between 0° C. and 5° C., whereas the low temperature units 102 may be configured to maintain the respective storage compartment at a temperature indicatively between -20° C. and -23° C.
The refrigeration machines of the peripheral units 102 and 103 use a primary fluid as refrigerant fluid.
This primary fluid may be R744, i.e. carbon dioxide, in short CO2.
The secondary fluid may consist of a liquid such as an aqueous mixture.
The use of a mixture of a water and glycol mixture is particularly advantageous.
This may be 30% by weight, so that at 15° C. it has a density of 1040 kg/m3, a specific heat of 3700 J/(kg x °C) and a freezing point of -15° C.
It can therefore be understood how it is possible in a plant according to this teaching to regulate the operating temperature of the secondary fluid in such a way as to determine specific heat exchange temperatures with the heat exchangers of the peripheral units regardless of the ambient temperature. That is, it is possible to maintain the operating temperature such that the operation of the refrigeration plant 100 can be optimised regardless of the temperature of the environment into which the refrigeration plant 100 dissipates heat.
It can therefore be understood how a refrigeration plant 100 according to this teaching may be operated in such a way as to achieve energy optimisation and allow considerable structural simplicity and greater reliability and durability with respect to conventional refrigeration plants.
In particular, it is possible to optimise the operating conditions of the refrigeration plant 100 with respect to the heat exchange conditions of the secondary fluid with the primary fluid of each peripheral unit 102, 103 so as to determine the most favourable operating conditions of the refrigeration machines.
Moreover, the refrigeration plant 100 according to this teaching allows to optimise its operation also with respect to the heat exchange between the secondary fluid and the environment, as will emerge even more clearly in the following description.
In particular, when the refrigeration machines of the peripheral units 102 and 103 are refrigeration machines using CO2 as a refrigerant fluid, it is possible to arrange the refrigeration plant 100 according to this teaching in such a way that the thermodynamic operating conditions of all the refrigeration machines of the peripheral units correspond to a subcritical operation.
Subcritical operation means operation in which the heat exchange temperature at the heat exchanger is not higher than the critical temperature, i.e. the heat yielded to the heat exchanger consists mainly of latent condensing heat of the refrigerant fluid.
This makes it possible to use structurally simple refrigeration machines for both medium temperature units 102 and low temperature units 103 whereas on the other hand, the refrigeration machines involved must be appropriately structured in conventional plants in which a transcritical operating condition is envisaged for all or some of the refrigeration machines, even if only for a few weeks a year.
The use of a refrigeration plant according to this teaching therefore results in a great advantage with respect to conventional plants such as, for example the one illustrated in
Thus, a refrigeration plant 100 according to this teaching makes it possible to avoid adopting the use of compressors for the refrigeration machines of the low temperature units 103 that are suitable for working under particularly severe compression ratio or structurally complex conditions, as in the case of multi-stage compressors with intermediate cooling possibly by means of a regenerative exchanger.
It also generally avoids the use of a flash gas discharge branch and its valve, as well as the use of a high pressure valve at the condenser discharge, in the refrigeration machines of the peripheral units 102, 103.
In general, the refrigeration plant 100 may comprise at least one temperature sensor 106a, 106b connected to the cooling circuit 101 so as to detect the operating temperature.
Generally speaking, the refrigeration plant 100 may also comprise one temperature sensor alone which may be arranged at the inlet of the cooling apparatus 104 or preferably, two temperature sensors placed one at the inlet of the secondary fluid into the cooling apparatus 104 and one at the outlet thereof, respectively.
The control device 105 may be configured to operate the cooling apparatus 104 according to the temperature of the secondary fluid at the inlet of the cooling apparatus 104 and the temperature of the secondary fluid at the outlet of the cooling apparatus 104, wherein the latter may be the operating temperature for which the control apparatus 105 operates the cooling apparatus 104 to achieve the temperature of the secondary fluid at the outlet of the cooling apparatus 104 within the reference range and/or to pursue a target and/or set-point value.
The refrigeration plant 100 will preferably also comprise a temperature sensor for each peripheral unit 102, 103, which is preferably arranged to detect the temperature of the secondary fluid at the outlet of each peripheral unit 102, 103, for example as shown in
The control device 105 may in general comprise:
The monitoring device may be configured to set the reference range and/or target value by possibly implementing an optimisation process, for example like one of those described below.
Thus, the control device 105 may in general be connected to the temperature sensor 106a, 106b and configured to operate the cooling apparatus 104 to maintain the operating temperature - which is detected by the temperature sensor 106a, 106b - within the reference range or to equalize it to at least a corresponding target value.
In general, the at least one operating temperature may comprise a first exchange temperature at which the secondary fluid exchanges heat with the primary fluid at the heat exchanger 102a, 103a.
In such a case, as mentioned above, in embodiments of this teaching providing for a refrigeration plant 100 having a plurality of peripheral units 102, 103, each of these may be provided with a temperature sensor 106a, for example placed downstream of the heat exchanger 102a, 103a of the respective peripheral unit 102 or 103, as by way of non-limiting example shown in
The control device 105 may comprise a plurality of controllers (which in themselves are conventional and not illustrated), each integrated in a peripheral unit 102, 103 and configured to operate the refrigeration machine according to a control algorithm, for example configured to perform a feedback control of the machine with respect to an overheating temperature upstream of the compressor with respect to a predefined set point.
The refrigeration plant 100 may also comprise, for each peripheral unit 102, 103, or for each group of peripheral units 102, 103:
In the example in
The refrigeration plant 100 may comprise at least one low temperature unit 103 of the peripheral units 102, 103, which has a refrigeration machine configured to operate at an evaporation temperature which is not greater than -18° C.
The reference range of the operating temperature of the secondary fluid in this case may have a maximum limit equal to 22° C. or the target value cannot be greater than 22° C., in this way the CO2 peripheral units 102 and 103 may be configured to operate always according to a subcritical thermodynamic regime, thus allowing to achieve the above-mentioned advantages of structural simplification.
The at least one operating temperature may comprise a second exchange temperature consisting of:
In particular, a general valve unit 109 and/or a pumping member 110, preferably with adjustable flow rate, each operable to modulate a flow of the secondary fluid interacting with the cooling apparatus 104, may be connected to the cooling circuit 101.
The control device 105 may be connected to the general valve unit 109 and/or to the pumping member 110 in order to operate them so as to regulate the flow rate of secondary fluid exchanging heat with the cooling apparatus 104, for example according to the operating temperature detected downstream of the cooling apparatus 104 as, for example visible in
In particular, the pumping member 110 may comprise a plurality of pumps in parallel, for example two as exemplified in
The pumping member 110 may comprise, for each pump, a driving device, for example an inverter, to modulate the motor speed of the respective pump to regulate the flow rate of the latter.
The cooling apparatus 104 may comprise:
The condenser member 112 and the radiator member 104a may be arranged in series so as to be crossed in sequence by an airflow Z generated by the ventilation means 104c, wherein preferably the radiator member 104a is placed upstream with respect to the condenser member 112.
For example, the condenser member 112 may have one face directly attached to the radiator member 104a, wherein the other face may be associated with the ventilation means 104c, which may for example comprise a plurality of fans, for example as exemplified in
The ventilation means 104c may be associated with one alone of the condenser member 112 and the radiator member 104a, or both, so for example they comprise first fans associated with the radiator member 104a and second fans associated with the condenser member 112, indicated by hatched lines in
In the case where the ventilation means comprise both first fans associated with the radiator member 104a and second fans associated with the condenser member 112, preferably the radiator member 104a and the condenser member 112 are not arranged in series with respect to the cooling airflow passing through them.
In this case, with respect to the configuration in which the condenser member 112 and the radiator member 104a are in series with respect to the ventilation means 104c, the latter may operate an autonomous forced convection cooling effect on the condenser member 112 and the radiator member 104a.
The control device 105 may be configured to actuate the auxiliary refrigeration machine 104b and/or the ventilation means 104c in order to regulate the operating temperature of the secondary fluid, for example the one detected downstream of the cooling apparatus, for example by the second temperature sensor 106b.
In particular, the control device 105 may be configured to operate the auxiliary refrigeration machine 104b, the ventilation means 104c and the general valve unit 109 and/or the pumping member 110 in a coordinated manner so as to control the operating temperature of the secondary fluid.
For example, where the temperature of the environment in which the cooling apparatus 101 dissipates heat is sufficiently low to allow the use of the radiator member 104a alone to maintain the operating temperature at the desired values, the control device may disable the auxiliary cooling apparatus 104b and possibly exclude it from the cooling circuit 101, for example by operating the general valve unit 109 which may, for example comprise a three-way valve 109a, as shown for example in
Vice versa, if the cooling action of the radiator member 104a alone does not prove to be sufficient, possibly also following the activation of the ventilation means 104c, the control device may operate the auxiliary refrigeration machine 104b to obtain the desired operating temperature, i.e. within the reference range, or to equalise it to or make it pursue a target or set-point value.
In this way, a significant energy improvement is achieved compared to a configuration in which, for example a step chiller was used to yield heat to the water in a radiator, which would then dissipate this heat into the environment by forced convection.
In fact, such a solution with a step chiller would obtain a double thermal gradient which instead is avoided by the cooling apparatus 104 described above when the auxiliary refrigeration machine 104b absorbs heat from the secondary fluid to disperse it into the environment directly through its own condenser member 112 which may be cooled by forced convection by the ventilation means 104c, thus allowing to operate with a lower compression ratio as compared to the aforementioned solution with a step chiller.
The general valve unit 109 may be configured to supply the radiator member 104a alone, the auxiliary refrigeration machine 104b alone, or both, with the secondary fluid, as well as to modulate the possible action of the ventilation means 104c to allow a combined action of the radiator member 104a and the auxiliary refrigeration machine 104b, thus allowing a greater energy optimisation. In a less functionally flexible alternative, the general valve unit 109 may be configured to supply the radiator member 104a alone or the auxiliary refrigeration machine 104b alone with the secondary fluid without partializing the secondary fluid between them, for example as in the solution visible in
The main valve unit 109 may also comprise a bypass branch 101b that runs parallel to the radiator member.
The bypass branch 101b may be connected to one of the paths of the aforementioned three-way valve 109a, the other two paths of which may be in communication with a discharge of the radiator member 104a and the inlet of the auxiliary refrigeration machine 104b, for example as shown in
Or a first motorised valve 109b may be connected between the discharge of the radiator member 104a and the inlet of the auxiliary refrigeration machine 104b, and the second motorised valve 109b may be connected between the bypass branch 101b and the inlet of the auxiliary refrigeration machine 104b in order to mix the secondary fluid from the bypass branch 101b and the secondary fluid from the radiator member 104a.
The control device 105 may be configured to operate the main valve unit 109, and in particular to operate the three-way valve 109a or the motorised valves 109b and 109c, in order to combine the secondary fluid flowing through the bypass branch 101b and/or through the radiator member 104a, to mix them in order to regulate the operating temperature, and/or through the auxiliary refrigeration machine 104b which, as in the example in
Thus for example, the control device 105 may be configured such that if the ambient temperature is low, it deactivates the auxiliary refrigeration machine 104b and, operating the main valve unit 109, mixes part of the secondary fluid crossing the bypass branch 101b with part of the secondary fluid cooled by the radiator member 104a, possibly deactivating or modulating the action of the ventilation means 104c, to control the operating temperature.
The three-way valve 109a and the motorised valves 109b and 109c are preferably modulating valves in order to be operated so as to regulate the flow of secondary fluid crossing them.
The cooling apparatus may also comprise, connected to the cooling circuit 101, preferably upstream of the pumping unit 110, an inertial tank 113 for containing the thermal cycling and useful in particular for applications in which the cooling apparatus 104, and especially the auxiliary refrigeration machine 104b, employ ON-OFF compressors instead of preferable variable speed compressors, for example compressors with an inverter-driven BLDC motor.
The control device 105 may be configured to define the reference range or the target value for the operating temperature according to an optimisation process which may be configured to maximise a coefficient of performance EERTOT given by the formula:
wherein EERSP consists of the energy efficiency average of each of the one peripheral units 102, 103; EERCH consists of the energy efficiency of the cooling apparatus 104.
This optimisation process may comprise, in sequence, for example as seen in
This optimisation process may comprise a standby step F of a predefined time Y which is carried out following step B and/or step D.
In addition, step D and/or step B may provide a sub-step D1 and B1, respectively, for assigning the value of a second parameter EER that is equal to the last value calculated of the coefficient of performance EERtot, to a first parameter EERprec. Steps C and/or E correspondingly may comprise a sub-step C1 and E1, respectively, which provide comparing the value of the first parameter EERprec with the value of the second parameter EER as recalculated.
Several methods may be used to calculate this plant EERSP.
A first, simpler and more effective method is to use the sum of the cooling capacities of each peripheral unit 102, 103 at instant (i) divided by the sum of the powers absorbed by the compressor of the refrigeration machine of each peripheral unit 102, 103 at the same instant. As per the formula below.
In this calculation, it is possible to exclude (or for example to zero) capacities and powers absorbed by the peripheral units 102, 103 which are in particular statuses of the refrigeration cycle (for example in a pull-down phase) or which operate in particularly unstable statuses so as not to destabilise the entire system as a result of unstable statuses of the peripheral units 102, 103.
The unstable status of a peripheral unit 102, 103 may be defined on the basis of parameters of the controller of the peripheral units 102, 103 or by evaluating the cooling capacity of the peripheral unit 102, 103 considered over time, for example by means of the difference between cooling capacity at instant (i) and instant (i-1) and deviation.
A second method of calculating the parameter EERSP may be carried out by considering weighted averages of the coefficients of performance EERSPi of each peripheral unit 102, 103 present in the plant, or by means of data filtration systems according to the statuses of the peripheral units 102, 103.
Such weighted averages or filtration systems may take into account factors such as:
An example of a weighted average with the cooling capacities of peripheral units 102, 103 is given by the following formula:
where kwSPi is a weight parameter associated with the coefficient of performance EERSPi of the corresponding peripheral unit 102, 103.
This same weighted average may also be used as a filter by applying temporary values to the weights kWSPi for particular machine statuses; e.g. kWSPi = 0 temporarily for OFF units or units in defrost, and kWSPi = K where K is a factor other than 1 for units in pull-down status.
Alternatively, the control device 105 may be configured to define the reference range or the target value according to an optimisation process configured to minimize a total energy consumption of the refrigeration plant 100.
For example, the optimisation process may be configured to minimise a total energy consumption Etot of the refrigeration plant where the total energy consumption Etot is given by the formula ETOT = ESP + ECH + EPC + EFAN, where:
In particular, these parameters may be defined as follows:
Finally, there will be functional limits imposed for the operating temperature, which are indicated as Twl_SET-MIN and Twl_SET-MAX, i.e. minimum and maximum operating temperature limit values, respectively, for plant reasons, external climate and/or climate of the working area of the compressors of the refrigeration machines of the peripheral units 102, 103 involved.
This optimisation process may comprise, in sequence, for example as seen in
This optimisation process may comprise a standby step N of a predefined time Y which is carried out following step H and/or step L.
In addition, step L and/or step B may provide a sub-step L1 and H1, respectively, for assigning the value of a second parameter Etot that is equal to the last value calculated of the total energy consumption Etot, to a first parameter Etot-prec.
Steps K and/or M correspondingly may comprise a sub-step K1 and M1, respectively, which provide comparing the value of the first parameter Etot-prec with the value of the second parameter Etot as recalculated.
In general, the optimisation process according to this teaching may be implemented in a trial and error mode or in a predictive mode.
In the trial and error mode, starting from an initial target value of the operating temperature, modifications are applied to this initial value by repeating the calculation of a reference parameter, such as the coefficient of performance EER or the total energy consumption Etot as exemplified above, and further modifying this target value according to a logic aimed at optimising this reference parameter.
In the predictive mode, the initial value, or a set of values, of the target value may be adopted following a simulation in which the optimisation process is carried out in the trial and error mode by calculating the results of each trial, i.e. of each variation of the target value on the reference parameter, without actually making such a variation on the refrigeration plant 100.
In this predictive mode, the optimisation process may therefore be developed in the same way as in the trial and error mode where however, the initial value of the target value of the operating temperature is not assigned in advance but is in fact calculated by means of the simulation.
In a variant of this predictive mode, the target value may always be adopted following a simulation in which the optimisation process is carried out in the trial and error mode by calculating the results of each trial, i.e. of each variation of the target value on the reference parameter, without actually making such a variation on the refrigeration plant 100.
In a further variant of this predictive mode, before performing the aforementioned steps B and D or H and L, i.e. before actually changing the target value of the predefined value X or its opposite -X, they are carried out in a simulation mode before applying the actual change.
With particular reference to the diagrams in
It is therefore understood how the optimisation process in question may provide that if the ambient temperature Text rises above a predefined value, which is lower than the value of the operating temperature Twl, the control device 105 activates the auxiliary refrigeration machine 104b to assist the cooling action of the secondary fluid implemented by the radiator member 104a in combination with the ventilation action of the ventilation means 104c.
In other words, in accordance with this optimisation process, it is possible to identify:
The upper part of
The optimisation process may provide that when the ambient temperature Text reaches and falls below the minimum value Text-A, then the minimum limit value Twl-set-MlN is assigned to the target value Twl-set.
Similarly, when the ambient temperature Text reaches and rises above the maximum value Text-D, then the maximum limit value Twl-set--MAX is assigned to the target value Twl-set.
In accordance with this optimisation process, the following may be defined in the first and second operating zones, respectively, mentioned above:
As can be seen for example in
Or the function f(Text) may be defined by a straight segment or by applying optimisation processes of the coefficient of performance EER or the energy consumption, such as those described above.
With particular reference to
In particular, a regenerative exchanger 112a configured to exchange heat between the secondary fluid and the tertiary fluid, recirculating in a tertiary circuit 1112, may be placed hydraulically coupled to the condenser member in order to recover and not dissipate heat via the condenser member 112.
The regenerative exchanger 112a in particular may be coupled to the condenser member 112 in an in parallel and/or series configuration, or may be coupled thereto by means of connecting piping and valves, for example as more fully exemplified below, so that the regenerative exchanger 112a and the condenser member 112 may be alternatively or simultaneously supplied in a configuration which may be selected between an in parallel configuration and a series configuration.
The regenerative exchanger 112a may be integrated in the auxiliary refrigeration machine 104b.
An auxiliary valve unit 114 of the auxiliary refrigeration machine 104b may be configured to implement an in parallel or series hydraulic connection of the condenser member 112 with the regenerative exchanger 112a in such a way that the secondary fluid may be supplied to the condenser member 112 alone or to the regenerative exchanger 112a alone, or to both, possibly in a partial manner. The control device 105 may be connected to the auxiliary valve unit 114 to operate it and may be configured or programmed to optimise heat recovery to the tertiary fluid, i.e., to favour the supply of the secondary fluid to the regenerative exchanger 112a by directing the secondary fluid to the condenser member 112 only when heat dissipation from the secondary fluid in the regenerative exchanger 112a is insufficient or does not allow optimised operation of the refrigeration plant 10.
Otherwise, the control device 105 may be connected to the auxiliary valve unit in order to operate it so as to provide on demand a thermal load to the tertiary fluid by means of the regenerative exchanger 112a, thus instead favouring the supply of the secondary fluid to the condenser member 112 under normal operating conditions.
Depending on the contingent requirements for implementing this teaching, the auxiliary valve unit may comprise, as for example visible in
In the exemplified variant shown in
In normal operation, the auxiliary valve unit diverts the flow by bypassing the regenerative exchanger 112a to direct the flow to the condenser member 112.
If for example, the tertiary circuit 1112 is required to obtain hot water at a temperature of for example, 50° C., the auxiliary valve unit may be operated so that the flow of refrigerant from the auxiliary refrigeration machine 104b supplies the regenerative exchanger 112a and the condenser member 112 is bypassed. Depending on the thermal load from the peripheral units 102, 103, the auxiliary refrigeration machine 104b dissipates heat by means of the condenser unit 112, the regenerative exchanger 112a or by both in a partialized manner. It has thus been ascertained how this teaching achieves the intended task and aims.
In fact, it should be noted that in a conventional plant, if the refrigerant fluid used in the refrigeration machines of the peripheral units were carbon dioxide, CO2, if the temperature of the cooling water, i.e. of the secondary fluid, exceeds about 25° C., the operation of the refrigeration machines of the peripheral units would switch to a transcritical cycle with progressively worse and even impracticable energy efficiencies for the low temperature units, both due to the pressures and the temperatures reached at the discharge of the compressors.
Conversely, in a refrigeration plant according to this teaching, the cooling water may be maintained permanently below that threshold or even colder, thus ensuring that the peripheral units can work constantly in a subcritical operation with a lower compression ratio and with much better and safer results.
In this way, by controlling the water temperature throughout the year, it is possible to limit the saturated delivery temperature of the compressors of the peripheral units and thus the compression ratio of the machines integrated in them.
This teaching thus conceived is susceptible to numerous modifications and variations, all of which fall within the scope of protection of the attached claims. In addition, all details may be replaced by other technically equivalent elements. In practice, the forms and dimensions can be varied according to the contingent requirements and the prior art.
Where the constructional and technical features mentioned in the following claims are followed by signs or reference numbers, the signs or reference numbers have been used only with the aim of increasing the intelligibility of the claims themselves and, consequently, they do not constitute in any way a limitation to the interpretation of each element identified, purely by way of example, by the signs or reference numerals.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102020000016504 | Jul 2020 | IT | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2021/056076 | 7/7/2021 | WO |
