• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Method and device for defrosting an evaporator (1) in a heat pump (2), in connection with an air treatment unit (9), and wherein the air treatment unit (9) comprises a controllable heat recovery unit (10). The heat pump (2) comprises a refrigerant system (3) with a refrigerant (4) and at least one compressor (5), at least one condenser (6), at least a first expansion valve (7) and at least one evaporator (1). Furthermore, the heat pump (2) comprises at least one four-way valve (8) which is arranged in the flow direction after the compressor (5) and before the condenser (6), and the four-way valve (8) is arranged to change the flow direction of the refrigerant (4) in the refrigerant system (3). The heat recovery (10) is arranged to recover energy from a first air stream (11) and transfer to a second air stream (12), and the evaporator (1) is arranged in the first air stream (11), in the flow direction the post-heat recovery (10), and the condenser ( 6) is arranged in the second air stream (12), in the direction of fate after the heat recovery (10). The invention is characterized in that when freezing the evaporator (1) the temperature of the refrigerant (4) is raised through the evaporator (1), at the same time as the heat recovery (10) is regulated down, i.e. the heat recovery is reduced, whereby a simultaneous heating of the evaporator (1), from inside the refrigerant ( 4) with elevated temperature, and based on the first air flow (11), whose temperature increases when heat recovery decreases, and thus cut double-sided defrosting of the evaporator (1).
    公开号:SE1200784A1
    申请号:SE1200784
    申请日:2012-12-21
    公开日:2014-06-22
    发明作者:Johan Andersson
    申请人:Fläkt Woods AB；
    IPC主号:
    专利说明:

    Thereafter, the refrigerant in the form of heated high-pressure steam is sent on to the condenser, where the high-pressure steam condenses and changes to a liquid form. During this process in the condenser, heat is released and it is this heat together with any compressor heat that is used for heating on the heat demand side. Then the refrigerant is sent to the expansion valve again and the heat pump cycle is thus closed. When the circuit is used for cooling in an air handling unit, the process is simply run reversibly, ie the refrigerant is sent in the other direction of the system, the respective DX battery, so to speak, shifts so that the evaporation takes place in the supply air, which is then cooled while the condensation takes place in exhaust air / exhaust air.
    When these systems are in operation, there is a need to defrost the evaporator side from time to time, as the evaporator side DX battery cools down greatly both due to the evaporation process itself, with very cold refrigerant in the evaporator, and the evaporator is exposed to cold and often humid air. passes through the evaporator / DX battery. This mainly applies in the case of heat, ie when heat is taken up from the exhaust air / exhaust air and transferred to the supply air for heating the same. The result of this is that heavy icing can occur on the evaporator if defrosting does not occur. Using the heat pump process for the cooling case and in connection with an air treatment unit is relatively common and sometimes even when the unit has a heat recovery unit. Due to the freezing problems described above, there are no known solutions with combinations of heat recovery and heat pump for the heat fall and with efficient and useful defrosting technology, as a sufficiently good way to defrost the evaporator has not been found. It simply costs too much energy and the supply air temperature becomes uneven due to the defrosting sequence (cooling of the supply air during defrosting despite heat demand). Because the air treatment unit comprises a heat recovery unit which, when heated, is regulated for maximum recovery of heat from the exhaust air, this means that the temperature after the heat recovery unit and before the evaporator is cold. The combination of this together with cold refrigerant inside the evaporator means that the risk of freezing of the evaporator increases and heavy icing can occur. According to conventional methods in most types of heat pumps, defrosting is carried out by reversibly running the refrigerant circuit, by arranging a multi-way valve or the like in the refrigerant circuit so that the defrost reverses the flow direction of the refrigerant when defrosting, instead sending hot refrigerant to the evaporator. long time that the ice melts and the DX battery is thus heated from the inside by the brine. The control of this consists either of a timer-controlled defrosting sequence where the sequence is repeated at preset intervals or either by a frost guard sensing when freezing takes place, after which the defrosting sequence begins. In these cases, the defrosting takes place according to the on / off principle, ie either defrosting takes place or it does not take place and the defrosting lasts according to a certain time or until the system indicates that the ice formation is gone.
    In other heat pump applications, such as a conventional air / air heat pump or a cooler, the evaporator part is usually placed separately in the outdoor air, on a roof or a wall or the like. The evaporator part then usually has a fl spike that pushes or sucks air through the evaporator. During defrosting, the brine circuit is reversed at the same time as the fan is switched off so as not to cause an extension of the defrosting time, if the ambient air is cold. In the context of ventilation, the conditions are partly different as the ets of the air handling unit fl must run continuously, even during the defrosting of the evaporator, due to the requirements for ventilation. This means that the time for defrosting is extended as the building, which is ventilated with the help of the air handling unit, cannot be without ventilation during the time for defrosting. The longer the defrost takes, the more energy is lost at the same time as the supply air temperature becomes colder and this is a problem that has made the use of heat pump solutions for heating the supply air unusual. Cooling with the help of a heat pump is as mentioned above, however, relatively common because then there is usually not the same problem because the evaporator part is then set to never get colder than for example + 15 ° C, because you can very rarely allow a supply air temperature that is colder.
    When an air treatment unit with a heat pump solution is run in the heat fall, ie during the cold season, the need for defrosting arises continuously during operation. On the supply air side, there is another disadvantage in the ventilation context as indicated above, namely the requirement for the supply air temperature, which is not a problem in other heat pumps arranged for heating, as the ventilation requirement does not exist. With reversible operation as a defrost technology, the respective DX battery changes, at least eventually, from the evaporator side to the condenser side and vice versa. The DX battery that is placed in the supply air after the heat recovery, in the case of heat, normally constitutes the final heating of the supply air to the setpoint, after the heat recovery has given off its heat to the supply air.
    The supply air side's DX battery thus constitutes a condenser in the heat fall, but when the evaporator is defrosted (in the exhaust air) through reversible operation, the supply air's DX battery becomes the cold side. As the ventilation cannot be interrupted, this means that the supply air is eventually cooled despite the actual need for heat. The supply air temperature can thus not be kept constant unless, for example, an extra heating battery is present in the supply air. It is desirable that the time for defrosting be minimized precisely because of these unique inconveniences that exist in ventilation contexts.
    The problem with the known solutions is that the defrosting sequence takes a relatively long time, as the controlled defrosting only takes place unilaterally, from inside the evaporator by heating the refrigerant. Furthermore, the recycling takes place in parallel with the defrost, which in itself cools, the air flowing through the evaporator and prolongs the defrosting time, and that both the supply and exhaust air fans must be in continuous operation.
    Disclosure of the Invention The present invention achieves the object of solving the above problems from the first aspect of the invention by the invented method that the defrosting of the evaporator takes place by simultaneous heating thereof, both inside and outside. This is done by raising the temperature of the refrigerant through the evaporator and thus heating the evaporator from the inside, at the same time as down-regulation takes place of the heat recovery included in the air treatment unit. By reducing the recovery during defrosting, the temperature of the air rises after the heat recovery, i.e. before the evaporator, and the air passing through the evaporator thus heats it from the outside. With the invented method, the time for defrosting in relation to the one-sided defrosting of older solutions is thus reduced and a more even supply air temperature is obtained, while the defrosting, if desired, can take place earlier in the freezing stage and in small, shorter sequences to offer a more even supply air temperature.
    According to a preferred embodiment of the invented method, the temperature of the refrigerant is raised during the defrosting sequence by reversibly running the heat pump, i.e. the refrigerant is pumped in the opposite direction in the refrigerant circuit relative to normal operation of the heat fall. This is done by the four-way valve changing the flow direction so that the heated high-pressure steam after the compressor is sent to the evaporator instead of to the condenser, without passing the expansion valve. In this way, the evaporator, ie the DX battery in the first air stream, is heated both from the inside of the heated refrigerant and also from the outside by the downregulation of the heat recovery, which makes the first air stream warmer than before, hotter than the operating case that caused the freezing of the evaporator. This significantly shortens the defrost time in relation to older solutions.
    According to a further preferred embodiment of the method, the brine circuit comprises a so-called hot gas valve, which is arranged in the direction of fate after the compressor as a bypass to the brine tube after the expansion valve. Through this valve it becomes possible to send the heated high-pressure steam after the compressor directly to the evaporator without passing the expansion valve or the four-way valve. Via the hot gas valve, all or part of the steam can be sent to the evaporator and, if applicable, the remaining amount is sent via the four-way valve to the condenser, just as usual. The amount of heated hot gas vapor sent directly to the evaporator heats it from the inside at the same time as the heat recovery is down-regulated and provides heating from the outside of the evaporator pipes.
    In the embodiment of the invented method described above, the energy will eventually only consist of the supplied compressor heat. According to a further preferred method, the above is combined with increasing the speed of the compressor at the same time as the hot gas valve is opened to a limited extent. As a result, the temperature in the evaporator is raised sufficiently for the freezing to cease and the ice to melt at the same time as the supply air is heated and the supply air temperature becomes more stable compared with conventional reversible operation where, so to speak, the condenser ceases to heat during defrosting. In this process, the condenser continues to deliver heat energy even during defrosting.
    An alternative way of achieving a temperature increase of the refrigerant during defrosting is to reduce the cooling effect by reducing the speed of the compressor so that the cooling effect in the evaporator decreases.
    In this way, the temperature of the refrigerant through the evaporator becomes higher and this in combination with, just as before, down-regulation of the heat recovery, a double-sided defrosting is obtained, inside and outside. In order to determine the most suitable way to control the defrost according to any of the methods described above to effect the double-sided defrosting of the evaporator, according to a preferred embodiment, the temperature between the heat recovery and the evaporator is measured. Based on this temperature, the defrost is controlled to, for example, run the circuit purely reversibly via the four-way valve, ie send the hot gas in the opposite direction to the evaporator instead of to the condenser, or let a subset be sent to evaporator or condenser, or reduce the cooling effect in the evaporator by downregulating the speed of the compressor, or if the system includes a hot gas valve send all or part of the hot gas to the evaporator or condenser. In particular, the temperature control in combination with a system comprising both a four-way valve and a hot gas valve provides very good flexibility in the choice of defrosting method, which in ventilation contexts could not previously be obtained.
    According to a further preferred embodiment of the method, the heat pump also comprises a reservoir and a second expansion valve, which are arranged between the first expansion valve and the condenser. Preferably, both expansion valves are also electronic and thus easily adjustable. The first expansion valve regulates the refrigerant fate of the evaporator and the second expansion valve regulates the refrigerant level in the reservoir in interaction with the first valve, in order to obtain a controlled so-called overheating. The overheating is defined by measuring the pressure before the compressor and then calculating the theoretical temperature of the refrigerant and further measuring the temperature of the pipe before the compressor. The theoretical temperature is compared with the measured temperature of the pipe and the difference between these is defined as the overheating. If the overheating is lower than the set so-called setpoint, the second expansion valve cools the refrigerant slightly, which leads to the overheating rising. If the overheating is instead higher than the setpoint, the second expansion valve opens slightly, and the overheating drops.
    The reservoir forms a buffer for the refrigerant as the consumption / need for refrigerant varies according to different temperatures. The advantage of the heat pump comprising a reservoir and a second expansion valve is in addition to the purely regulatory advantages of refrigerant buffer in the reservoir, that the overheating can be regulated / balanced taking into account which of the above-described defrosting techniques is used. This results in a controlled amount of refrigerant for the operating case and a balanced back pressure in the condenser even at partial load of the compressor. In all cases, the inventive idea is achieved with double-sided defrosting of the evaporator through heated refrigerant and heated flow-through exhaust air / exhaust air.
    An alternative to balancing the overheating with regard to any of the defrosting techniques described above is to use the overheating itself for defrosting according to a preferred embodiment of the method. By downshifting the compressor in combination with the first expansion valve restricting the refrigerant flow, the overheating increases. This process is used to advantage to make quick and short defrosts and preferably at an early stage of freezing in the evaporator.
    Due to the increased overheating, the refrigerant in the evaporator is heated, the defrosting taking place from the inside, and in combination with reduced heat recovery, the defrosting of the evaporator 40 also takes place from the outside due to the slightly elevated temperature of the air after the heat recovery. This type of heat pump solution in connection with ventilation units is not previously known and the advantages over conventional technology are då era as the defrosting methodology is both more flexible than older solutions both depending on the number of expansion valves, the refrigerant reservoir and the ability to control defrost to small short defrosts early in the freezing phase. that is, by height superheating, or in combination with other of the methods described above to effect the double-sided defrosting.
    From the second aspect of the invention, the object is achieved in that a device of the initially specified type has the special feature that the heat pump comprises a hot gas valve, which is arranged seen from the flow direction of the refrigerant, after the compressor. Because the device comprises a hot gas valve, it becomes possible, instead of running with completely reversible operation as in conventional plants, to have hot high-pressure steam sent directly to the evaporator for defrosting it, without the steam passing the expansion valve. Via the hot gas valve, all or a subset of the hot high-pressure steam after the compressor can be sent to the evaporator and, if applicable, the remaining subset is sent via the four-way valve to the condenser, just as usual. The amount of heated high-pressure steam sent directly to the evaporator heats it from the inside at the same time as the heat recovery is down-regulated and provides heating from the outside of the evaporator pipes, whereby the inventive concept is utilized. By using the possibility of sending a subset of heated high-pressure steam via the hot gas valve to the evaporator and letting the rest go to the condenser via the four-way valve, it is still possible to heat the supply air with condenser energy even if defrosting is taking place from the evaporator. This possibility does not exist in older plants as only reversible operation does not allow this alternative. The result of the fact that it is still possible to heat the supply air with condenser energy is that the supply air temperature as a whole becomes much more stable as the condenser does not become, so to speak, the “cold side” during defrosting as in older solutions.
    According to a preferred embodiment of the device, the heat pump also comprises a reservoir and a second expansion valve, which are arranged between the first expansion valve and the condenser.
    Preferably, both expansion valves are electronic and thus easily adjustable. The first expansion valve is arranged to regulate the refrigerant flow to the evaporator and the second expansion valve is arranged to regulate the refrigerant level in the reservoir, in interaction with the first valve, in order to obtain a controlled amount of refrigerant and a balanced back pressure in the condenser at partial load of the compressor. The reservoir is arranged to form a buffer for the refrigerant as the consumption / need for refrigerant varies according to temperature. The advantage of the heat pump comprising a reservoir and a second expansion valve is, in addition to the purely regulatory advantages of refrigerant buffer in the reservoir, that the overheating can be regulated / balanced taking into account the defrosting technique used. Regardless of the defrosting technique used according to the invention, good flexibility is obtained in all cases and the inventive idea with double-sided defrosting of the evaporator through heated refrigerant and heated flow-through exhaust air / exhaust air is achieved. According to a further preferred embodiment, the device comprises a temperature sensor, which is arranged between the heat recovery and the evaporator. The temperature is measured in between to determine the most suitable way to control the defrost according to any of the preferred embodiments of the process, and thus to provide the double-sided defrosting of the evaporator, as desired and suitable method of operation. Based on this temperature, for example, the defrost is controlled according to purely reversible operation via the four-way valve, ie send the refrigerant in the opposite direction to the evaporator instead of to the condenser, or have a subset of refrigerant sent to the evaporator or condenser using the hot gas valve, or to reduce the cooling effect. the evaporator by adjusting the speed of the compressor. In particular, the temperature control in combination with a system comprising both a four-way valve and a hot gas valve provides very good flexibility in the choice of defrosting method, which in ventilation contexts could not previously be obtained.
    According to a preferred embodiment of the device, the heat pump comprises a liquid separator, which is arranged in the flow direction of the shield medium before the compressor but after the four-way valve. To achieve the best performance in the heat pump system, try to inject as much refrigerant as possible into the evaporator without any refrigerant coming out as liquid after the evaporator. Furthermore, the compressor is very sensitive to liquid and for these reasons it is advantageous to have a tank in the form of a liquid separator in front of the compressor. This provides both a buffer of refrigerant for optimization of operation and a safety against any liquid reaching the compressor. Due to external circumstances, ie rapidly changing operating conditions, instability can occur in the system and thus lead to liquid coming out of the evaporator. This can also occur, for example, if the cooling circuit is turned without stopping the compressor or when stopping quickly in the ventilation system. Through the liquid separator, any liquid coming out of the evaporator can be captured before it reaches the compressor. This achieves increased safety for the compressor and the operation of the plant under the special conditions that exist in heat pump solutions for heating supply air in connection with air handling units.
    Through the invention, a number of advantages over known solutions have been obtained: - Double-sided defrosting of the evaporator, which means that the defrosting goes faster and the supply air temperature becomes more even. Even during defrosting, it is possible to continue heating the supply air in the air handling unit via the condenser, whereby the supply air temperature becomes more even.
    - A great flexibility regarding the choice of defrosting method through configurations with, among other things, four-way valve, hot gas valve, double expansion valves which are preferably electronic, reservoir for regulation and buffering of refrigerant and also the possibility of controlling the overheating.
    Brief description of the figures The following schematic principle figures show: - Fig. 1 shows a principle sketch of the heat pump according to the invention, arranged in connection with an air treatment unit with heat recovery, and in normal operation for heating the supply air.
    Fig. 2 shows a principle sketch of the heat pump according to the invention during simultaneous defrosting of the evaporator and heating via the condenser, by means of, among other things, the hot gas valve.
    Fig. 3 shows a principle sketch of the heat pump according to the invention during reversible operation for defrosting the evaporator. In principle, the figure also shows cooling operation when there is a need for cooling.
    The constructive design of the present invention will become apparent in the following detailed description of an embodiment of the invention with reference to the accompanying figures which show a preferred, but not limiting, embodiment of the invention.
    Detailed description of the figures Fig. 1 shows a principle sketch of a preferred embodiment of a heat pump 2 according to the invention, arranged as part of an air treatment unit 9. It should be understood, however, that the functions can just as easily be arranged as a whole unit module or a number of smaller modules. joining to an air treatment unit 9. It should also be mentioned that the air treatment unit 9 also comprises other components which are not shown in the figures, such as filters, other possible heaters and coolers, sensors etc.
    According to the embodiment shown in the figure, a first air stream 11 is arranged in the upper half of the complete air handling unit 9 and in the flow direction of the first air stream 11 in the figure from right to left, the first air stream 11 comprises exhaust air 18 from, for example, a room, apartment or the like. Typically, the exhaust air 18 passes a filter (not shown) before it reaches a heat recovery 10. According to the preferred embodiment, it is a controllable rotary heat recovery 10. Thereafter, the first air stream 11 passes an evaporator 1, which is constituted by a first DX battery 29, and then the air passes an exhaust air fl 22, which is the one that drives the first air stream 11. The air then leaves the air treatment unit 9 and is thus called exhaust air 19, which is discharged into the open air outside the building. In the lower part of the air treatment unit 9 is found in a second air stream 12, and in order in the figure from left to right, outdoor air 20 which is sucked into the air treatment unit 9. The outdoor air 20 usually passes a filter (not shown) before it reaches the heat recovery 10. Thereafter, the second air stream 12 arrives at a condenser 6, which is constituted by a second DX battery 30, and then the air passes through a supply air duct 23, which drives the second air stream 12 through the air handling unit 9 and into the room. After supply air source 23, the air is usually called supply air 21.
    The heat pump 2 in turn comprises a brine system 3 with a refrigerant 4, and during normal operation in the heat event, the following components are found, all of course with brine tubes between them, in order as follows. First a compressor 5, accompanied by a four-way valve 8 with a first inlet 24 arranged for the inflow of the refrigerant 4 from the compressor 5, further a first outlet 25 for the outflow of the refrigerant 4 to the condenser 6, and a second outlet 26, for refluxing refrigerant 4 in the direction against the compressor 5. However, a liquid separator 17 is found between the second outlet 26 and 40 the compressor 5, which liquid separator 17 is arranged to separate any liquid refrigerant 4, so that only gaseous refrigerant 4 reaches the compressor 5. The compressor 5 is very sensitive to liquid and to achieve the best performance in the system, try to inject a maximum of refrigerant 4 into the evaporator 1 without liquid coming out of the evaporator 1. Due to external circumstances, ie rapidly changing operating conditions, instability can also occur in the system, which can lead to liquid can come out of the evaporator 1. This can also occur if the cooling circuit is turned without stopping the compressor 5. Through the liquid separator 17 any liquid coming out of the evaporator 1 can be captured before it reaches the compressor 5. After the first outlet 25 of the four-way valve 8 follows the condenser 6 / the second DX battery 30, further on in the flow direction a second expansion valve 15 followed by a reservoir 14, arranged as a buffer for the refrigerant 4 in the refrigerant system 3. When the cooling circuit operates under different operating conditions, different amounts of refrigerant 4 are needed in the system and these differences in the need for refrigerant 4 are buffered in the preferred embodiment in reservoir 14 instead of condenser 6, is common.
    Further in the flow direction, a first expansion valve 7 follows after the reservoir 14, accompanied by the evaporator 1 / the first DX battery 29 and after this the heat pump cycle is closed by connecting the outlet of the evaporator 1 to a second inlet 27 to the four-way valve 8. In addition there is also a so-called bypass 28 for the refrigerant 4, which is arranged to send heated high-pressure steam directly from the compressor 5, via a hot gas valve 13, to the evaporator 1, without passing the first expansion valve 7 or the second expansion valve 15.
    Function heating operation During times when there is a heat demand, the heat recovery 10 is primarily used to recover heat energy from the exhaust air 18 and heat the supply air 21. According to the example in figure 2, the adjustable rotary heat recovery 10 is run at maximum speed for maximum heat recovery.
    Thus, the temperature T1 after the heat recovery 10 becomes low and not infrequently the exhaust air 18 also contains some moisture. The temperature T1 is measured by a temperature sensor 16, which is located after the heat recovery 10 in the direction of flow of the first air stream 11. When the heat recovery capacity is not sufficient, extra heat must be supplied to the supply air 21, and this according to the invention by means of the heat pump 2. In this case energy is supplied to the compressor 5 to drive the heat pump process and recover additional heat from the exhaust air via evaporator 1 and transfer this heat to the supply air 21 via the condenser 6. The compressor 5 normally controls against the setpoint in the supply air 21 and the heating power that the condenser 6 provides depends on the compressor 5 speed. In the condenser 6, i.e. in the second DX battery 30, which is found in the supply air 21, both compressor heat and condenser heat are emitted to the supply air 21. The cooling effect is emitted in the evaporator 1, i.e. the first DX battery 29, which is found in exhaust air 19, and follows the exhaust air 19 into the open air. The latter is the same as heat being taken up from the exhaust air 18 and thus cooling what then becomes exhaust air 19. During the clean heating operation the hot gas valve 13 is completely closed, while the second expansion valve 15 is completely open and the first expansion valve 7 regulates the refrigerant flow over the evaporator 1 and steers against the so-called overheating, which is described above. The overheating is preferably about 4-8 K for optimal operation.
    When the temperature T1 between the recycler 10 and the evaporator 1 drops to 2-4 ° C, freezing will take place in the evaporator. When the freezing begins and how strong it becomes, depends on the air temperature, humidity and the cooling effect in the evaporator 1. This thus creates the need for defrosting, which can take place in different ways as below.
    Soft defrost In cases where the freezing is in its initial stage or when the conditions are such that short defrost sequences are sufficient to keep the ice formation away, it is possible according to an alternative method to reduce the cooling effect of the evaporator 1 by reducing the compressor 5 and at the same time throttle the second expansion valve 15, which raises the overheating. When the passing first air stream 11 / exhaust air 18 is not cooled down as much as during freezing, due to the reduced cooling effect and at the same time the refrigerant 4 is heated by increased overheating, a double-sided defrosting of the evaporator is obtained, and this method is suitable for fast and recurrent defrosts.
    Fig. 2 shows a preferred embodiment of the invention where the hot gas valve 13 is used for defrosting the evaporator 1, as described below.
    Hot gas defrost When freezing in the evaporator 1 is indicated, the hot gas valve 13 is opened during operation, i.e. at the same time as heating of the supply air 21 takes place via the condenser 6, and hot hot gas is sent via bypass 28 directly to the evaporator 1, to thaw it from inside. Since no energy is supplied via the evaporator 1, the energy is gradually consumed in the system and eventually the energy consists only of supplied compressor energy, unless new energy is supplied. But by instead opening the hot gas valve 13 limited and at the same time increasing the speed of the compressor 5, the defrosting and energy use is controlled and the temperature is raised in the evaporator 1 while heat energy is delivered to the condenser 6. Then it is possible to raise the temperature in the evaporator 1 to a level where freezing disappears at the same time as the energy is sufficient for both defrosting and heating of the supply air 21. In addition, the defrosting of the evaporator 1 is further accelerated by lowering the speed of the rotary heat recovery 10 so that the exhaust air temperature T1 between the rotor and the evaporator 1 increases and defrosting thereby occurs both from outside and inside. Through the reservoir 14 together with the first and second expansion valve 7,15, the overheating and the amount of refrigerant 4 in the system for optimal operation are constantly balanced.
    Preferably, the two expansion valves 7,15 and the hot gas valve 13 are electronically controlled.
    The first expansion valve 7, together with the electronic hot gas valve 13, balances the relationship between hot gas bypass and refrigerant flow over the evaporator 1 while the second expansion valve 15 balances the refrigerant flow over the condenser 6.
    Fig. 3 shows a principle sketch of the heat pump 2 according to the invention during reversible operation for defrosting the evaporator 1. In principle, the figure also shows cooling operation when there is a need for cooling. As with conventional heat pumps, it is quite possible to run the heat pump 2 reversibly for defrosting the evaporator 1. When freezing is indicated in the evaporator 1, the four-way valve 8 switches for reversible operation and sends the hot hot gas / refrigerant 4 directly to the evaporator 1, ie say the first DX battery 29 found in the first air stream 11. In this way the first DX battery 29 is heated from the inside and as the cooling effect then decreases in the evaporator 1 / the first DX battery 29 becomes flowing exhaust air 18 / of | uft 19 warmer and double-sided defrosting of the evaporator 1 / the first DX battery 29 takes place. This can also be advantageously combined with simultaneous down-regulation of the heat recovery, which in the preferred embodiment means a downshifting of the speed of the rotary heat recovery 10. This results in a faster course of the defrosting sequence.
    Thus, by this method, the first DX battery 29, in the first air stream 11, i.e. that which constitutes the evaporator 1 during heating operation, will be heated. The second DX battery 30, on the other hand, is cooled down during the reversible operation, whereby the supply air 21 will be cooled. This can be a disadvantage as the supply air temperature can become too cold for blowing into a room. This of course depends on the type of room that the air handling unit 9 serves, but usually one tries to minimize the oscillation between cold and hot supply air 21. This makes it extra important that the defrosting of the evaporator 1 / the first DX battery 29 takes place quickly, and this is solved by the double-sided defrosting according to the invention.
    Cooling operation During times when there is a need for cooling, the heat recovery unit 10 is primarily used to recover cooling from the exhaust air, 18 if the exhaust air 18 is colder than the outdoor air 20, and cool down the supply air 21. According to the example in Figure 3, the adjustable rotary heat recovery system 10 speed for maximum cooling recovery. The four-way valve 8 has switched the flow direction of the refrigerant 4 to reversible operation, in this case cooling operation. The compressor 5 controls against the setpoint in the supply air 21 and the cooling power emitted by the cooling circuit depends on the speed of the compressor 5. From the second DX battery 30, cooling is now emitted to the supply air 21, while the condenser heat and the compressor heat are emitted in the first DX battery 29 and follow the exhaust air 19 out to the surroundings. Thus, in pure cooling operation, the first DX battery 29 constitutes condenser 6, and the second DX battery 30 thus evaporator 1. During cooling operation, the hot gas valve 13 is completely closed, while the first expansion valve 7 is completely open and the second expansion valve regulates the refrigerant the second DX battery 30 and controls against the setpoint for overheating.
    For optimal cooling operation, the overheating is preferably about 4-8 K. 12 BOME LIST 1 = evaporator 2 = heat pump 3 = refrigerant system 4 = refrigerant = compressor 6 = Condenser 7 = first expansion valve 8 = four-way valve 9 = Air treatment unit = heat recovery 1 1 = first air flow second air flow 13 = hot gas valve 14 = reservoir = second expansion valve 16 = temperature sensor 17 = liquid separator 18 = exhaust air 19 = exhaust air = outdoor air 21 = supply air 22 = exhaust air fl genuine 23 = supply air kt genuine 24 = first inlet = first outlet 26 = second outlet 27 = second inlet 28 = bypass 29 = first DX battery = second DX battery
    权利要求:
    Claims (12)
    [1]
    Method for defrosting an evaporator (1) in a heat pump (2), which heat pump (2) comprises a refrigerant system (3) with a refrigerant (4) and in the flow direction arranged at least one compressor (5), at least one condenser ( 6), at least a first expansion valve (7) and at least one evaporator (1), and further the heat pump (2) comprises at least one four-way valve (8) which is arranged in the flow direction after the compressor (5) and before the condenser (6), and further the four-way valve (8) is arranged to change the flow direction of the refrigerant (4) in the refrigerant system (3), so-called reversible operation, and furthermore the heat pump (2) is arranged in connection with an air treatment unit (9), which air treatment unit (9) comprises an adjustable heat recovery (10), arranged to recover energy from a first air stream (11) and transfer to a second air stream (12), and the evaporator (1) is arranged in the first air stream (11), in the direction of fate after the heat recovery (10), and the condenser (6) is arranged in the second air stream (12), in the direction of fate after the heat recovery (10), characterized in that when the evaporator (1) is frozen, the temperature of the refrigerant (4) is raised through the evaporator (1), at the same time as the heat recovery (10) is regulated down, i.e. the heat recovery is reduced, whereby a simultaneous heating takes place of the evaporator (1), from inside of the refrigerant (4) with elevated temperature, and from outside of the first air stream (11), whose temperature increases when the heat recovery decreases, and thus the evaporator is defrosted (1).
    [2]
    Method according to claim 1, characterized in that the temperature rise of the refrigerant (4) during defrosting takes place by the heat pump (2) running reversibly by the four-way valve (8) changing the flow direction of the refrigerant (4) in the refrigerant system (3), wherein heated refrigerant (4) ) is sent to the evaporator (1) instead of to the condenser (6).
    [3]
    Method according to claim 1, characterized in that the temperature increase of the refrigerant (4) during defrosting takes place in that the heat pump (2) comprises a hot gas valve (13), which is arranged in the efter direction of direction after the compressor (5), and where the hot gas valve (13) completely or partially opens during operation and thus controls a subset of hot refrigerant (4) directly to the evaporator (6) without the refrigerant (4) passing the first expansion valve (7), at the same time as the remaining subset of the refrigerant (4) is supplied to the condenser (6) .
    [4]
    Method according to Claim 3, characterized in that the speed of the compressor (5) is increased at the same time as the hot gas valve (13) opens in whole or in part.
    [5]
    Method according to Claim 1, characterized in that the temperature increase of the refrigerant (4) during defrosting takes place by reducing the cooling effect in the evaporator (1) by reducing the speed of the compressor (5).
    [6]
    Method according to one of the preceding claims, characterized in that the temperature (T1) between the heat recovery (10) and the evaporator (1) is measured and when the evaporator (1) is frozen, the choice of defrosting method is determined by the temperature ( T1).
    [7]
    Method according to one of the preceding claims, characterized in that the heat pump (2) further comprises a reservoir (14) and a second expansion valve (15), which are arranged between the first expansion valve (7) and the condenser (6), and that the the first expansion valve (7) regulates the refrigerant fl fate (4) over the evaporator (1) and the second expansion valve (15) regulates the refrigerant level in the reservoir (14) in coordination with the first valve (7), in order to obtain a controlled amount of refrigerant (4) and a balanced back pressure in the condenser (6) at partial load of the compressor (5).
    [8]
    Method according to claim 7, characterized in that the defrosting takes place by raising the overheating above the normally set operating value, by reducing the speed of the compressor (5) and at the same time throttling the first expansion valve (7), and thereby reducing the cooling effect in the evaporator (1) -
    [9]
    Device for defrosting an evaporator (1) in a heat pump (2), which heat pump (2) comprises a refrigerant system (3) with a refrigerant (4) and in the flow direction arranged at least one compressor (5), at least one condenser ( 6), at least a first expansion valve (7) and at least one evaporator (1), and further the heat pump (2) comprises at least one four-way valve (8) which is arranged in the flow direction after the compressor (5) and before the condenser (6), and further the four-way valve (8) is arranged to change the flow direction of the refrigerant (4) in the refrigerant system (3), so-called reversible operation, and furthermore the heat pump (2) is arranged in connection with an air treatment unit (9), which air treatment unit (9) comprises an adjustable heat recovery (10), arranged to recover energy from a first air stream (11) and transfer to a second air stream (12), and the evaporator (1) is arranged in the first air stream (11), in the flow direction after the heat recovery (10), and the condenser(6) is arranged in the second air stream (12), in the flow direction after the heat recovery (10), characterized by the heat pump (2) comprising a hot gas valve (13), which is arranged in the direction of fate of the refrigerant (4) after the compressor (5), and where the hot gas valve (13) is arranged to be fully or partially opened during operation and thereby control a subset of heated refrigerant (4) directly to the evaporator (1) without the refrigerant (4) passing the first expansion valve (7), at the same time as the remaining subset of the refrigerant (4) is supplied to the condenser (6).
    [10]
    Device according to claim 9, characterized in that the heat pump (2) comprises a reservoir (14) and a second expansion valve (15), which are arranged between the first expansion valve (7) and the condenser (6), and that the first expansion valve ( 7) is arranged to regulate the refrigerant fl the fate of the evaporator (1) and the second expansion valve (15) is arranged to regulate the refrigerant level in the reservoir (14) in coordination with the first expansion valve (7), in order to obtain a controlled amount of refrigerant (4) and a balanced back pressure in the condenser (6) at partial load of the compressor (5). 15
    [11]
    Device according to one of Claims 9 or 10, characterized in that a temperature sensor (16) is arranged between the heat recovery (10) and the evaporator (1).
    [12]
    Device according to one of Claims 9 to 11, characterized in that the heat pump (2) comprises a liquid separator (17), which is arranged in the flow direction before the compressor (5) and after the four-way valve (8).
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    同族专利:
    公开号 | 公开日
    JP2015535071A|2015-12-07|
    US20150292786A1|2015-10-15|
    EP2936008A4|2016-09-07|
    SE537022C2|2014-12-09|
    CN104813122A|2015-07-29|
    KR101576431B1|2015-12-21|
    RU2015114916A|2016-11-10|
    US9423164B2|2016-08-23|
    HK1211079A1|2016-05-13|
    KR20150062172A|2015-06-05|
    RU2638704C2|2017-12-15|
    CN104813122B|2017-08-29|
    WO2014098724A1|2014-06-26|
    EP2936008A1|2015-10-28|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1200784A|SE537022C2|2012-12-21|2012-12-21|Process and apparatus for defrosting an evaporator wide air handling unit|SE1200784A| SE537022C2|2012-12-21|2012-12-21|Process and apparatus for defrosting an evaporator wide air handling unit|
    JP2015541742A| JP2015535071A|2012-12-21|2013-12-03|Method and apparatus for defrosting an evaporator for an air conditioner|
    KR1020157011524A| KR101576431B1|2012-12-21|2013-12-03|Method and apparatus for defrosting of an evaporator in connection with an air handling unit|
    PCT/SE2013/051440| WO2014098724A1|2012-12-21|2013-12-03|Method and apparatus for defrosting of an evaporator in connection with an air handling unit|
    RU2015114916A| RU2638704C2|2012-12-21|2013-12-03|Method and device for defrosting evaporator relating to for air conditioning unit|
    CN201380061069.9A| CN104813122B|2012-12-21|2013-12-03|For a pair method and apparatus for the evaporator deicing being connected with air-conditioning unit|
    EP13864219.4A| EP2936008A4|2012-12-21|2013-12-03|Method and apparatus for defrosting of an evaporator in connection with an air handling unit|
    US14/441,347| US9423164B2|2012-12-21|2013-12-03|Method and apparatus for the defrosting of an evaporator in connection with an air handling unit|
    HK15111641.3A| HK1211079A1|2012-12-21|2015-11-26|Method and apparatus for defrosting of an evaporator in connection with an air handling unit|
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