CN203203287U - Turbine refrigerating machine - Google Patents
Turbine refrigerating machine Download PDFInfo
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- CN203203287U CN203203287U CN201320113337.4U CN201320113337U CN203203287U CN 203203287 U CN203203287 U CN 203203287U CN 201320113337 U CN201320113337 U CN 201320113337U CN 203203287 U CN203203287 U CN 203203287U
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- 238000005057 refrigeration Methods 0.000 claims description 65
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- 238000000926 separation method Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
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Abstract
The utility model relates to a turbine refrigerating machine. When the turbine refrigerating machine starts to run, the situation that refrigerating fluid liquid drops are sucked from an economizer to an intermediate stage of a multi-stage compressor can be avoided. The turbine refrigerating machine comprises an evaporator, the multi-stage turbine compressor, a condenser and an intermediate cooler, namely the economizer, and further comprises a control device and a control valve. The evaporator captures heat from fluid to be cooled to evaporate refrigerating fluid so as to achieve the refrigerating effect, the multi-stage turbine compressor compresses the refrigerating fluid through a multi-stage impeller, the condenser uses refrigerating fluid gas after the refrigerating fluid gas is cooled and compressed by cooling fluid to condensate the turbine refrigerating machine, the intermediate cooler enables a part of condensed refrigerating fluid liquid to be evaporated, supplies evaporated refrigerating fluid gas to the intermediate part of a multi-stage compression stage of the multi-stage turbine compressor, the control device conduct control to enable the control valve to be closed when the refrigerating machine starts to run and enable the control valve to be opened after the refrigerating machine starts to run and a pressure difference of the condenser and the evaporator is higher than the authorized pressure, and the control valve is arranged in a flowing way where the economizer is communicated with the intermediate part of the multi-stage compression stage of the multi-stage turbine compressor to open and close the flowing way.
Description
Technical field
The utility model relates to the turborefrigerator that possesses energy-saving appliance, particularly relates to the turborefrigerator that uses the multi-stage compression economizer cycle.
Background technology
In the past, the turborefrigerator that utilizes in the refrigerating air conditioning device etc., there is the closed system of cold-producing medium to consist of by inclosure, will be from cold water (fluid is cooled) thus capture heat and make the evaporimeter of cold-producing medium evaporation performance refrigeration, will be by above-mentioned evaporator evaporation the refrigerant gas compression, make it become the compressor of the refrigerant gas of high pressure, by cooling water (cooling fluid) refrigerant gas of high pressure is cooled off and make the condenser of its condensation, above-mentioned condensed cold-producing medium is reduced pressure and the expansion valve (expansion mechanism) that makes its expansion links by refrigerant piping and consists of.And, the compound compressor that refrigerant gas carries out multi-stage compression is used as in the situation of compressor by multi-stage impeller in use, carry out to be directed into the action (for example, patent documentation 1) of the intergrade (mid portion of multi-stage impeller) of compressor by the refrigerant gas that the intercooler in the refrigerant piping that is arranged between condenser and the evaporimeter that is energy-saving appliance produce.
Patent documentation 1: TOHKEMY 2009-236430 communique
In possessing the turborefrigerator of above-mentioned energy-saving appliance, utilize energy-saving appliance that liquid refrigerant is separated with refrigerant gas, and the refrigerant gas after will separating is directed into the intergrade (mid portion of multi-stage impeller) of compound compressor, and the refrigeration as kind of refrigeration cycle integral body is increased.In the situation that makes the turborefrigerator running that possesses energy-saving appliance, near specified running, pressure differential between condenser and the evaporimeter is sufficient, therefore cold-producing medium turns back to evaporimeter from condenser via energy-saving appliance, do not exist liquid refrigerant to be trapped in the interior situation of energy-saving appliance, thereby effectively bring into play the gas-liquid separating function of energy-saving appliance.
Yet when the running of refrigeration machine began, the pressure differential between condenser and the evaporimeter did not produce, thus cold-producing medium to evaporimeter to return situation bad, liquid refrigerant can be trapped in the energy-saving appliance.
In recent years, the requirement that the refrigeration machine miniaturization is reduced arrange the space is more and more higher, and energy-saving appliance also is in the trend that realizes as far as possible miniaturization.Therefore when the refrigeration machine entry into service, also there is the impaired situation of function that causes demister because of the liquid refrigerant that is detained in the energy-saving appliance, can't give full play to the gas-liquid separating function of energy-saving appliance, so the cold-producing medium drop can be inhaled into the intergrade (mid portion of multi-stage impeller) of multistage turbocompressor.That is, the transfer (carry-over) of the cold-producing medium drop of the intergrade from energy-saving appliance to multistage turbocompressor occurs, so the cold-producing medium drop can contact with the impeller in the High Rotation Speed.The frequency that starting stops to uprise, and impeller suffers erosion if such situation continues then for a long time, can reduce the performance of compressor.The problem that also has in addition the stable running that can't carry out compressor.
The utility model content
The utility model is In view of the foregoing made, and its purpose is to provide a kind of turborefrigerator, when the running of refrigeration machine begins, can prevent the suction of the cold-producing medium drop of the intergrade from energy-saving appliance to compound compressor.
For achieving the above object, the first mode of turborefrigerator of the present utility model is a kind of turborefrigerator, possesses: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that, also possess: control device, control valve and difference gauge measurement unit, described control device carries out the open and close controlling of described control valve according to the pressure differential that is obtained by described difference gauge measurement unit, described control device controls so that cut out first described control valve when the running of refrigeration machine begins, after running beginning, reach authorized pressure when above when the pressure differential of described condenser and described evaporimeter, open described control valve, described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, and described difference gauge measurement unit carries out instrumentation to the pressure differential of described condenser and described evaporimeter.
According to the utility model, when the running of refrigeration machine begins, close by the control valve that will be arranged in the stream that connects energy-saving appliance and multistage turbocompressor, control thus so that the cold-producing medium drop can not be inhaled into (transfer) to the mid portion of the multi-stage compression level of multistage turbo-compressor.And, after running beginning, reach authorized pressure when above, the control of opening control valve when the pressure differential of condenser and evaporimeter.This be because, after the running of refrigeration machine begins, the pressure differential of condenser and evaporimeter increases gradually, therefore liquid refrigerant can not be trapped in the energy-saving appliance but therefore Returning evaporimeter can prevent that the mid portion of the multi-stage compression level of cold-producing medium drop from energy-saving appliance to multistage turbocompressor from shifting.
Wherein, the pressure differential of so-called condenser and evaporimeter (Δ P) is more than the authorized pressure, for example, in the situation that use R134a as cold-producing medium, refers to that the pressure differential (Δ P) of condenser and evaporimeter is for more than the 0.2MPa.Although afore mentioned rules pressure is different because of the kind of cold-producing medium, but with normal operation (for example, 6 ℃ of evaporating temperatures, 38 ℃ of condensation temperatures) under the condensing pressure determined by the cold-producing medium physical characteristic and the difference of evaporating pressure be benchmark, and consider it is when turning round beginning, by obtaining accordingly the difference of the condensing pressure that determined by the cold-producing medium physical characteristic and evaporating pressure and definite value with the temperature difference (for example, 13 ℃) of evaporating temperature and condensation temperature.
According to optimal way of the present utility model, described difference gauge measurement unit comprises: be arranged at the pressure gauge of described condenser and be arranged at the pressure gauge of described evaporimeter.
According to optimal way of the present utility model, the pressure differential of described condenser and described evaporimeter does not reach in the situation more than the authorized pressure after the running of refrigeration machine begins even described control device is controlled, from beginning, running through after the stipulated time, also opens described control valve.
Usually, after the running of turborefrigerator begins, the pressure differential (Δ P) of short time (1～a few minutes) inner condenser and evaporimeter can reach authorized pressure (for example, 0.2MPa) more than.Yet, under the condition of the exception of excessively low situation of the temperature of cooling water etc., exist pressure differential (Δ P) not reach the situation of authorized pressure.In this situation, use economizer cycle even open control valve, because cooling load is that circulating mass of refrigerant itself is less, so the cold-producing medium drop is extremely low from the possibility that energy-saving appliance is transferred to multistage turbocompressor.Therefore in the utility model, the running from refrigeration machine begin in the situation through stipulated time (for example, passing through 30 minutes), open control valve, bring into use economizer cycle.
According to optimal way of the present utility model, possesses the liquid level gauge measurement unit that the liquid level of described energy-saving appliance is carried out instrumentation, described control device controls so that cut out first described control valve when the running of refrigeration machine begins, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve.
According to optimal way of the present utility model, possesses the thermometer measurement unit, its temperature to the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance is carried out instrumentation, described control device is controlled so that open first described control valve in the operation process of refrigeration machine, in operation process, when the fluctuation of repeatedly change occurs the instrumentation value that is obtained by described thermometer measurement unit, close described control valve.
The second mode of turborefrigerator of the present utility model is a kind of turborefrigerator, possesses: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that, also possess: control device, control valve and liquid level gauge measurement unit, described control device carries out the open and close controlling of described control valve according to the liquid level that is obtained by described liquid level gauge measurement unit, described control device controls so that cut out first described control valve when the running of refrigeration machine begins, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve, described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, and described liquid level gauge measurement unit carries out instrumentation to the liquid level of described energy-saving appliance.
For energy-saving appliance, be to consist of at the top of the container-like accumulating part that stockpiles liquid refrigerant configuration demister, utilize demister with drop separation contained in the cold-producing medium, and drop is recycled to container-like accumulating part.Yet, when the running of refrigeration machine begins, owing to liquid refrigerant is trapped in the energy-saving appliance, so near the lower end or lower end of the liquid level of liquid refrigerant arrival demister, therefore have the situation of the gas-liquid separating function that diminishes demister.Through after the stipulated time, the liquid level line of energy-saving appliance for example reaches normal level after 1～2 minute from the running of refrigeration machine begins, therefore from running begins through the stipulated time after, beginning instrumentation liquid level line after 1～2 minute for example.If the distance from the liquid level line of energy-saving appliance to the lower end of demister be predetermined distance (for example, 100mm) more than, then do not have the transfer of cold-producing medium drop, therefore open control valve, bring into use economizer cycle.
Wherein, the liquid level of so-called energy-saving appliance is that specified altitude refers to, the liquid level that the cold-producing medium drop shifts from energy-saving appliance to multistage turbocompressor can not occur the distance from the liquid level line of energy-saving appliance to the lower end of demister enough (for example, more than 100mm).Above-mentioned liquid level line from energy-saving appliance (100mm) is the numerical value of obtaining by experiment for example, to the distance of the lower end of demister.
According to optimal way of the present utility model, described liquid level gauge measurement unit comprises liquid level meter.
According to optimal way of the present utility model, liquid level through described energy-saving appliance after the stipulated time surpasses in the situation of described specified altitude from the running of refrigeration machine begins even described control device is controlled, if the pressure differential of described condenser and described evaporimeter is more than the authorized pressure, then open described control valve.
According to the utility model, even the running from refrigeration machine begin through the stipulated time after the liquid level of energy-saving appliance surpass in the situation of specified altitude, if the pressure differential of condenser and evaporimeter (Δ P) is more than the authorized pressure, then do not exist the cold-producing medium drop to be transferred to the worry of multistage turbocompressor, therefore open control valve, bring into use economizer cycle.Afore mentioned rules pressure is for example in the situation that use R134a to be 0.2MPa as cold-producing medium.
The Third Way of turborefrigerator of the present utility model is a kind of turborefrigerator, possesses: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that, also possess: control device, control valve and thermometer measurement unit, described control device carries out the open and close controlling of described control valve according to the instrumentation value that is obtained by described thermometer measurement unit, described control device is controlled so that open first described control valve in the operation process of refrigeration machine, in operation process when the fluctuation of repeatedly change occurs in the instrumentation value that is obtained by described thermometer measurement unit, close described control valve, described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, and described thermometer measurement unit carries out instrumentation to the temperature of the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance.
According to the utility model, when the cold-producing medium drop was inhaled into the mid portion of multi-stage compression level of multistage turbocompressor if produce the transfer of cold-producing medium drop, then the cold-producing medium drop can the contact thermometer measurement unit.So, because the cold-producing medium drop is immediately in the surface evaporation of thermometer measurement unit, so detected temperatures reduces.Because the cold-producing medium drop is the contact thermometer measurement unit repeatedly, so the what is called fluctuation of repeatedly change occurs in the thermometer measured value.So in the utility model, when fluctuation occurs in the instrumentation value of thermometer measurement unit, closed control valve.
According to optimal way of the present utility model, described thermometer measurement unit comprises the temperature sensor of the mid portion of the multi-stage compression level that is arranged at described multistage turbocompressor.
According to optimal way of the present utility model, described control device controls so that after cutting out described control valve, when the liquid level of the pressure differential of described condenser and described evaporimeter or described energy-saving appliance satisfies rated condition, opens described control valve.
According to the utility model, after closed control valve, when the liquid level of the pressure differential of condenser and evaporimeter or energy-saving appliance satisfies rated condition, there is not the worry of the transfer of cold-producing medium drop, therefore open control valve, the use of beginning economizer cycle.
Wherein, the pressure differential of so-called condenser and above-mentioned evaporimeter or the liquid level of above-mentioned energy-saving appliance refer to following situation when satisfying rated condition: during closed control valve, measure the pressure differential (Δ P) of condenser and evaporimeter, and measure the liquid level (H1) of energy-saving appliance, afterwards, exceed authorized pressure (for example, 0.05MPa) above situation in the pressure differential (Δ P2) of condenser and the evaporimeter pressure differential (Δ P1) during than closed control valve; The liquid level (H1) of the energy-saving appliance when perhaps the liquid level of energy-saving appliance (H2) is with closed control valve is compared low specified altitude (for example, 20mm) above situation.Afore mentioned rules pressure (for example, 0.05MPa) and the afore mentioned rules height (20mm) be the numerical value of obtaining by experiment for example.
The first mode of the control method of turborefrigerator of the present utility model is a kind of control method of turborefrigerator, and this turborefrigerator possesses: possess: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor; Control valve, it is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, the control method of described turborefrigerator is characterised in that, when beginning, the running of refrigeration machine closes first described control valve, after running beginning, reach authorized pressure when above when the pressure differential of described condenser and described evaporimeter, open described control valve.
According to optimal way of the present utility model, the pressure differential of described condenser and described evaporimeter is carried out instrumentation by the pressure gauge that is arranged at described condenser and the pressure gauge that is arranged at described evaporimeter.
According to optimal way of the present utility model, even the pressure differential of described condenser and described evaporimeter does not reach in the situation more than the authorized pressure after the running of refrigeration machine begins, from beginning, running through after the stipulated time, also opens described control valve.
According to optimal way of the present utility model, when the running of refrigeration machine begins, close first described control valve, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve.
According to optimal way of the present utility model, in the operation process of refrigeration machine, open first described control valve, in operation process, when the fluctuation of repeatedly change occurs the thermometer measured value of the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance, close described control valve.
The second mode of the control method of turborefrigerator of the present utility model is a kind of control method of turborefrigerator, and this turborefrigerator possesses: possess: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor; Control valve, it is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, the control method of described turborefrigerator is characterised in that, when beginning, the running of refrigeration machine closes first described control valve, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve.
According to optimal way of the present utility model, the liquid level of described energy-saving appliance is carried out instrumentation by liquid level meter.
According to optimal way of the present utility model, even the running from refrigeration machine begin through the stipulated time after the liquid level of described energy-saving appliance surpass in the situation of described specified altitude, if the pressure differential of described condenser and described evaporimeter is more than the authorized pressure, then open described control valve.
The 3rd mode of the control method of turborefrigerator of the present utility model is a kind of control method of turborefrigerator, and this turborefrigerator possesses: possess: evaporimeter, thus it is captured heat and refrigeration is brought into play in the cold-producing medium evaporation from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor; Control valve, it is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream is opened and closed, the control method of described turborefrigerator is characterised in that, in the operation process of refrigeration machine, open first described control valve, in operation process, when the fluctuation of repeatedly change occurs the thermometer measured value of the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance, close described control valve.
According to optimal way of the present utility model, be supplied to the temperature of cold-producing medium of mid portion of the multi-stage compression level of described multistage turbocompressor from described energy-saving appliance, carry out instrumentation by the temperature sensor of the mid portion of the multi-stage compression level that is arranged at described multistage turbocompressor.
According to optimal way of the present utility model, after closing described control valve, when the liquid level of the pressure differential of described condenser and described evaporimeter or described energy-saving appliance satisfies rated condition, open described control valve.
The utility model plays the following effect of enumerating.
(1) when the running of refrigeration machine begins, the cold-producing medium drop can not be transferred to from energy-saving appliance the mid portion of the multi-stage compression level of multistage turbocompressor, can avoid the erosion of the impeller that caused by the cold-producing medium drop.Therefore can realize having for a long time the running of the high refrigeration machine of stability and reliability.
(2) in the operation process of refrigeration machine when having produced in the situation that the cold-producing medium drop shifts from energy-saving appliance to multistage turbocompressor, by the control valve between energy-saving appliance and the compressor is closed, can stop rapidly thus the transfer of cold-producing medium drop.
Description of drawings
Fig. 1 is the schematic diagram of an embodiment of expression turborefrigerator of the present utility model.
Fig. 2 (a) and (b), (c) are the runnings that are illustrated in turborefrigerator when beginning and in operation process, the flow chart of the control sequence of implementing by control device according to control method of the present utility model.
Description of reference numerals: 1 ... first order compressor; 2 ... high stage compressor; 3 ... compressor motor; 4 ... condenser; 5 ... evaporimeter; 6 ... energy-saving appliance; 7 ... control valve; 8 ... expansion mechanism; 10,11 ... stream; 20 ... control device; LV ... liquid level meter; P1, P2 ... pressure sensor; T1 ... temperature sensor; TC ... multistage turbocompressor.
The specific embodiment
Below, with reference to Fig. 1 and Fig. 2 the embodiment of turborefrigerator of the present utility model and control method thereof is described.In Fig. 1 and Fig. 2, for identical or suitable inscape, also the repetitive description thereof will be omitted to mark identical Reference numeral.
Fig. 1 is the schematic diagram of an embodiment of expression turborefrigerator of the present utility model.In embodiment shown in Figure 1, the turborefrigerator that has used two-stage compression single-stage economizer cycle is described.As shown in Figure 1, turborefrigerator possesses: the multistage turbocompressor TC of compressed refrigerant; Refrigerant gas after utilizing cooling water (cooling fluid) to compression cools off so that the condenser 4 of its condensation; From cold water (fluid is cooled) thus capture heat and with the evaporimeter 5 of cold-producing medium evaporation performance refrigeration; Be configured in intercooler that is energy-saving appliance 6 between condenser 4 and the evaporimeter 5; Be arranged on the front and back of energy-saving appliance 6 and to condensating refrigerant decompression so that the expansion mechanism 8,8 of its expansion, above-mentioned each equipment linked by the refrigerant piping 9 for refrigerant circulation consist of turborefrigerator.
In embodiment shown in Figure 1, multistage turbocompressor TC is made of the two-stage turbine compressor, constitutes to comprise: first order compressor 1, high stage compressor 2 and drive above-mentioned compressor 1,2 compressor motor 3.The discharge side of first order compressor 1 is connected by stream 10 with the suction side of high stage compressor 2.In multistage turbocompressor TC, the refrigerant gas that imports to first order compressor 1 from evaporimeter 5 carries out first order compression by first order compressor 1, then be directed to the refrigerant gas of high stage compressor 2 by stream 10, carry out second level compression by high stage compressor 2, be sent to afterwards condenser 4.
In addition, energy-saving appliance 6 is connected by stream 11 with above-mentioned stream 10, and the refrigerant gas that is separated by energy-saving appliance 6 is directed to the mid portion (being the part between the first order and the second level in this example) of the multi-stage compression level (being two-stage in this example) of multistage turbocompressor TC.With in energy-saving appliance 6 and the stream 11 that multistage turbocompressor TC is connected, be provided with DYN dynamic control valve 7, this control valve 7 can stop to control to supply and the supply of the compression stage of refrigerant gas from energy-saving appliance 6 to multistage turbocompressor TC.
In the kind of refrigeration cycle of the turborefrigerator that consists of as shown in Figure 1, cold-producing medium circulates in multistage turbocompressor TC, condenser 4, evaporimeter 5 and energy-saving appliance 6, the Cooling and Heat Source that utilization is obtained by evaporimeter 5 is made cold water and corresponding with load, is taken into the heat that comes flash-pot 5 in the kind of refrigeration cycle and the heat suitable with the merit of the multistage turbocompressor TC that supplies with from compressor motor 3 and is released to the cooling water that is supplied to condenser 4.On the other hand, separated refrigerant gas is directed to the mid portion of the multi-stage compression level of multistage turbocompressor TC by energy-saving appliance 6, and compresses from the refrigerant gas of first order compressor 1 interflow and by high stage compressor 2.Adopt two stages of compression single-stage economizer cycle, owing to being attached with the refrigeration part that energy-saving appliance 6 is realized, so this partial response ground can increase refrigeration, compares with the situation that energy-saving appliance 6 is not set, and can realize the high efficiency of refrigeration.
As described above, the turborefrigerator that possesses energy-saving appliance 6 can make up high efficiency kind of refrigeration cycle, but when the running of refrigeration machine begins, owing to not producing the pressure differential between condenser 4 and the evaporimeter 5, therefore cold-producing medium is bad to the situation that evaporimeter 5 returns, and liquid refrigerant can be trapped in the energy-saving appliance 6.Therefore have the impaired situation of function that causes demister because being trapped in energy-saving appliance 6 interior liquid refrigerants, existence can't be given full play to the problem of the mid portion of the gas-liquid separating function of energy-saving appliance 6, multi-stage compression level that the cold-producing medium drop is inhaled into multistage turbocompressor TC.
Therefore, in the utility model, when the running of refrigeration machine begins, the control valve 7 that is arranged in the stream 11 that connects energy-saving appliance 6 and multistage turbocompressor TC is closed, do not control thus so that the cold-producing medium drop do not occur and be inhaled into (transfer) to mid portion of the multi-stage compression level of multistage turbo-compressor TC.
Next, the formation that is used for the control switching of control valve 7 described.
As shown in Figure 1, be respectively arranged with pressure sensor P1, pressure sensor P2 at condenser 4 and evaporimeter 5.Inlet portion at the high stage compressor 2 of multistage turbocompressor TC is provided with the temperature sensor T1 that the entrance refrigerant temperature of high stage compressor is carried out instrumentation.Be provided with liquid level meter LV at energy-saving appliance 6.Pressure sensor P1, pressure sensor P2, temperature sensor T1 and liquid level meter LV are connected with control device 20 respectively.In addition, control valve 7 is connected with control device 20.
According to above-mentioned formation, from the pressure signal S1 of pressure sensor P1, be input to respectively control device 20 from the pressure signal S2 of pressure sensor P2 and from the liquid level line signal S3 of liquid level meter LV, detect pressure differential (Δ P) between condenser 4 and the evaporimeter 5 according to pressure signal S1, S2, detect the liquid level line (L of the liquid refrigerant in the energy-saving appliance 6 according to liquid level line signal S3
H).In addition, the temperature signal S4 from temperature sensor T1 is input to control device 20, the inlet portion refrigerant temperature of detection high stage compressor 2.
In the utility model, when the running of refrigeration machine begins, the control valve 7 that is arranged on the stream 11 that connects energy-saving appliance 6 and multistage turbocompressor TC is closed, do not control thus so that the cold-producing medium drop can not occur and be inhaled into (transfer) to the mid portion of the multi-stage compression level of multistage turbo-compressor TC, but after running beginning, control so that when satisfying the cold-producing medium drop and can not be transferred to the condition of multistage turbocompressor TC side, open control valve 7, make the energy-saving appliance periodic duty.
Next, use the condition of economizer cycle to describe to opening control valve 7 after beginning for the running at refrigeration machine.This condition is obtained according to experiment.
1) under reaching situation more than the authorized pressure, the pressure differential of condenser 4 and evaporimeter 5 opens control valve 7.
Suppose the operating condition (normal operation) of standard, in the situation that use R134a as cold-producing medium, if the evaporating temperature of evaporimeter is 6 ℃, the condensation temperature of condenser is 38 ℃, then owing to the cold-producing medium physical characteristic, evaporating pressure is 0.362MPa, and condensing pressure is 0.963MPa.So the condenser under the operating condition (normal operation) of standard and pressure differential (Δ P) the ≈ 0.6MPa of evaporimeter.
Relative therewith, consider when being the running beginning, if the temperature difference of evaporating temperature and condensation temperature is 13 ℃, the evaporating temperature of evaporimeter is 7 ℃, and the condensation temperature of condenser is 20 ℃, then because the cold-producing medium physical characteristic, evaporating pressure is 0.375MPa, and condensing pressure is 0.572MPa.Condenser when the running that therefore can derive refrigeration machine begins and pressure differential (Δ P) the ≈ 0.2MPa of evaporimeter.That is, if the pressure differential of condenser and evaporimeter (Δ P) is more than the 0.2MPa, consider that then liquid refrigerant can not be trapped in the energy-saving appliance but is back to evaporimeter.
Therefore, invention people of the present utility model use the turborefrigerator that consists of as shown in Figure 1, have repeatedly carried out the starting/stopping experiment while confirm the pressure differential (Δ P) of condenser and evaporimeter.At this moment, come the entrance refrigerant temperature of instrumentation compressor by the temperature sensor T1 of the high stage compressor 2 that is arranged at multistage turbocompressor TC, and have or not the transfer of cold-producing medium drop from the hagioscope observation that is arranged on the stream 11 that connects energy-saving appliance 6 and multistage turbocompressor TC.In this case, the cold-producing medium drop is inhaled into high stage compressor 2 if produce the transfer of cold-producing medium drop, and then the cold-producing medium drop can contact with the temperature sensor T1 of the inlet portion that is arranged at high stage compressor 2.So, the cold-producing medium drop can be immediately in the surface evaporation of temperature sensor T1, so detected temperatures can reduce.Because the cold-producing medium drop is contact temperature sensor T1 repeatedly, therefore can cause that it is so-called fluctuation (hunting) that the thermometer measured value changes repeatedly.This fluctuation refers in the variations in temperature of repeatedly carrying out set point of temperature above (for example, ± 0.5 ℃ more than) in the short time (for example, 5 minutes).That is, can detect according to the instrumentation value of temperature sensor T1 the transfer of cold-producing medium drop.
Like this, by carrying out having or not transfer based on the instrumentation of the entrance refrigerant temperature of the compressor of temperature sensor T1 and from hagioscope observation cold-producing medium drop, if condenser 4 is more than the 0.2MPa with the pressure differential (Δ P) of evaporimeter 5 thus, then can confirm not exist the transfer of cold-producing medium drop.Namely, in the situation that cold-producing medium is R134a, after beginning, the running of refrigeration machine reaches 0.2MPa when above when the pressure differential (Δ P) of condenser 4 and evaporimeter 5, open the control of control valve 7, can prevent that thus the mid portion of the multi-stage compression level of cold-producing medium drop from energy-saving appliance 6 to multistage turbocompressor TC from shifting.
2) under being situation below the specified altitude, the liquid level of energy-saving appliance 6 opens control valve 7.
For energy-saving appliance 6, configure demister 12(with reference to Fig. 1 on the top of the container-like accumulating part that stockpiles liquid refrigerant) and consist of, utilize demister with drop separation contained in the cold-producing medium, and drop is recovered to container-like accumulating part.
Yet when the running of refrigeration machine began, liquid refrigerant was stranded in the energy-saving appliance 6, so the liquid level of liquid refrigerant arrives near the lower end or lower end of demister, and had the impaired situation of gas-liquid separating function of demister.
Therefore, the people of invention of the present utility model on one side use the turborefrigerator that consists of as shown in Figure 1 and utilize liquid level meter LV that the liquid level line of energy-saving appliance 6 is carried out instrumentation and repeatedly carry out starting/stopping and test.At this moment, temperature sensor T1 by the high stage compressor 2 that is arranged at multistage turbocompressor TC, entrance refrigerant temperature to compressor is carried out instrumentation, and observes the cold-producing medium drop have or not transfer from the hagioscope that is arranged at the stream 11 that connects energy-saving appliance 6 and multistage turbocompressor TC.Through after the stipulated time, the liquid level line of energy-saving appliance 6 for example reached normal level after 1～2 minute from the running of refrigeration machine begins.Therefore after after the running beginning 1～2 minute, begin instrumentation liquid level line.
Like this, by carrying out having or not transfer based on the instrumentation of the entrance refrigerant temperature of the compressor of temperature sensor T1 and from hagioscope observation cold-producing medium drop, if the distance from the liquid level line of energy-saving appliance 6 to the lower end of demister is more than the 100mm thus, then can confirm not exist the transfer of cold-producing medium drop.Namely, if the liquid level of the energy-saving appliance 6 the when distance from the liquid level line of energy-saving appliance 6 to the lower end of demister is 100mm is defined as upper limit liquid level, if then the liquid level of energy-saving appliance 6 is below the upper limit liquid level, then carry out control that control valve 7 is opened, can prevent that thus the mid portion of the multi-stage compression level of cold-producing medium drop from energy-saving appliance 6 to multistage turbocompressor TC from shifting.
3) after the running of refrigeration machine begins, open control valve 7 and use in the normal operation process of two-stage compression single-stage economizer cycle, occur in the situation of fluctuation control valve 7 to be closed in the instrumentation value of temperature sensor T1.
Even after the running of refrigeration machine begins, satisfy 1) or 2) condition, control valve 7 opened make the energy-saving appliance periodic duty and when running well, still exist because of the bad grade of demister and can't give full play to the gas-liquid separating function of energy-saving appliance 6, the situation that the cold-producing medium drop is transferred to the intergrade of multistage turbocompressor TC.In this situation, the instrumentation value of temperature sensor T1 that is arranged at the inlet portion of high stage compressor 2 can fluctuate, and therefore rapidly control valve 7 is closed.
Fig. 2 (a) and (b), (c) be the running that is illustrated in turborefrigerator when beginning and in operation process according to above-mentioned 1)～3) the flow chart of the control sequence implemented by control device 20 of control method.
Fig. 2 (a) is that expression has used above-mentioned 1) the flow chart of the running of turborefrigerator of the control method control sequence when beginning.Shown in Fig. 2 (a), after this running of beginning turborefrigerator, judges whether condenser 4 and the pressure differential (Δ P) of evaporimeter 5 reach more than the authorized pressure.In the situation that pressure differential (Δ P) is more than the authorized pressure, open control valve 7, bring into use economizer cycle.In this situation, although authorized pressure is different because of the kind of cold-producing medium, in the situation that R134a is 0.2MPa.In the situation that whether pressure differential (Δ P) less than authorized pressure, is judged and has been passed through the stipulated time from running begins.In the situation that from running begins through the stipulated time, open control valve 7, bring into use economizer cycle.Wherein, the stipulated time for example is 30 minutes, is the time of obtaining according to experiment.In the situation that from running begins, do not pass through the stipulated time determining step of returning pressure poor (Δ P).
Usually, after the running of turborefrigerator begins, can reach more than the authorized pressure (0.2MPa) in short time (1～2 minute) internal pressure differences (Δ P).Yet, under the condition of the exceptions such as the excessively low situation of the temperature of cooling water, exist pressure differential (Δ P) not reach the situation of authorized pressure.In this situation, because cooling load is that circulating mass of refrigerant itself is less, use economizer cycle even therefore open control valve 7, the cold-producing medium drop is also extremely low from the possibility that energy-saving appliance 6 is transferred to multistage turbocompressor TC.Therefore the running from refrigeration machine begin in the situation through stipulated time (for example, passing through 30 minutes), open control valve 7, bring into use economizer cycle.
Fig. 2 (b) is that expression has used above-mentioned 2) the flow chart of the running of turborefrigerator of the control method control sequence when beginning.Shown in Fig. 2 (b), if passed through the stipulated time from the running of beginning turborefrigerator, judge then whether the liquid level of energy-saving appliance 6 is below the above-mentioned upper limit liquid level.Under the liquid level of energy-saving appliance 6 is situation below the upper limit liquid level, open control valve 7, bring into use economizer cycle.Liquid level at energy-saving appliance 6 surpasses in the situation of upper limit liquid level, judges whether condenser 4 and the pressure differential (Δ P) of evaporimeter 5 reach more than the authorized pressure.In the situation that pressure differential (Δ P) is more than the authorized pressure, open control valve 7, bring into use economizer cycle.In this situation, although authorized pressure is different because of the kind of cold-producing medium, in the situation that R134a is 0.2MPa.This is because even it is abundant with the pressure differential of evaporimeter 5 to need only condenser 4 in the high situation of the liquid level of energy-saving appliance 6, then do not exist the cold-producing medium drop to be transferred to the worry of multistage turbocompressor TC.Relative therewith, in the situation that pressure differential (Δ P), is returned the step that the liquid level of energy-saving appliance 6 is judged less than authorized pressure.
Fig. 2 (c) is that expression has used above-mentioned 3) the operation process of turborefrigerator of control method in the flow chart of control sequence.After the running of refrigeration machine begins, even satisfying the condition shown in Fig. 2 (a) or Fig. 2 (b), opening that control valve 7 makes the energy-saving appliance periodic duty and when running well, also exist the bad grade because of demister to cause the situation that the gas-liquid separating function of energy-saving appliance 6 can't be given full play to, the cold-producing medium drop is transferred to the intergrade of multistage turbocompressor TC.Therefore, shown in Fig. 2 (c), in the operation process of turborefrigerator, whether the instrumentation value of the temperature sensor T1 of the inlet portion that is arranged at multistage turbocompressor TC fluctuation is occured judge, in the situation that fluctuation closed control valve 7 has occured, stop rapidly the transfer of cold-producing medium drop.And when having closed control valve 7, measure the pressure differential (Δ P) of condenser 4 and evaporimeter 5, and measure the liquid level (H1) of energy-saving appliance 6.After this, pressure differential (Δ P1) to the pressure differential (Δ P) of condenser 4 and evaporimeter 5 during with closed control valve 7 compares (for example whether to exceed authorized pressure, 0.05MPa) more than, whether the liquid level (H1) of the energy-saving appliance 6 when perhaps the liquid level of energy-saving appliance 6 (H2) is with closed control valve 7 is compared low specified altitude and (for example, is judged more than 20mm).That is, carry out the judgement of following formula.
ΔP2≥ΔP1+0.05MPa·····(1)
H2≤H1-20mm·····(2)
In the situation that satisfy (1) formula or (2) formula, therefore the worry that does not exist the cold-producing medium drop to shift from energy-saving appliance 6 to multistage turbocompressor TC opens control valve 7.All in the ungratified situation, continue closed control valve in any of (1) formula and (2) formula.
So far embodiment of the present utility model is illustrated, but the utility model is not limited to above-mentioned embodiment certainly, can implement in a variety of ways in the scope of its technological thought.
Claims (11)
1. turborefrigerator possesses: evaporimeter, thus it captures heat and with cold-producing medium evaporation performance refrigeration from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that,
Also possess: control device, control valve and difference gauge measurement unit,
Described control device carries out the open and close controlling of described control valve according to the pressure differential that is obtained by described difference gauge measurement unit, described control device controls so that cut out first described control valve when the running of refrigeration machine begins, after running beginning, reach authorized pressure when above when the pressure differential of described condenser and described evaporimeter, open described control valve
Described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream opened and closed,
Described difference gauge measurement unit carries out instrumentation to the pressure differential of described condenser and described evaporimeter.
2. turborefrigerator as claimed in claim 1 is characterized in that,
Described difference gauge measurement unit comprises: be arranged at the pressure gauge of described condenser and be arranged at the pressure gauge of described evaporimeter.
3. turborefrigerator as claimed in claim 1 is characterized in that,
The pressure differential of described condenser and described evaporimeter does not reach in the situation more than the authorized pressure after the running of refrigeration machine begins even described control device is controlled, and through after the stipulated time, opens described control valve from running begins yet.
4. turborefrigerator as claimed in claim 1 is characterized in that,
Possess the liquid level gauge measurement unit that the liquid level of described energy-saving appliance is carried out instrumentation,
Described control device controls so that cut out first described control valve when the running of refrigeration machine begins, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve.
5. turborefrigerator as claimed in claim 1 is characterized in that,
Possess the thermometer measurement unit, its temperature to the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance is carried out instrumentation,
Described control device is controlled so that open first described control valve in the operation process of refrigeration machine, when the fluctuation of repeatedly change occurs the instrumentation value that is obtained by described thermometer measurement unit, closes described control valve in operation process.
6. turborefrigerator possesses: evaporimeter, thus it captures heat and with cold-producing medium evaporation performance refrigeration from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that,
Also possess: control device, control valve and liquid level gauge measurement unit,
Described control device carries out the open and close controlling of described control valve according to the liquid level that is obtained by described liquid level gauge measurement unit, described control device controls so that cut out first described control valve when the running of refrigeration machine begins, from running begins through the stipulated time after the liquid level of described energy-saving appliance be in the situation below the specified altitude, open described control valve
Described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream opened and closed,
Described liquid level gauge measurement unit carries out instrumentation to the liquid level of described energy-saving appliance.
7. turborefrigerator as claimed in claim 6 is characterized in that,
Described liquid level gauge measurement unit comprises liquid level meter.
8. turborefrigerator as claimed in claim 6 is characterized in that,
Liquid level through described energy-saving appliance after the stipulated time surpasses in the situation of described specified altitude from the running of refrigeration machine begins even described control device is controlled, if the pressure differential of described condenser and described evaporimeter is more than the authorized pressure, then open described control valve.
9. turborefrigerator possesses: evaporimeter, thus it captures heat and with cold-producing medium evaporation performance refrigeration from the fluid that is cooled; Multistage turbocompressor, its by multi-stage impeller with refrigerant compression; Condenser, the refrigerant gas after it utilizes cooling fluid to compression cools off so that its condensation; Intercooler that is energy-saving appliance, its make the part evaporation of condensed refrigerant liquid and will evaporate after refrigerant gas be supplied to the mid portion of the multi-stage compression level of described multistage turbocompressor, described turborefrigerator is characterised in that,
Also possess: control device, control valve and thermometer measurement unit,
Described control device carries out the open and close controlling of described control valve according to the instrumentation value that is obtained by described thermometer measurement unit, described control device is controlled so that open first described control valve in the operation process of refrigeration machine, in operation process when the fluctuation of repeatedly change occurs in the instrumentation value that is obtained by described thermometer measurement unit, close described control valve
Described control valve is arranged in described energy-saving appliance and the stream that the mid portion of the multi-stage compression level of described multistage turbocompressor is communicated with, described stream opened and closed,
Described thermometer measurement unit carries out instrumentation to the temperature of the cold-producing medium of the mid portion of the multi-stage compression level that is supplied to described multistage turbocompressor from described energy-saving appliance.
10. turborefrigerator as claimed in claim 9 is characterized in that,
Described thermometer measurement unit comprises the temperature sensor of the mid portion of the multi-stage compression level that is arranged at described multistage turbocompressor.
11. turborefrigerator as claimed in claim 9 is characterized in that,
Described control device controls so that after cutting out described control valve, when the liquid level of the pressure differential of described condenser and described evaporimeter or described energy-saving appliance satisfies rated condition, opens described control valve.
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| JP2012-056231 | 2012-03-13 | ||
| JP2012056231A JP5878046B2 (en) | 2012-03-13 | 2012-03-13 | Turbo refrigerator and control method thereof |
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| CN201310079486.8A Active CN103307795B (en) | 2012-03-13 | 2013-03-13 | Turborefrigerator and control method thereof |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103307795A (en) * | 2012-03-13 | 2013-09-18 | 荏原冷热系统株式会社 | Turborefrigerator and method thereof |
| CN104676936A (en) * | 2013-11-29 | 2015-06-03 | 荏原冷热系统株式会社 | Turbo-refrigerator |
| CN104949370A (en) * | 2014-03-31 | 2015-09-30 | 荏原冷热系统株式会社 | Turbine refrigerator |
| CN104949369A (en) * | 2014-03-31 | 2015-09-30 | 荏原冷热系统株式会社 | Turbine refrigerator |
| CN111587352A (en) * | 2018-01-19 | 2020-08-25 | 住友精密工业株式会社 | Boiling type refrigerator |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2015194301A (en) * | 2014-03-31 | 2015-11-05 | 荏原冷熱システム株式会社 | turbo refrigerator |
| CN106766306A (en) * | 2016-11-29 | 2017-05-31 | 天津商业大学 | A kind of double stage compresses hot pump in low temp system |
| CN106958957A (en) * | 2017-03-31 | 2017-07-18 | 丁金虎 | The centrifugal frequency-changeable compressor group of three-level and control method |
| FR3072160B1 (en) * | 2017-10-09 | 2019-10-04 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | REFRIGERATION DEVICE AND METHOD |
| CN109341153B (en) * | 2018-12-13 | 2024-07-16 | 珠海格力电器股份有限公司 | Refrigerant circulation system and refrigeration equipment |
| EP3997343B1 (en) | 2019-07-01 | 2023-08-09 | Carrier Corporation | Surge protection for a multistage compressor |
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| JPS56142359A (en) * | 1980-04-09 | 1981-11-06 | Hitachi Ltd | Turbo refrigerating machine |
| JPH04313647A (en) * | 1991-04-10 | 1992-11-05 | Matsushita Electric Ind Co Ltd | Heat pump type air conditioner |
| JPH08152210A (en) * | 1994-11-29 | 1996-06-11 | Hitachi Ltd | Refrigerating apparatus |
| JPH0979667A (en) * | 1995-09-19 | 1997-03-28 | Denso Corp | Gas injection type refrigerating cycle equipment |
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| CN100526765C (en) * | 2004-05-28 | 2009-08-12 | 约克国际公司 | System and method for controlling an economizer circuit |
| CN1299084C (en) * | 2004-07-01 | 2007-02-07 | 清华大学 | Double temperature cold water unit for air conditioning system |
| JP2009150594A (en) * | 2007-12-19 | 2009-07-09 | Mitsubishi Heavy Ind Ltd | Refrigeration device |
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| JP5642448B2 (en) * | 2010-08-02 | 2014-12-17 | 三菱重工業株式会社 | Flow rate estimation device, heat source unit, and flow rate estimation method |
| JP5878046B2 (en) * | 2012-03-13 | 2016-03-08 | 荏原冷熱システム株式会社 | Turbo refrigerator and control method thereof |
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2012
- 2012-03-13 JP JP2012056231A patent/JP5878046B2/en active Active
-
2013
- 2013-03-13 CN CN201320113337.4U patent/CN203203287U/en not_active Expired - Lifetime
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103307795A (en) * | 2012-03-13 | 2013-09-18 | 荏原冷热系统株式会社 | Turborefrigerator and method thereof |
| CN103307795B (en) * | 2012-03-13 | 2016-11-16 | 荏原冷热系统株式会社 | Turborefrigerator and control method thereof |
| CN104676936A (en) * | 2013-11-29 | 2015-06-03 | 荏原冷热系统株式会社 | Turbo-refrigerator |
| CN104949370A (en) * | 2014-03-31 | 2015-09-30 | 荏原冷热系统株式会社 | Turbine refrigerator |
| CN104949369A (en) * | 2014-03-31 | 2015-09-30 | 荏原冷热系统株式会社 | Turbine refrigerator |
| CN111587352A (en) * | 2018-01-19 | 2020-08-25 | 住友精密工业株式会社 | Boiling type refrigerator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103307795A (en) | 2013-09-18 |
| JP2013190151A (en) | 2013-09-26 |
| CN103307795B (en) | 2016-11-16 |
| JP5878046B2 (en) | 2016-03-08 |
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