JP6644620B2 - Bleeding device, refrigerator provided with the same, and method of controlling bleeding device - Google Patents

Description

  The present invention relates to an air extraction device for extracting non-condensable gas such as air that has entered a refrigerator, a refrigerator equipped with the air extraction device, and a method of controlling the air extraction device.

  In refrigeration equipment using a refrigerant whose operating pressure during operation is partially negative in the machine (so-called low-pressure refrigerant), non-condensable gas such as air enters the machine from the negative pressure section and passes through a compressor and the like. Stay in the condenser. When the non-condensable gas stays in the condenser, the condensation performance of the refrigerant in the condenser is hindered, and the performance as a refrigeration equipment is reduced. For this reason, constant performance is ensured by extracting air from the refrigerator and discharging non-condensable gas to the outside of the device. By the bleeding, the non-condensable gas is drawn into the bleeding device together with the refrigerant gas, and the refrigerant is cooled and condensed, whereby the non-condensable gas is separated from the refrigerant and discharged out of the machine by an exhaust pump or the like (see Patent Document 1 below). And 2).

JP 2001-50618 A JP 2006-38346 A

  However, if the operation of the air extraction device is excessively continued without appropriately performing the operation stop timing, the refrigerant may be excessively bled from the refrigerator to reduce the performance of the refrigerator.

  The present invention has been made in view of such circumstances, and a bleed device capable of appropriately determining the timing of operation stop and preventing excessive continuation of operation, a refrigerator including the same, and a control method of the bleed device. The purpose is to provide.

In order to solve the above-mentioned problems, a bleeding apparatus of the present invention, a refrigerator including the bleeding apparatus, and a method of controlling the bleeding apparatus employ the following means.
That is, the bleeding device according to the present invention includes: a bleeding pipe for bleeding a mixed gas containing a refrigerant and a non-condensable gas from a refrigerator; a bleeding tank for storing the mixed gas bleeding from the bleeding pipe; A condenser that cools and condenses the refrigerant in the mixed gas, a drain pipe that discharges the liquid refrigerant in the bleed tank to the refrigerator, and a non-condensable gas in the mixed gas in the bleed tank. An exhaust pipe that is discharged to the outside, and a control unit that stops the operation of the bleeding device when the amount of discharged non-condensable gas discharged from the exhaust pipe exceeds the amount of intruded non-condensable gas that has entered the refrigerator. It is characterized by having.

When the inside of the bleeding tank is cooled by the cooler, the pressure in the bleeding tank decreases, so that a differential pressure with the refrigerant system (for example, a condenser) of the refrigerator is formed, and the bleeding tank is moved from the refrigerator to the bleeding tank through the bleeding pipe. A mixed gas containing a refrigerant and a non-condensable gas is drawn. In the bleed tank, the refrigerant in the mixed gas is condensed by the cooler to become a liquid refrigerant and is accumulated below the bleed tank. On the other hand, the non-condensable gas in the mixed gas introduced into the bleed tank remains in the bleed tank without being condensed even when cooled by the cooler. Thereby, the refrigerant and the non-condensable gas are separated in the extraction tank. The separated non-condensable gas is discharged to the outside via an exhaust pipe. The liquid refrigerant accumulated in the bleeding tank is discharged to a refrigerator (for example, an evaporator) via a drain pipe, and is reused in the refrigerator.
When the amount of non-condensable gas discharged from the exhaust pipe exceeds the amount of infiltration non-condensable gas that has entered the refrigerator, the bleed device is stopped. Excessive operation continuation can be prevented.

  Further, in the bleeding device of the present invention, the control unit is configured to control the discharge based on a non-condensable gas density in the bleed tank obtained from a temperature and a pressure in the bleed tank and a discharge gas amount from the exhaust pipe. It is characterized by obtaining the amount of non-condensable gas.

  When only the refrigerant is present in the bleed tank, the pressure and temperature in the bleed tank have a saturated relationship. However, when the non-condensable gas is contained in the bleeding tank, the bleeding tank pressure increases by the partial pressure of the non-condensable gas in accordance with the density of the non-condensable gas contained. By utilizing this, the density of the non-condensable gas was determined from the temperature and the pressure in the extraction tank. That is, by obtaining the partial pressure of the refrigerant in the extraction tank from the temperature in the extraction tank and subtracting the partial pressure of the refrigerant from the pressure in the extraction tank, the partial pressure of the non-condensable gas is obtained. Then, the density of the non-condensable gas can be obtained from the partial pressure of the non-condensable gas using the equation of state of the ideal gas. If the density of the non-condensable gas is obtained, the amount of the discharged non-condensable gas can be obtained using the amount of the exhaust gas from the exhaust pipe. The exhaust gas amount can be determined, for example, from the differential pressure of the exhaust pipe during exhaust and the exhaust time, or can be determined from the internal volume of the extraction tank and the pressure difference before and after exhaust.

  Further, in the bleeding device of the present invention, the control unit obtains the amount of the infiltrating non-condensable gas based on a differential pressure between a pressure in a refrigerant system of the refrigerator and a pressure outside the refrigerator. .

  When the pressure in the refrigerant system of the refrigerator becomes lower than the pressure outside the refrigerator, the non-condensable gas enters the refrigerant system of the refrigerator. Then, based on the pressure difference between the pressure inside the refrigerant system of the refrigerator and the pressure outside the refrigerator, the amount of infiltration non-condensable gas is obtained.

  Further, in the bleeding device of the present invention, the control unit stops the operation of the bleeding device when the increase in the partial pressure of the non-condensable gas in the bleeding tank within a predetermined time is equal to or less than a set value. It is characterized by doing.

  If the increase in the partial pressure of the non-condensable gas in the bleed tank is equal to or less than the set value, it can be determined that the non-condensable gas in the bleed tank is substantially exhausted, so the bleed device is stopped.

  Further, a refrigerator according to the present invention includes the air extraction device according to any one of the above.

  Since any one of the above-described air extraction devices is provided, it is possible to provide a refrigerator capable of preventing excessive operation continuation of the air extraction device.

  In addition, the control method of the extraction device of the present invention includes an extraction pipe for extracting a mixed gas containing a refrigerant and a non-condensable gas from a refrigerator, an extraction tank for storing the mixed gas extracted from the extraction pipe, and an extraction tank. A cooler for cooling the inside of the tank to condense the refrigerant in the mixed gas, a drain pipe for discharging the liquid refrigerant in the bleeding tank to the refrigerator, and a non-condensation in the mixed gas in the bleeding tank An exhaust pipe that discharges gas to the outside, the method comprising: The operation of the bleeding device is stopped.

  By appropriately determining the timing of stopping the operation of the air extraction device, it is possible to prevent the operation of the air extraction device from continuing excessively.

It is a schematic structure figure showing the refrigerator using the bleeding device concerning one embodiment of the present invention. It is the schematic block diagram which showed the periphery of the air extraction apparatus of FIG. 5 is a flowchart illustrating the operation of the air extraction device. 5 is a flowchart illustrating the operation of the air extraction device. 5 is a flowchart illustrating the operation of the air extraction device.

Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
FIG. 1 shows a schematic configuration of a refrigerator using the extraction device of the present invention. As shown in FIG. 1, the refrigerator 1 is a turbo refrigerator, and includes a turbo compressor 11 for compressing a refrigerant and a condenser 12 for condensing a high-temperature and high-pressure gas refrigerant compressed by the compressor 11. An expansion valve 13 for expanding the liquid refrigerant from the condenser 12, an evaporator 14 for evaporating the liquid refrigerant expanded by the expansion valve 13, and air (non-condensable gas) that has entered the refrigerant system of the refrigerator 1. ) To the atmosphere, and a control device (control unit) 16 that controls each unit included in the refrigerator 1 as main components.
As the refrigerant, for example, a low-pressure refrigerant such as HFO-1233zd (E) is used, and a low-pressure portion such as an evaporator becomes lower than the atmospheric pressure during operation.

  The compressor 11 is a multi-stage centrifugal compressor driven by the inverter motor 20. The output of the inverter motor 20 is controlled by the control device 16.

The condenser 12 is, for example, a shell-and-tube heat exchanger. The condenser 12 has a cooling water heat transfer tube 12a through which cooling water for cooling the refrigerant flows. A cooling water going pipe 22a and a cooling water returning pipe 22b are connected to the cooling water heat transfer pipe 12a. The cooling water guided to the condenser 12 via the cooling water outgoing pipe 22a is guided to a cooling tower (not shown) via a cooling water returning pipe 22b and exhausted to the outside. It is led to the condenser 12 again.
The cooling water delivery pipe 22a is provided with a cooling water pump (not shown) for supplying cooling water, and a cooling water inlet temperature sensor 23a for measuring a cooling water inlet temperature Tcin. The cooling water return pipe 22b is provided with a cooling water outlet temperature sensor 23b for measuring a cooling water outlet temperature Tcout and a cooling water flow sensor 24 for measuring a cooling water flow rate F2.
The condenser 12 is provided with a condenser pressure sensor 25 for measuring the condensation pressure Pc in the condenser 12.
The measured values of these sensors 23a, 23b, 24, 25 are transmitted to the control device 16.

  The expansion valve 13 is of an electric type, and the opening thereof is set by the control device 16.

The evaporator 14 is, for example, a shell-and-tube heat exchanger. The evaporator 14 has a cold water heat transfer tube 14a through which cold water that exchanges heat with the refrigerant flows. The cold water heat transfer pipe 14a is connected to a cold water outgoing pipe 32a and a cold water return pipe 32b. The chilled water guided to the evaporator 14 through the chilled water outgoing pipe 32a is cooled to a rated temperature (for example, 7 ° C.), supplied to an external load (not shown) through the chilled water return pipe 32b, and supplied with chilled water. The evaporator 14 is again guided to the evaporator 14 via the outgoing pipe 32a.
The cold water outgoing pipe 32a is provided with a cold water pump (not shown) for supplying cold water and a cold water inlet temperature sensor 33a for measuring a cold water inlet temperature Tin. The chilled water return pipe 32b is provided with a chilled water outlet temperature sensor 33b for measuring a chilled water outlet temperature Tout and a chilled water flow sensor 34 for measuring a chilled water flow rate F1.
The evaporator 14 is provided with an evaporator pressure sensor 35 for measuring the evaporating pressure Pe in the evaporator 14.
The measurement values of these sensors 33a, 33b, 34, 35 are transmitted to the control device 16.

A bleed device 15 is provided between the condenser 12 and the evaporator 14. The bleed device 15 is connected to a bleed pipe 17 that guides a mixed gas containing a refrigerant and a non-condensable gas (air) from the condenser 12. The bleeding pipe 17 is provided with a bleeding solenoid valve (bleeding valve) 18 for controlling the flow and cutoff of the mixed gas. The opening and closing of the bleed solenoid valve 18 is controlled by the control device 16.
A drain pipe 19 for discharging the liquid refrigerant condensed in the extraction device 15 to the evaporator 14 is connected to the extraction device 15. The drainage pipe 19 is provided with a drainage electromagnetic valve (drainage valve) 21 for controlling the flow and shutoff of the liquid refrigerant. The opening and closing of the drain electromagnetic valve 21 is controlled by the control device 16.

  FIG. 2 shows a configuration around the extraction device 15. The bleeding device 15 includes a bleeding tank 40 that stores a mixed gas containing a refrigerant and an uncondensable gas introduced from the bleeding pipe 17. The bleeding tank 40 is provided with a cooler 42 for cooling the inside of the bleeding tank 40 and a heater 44 for heating the inside of the bleeding tank 40.

  The cooler 42 has a Peltier element, and is provided so that the cooling heat transfer surface 42 a cooled by the Peltier element is exposed in the bleeding tank 40. The cooling heat transfer surface 42 a is provided along the vertical direction of the bleeding tank 40. A power supply unit (not shown) is connected to the Peltier element of the cooler 42. By controlling the current flowing to the power supply unit by the control device 16, the start and stop of the cooler 42 can be switched. The Peltier element of the cooler 42 is provided with a heat radiating portion (not shown) for releasing the heat absorbed by the cooling heat transfer surface 42a to the outside. The heat radiating unit is provided with a water cooling device that allows cooling water to flow, and radiates heat at a constant temperature. Note that the heat radiating section may be an air-cooled type without a water cooling device.

  The heater 44 is, for example, an electric heater, and is attached to the bottom of the bleeding tank 40. The start and stop of the heater 44 are controlled by the control device 16.

The bleeding tank 40 is provided with a bleeding tank pressure sensor 46 for detecting the pressure Pt in the bleeding tank 40 and a bleeding tank temperature sensor 48 for detecting the temperature Tt in the bleeding tank 40. The measurement values of these sensors 46 and 48 are transmitted to the control device 16.
An exhaust pipe 50 for discharging gas (mainly non-condensable gas) in the bleed tank 40 is connected to an upper portion of the bleed tank 40. The exhaust pipe 50 is provided with an exhaust solenoid valve (exhaust valve) 52 for controlling gas flow and shutoff. The opening and closing of the exhaust electromagnetic valve 52 is controlled by the control device 16.

  The control device 16 has a function of controlling the number of revolutions of the compressor 11 and the like based on a measurement value received from each sensor and a load factor sent from a higher system, a control function of the bleed device 15, and the like. I have.

  The control device 16 includes, for example, a CPU (Central Processing Unit) (not shown), a memory such as a RAM (Random Access Memory), and a computer-readable recording medium. A series of processes for realizing various functions described below are recorded in a recording medium or the like in the form of a program, and the CPU reads the program into a RAM or the like to execute information processing and arithmetic processing. Thereby, various functions described below are realized.

  Since the refrigerator 1 described above uses a low-pressure refrigerant, air, which is an uncondensable gas, enters the refrigerator 1 from the negative pressure portion during operation. As the negative pressure portion, a region where the pressure becomes relatively low mainly during a refrigeration cycle of an evaporator or the like can be given, but in winter, the condenser 12 can also have a negative pressure. The air that has entered the refrigerator 1 is mainly accumulated in the condenser 12. The air extraction device 15 operates the air accumulated in the condenser 12 at predetermined intervals to discharge the air in the refrigerator 1 to the outside.

Next, the operation of the bleeding device 15 will be described with reference to FIGS.
Table 1 summarizes the operation states of the Peltier element, each solenoid valve, and the like in each step described below. In the table below, a mark indicates ON or open, and a mark indicates OFF or closed.

  During the operation of the refrigerator 1, if the amount of air that is the non-condensable gas has entered the refrigerator 1 is less than a predetermined value, the air extraction device 15 is stopped (step S1). At this time, the Peltier element of the cooler 42 is turned off, the bleed solenoid valve 18 and the exhaust solenoid valve 52 are closed, the drain solenoid valve 21 is open, and the heater 44 is off.

In step S2, the calculation of the amount of air entering the refrigerant system of the refrigerator 1 is performed as follows. The control device 16 acquires the condensing pressure Pc from the condenser pressure sensor 25 and the evaporating pressure Pe from the evaporator pressure sensor 35, and calculates the differential pressure between the atmospheric pressure in the condenser 12 and the evaporator 14 according to the following equation. Do so.
Differential pressure (condenser) = Atmospheric pressure-Condensing pressure Pc (1)
Differential pressure (evaporator) = atmospheric pressure−evaporation pressure Pe (2)
Then, based on Expressions (1) and (2), the air intrusion amount (instantaneous value) is calculated as in the following expression.
Air penetration (instantaneous value) = f (differential pressure) (3)
That is, the amount of air intrusion (instantaneous value) is a function of the differential pressure (for example, a function of the square of the differential pressure), and is the sum of the amount of air intrusion in the condenser 12 and the amount of air intrusion in the evaporator 14.
The amount of air (integrated value) that has entered the refrigerant system of the refrigerator 1 is calculated as a value obtained by integrating the amount of air that has entered (instantaneous value) with time.
Air penetration (integrated value) = Σ air penetration (instantaneous value) (4)

When the air intrusion amount (integrated value) calculated as described above exceeds a predetermined set value (step S3), preparation for starting the air extraction device 15 is performed (step S4). Specifically, the Peltier element of the cooler 42 is turned on, and the drain electromagnetic valve 21 is closed. Thereby, the inside of the bleeding tank 40 becomes a closed space, and heat is absorbed from the cooling heat transfer surface 42a by cooling by the Peltier element. Due to the heat absorption from the cooling heat transfer surface 42a, the temperature in the bleeding tank 40 decreases and the pressure in the bleeding tank 40 also decreases.
When the value obtained by subtracting the bleed tank pressure Pt obtained by the bleed tank pressure sensor 46 from the condensed pressure Pc obtained by the condenser pressure sensor 25 exceeds the set value (step S5), the bleed solenoid valve 18 is opened. (Step S6).

By opening the bleed solenoid valve 18, a mixed gas containing refrigerant and air flows from the condenser 12 through the bleed pipe 17 into the bleed tank 40 in accordance with the pressure difference between the condenser 12 and the bleed tank 40. Flow in. In the bleeding tank 40, the refrigerant is cooled down to a condensation temperature or lower and liquefied by cooling from the cooling heat transfer surface 42a. On the other hand, the air that is the non-condensable gas stays in the extraction tank 40 in a gas state without being condensed even by cooling from the cooling heat transfer surface 42a.
As will be described below, the liquid level of the liquid refrigerant condensed in the bleeding tank 40 and accumulated below the bleeding tank 40 is detected by two methods.

[Liquid level detection by pressure change (step S7)]
As shown in step S7, when the value obtained by subtracting the bleed tank pressure Pt obtained by the bleed tank pressure sensor 46 from the condensing pressure Pc obtained by the condenser pressure sensor 25 exceeds the set value, the bleed tank 40 It is determined that the liquid level of the liquid refrigerant inside has risen. This set value is determined in advance by a test or the like.

Since the cooling heat transfer surface 42a is installed in the bleed tank 40 in the height direction (see FIG. 2), when the liquid level of the liquid refrigerant accumulated below the bleed tank 40 rises, the cooling heat transfer surface 42a is cooled. The surface 42a is submerged in liquid refrigerant from below. When the cooling heat transfer surface 42a is submerged by the liquid refrigerant, the heat transfer area for cooling the gas is reduced, so that the condensing ability is reduced. When the condensing capacity decreases, the pressure Pt in the bleeding tank 40 increases, and the pressure difference between the condensing pressure Pc of the condenser 12 and the condensing pressure Pc decreases. As described above, when the inside of the bleeding tank 40 is cooled, the pressure in the bleeding tank 40 decreases. However, as the refrigerant condenses in the bleeding tank 40, the liquid refrigerant is accumulated in the bleeding tank 40 and the cooling heat transfer surface 42a Is covered by the liquid refrigerant, the pressure Pt in the bleeding tank 40 increases and the pressure Pt decreases. Therefore, the pressure Pt in the bleeding tank 40 is measured by the bleeding tank pressure sensor 46, and it is determined that the measured value decreases and then increases to a predetermined value or more, and that the differential pressure from the condensing pressure Pc exceeds the set value. Then, the rise of the liquid level of the liquid refrigerant in the bleeding tank 40 is detected.
When the rise in the liquid level of the liquid refrigerant in the bleeding tank 40 is detected as described above, the process proceeds to step S10, and the liquid is discharged.

[Liquid level detection by calculation (Steps S8 and S9)]
In the detection of the liquid level of the liquid refrigerant by calculation, as shown in step S8, the refrigerant condensation amount is calculated.
First, in order to calculate the refrigerant condensation amount (instantaneous value), the temperature in the bleed tank 40 is obtained. Specifically, the bleeding tank temperature Tt is obtained by the bleeding tank temperature sensor 48. When the temperature sensor 48 for the extraction tank is not used, the temperature of the extraction tank may be calculated from the extraction tank pressure Pt obtained by the pressure sensor 46 for the extraction tank. Specifically, the saturation temperature obtained from the bleed tank pressure Pt is defined as the bleed tank temperature.

Then, the refrigerant condensation amount (instantaneous value) is obtained from the cooling capacity of the cooler 42 and the latent heat of condensation of the refrigerant.
The cooling capacity of the Peltier element used in the cooler 42 is determined by the difference between the heat absorption side temperature and the heat radiation temperature and the current flowing through the Peltier element. Assuming that the heat radiation temperature (cooling water temperature or outside air temperature) and the current flowing through the Peltier element are constant, the cooling capacity Qp_W [W] is calculated as a function of the heat absorption side temperature (≒ extraction tank internal temperature Tt) as follows. .
Qp_W = f (Tt) (5)
Since the condensation latent heat Q_LH [kJ / kg] of the refrigerant is the difference between the gas enthalpy and the liquid enthalpy at the saturation temperature (saturation pressure), it is defined as a function of the temperature Tt in the bleed tank for each refrigerant as in the following equation. .
Q_LH = f (Tt) (6)
Based on the cooling capacity Qp_W and the latent heat of condensation Q_LH obtained as described above, the refrigerant condensation amount (instantaneous value) G_in_ref [kg / h] is calculated as follows.
G_in_ref = Qp_W / Q_LH × 3600/10 ³ (7)
By integrating the refrigerant condensed amount (instantaneous value) obtained by the above equation (7) with time, the refrigerant condensed amount (integrated value) is obtained.
Refrigerant condensed amount (integrated value) = ΣRefrigerant condensed amount (instantaneous value) (8)

  When the refrigerant condensed amount (integrated value) exceeds the set value (step S9), it is determined that the liquid level of the liquid refrigerant in the bleeding tank 40 has increased, and the process proceeds to step S10 to perform drainage.

  In step S10, the liquid discharge electromagnetic valve 21 is opened, and the liquid refrigerant in the bleed tank 40 is discharged. The liquid refrigerant in the bleed tank 40 is guided to the evaporator 14 through the drain pipe 19.

  After a certain period of time has passed since the electromagnetic valve 21 was opened in step S10, the electromagnetic valve 21 was closed, and the drainage was terminated (step S11). This fixed time is set in advance by a test before installing the refrigerator 1 or the like.

Next, the determination as to whether or not to discharge the air, which is the non-condensable gas stored in the bleeding tank 40, to the outside (atmosphere) via the exhaust pipe 50 is performed by detecting the following two methods. Do.
[Detection by Pressure Change (Step S12)]
When the liquid refrigerant is discharged from the bleed tank 40 in step S10, the immersion of the cooling heat transfer surface 42a of the cooler 42 is eliminated and the cooling capacity is restored, so that the pressure in the bleed tank 40 decreases. However, if air, which is an uncondensable gas, stays in the bleeding tank 40 for a predetermined amount or more, the air covers the cooling heat transfer surface 42a and the heat transfer performance is impaired. Therefore, if the pressure in the bleed tank 40 does not drop below the predetermined value after the liquid refrigerant is drained, it can be determined that the air remains in the bleed tank 40 for a predetermined amount or more. Therefore, in step S12, when the difference value obtained by subtracting the bleeding tank pressure Pt obtained by the bleeding tank pressure sensor 46 from the condensing pressure Pc obtained by the condenser pressure sensor 25 remains above the set value, that is, If the extraction tank pressure Pt does not drop below the predetermined value, it is determined that air is remaining in the extraction tank 40 for a predetermined amount or more.
If it is determined that the air remains in the bleeding tank 40 for a predetermined amount or more, the process proceeds to step S15 to prepare for exhaust.

[Detection by Calculation (Steps S13 and S14)]
In step S13, the air amount (integrated value) in the bleeding tank, which is the amount of air retained in the bleeding tank 40, is obtained by calculation. Specifically, it is calculated based on the air intrusion amount (integrated value) calculated in step S2 described above. When the amount of air in the bleed tank (integrated value) exceeds the set value (step S14), it is determined that air has stayed in the bleed tank 40 for a predetermined amount or more, and the process proceeds to step S15, where the exhaust gas is discharged. Get ready.

  In step S15, preparation for exhausting the gas in the bleeding tank 40 is performed. Specifically, the Peltier element of the cooler 42 is turned off, the bleed solenoid valve 18 is closed, and the heater 44 is turned on. Thereby, the inside of the bleeding tank 40 is sealed and the temperature inside rises, so that the pressure in the bleeding tank 40 rises. If the bleed tank pressure Pt obtained from the bleed tank pressure sensor 46 increases and exceeds a set value (atmospheric pressure + α) higher than the atmospheric pressure by a predetermined value α (step S16), the process proceeds to step S17. Proceed and start exhausting.

  In step S17, the exhaust electromagnetic valve 52 is opened, and the heater 44 is turned off. As a result, the gas mainly containing air in the bleeding tank 40 is discharged to the outside (atmosphere) through the exhaust pipe 50. The reason why the heater 44 is turned off at this time is that the refrigerant remaining in the bleeding tank 40 is not released to the outside more than necessary.

When the pressure in the bleeding tank 40 falls below a set value (atmospheric pressure + β) higher than the atmospheric pressure by a predetermined value β (step S18), the process proceeds to step S19. The reason for setting this set value to a pressure higher than the atmospheric pressure by the predetermined value β is that if the exhaust solenoid valve 52 is opened until the pressure falls below the atmospheric pressure, the air flows backward and is guided into the extraction tank 40. This is to prevent it.
In step S19, the exhaust electromagnetic valve 52 is closed to end the exhaust.

Next, the process proceeds to step S20 and thereafter, and it is determined that the air extraction device 15 is stopped.
In step S20, the exhaust air amount (integrated value), which is the total amount of air exhausted to the outside (atmosphere) via the exhaust pipe 50, is calculated. Specifically, it is as follows.
First, in order to obtain the air density ρ_t_air [kg / m ³ ] in the bleed tank 40, the refrigerant saturation pressure Pt_ref [MPa (abs)] in the bleed tank 40 is calculated. The refrigerant saturation pressure Pt_ref in the bleed tank 40 is a saturated pressure corresponding to the temperature Tt in the bleed tank 40. The relational expression between the saturation pressure and the saturation temperature can be defined as the following expression as a function of the saturation temperature for each refrigerant.
Pt_ref = f (Tt) (9)
Then, the air partial pressure Pt_air [MPa (abs)] in the bleed tank 40 can be calculated using the bleed tank pressure Pt (total pressure) as in the following equation.
Pt_air = Pt-Pt_ref (10)
Therefore, the air mass w_t_air [kg] in the bleeding tank 40 is expressed by the following equation from the ideal gas state equation.
w_t_air = Pt_air × Vt × M_air / (R × Tt) (11)
Here, Vt is the volume [m ³ ] of the extraction tank 40, M_air is the molecular weight of air [kg / mol], R is the gas constant, and Tt is the temperature [K] in the extraction tank 40.
Therefore, the air density ρ_t_air in the bleeding tank 40 is as follows.
ρ_t_air = w_t_air / Vt (12)

As described above, when the air density ρ_t_air in the bleeding tank 40 is obtained, the exhaust air amount w_ex_air [kg] is calculated.
The exhaust gas volume V_ex [m ³ ] is estimated from the differential pressure between the pressure Pt in the bleeding tank 40 and the atmospheric pressure Pa, and the time Time_ex [sec] during which the exhaust electromagnetic valve 52 was opened in step S17.
V_ex = f (Pt-Pa, Time_ex) (13)
Note that the exhaust gas volume V_ex may be obtained from the volume Vt of the bleed tank 40 and the pressure difference between before and after the exhaust, instead of the above equation (13).
Using the exhaust gas volume V_ex obtained by the above equation and the air density ρ_t_air in the bleeding tank 40, the exhaust air amount w_ex_air is calculated as in the following equation.
w_ex_air = V_ex × ρ_t_air (14)

Since the exhaust air amount w_ex_air obtained by the above equation (14) is a value per one exhaust, when a plurality of exhausts are performed, the exhaust air amount w_ex_air is multiplied by the number of exhausts n. The obtained value is the discharged air amount (integrated value).
Discharged air amount (integrated value) = w_ex_air × n (15)
When the discharged air amount (integrated value) is obtained as described above, the process proceeds to step S21.

In step S21, it is determined whether or not the discharged air amount (integrated value) has exceeded the intruded air amount (integrated value) obtained in step S2.
If the discharged air amount (integrated value) exceeds the intruded air amount (integrated value), it is determined that the air has been sufficiently exhausted, the process proceeds to step S23, and the extraction device 15 is stopped.

On the other hand, if the discharged air amount (integrated value) does not exceed the intruded air amount (integrated value), the process returns to step S4, and the above-described bleeding, draining, and discharging are repeated.
Further, even when the discharged air amount (integrated value) does not exceed the intruded air amount (integrated value), as shown in step S22, the air partial pressure in the bleeding tank 40 within a predetermined time period is set. If the rise of Pt_air (see equation (10)) is equal to or less than the set value, the process proceeds to step S23, and the extraction device 15 is stopped. In this step S22, even if the calculation of the discharged air amount (integrated value) or the intruded air amount (integrated value) is inaccurate for some reason, the increase of the air partial pressure in the extraction tank 40 is set. If the value is equal to or less than the value, it can be determined that the air in the bleeding tank 40 is substantially exhausted.

  In step S23 for stopping the air extraction device 15, the drainage electromagnetic valve 21 is opened. Thereby, the inside of the bleeding tank 40 is communicated with the evaporator 14. This is to prevent the pressure inside the bleeding tank 40 from rising due to the influence of the outside air temperature.

As described above, according to the present embodiment, the following operation and effect can be obtained.
As described in steps S20 and S21, when the amount of exhaust air (integrated value) discharged from the exhaust pipe 50 exceeds the amount of intruded air (integrated value) that has entered the refrigerator 1, the air extraction device 15 is activated. Since the operation is stopped, it is possible to appropriately determine the timing of the operation stop and prevent the bleeding device 15 from continuing excessively.

  When only the refrigerant exists in the bleed tank 40, the pressure Pt and the temperature Tt in the bleed tank 40 have a saturation relationship. However, when air is contained in the bleeding tank 40, the bleeding tank pressure Pt is increased by the partial pressure of air according to the contained air density. By utilizing this, the air density is obtained from the temperature Tt and the pressure Pt in the bleeding tank 40 (see equations (9) to (12)). As described above, by simply obtaining the temperature Tt and the pressure Pt of the bleeding tank 40, the air density can be obtained by calculation, and the amount of exhaust air can be obtained by calculation.

  As described in step S22, in consideration of the case where the calculation of the discharged air amount (integrated value) or the intruded air amount (integrated value) is inaccurate for some reason, the discharged air amount (integrated value) is determined in step S21. Even if the integrated value) does not exceed the intruded air amount (integrated value), if the increase in the air partial pressure in the extraction tank 40 is equal to or less than the set value, the air in the extraction tank 40 is substantially exhausted. Therefore, it was decided to stop the bleeding device. This can prevent the bleed device 15 from continuing excessively.

  Note that the configuration of the refrigerator 1 shown in FIG. 1 is an example, and is not limited to this configuration. For example, an air heat exchanger may be provided in place of the water-cooled condenser 12 so as to exchange heat between the outside air and the refrigerant. Further, the refrigerator 1 is not limited to the case having only the cooling function, and may be, for example, a refrigerator having only the heat pump function, or having both the cooling function and the heat pump function.

  Further, a Peltier element is used as a cooling device used for the cooler 42. However, the present invention is not limited to this, and any other device can be used as long as the inside of the bleeding tank 40 can be cooled below the condensation temperature of the refrigerant. Cooling device.

  Further, although an electric heater is used as the heater 44, the present invention is not limited to this, and a heat transfer tube through which a high-temperature refrigerant flows is used as long as it can heat the inside of the bleeding tank 40. Other types of heaters such as heaters may be used.

DESCRIPTION OF SYMBOLS 1 Refrigerator 11 Compressor 12 Condenser 13 Expansion valve 14 Evaporator 15 Extraction device 16 Control device (control part)
17 Bleed piping 18 Bleed solenoid valve (Bleed valve)
19 Drainage pipe 20 Inverter motor 21 Drainage solenoid valve (Drainage valve)
22a Cooling water going pipe 22b Cooling water returning pipe 23a Cooling water inlet temperature sensor 23b Cooling water outlet temperature sensor 24 Cooling water flow sensor 25 Condenser pressure sensor 32a Cold water going pipe 32b Cold water returning pipe 33a Cold water inlet temperature sensor 33b Cold water outlet temperature sensor 34 Cold water flow sensor 35 Evaporator pressure sensor 40 Extraction tank 42 Cooler 44 Heater 46 Extraction tank pressure sensor 48 Extraction tank temperature sensor 50 Exhaust pipe 52 Exhaust solenoid valve (exhaust valve)

Claims (6)

An extraction pipe for extracting a mixed gas containing a refrigerant and a non-condensable gas from the refrigerator;
An extraction tank that stores the mixed gas extracted from the extraction pipe,
A cooler that cools the bleeding tank and condenses the refrigerant in the mixed gas,
A drain pipe for discharging the liquid refrigerant in the bleeding tank to the refrigerator,
An exhaust pipe for discharging non-condensable gas in the mixed gas in the bleeding tank to the outside,
A control unit that stops the operation of the bleeding device when the amount of discharged non-condensable gas discharged from the exhaust pipe exceeds the amount of intruded non-condensable gas that has entered the refrigerator.
A bleeding device comprising:   The controller is configured to obtain the discharged non-condensable gas amount from a non-condensable gas density in the bleed tank obtained from a temperature and a pressure in the bleed tank and a discharge gas amount from the exhaust pipe. The bleed device according to claim 1, wherein   3. The bleed air according to claim 1, wherein the control unit obtains the amount of the infiltrating non-condensable gas based on a differential pressure between a pressure inside a refrigerant system of the refrigerator and a pressure outside the refrigerator. 4. apparatus.   2. The controller according to claim 1, wherein the controller stops the operation of the bleeding device when a rise in the partial pressure of the non-condensable gas in the bleeding tank within a predetermined time period is equal to or less than a set value. 3. The bleed device according to any one of claims 1 to 3.   A refrigerator comprising the bleed device according to any one of claims 1 to 4. An extraction pipe for extracting a mixed gas containing a refrigerant and a non-condensable gas from the refrigerator;
An extraction tank that stores the mixed gas extracted from the extraction pipe,
A cooler that cools the bleeding tank and condenses the refrigerant in the mixed gas,
A drain pipe for discharging the liquid refrigerant in the bleeding tank to the refrigerator,
An exhaust pipe for discharging non-condensable gas in the mixed gas in the bleeding tank to the outside,
A method of controlling a bleeding apparatus comprising:
A method for controlling a bleed device, wherein the operation of the bleed device is stopped when the amount of non-condensable gas discharged from the exhaust pipe exceeds the amount of non-condensable gas that has entered the refrigerator.

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