Air conditioning apparatus
First Claim
1. An air conditioning apparatus comprising:
- a refrigerating cycle to connect a compressor, a high-pressure-side heat exchanger, a throttle device and a low-pressure-side heat exchanger by piping, to circulate a refrigerant of high temperature and high pressure in the high-pressure-side heat exchanger, and to circulate a refrigerant of low temperature and low pressure in the low-pressure-side heat exchanger;
a temperature detection part of high-pressure refrigerant to detect a temperature of the refrigerant in the high-pressure-side heat exchanger;
a temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant to detect a temperature of the refrigerant at an entrance side of the high-pressure-side heat exchanger;
a temperature detection part of high-pressure-side heat exchanger exit-side refrigerant to detect a temperature of the refrigerant at an exit side of the high-pressure-side heat exchanger;
a fluid temperature detection part to detect a temperature at a location of the fluid circulating outside of the high-pressure-side heat exchanger;
a calculation comparison part to calculate a first value obtained by dividing a supercooling degree SC which is obtained by subtracting the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant from the temperature detected by the temperature detection part of high-pressure refrigerant, by dTc which is a value obtained by subtracting the temperature detected by the fluid temperature detection part from the temperature detected by the temperature detection part of high-pressure refrigerant, and 1−
EXP(−
NTUR) as a second value based on NTUR which is obtained by calculating (Δ
HCON×
AL)/(dTc×
Cpr×
A) (where Δ
HCON is an enthalpy difference between an enthalpy at the entrance of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant and the temperature detected by the temperature detection part of high-pressure refrigerant and an enthalpy at the exit of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant and the temperature detected by the temperature detection part of high-pressure refrigerant, AL is a heating surface area of liquid phase of the high-temperature-side heat exchanger, A is a heating surface area of the high-temperature-side heat exchanger, and Cpr is a specific heat at constant pressure of the refrigerant), and compare the first value calculated and the second value calculated; and
a judgment part to judge a refrigerant leak based on a comparison result of the calculation comparison part.
1 Assignment
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Accused Products
Abstract
By studying or storing refrigerating cycle characteristics of an air conditioning apparatus at the normal time and comparing them with refrigerating cycle characteristics acquired from the air conditioning apparatus at the time of operation, it becomes possible to exactly and accurately diagnose normality or abnormality of the air conditioning apparatus under any installation conditions and environmental conditions, which eliminates operations of inputting a difference between apparatus model names, a piping length, a height difference, etc at the time of apparatus installation. Accordingly, it aims at shortening the time of judging normality or abnormality, and improving the operability. It is characterized by calculating and comparing a measured value (a value of liquid phase temperature efficiency εL (SC/dTc) calculated from temperature information) concerning an amount of a liquid phase part of the refrigerant in the high-pressure-side heat exchanger with a theoretical value (a value of liquid phase temperature efficiency εL (1−EXP(−NTUR)) calculated from the transfer unit number NTUR at refrigerant side).
55 Citations
14 Claims
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1. An air conditioning apparatus comprising:
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a refrigerating cycle to connect a compressor, a high-pressure-side heat exchanger, a throttle device and a low-pressure-side heat exchanger by piping, to circulate a refrigerant of high temperature and high pressure in the high-pressure-side heat exchanger, and to circulate a refrigerant of low temperature and low pressure in the low-pressure-side heat exchanger; a temperature detection part of high-pressure refrigerant to detect a temperature of the refrigerant in the high-pressure-side heat exchanger; a temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant to detect a temperature of the refrigerant at an entrance side of the high-pressure-side heat exchanger; a temperature detection part of high-pressure-side heat exchanger exit-side refrigerant to detect a temperature of the refrigerant at an exit side of the high-pressure-side heat exchanger; a fluid temperature detection part to detect a temperature at a location of the fluid circulating outside of the high-pressure-side heat exchanger;
a calculation comparison part to calculate a first value obtained by dividing a supercooling degree SC which is obtained by subtracting the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant from the temperature detected by the temperature detection part of high-pressure refrigerant, by dTc which is a value obtained by subtracting the temperature detected by the fluid temperature detection part from the temperature detected by the temperature detection part of high-pressure refrigerant, and 1−
EXP(−
NTUR) as a second value based on NTUR which is obtained by calculating (Δ
HCON×
AL)/(dTc×
Cpr×
A) (where Δ
HCON is an enthalpy difference between an enthalpy at the entrance of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant and the temperature detected by the temperature detection part of high-pressure refrigerant and an enthalpy at the exit of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant and the temperature detected by the temperature detection part of high-pressure refrigerant, AL is a heating surface area of liquid phase of the high-temperature-side heat exchanger, A is a heating surface area of the high-temperature-side heat exchanger, and Cpr is a specific heat at constant pressure of the refrigerant), and compare the first value calculated and the second value calculated; anda judgment part to judge a refrigerant leak based on a comparison result of the calculation comparison part. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12)
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13. An air conditioning apparatus comprising:
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a refrigerating cycle to connect a compressor, a high-pressure-side heat exchanger, a throttle device and a low-pressure-side heat exchanger by piping, to circulate a refrigerant of high temperature and supercritical pressure in the high-pressure-side heat exchanger, and to circulate a refrigerant of low temperature and low pressure in the low-pressure-side heat exchanger; a pressure detection part of high-pressure refrigerant to detect a pressure of the refrigerant in the high-pressure-side heat exchanger;
a temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant to detect a temperature of the refrigerant at an entrance side of the high-pressure-side heat exchanger; a temperature detection part of high-pressure-side heat exchanger exit-side refrigerant to detect a temperature of the refrigerant at an exit side of the high-pressure-side heat exchanger; a fluid temperature detection part to detect a temperature at a location of the fluid circulating outside of the high-pressure-side heat exchanger; a calculation comparison part to calculate a first value obtained by dividing SC which is a value obtained by subtracting the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant from an imaginary saturation temperature which is a temperature of the refrigerant in a case wherein an enthalpy of a refrigerant at the pressure detected by the pressure detection part of high-pressure refrigerant is an enthalpy at a critical point of the refrigerant, by dTc which is a value obtained by subtracting the temperature detected by the fluid temperature detection part from the imaginary saturation temperature, and 1−
EXP(−
NTUR) as a second value based on NTUR which is obtained by calculating (Δ
HCON×
AL)/(dTc×
Cpr×
A) (where Δ
HCON is an enthalpy difference between an enthalpy at the entrance of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger entrance-side refrigerant and the pressure detected by the pressure detection part of high-pressure refrigerant and an enthalpy at the exit of the high-pressure-side heat exchanger which is calculated from the temperature detected by the temperature detection part of high-pressure-side heat exchanger exit-side refrigerant and the pressure detected by the pressure detection part of high-pressure refrigerant, AL is a heating surface area of liquid phase of the high-temperature-side heat exchanger, A is a heating surface area of the high-temperature-side heat exchanger, and Cpr is a specific heat at constant pressure of the refrigerant), and compare the first value calculated and the second value calculated; anda judgment part to judge a refrigerant leak based on a comparison result of the calculation comparison part. - View Dependent Claims (14)
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Specification