EP1275917B1 - Method for limiting the condensation pressure in a refrigerating machine - Google Patents
Method for limiting the condensation pressure in a refrigerating machine Download PDFInfo
- Publication number
- EP1275917B1 EP1275917B1 EP02014999A EP02014999A EP1275917B1 EP 1275917 B1 EP1275917 B1 EP 1275917B1 EP 02014999 A EP02014999 A EP 02014999A EP 02014999 A EP02014999 A EP 02014999A EP 1275917 B1 EP1275917 B1 EP 1275917B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- condensation
- saturation temperature
- temperature
- superheating
- evaporator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
- F25B49/027—Condenser control arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/07—Exceeding a certain pressure value in a refrigeration component or cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2513—Expansion valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/195—Pressures of the condenser
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/197—Pressures of the evaporator
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2117—Temperatures of an evaporator
- F25B2700/21175—Temperatures of an evaporator of the refrigerant at the outlet of the evaporator
Definitions
- the present invention relates to a method for limiting the condensation pressure of a refrigerating machine according to the preamble of claim 1. Such a method is known from EP-A-1 050 727 .
- the refrigerating capacity of a refrigerating machine increases with the saturation temperature at evaporation, which in turn is linked to the temperature of the refrigerated fluid.
- the increase in refrigerating capacity also entails automatically an increase in the thermal power that the refrigerating machine must dissipate at the condenser.
- an increase in the saturation temperature at evaporation (which generally depends on an increase in the temperature of the cooled fluid) leads to an increase in the saturation temperature at condensation.
- a decrease in refrigerating capacity automatically leads to a decrease in the thermal power to be dissipated at the condenser and therefore to a decrease in the saturated temperature at condensation for an equal temperature of the hot source.
- condensation temperature tends to approach the safety value that would require shutting down the machine, it is possible to limit this rise by reducing the refrigerating capacity absorbed by the evaporator, since this is equivalent to a reduction in the thermal power affecting the condenser.
- US-A-4 523 435 discloses a refrigeration system wherein the flow of refrigerant from the refrigerant condenser to the refrigerant evaporator is controlled by an adjustable expansion valve which is responsive to superheat of the refrigerant to be compressed. Adjusting the refrigerant flow in response to both the magnitude of the superheat and the rate at which it is changing, allows to stabilize the system with respect to the over and under-corrections of refrigerant flow that afflict the known systems. Therefore, the system of US-A-4 523 435 is suitable to prevent excessive variations of the operative conditions. This result is achieved by means of a fast adjustment of the expansion valve.
- EP-A-1 050 727 discloses a system suitable to automatically reach a minimum value for the condensation temperature in compliance with the functional parameters of the refrigerating machine. With this method, if the opening of the valve exceeds a pre-set value the condensation pressure is increased in order to have the correct pressure values at the inlet and output of the valve.
- JP-A-03164658 and DE-A-43 03 533 concern control systems suitable to prevent excessive temperature at the delivery (high pressure side) of the compressor by means of increasing the opening of the electronic expansion valve, which results in an overfeeding of the evaporator.
- the control systems are based on the measurement of the high pressure side (delivery) pressure. In these systems, the expansion valve is opened only if the delivery temperature exceeds a pre-set value.
- EP-A-1 134 518 discloses a method for controlling the electronic expansion valve of a refrigerating machine, the method including the steps of monitoring a change in temperature between the fluid in a flooded cooler and a saturated suction temperature of the system, monitoring the discharge superheat of the system, and correcting the opening of the expansion valve when the discharge superheat is lower than a pre-set value.
- the aim of the present invention is to provide a method that is capable of modulating the refrigerating capacity absorbed by the evaporator according to the requirements of the moment, so as to adapt in each instance to:
- This aim is achieved by a method for limiting the condensation pressure of a refrigerating machine, according to claim 1.
- a refrigerating machine comprises an evaporator 10, a compressor 11, a condenser 12 and a throttling valve 13, which are connected in succession and in series to each other.
- a device for limiting the condensation pressure of the refrigerating machine comprises means for the continuous and controlled regulation of superheating at the evaporator, constituted by a sensor 14 for detecting the evaporation pressure (or saturation temperature at evaporation), a sensor 15 for detecting the temperature of the superheated vapor in output from the evaporator, a sensor 16 for detecting the condensation pressure (or saturation temperature at condensation), and a microprocessor-based controller 17.
- the per se known throttling valve is of the type that is servoactuated, for example by a motor 13a.
- the throttling valve 13 is chosen among the ones that have recently been introduced commercially and are servoactuated automatically, usually but not exclusively by means of an electric servomotor, and are controlled by electronic devices that allow to adjust the superheating according to the instantaneous requirements or convenience (known self-actuated mechanical valves instead do not allow automatic variation of the overheating value according to the operating conditions, because setting occurs by means of a manually operated screw).
- the microprocessor-based controller 17 is connected to said sensors 14, 15 and 16 and to the servoactuation of the throttling valve 13.
- the method according to the invention utilizes the fact that the capacity of a refrigerating machine is, as a first approximation, proportional to the flow-rate of the evaporated refrigerating fluid, and that therefore if this flow-rate is decreased the overall refrigerating capacity is also decreased.
- the method acts so as to decrease in a controlled fashion the flow-rate of refrigerating fluid introduced in the evaporator by way of the gradual throttling of the throttling valve, the evaporator is underfed and accordingly the refrigerating capacity of the machine is reduced.
- the refrigerating fluid first changes state and is then superheated: i.e., to ensure the complete absence of a liquid phase (which is potentially harmful to the compressor) in output, the temperature of the vapor produced by the complete evaporation of the fluid is raised by a controlled extent with respect to the saturation temperature at evaporation.
- a reduction in the mass flow of fluid fed to the evaporator leads to faster evaporation, i.e., to a reduction of the portion of surface used to change the state of the refrigerating fluid and to a consequent increase of the portion where the fluid is superheated.
- the method according to the invention causes an increase in the superheating of the vapor that leaves the evaporator and obtains in cascade:
- the saturation temperature at condensation By limiting indirectly the saturation temperature at condensation, one is conditioned by the minimum evaporation temperature that can be tolerated before the occurrence of undesirable effects or of effects that damage the process (for example, in a water refrigerator the evaporation temperature should never be lower than 0 °C due to the risk of freezing).
- the microprocessor-based controller 17 in addition to the normal functions of controlling the machine, measures the saturation temperature at evaporation (usually by means of a measurement of the corresponding pressure) and the temperature of the superheated vapor by way of the sensors 14 and 15, mounted proximate to the evaporator 10 or inside it, and calculates their difference, obtaining the value of the superheating; then it applies a regulation action to the servomotor 13a of the throttling valve 13, in order to keep the superheating at the optimum value (in normal conditions, the lowest value that is compatible with regulation stability, in order to ensure maximum refrigerating capacity).
- the microprocessor-based controller 17 further measures the saturation temperature at condensation (usually by means of a measurement of the corresponding pressure) by way of the sensor 16 mounted proximate to the condenser 12 or inside it.
- the microprocessor 17 raises appropriately the value of the superheating by closing partially the throttling valve 13, with the result of underfeeding the evaporator 10 and of decreasing the refrigeration capacity, consequently also reducing the thermal power affecting the condenser 12 and ultimately the saturation temperature at condensation.
- the saturation temperature at evaporation also tends to decrease with respect to the initial value, until it might drop below the preset threshold following a marked increase in superheating.
- the microprocessor-based controller 17 is designed to check that the maximum threshold of the saturation temperature at condensation and the minimum threshold of the saturation temperature of evaporation are not passed, giving however priority to the latter and therefore preventing an excessive throttling of the throttling valve 13.
- the microprocessor-based controller 17 would stop the compressor 11 in order to prevent unacceptable operating conditions.
- the microprocessor-based controller 17 restores the superheating to lower values, opening the throttling valve 13 in a controlled fashion.
- the method according to the present invention is in fact able to modulate simply, cheaply and functionally, by controlling the superheating, the refrigerating capacity absorbed by the evaporator according to the instantaneous requirements, so as to adapt in each instance to:
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Air Conditioning Control Device (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
- The present invention relates to a method for limiting the condensation pressure of a refrigerating machine according to the preamble of claim 1. Such a method is known from
EP-A-1 050 727 . - As is known, the refrigerating capacity of a refrigerating machine increases with the saturation temperature at evaporation, which in turn is linked to the temperature of the refrigerated fluid.
- The increase in refrigerating capacity also entails automatically an increase in the thermal power that the refrigerating machine must dissipate at the condenser.
- As the thermal power to be dissipated increases, so does necessarily the difference in primary temperature at the condenser (difference between the condensation temperature and the temperature of the cooling fluid).
- Accordingly, in a refrigerating machine, for an equal temperature of the cooling fluid at the condenser, an increase in the saturation temperature at evaporation (which generally depends on an increase in the temperature of the cooled fluid) leads to an increase in the saturation temperature at condensation.
- Conversely, a decrease in refrigerating capacity automatically leads to a decrease in the thermal power to be dissipated at the condenser and therefore to a decrease in the saturated temperature at condensation for an equal temperature of the hot source.
- Therefore, if the condensation temperature tends to approach the safety value that would require shutting down the machine, it is possible to limit this rise by reducing the refrigerating capacity absorbed by the evaporator, since this is equivalent to a reduction in the thermal power affecting the condenser.
- Among the various methods of achieving this, the best-known are:
- a. regulation of the speed of the refrigerating compressor;
- b. throttling, by means of appropriate regulator elements, the intake duct of the compressor in order to limit the flow-rate of refrigerating fluid;
- c. mechanical reduction of the capacity of the compressor;
- d. regulation of the temperature and/or flow-rate of the cooled fluid;
- e. recirculation, in the evaporator, of part of the hot gases pumped by the compressor (known as hot gas bypass).
- Examples of known devices and methods are given in the following prior art documents.
-
US-A-4 523 435 discloses a refrigeration system wherein the flow of refrigerant from the refrigerant condenser to the refrigerant evaporator is controlled by an adjustable expansion valve which is responsive to superheat of the refrigerant to be compressed. Adjusting the refrigerant flow in response to both the magnitude of the superheat and the rate at which it is changing, allows to stabilize the system with respect to the over and under-corrections of refrigerant flow that afflict the known systems. Therefore, the system ofUS-A-4 523 435 is suitable to prevent excessive variations of the operative conditions. This result is achieved by means of a fast adjustment of the expansion valve. -
EP-A-1 050 727 discloses a system suitable to automatically reach a minimum value for the condensation temperature in compliance with the functional parameters of the refrigerating machine. With this method, if the opening of the valve exceeds a pre-set value the condensation pressure is increased in order to have the correct pressure values at the inlet and output of the valve. -
JP-A-03164658 DE-A-43 03 533 concern control systems suitable to prevent excessive temperature at the delivery (high pressure side) of the compressor by means of increasing the opening of the electronic expansion valve, which results in an overfeeding of the evaporator. The control systems are based on the measurement of the high pressure side (delivery) pressure. In these systems, the expansion valve is opened only if the delivery temperature exceeds a pre-set value. -
EP-A-1 134 518 discloses a method for controlling the electronic expansion valve of a refrigerating machine, the method including the steps of monitoring a change in temperature between the fluid in a flooded cooler and a saturated suction temperature of the system, monitoring the discharge superheat of the system, and correcting the opening of the expansion valve when the discharge superheat is lower than a pre-set value. - However, these known methods are affected by high manufacturing costs (for example a. and b.), discontinuous regulation (for example c.), sometimes unacceptable functional interference with the cooling process (for example d.), or unacceptable energy inefficiencies.
- The aim of the present invention is to provide a method that is capable of modulating the refrigerating capacity absorbed by the evaporator according to the requirements of the moment, so as to adapt in each instance to:
- -- delivering the maximum refrigerating capacity that is compatible with the functional conditions of the machine;
- -- reducing the refrigerating capacity only when necessary and only to the required extent, in order to limit the saturation temperature at condensation when phenomena that might cause an excessive increase thereof occur.
- This aim is achieved by a method for limiting the condensation pressure of a refrigerating machine, according to claim 1.
- An embodiment of the invention is illustrated in the accompanying drawings, wherein:
-
Figure 1 is a system diagram of a known refrigerating machine; -
Figure 2 is a flowchart of the regulation process. - With reference to the figures, a refrigerating machine comprises an
evaporator 10, acompressor 11, acondenser 12 and athrottling valve 13, which are connected in succession and in series to each other. - A device for limiting the condensation pressure of the refrigerating machine comprises means for the continuous and controlled regulation of superheating at the evaporator, constituted by a
sensor 14 for detecting the evaporation pressure (or saturation temperature at evaporation), asensor 15 for detecting the temperature of the superheated vapor in output from the evaporator, asensor 16 for detecting the condensation pressure (or saturation temperature at condensation), and a microprocessor-basedcontroller 17. - Further, the per se known throttling valve is of the type that is servoactuated, for example by a
motor 13a. - The
throttling valve 13 is chosen among the ones that have recently been introduced commercially and are servoactuated automatically, usually but not exclusively by means of an electric servomotor, and are controlled by electronic devices that allow to adjust the superheating according to the instantaneous requirements or convenience (known self-actuated mechanical valves instead do not allow automatic variation of the overheating value according to the operating conditions, because setting occurs by means of a manually operated screw). - The microprocessor-based
controller 17 is connected to saidsensors throttling valve 13. - The method according to the invention utilizes the fact that the capacity of a refrigerating machine is, as a first approximation, proportional to the flow-rate of the evaporated refrigerating fluid, and that therefore if this flow-rate is decreased the overall refrigerating capacity is also decreased.
- Therefore, if the method acts so as to decrease in a controlled fashion the flow-rate of refrigerating fluid introduced in the evaporator by way of the gradual throttling of the throttling valve, the evaporator is underfed and accordingly the refrigerating capacity of the machine is reduced.
- In the normal operation of known dry-expansion evaporators, the refrigerating fluid first changes state and is then superheated: i.e., to ensure the complete absence of a liquid phase (which is potentially harmful to the compressor) in output, the temperature of the vapor produced by the complete evaporation of the fluid is raised by a controlled extent with respect to the saturation temperature at evaporation.
- A reduction in the mass flow of fluid fed to the evaporator leads to faster evaporation, i.e., to a reduction of the portion of surface used to change the state of the refrigerating fluid and to a consequent increase of the portion where the fluid is superheated.
- The method according to the invention causes an increase in the superheating of the vapor that leaves the evaporator and obtains in cascade:
- a. an increase in the portion of surface intended for superheating;
- b. a decrease in the portion of surface dedicated to evaporation;
- c. a decrease in the flow-rate of refrigerant throttled by the valve;
- d. a decrease in the refrigerating capacity associated with a decrease in the saturation temperature at evaporation;
- e. a decrease in the thermal power at the condenser;
- f. a decrease in the saturation temperature at condensation for an equal temperature of the cooling fluid.
- By limiting indirectly the saturation temperature at condensation, one is conditioned by the minimum evaporation temperature that can be tolerated before the occurrence of undesirable effects or of effects that damage the process (for example, in a water refrigerator the evaporation temperature should never be lower than 0 °C due to the risk of freezing).
- By lowering the superheating, which must nonetheless be given a value that is high enough to allow a stable and safe regulation process, one can also achieve an increase in the flow-rate of refrigerating fluid and therefore in the refrigerating capacity.
- The flowchart of the regulation process is summarized in
Figure 2 . - The microprocessor-based
controller 17, in addition to the normal functions of controlling the machine, measures the saturation temperature at evaporation (usually by means of a measurement of the corresponding pressure) and the temperature of the superheated vapor by way of thesensors evaporator 10 or inside it, and calculates their difference, obtaining the value of the superheating; then it applies a regulation action to theservomotor 13a of thethrottling valve 13, in order to keep the superheating at the optimum value (in normal conditions, the lowest value that is compatible with regulation stability, in order to ensure maximum refrigerating capacity). - The microprocessor-based
controller 17 further measures the saturation temperature at condensation (usually by means of a measurement of the corresponding pressure) by way of thesensor 16 mounted proximate to thecondenser 12 or inside it. - If the saturation temperature at condensation exceeds the threshold allowed for what is defined as normal operation, the
microprocessor 17 raises appropriately the value of the superheating by closing partially thethrottling valve 13, with the result of underfeeding theevaporator 10 and of decreasing the refrigeration capacity, consequently also reducing the thermal power affecting thecondenser 12 and ultimately the saturation temperature at condensation. - As a consequence of the underfeeding of the
evaporator 10, the saturation temperature at evaporation also tends to decrease with respect to the initial value, until it might drop below the preset threshold following a marked increase in superheating. - The microprocessor-based
controller 17 is designed to check that the maximum threshold of the saturation temperature at condensation and the minimum threshold of the saturation temperature of evaporation are not passed, giving however priority to the latter and therefore preventing an excessive throttling of thethrottling valve 13. - However, if the safety threshold of either temperature were passed, the microprocessor-based
controller 17 would stop thecompressor 11 in order to prevent unacceptable operating conditions. - Obviously, as soon as the saturation temperature at condensation drops below the threshold, the microprocessor-based
controller 17 restores the superheating to lower values, opening thethrottling valve 13 in a controlled fashion. - The method according to the present invention is in fact able to modulate simply, cheaply and functionally, by controlling the superheating, the refrigerating capacity absorbed by the evaporator according to the instantaneous requirements, so as to adapt in each instance to:
- -- delivering automatically the maximum refrigerating capacity that is compatible with the functional conditions of the machine;
- -- reducing the refrigerating capacity only when required and to the required extent, in order to limit the saturation temperature at condensation when phenomena occur that would cause its excessive increase.
Claims (1)
- A method for limiting the condensation pressure of a refrigerating machine comprising a compressor, a condenser, an expansion valve and an evaporator, comprising the steps of:- measuring the saturation temperature at evaporation;- measuring the temperature of the superheated vapor;- calculate the difference between the saturation temperature and the temperature of the superheated vapour, obtaining the value of the superheating;- measuring the saturation temperature or pressure at condensation;- defining a threshold value for the saturation temperature at condensation;- comparing the measured saturation temperature at condensation with the threshold value;- if the saturation temperature at condensation exceeds the threshold value, underfeeding the evaporator (10) by partially closing the throttling valve (13), so reducing the thermal power affecting the condenser (12) and consequently the saturation temperature at condensation, the value of superheating being raised and the refrigerating capacity being reduced if the saturation temperature at condensation exceeds the threshold, and characterized in that it further comprises the step of blocking the normal operation of the refrigerating machine by stopping the compressor if, despite the superheating regulation action or as a consequence thereof, a maximum safety threshold of the saturation temperature at condensation or a minimum safety threshold of the saturation temperature at evaporation is passed for a minimum significant time, and in that if the saturation temperature at condensation does not exceed the threshold value, the method comprises the steps of restoring the superheating to lower values by opening the throttling valve (13) in a controlled way and regulating the superheating at the evaporator to the minimum value that is compatible with operating stability and safety.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITPD20010173 | 2001-07-12 | ||
IT2001PD000173A ITPD20010173A1 (en) | 2001-07-12 | 2001-07-12 | DEVICE TO LIMIT THE CONDENSING PRESSURE OF A REFRIGERATING MACHINE |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1275917A2 EP1275917A2 (en) | 2003-01-15 |
EP1275917A3 EP1275917A3 (en) | 2004-01-07 |
EP1275917B1 true EP1275917B1 (en) | 2008-04-02 |
Family
ID=11452412
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02014999A Expired - Lifetime EP1275917B1 (en) | 2001-07-12 | 2002-07-10 | Method for limiting the condensation pressure in a refrigerating machine |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1275917B1 (en) |
AT (1) | ATE391272T1 (en) |
DE (1) | DE60225877T2 (en) |
ES (1) | ES2306746T3 (en) |
IT (1) | ITPD20010173A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4268931B2 (en) | 2004-12-30 | 2009-05-27 | 中山エンジニヤリング株式会社 | Refrigeration / freezing equipment and control method thereof |
EP1775533B1 (en) * | 2005-10-13 | 2018-03-28 | STIEBEL ELTRON GmbH & Co. KG | Method for operating a compression type refrigeration system |
BE1021838B1 (en) * | 2014-05-09 | 2016-01-21 | Atlas Copco Airpower, Naamloze Vennootschap | METHOD AND APPARATUS FOR COOLING A GAS |
US10823474B2 (en) | 2016-05-24 | 2020-11-03 | Carrier Corporation | Perturbation of expansion valve in vapor compression system |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4523435A (en) * | 1983-12-19 | 1985-06-18 | Carrier Corporation | Method and apparatus for controlling a refrigerant expansion valve in a refrigeration system |
DE3832226A1 (en) * | 1988-09-22 | 1990-04-12 | Danfoss As | REFRIGERATION SYSTEM AND METHOD FOR CONTROLLING A REFRIGERATION SYSTEM |
JPH03164658A (en) * | 1989-11-24 | 1991-07-16 | Toshiba Corp | Air conditioner |
WO1994017346A1 (en) * | 1993-01-19 | 1994-08-04 | Parker-Hannifin Corporation | System for controlling flow of working fluids |
DE4303533A1 (en) * | 1993-02-06 | 1994-08-11 | Stiebel Eltron Gmbh & Co Kg | Method for limiting the hot-gas temperature in a refrigerant circuit and expansion valve |
US5806327A (en) * | 1996-06-28 | 1998-09-15 | Lord; Richard G. | Compressor capacity reduction |
EP1050727A1 (en) * | 1999-05-06 | 2000-11-08 | Siemens Building Technologies AG | Method and apparatus for controlling a thermodynamic cycle |
US6318101B1 (en) * | 2000-03-15 | 2001-11-20 | Carrier Corporation | Method for controlling an electronic expansion valve based on cooler pinch and discharge superheat |
-
2001
- 2001-07-12 IT IT2001PD000173A patent/ITPD20010173A1/en unknown
-
2002
- 2002-07-10 AT AT02014999T patent/ATE391272T1/en not_active IP Right Cessation
- 2002-07-10 ES ES02014999T patent/ES2306746T3/en not_active Expired - Lifetime
- 2002-07-10 DE DE60225877T patent/DE60225877T2/en not_active Expired - Lifetime
- 2002-07-10 EP EP02014999A patent/EP1275917B1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
ATE391272T1 (en) | 2008-04-15 |
ES2306746T3 (en) | 2008-11-16 |
EP1275917A2 (en) | 2003-01-15 |
DE60225877D1 (en) | 2008-05-15 |
DE60225877T2 (en) | 2009-04-09 |
EP1275917A3 (en) | 2004-01-07 |
ITPD20010173A1 (en) | 2003-01-12 |
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