CN108981101A - Control method and control device of electronic expansion valve and unit - Google Patents

Control method and control device of electronic expansion valve and unit Download PDF

Info

Publication number
CN108981101A
CN108981101A CN201810689042.9A CN201810689042A CN108981101A CN 108981101 A CN108981101 A CN 108981101A CN 201810689042 A CN201810689042 A CN 201810689042A CN 108981101 A CN108981101 A CN 108981101A
Authority
CN
China
Prior art keywords
degree
superheat
temperature
heat transfer
result
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.)
Granted
Application number
CN201810689042.9A
Other languages
Chinese (zh)
Other versions
CN108981101B (en
Inventor
曾凡卓
谷月明
秦自强
高莹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gree Electric Appliances Inc of Zhuhai
Original Assignee
Gree Electric Appliances Inc of Zhuhai
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Gree Electric Appliances Inc of Zhuhai filed Critical Gree Electric Appliances Inc of Zhuhai
Priority to CN201810689042.9A priority Critical patent/CN108981101B/en
Publication of CN108981101A publication Critical patent/CN108981101A/en
Application granted granted Critical
Publication of CN108981101B publication Critical patent/CN108981101B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/62Control or safety arrangements characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
    • F24F11/63Electronic processing
    • F24F11/64Electronic processing using pre-stored data
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • F24F11/84Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers using valves

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Signal Processing (AREA)
  • Physics & Mathematics (AREA)
  • Fuzzy Systems (AREA)
  • Mathematical Physics (AREA)
  • Air Conditioning Control Device (AREA)
  • Electrically Driven Valve-Operating Means (AREA)

Abstract

The invention discloses a control method and a control device of an electronic expansion valve and a unit. The control method comprises the following steps: determining the superheat degree and the heat exchange temperature difference of the unit; and adjusting the opening degree of the electronic expansion valve according to the superheat degree and the heat exchange temperature difference. According to the invention, two factors of the heat exchange characteristic and the superheat degree of the unit can be systematically considered, and after comprehensive judgment and evaluation, a proper mode for adjusting the electronic expansion valve is selected. The refrigerant flow that passes through after the regulation can make superheat degree and heat transfer difference in temperature all be in suitable scope, from this, can improve the performance and the reliability of unit operation (especially under the low temperature condition).

Description

A kind of control method of electric expansion valve, control device and a kind of unit
Technical field
The present invention relates to machine set technology fields, control method, control device in particular to a kind of electric expansion valve And a kind of unit.
Background technique
Currently, most of heat pump units are both provided with electric expansion valve, for example, air-conditioner set is controlled using electric expansion valve The flow of refrigeration matchmaker.And the side that electric expansion valve is a kind of common control electric expansion valve is adjusted according to evaporator superheat Formula.But when heat pump unit is run at a lower temperature, the heat that refrigerant is drawn from air is less, and it is complete to be not enough to a refrigerant Evaporation, causes the degree of superheat of evaporator exit lower, and even zero.And electric expansion valve is adjusted according to the degree of superheat When, the adjusting unit of the degree of superheat is 1 degree Celsius.This is resulted at low temperatures, above-mentioned adjusting electric expansion valve Mode can make the amplitude of accommodation less than normal, make cold medium flux be unsatisfactory for unit high energy efficiency operation, reduce unit performance and can By property.
Aiming at the problem that regulative mode of electric expansion valve in the prior art can reduce unit performance, not yet propose have at present The solution of effect.
Summary of the invention
Control method, control device and a kind of unit of a kind of electric expansion valve are provided in the embodiment of the present invention, to solve The regulative mode of electric expansion valve can reduce the problem of unit performance in the prior art.
In order to solve the above technical problems, in a first aspect, the present invention provides a kind of control method of electric expansion valve, it is described Method includes:
Determine the degree of superheat and heat transfer temperature difference of unit;
The aperture of electric expansion valve is adjusted according to the degree of superheat and the heat transfer temperature difference.
Further, it is determined that the degree of superheat and heat transfer temperature difference of unit, comprising:
Suction temperature and pressure of inspiration(Pi) saturation temperature are obtained, according to the suction temperature and the pressure of inspiration(Pi) saturation temperature Determine the degree of superheat of unit;Alternatively, suction temperature and defrost tube temperature degree are obtained, according to the suction temperature and the defrost tube temperature Spend the degree of superheat for determining unit;And
Obtain tracheae temperature, liquid pipe temperature, leaving water temperature, inflow temperature;According to the tracheae temperature, the liquid pipe temperature Degree, the leaving water temperature, the inflow temperature determine the heat transfer temperature difference of unit.
Further, the degree of superheat that unit is determined according to the suction temperature and the pressure of inspiration(Pi) saturation temperature, passes through Following formula is realized:
The degree of superheat=suction temperature-pressure of inspiration(Pi) saturation temperature.
Further, the degree of superheat that unit is determined according to the suction temperature and the defrost tube temperature degree, passes through following public affairs Formula is realized:
The degree of superheat=suction temperature-defrost tube temperature degree.
Further, it is determined according to the tracheae temperature, the liquid pipe temperature, the leaving water temperature, the inflow temperature Heat transfer temperature difference is realized by following formula:
Further, include: according to the aperture that the degree of superheat and the heat transfer temperature difference adjust electric expansion valve
The size relation for comparing the degree of superheat and the first preset threshold or the first pre-set interval, obtains the first result;With And
The size relation for comparing the heat transfer temperature difference and the second preset threshold or the second pre-set interval obtains the second result;
The aperture of the electric expansion valve is adjusted according to first result and second result.
Further, include: according to the aperture that first result and second result adjust the electric expansion valve
If described first the result is that: the degree of superheat be greater than first preset threshold, alternatively, the degree of superheat is greater than The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be less than second preset threshold, or Person, the heat transfer temperature difference are less than the left end point value of second pre-set interval;The aperture of the electric expansion valve is then controlled with institute It states the increase of the degree of superheat and increases;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the overheat Degree is located at the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: it is described Heat transfer temperature difference is less than second preset threshold, alternatively, the heat transfer temperature difference is less than the left end point value of second pre-set interval; The aperture for then controlling the electric expansion valve is constant;
If described first the result is that: the degree of superheat be greater than first preset threshold, alternatively, the degree of superheat is greater than The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be equal to the second threshold, alternatively, The heat transfer temperature difference is located in second pre-set interval, then controls the aperture of the electric expansion valve with the increasing of the degree of superheat Increase greatly;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the overheat Degree is located at the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: it is described Heat transfer temperature difference is equal to second preset threshold and then controls institute alternatively, the heat transfer temperature difference is located in second pre-set interval The aperture for stating electric expansion valve is constant;
If described first the result is that: the degree of superheat be greater than first preset threshold, alternatively, the degree of superheat is greater than The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than the second threshold, alternatively, The heat transfer temperature difference is greater than the right end point value of second pre-set interval, then the aperture for controlling the electric expansion valve is constant;
If described first the result is that: the degree of superheat be equal to first preset threshold, alternatively, the degree of superheat is located at In first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, alternatively, described Heat transfer temperature difference is greater than the right end point value of second pre-set interval, then controls the aperture of the electric expansion valve with the heat exchange temperature Difference reduction and reduce;
If described first the result is that: the degree of superheat be less than first preset threshold, alternatively, the degree of superheat is less than The left end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, or Person, the heat transfer temperature difference are greater than the right end point value of second pre-set interval, then control the aperture of the electric expansion valve with institute It states the reduction of the degree of superheat and reduces.
Second aspect, the embodiment of the present invention also provide a kind of unit, and the unit is for executing side described in first aspect Method, the unit include: mainboard and electric expansion valve;
The mainboard is connect with the electric expansion valve, for determining the degree of superheat and heat transfer temperature difference of unit;According to described The degree of superheat and the heat transfer temperature difference adjust the aperture of electric expansion valve.
Further, the unit further include: air-breathing temperature sensing package, low pressure sensor, defrost temperature sensing package, tracheae and tracheae sense Thermometer bulb, water outlet temperature sensing package, liquid pipe and liquid pipe temperature sensing package and water inlet temperature sensing package,
The air-breathing temperature sensing package is connect with the low pressure sensor;
The low pressure sensor, for detecting pressure of inspiration(Pi), wherein the pressure of inspiration(Pi) is for determining that pressure of inspiration(Pi) is saturated Temperature;
The mainboard, with the air-breathing temperature sensing package, low pressure sensor, tracheae temperature sensing package, water outlet temperature sensing package, liquid pipe temperature sensing package And water inlet temperature sensing package is separately connected, for determining the degree of superheat according to suction temperature and the pressure of inspiration(Pi) saturation temperature; Alternatively, determining the degree of superheat according to the suction temperature and defrost tube temperature degree;
And heat transfer temperature difference is determined according to tracheae temperature, leaving water temperature, liquid pipe temperature and inflow temperature.
Further, the mainboard is also used to the degree of superheat described in comparison and the first preset threshold or the first pre-set interval Size relation obtains the first result;And the size of the heat transfer temperature difference and the second preset threshold or the second pre-set interval Relationship obtains the second result;The aperture of the electric expansion valve is adjusted according to first result and second result.
Further, the unit further include:
Four-way valve, evaporator, high pressure sensor, high-voltage switch gear, compressor, low tension switch, vapour point,
The S hydraulic fluid port of the four-way valve is connected to the air-breathing temperature sensing package, C hydraulic fluid port is connected to the evaporator, the connection of D hydraulic fluid port In the high pressure sensor, E hydraulic fluid port is connected to the tracheae;
The evaporator is connected to the defrost temperature sensing package;
The electric expansion valve is between the defrost temperature sensing package and the liquid pipe;
The high pressure sensor, the high-voltage switch gear, the compressor, the low tension switch, the vapour point and described Low pressure sensor is successively linked in sequence.
The third aspect, the embodiment of the present invention also provide a kind of control device of electric expansion valve, and described device is for executing Method described in first aspect, described device include:
Determining module, for determining the degree of superheat and heat transfer temperature difference of unit;
Adjustment module, for adjusting the aperture of electric expansion valve according to the degree of superheat and the heat transfer temperature difference.
Further, the determining module is also used to obtain suction temperature and pressure of inspiration(Pi) saturation temperature, according to the suction Temperature degree and the pressure of inspiration(Pi) saturation temperature determine the degree of superheat of unit;Alternatively, obtaining suction temperature and defrost tube temperature degree, root The degree of superheat of unit is determined according to the suction temperature and the defrost tube temperature degree;And it obtains tracheae temperature, liquid pipe temperature, go out Coolant-temperature gage, inflow temperature;Machine is determined according to the tracheae temperature, the liquid pipe temperature, the leaving water temperature, the inflow temperature The heat transfer temperature difference of group.
Further, the adjustment module is also used to the degree of superheat described in comparison and the first preset threshold or the first preset areas Between size relation, obtain the first result;And the heat transfer temperature difference and the second preset threshold or the second pre-set interval Size relation obtains the second result;The aperture of the electric expansion valve is adjusted according to first result and second result.
It applies the technical scheme of the present invention, the aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference.With only Consider that this factor of the degree of superheat is compared, can systematically assess two kinds of factors of heat transfer characteristic and the degree of superheat of unit, comprehensive descision Afterwards, the suitable mode for adjusting electric expansion valve of selection, the cold medium flux after adjusting enable to the degree of superheat and heat transfer temperature difference It is in suitable range, Performance And Reliability (especially at low temperatures) when unit is run can be improved as a result,.
Detailed description of the invention
Fig. 1 is a kind of flow chart of the control method of electric expansion valve according to an embodiment of the present invention;
Fig. 2 is a kind of flow chart of the control method of electric expansion valve according to an embodiment of the present invention;
Fig. 3 is a kind of structural schematic diagram of unit according to an embodiment of the present invention;
Fig. 4 is a kind of structural block diagram of the control device of electric expansion valve according to an embodiment of the present invention.
Specific embodiment
Present invention is further described in detail in the following with reference to the drawings and specific embodiments, it should be understood that described herein Specific embodiment be only used to explain the present invention, be not intended to limit the present invention.
In subsequent description, it is only using the suffix for indicating such as " module ", " component " or " unit " of element Be conducive to explanation of the invention, itself there is no a specific meaning.Therefore, " module ", " component " or " unit " can mix Ground uses.
In order to solve the problems, such as that the regulative mode of electric expansion valve in the related technology can reduce unit performance, the present invention is implemented Example provides a kind of control method of electric expansion valve, as shown in Figure 1, method includes:
Step S101, the degree of superheat and heat transfer temperature difference of unit are determined;
Step S102, the aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference.
The aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference.With only consideration this factor phase of the degree of superheat Than can systematically assess two kinds of factors of heat transfer characteristic and the degree of superheat of unit, after comprehensive descision, select suitable to adjust electronics The mode of expansion valve, the cold medium flux after adjusting enable to the degree of superheat and heat transfer temperature difference to be in suitable range, by This, can be improved Performance And Reliability (especially at low temperatures) when unit is run.
In one possible implementation, heat transfer temperature difference can be the heat transfer temperature difference of water and refrigerant in water chiller.Step Rapid S101 determines the degree of superheat of unit and heat transfer temperature difference may include: to obtain suction temperature and pressure of inspiration(Pi) saturation temperature, according to Suction temperature and pressure of inspiration(Pi) saturation temperature determine the degree of superheat of unit;Alternatively, suction temperature and defrost tube temperature degree are obtained, according to Suction temperature and defrost tube temperature degree determine the degree of superheat of unit;And obtain tracheae temperature, liquid pipe temperature, leaving water temperature, water inlet Temperature;The heat transfer temperature difference of unit is determined according to tracheae temperature, liquid pipe temperature, leaving water temperature, inflow temperature.
Generally, by the available above-mentioned parameter of related component of unit, and can be according to " the degree of superheat=air-breathing Temperature-pressure of inspiration(Pi) saturation temperature " or " degree of superheat=suction temperature-defrost tube temperature degree " determine the degree of superheat of unit.According to Following formula acquire the heat transfer temperature difference of unit.
When unit does not detect the device of pressure of inspiration(Pi) for example: when low pressure sensor, then it is approximate that defrost tube temperature degree can be used Instead of the evaporating temperature (i.e. pressure of inspiration(Pi) saturation temperature) of evaporator.The diversity for obtaining degree of superheat mode can be increased as a result,.But Pressure of inspiration(Pi) is determined with using low pressure sensor, and then calculates pressure of inspiration(Pi) saturation temperature, and substitute into the degree of superheat that formula acquires It compares, such mode temperature feedback more lags, and the degree of superheat of calculating may be inaccurate, so as to the tune of electric expansion valve Section is not suitable for.Therefore, in conditions permit, it is proposed that calculated by the way of directly acquiring pressure of inspiration(Pi) saturation temperature Temperature.
In one possible implementation, as shown in Fig. 2, step S102, being adjusted according to the degree of superheat and heat transfer temperature difference The aperture of electric expansion valve includes:
Step S201, the size relation for comparing the degree of superheat and the first preset threshold or the first pre-set interval, obtains the first knot Fruit;And
Step S202, the size relation for comparing heat transfer temperature difference and the second preset threshold or the second pre-set interval, obtains second As a result;
Step S203, the aperture of electric expansion valve is adjusted according to the first result and the second result.
It is during heat pump unit actual motion, the degree of superheat and heat transfer temperature difference control is relatively difficult to achieve in certain certain value, Control is then more conform with actual conditions within a certain range, and the embodiment of the present invention has comprehensively considered reality factor and error component. Using mode shown in Fig. 2 come threshold value and pre-set interval, and by the degree of superheat, heat transfer temperature difference respectively with mutual threshold value and Pre-set interval is compared, and adjusts electric expansion valve according to comparison result.Wherein, preset threshold and pre-set interval can bases The self performance of demand and electric expansion valve of the user to unit performance is set.It is understood that using preset areas Between the adjusting to electric expansion valve can be made more stable as the reference point of the degree of superheat or heat transfer temperature difference, further improving can By property.And two ways can be with cross-reference.For example, by the degree of superheat compared with preset threshold, by heat transfer temperature difference and pre-set interval It compares, obtains the first comparison result and the second comparison result.The present invention is without limitation.
In one possible implementation, the aperture packet of electric expansion valve is adjusted according to the first result and the second result Include: if first the result is that: the degree of superheat be greater than the first preset threshold, alternatively, the degree of superheat be greater than the first pre-set interval right endpoint Value;Second the result is that: heat transfer temperature difference is less than the second preset threshold, alternatively, left end point of the heat transfer temperature difference less than the second pre-set interval Value;The aperture for then controlling electric expansion valve increases with the increase of the degree of superheat;
If first the result is that: the degree of superheat be less than or equal to the first preset threshold, alternatively, the degree of superheat is located at the first preset areas Left end point value interior or less than the first pre-set interval;Second the result is that: heat transfer temperature difference is less than the second preset threshold, alternatively, changing Left end point value of the hot temperature difference less than the second pre-set interval;The aperture for then controlling electric expansion valve is constant;
If first the result is that: the degree of superheat be greater than the first preset threshold, alternatively,
The degree of superheat is greater than the right end point value of the first pre-set interval;Second the result is that: heat transfer temperature difference be equal to second threshold, or Person, heat transfer temperature difference are located in the second pre-set interval, then the aperture for controlling electric expansion valve increases with the increase of the degree of superheat;
If first the result is that: the degree of superheat be less than or equal to the first preset threshold, alternatively, the degree of superheat is located at the first preset areas Left end point value interior or less than the first pre-set interval;Second the result is that: heat transfer temperature difference be equal to the second preset threshold, alternatively, changing The hot temperature difference is located in the second pre-set interval, then the aperture for controlling electric expansion valve is constant;
If first the result is that: the degree of superheat be greater than the first preset threshold, alternatively, the degree of superheat be greater than the first pre-set interval the right side Endpoint value;Second the result is that: heat transfer temperature difference be greater than second threshold, alternatively, heat transfer temperature difference be greater than the second pre-set interval right endpoint Value, the then aperture for controlling electric expansion valve are constant;
If first the result is that: the degree of superheat be equal to the first preset threshold, alternatively, the degree of superheat is located in the first pre-set interval; Second the result is that: heat transfer temperature difference be greater than the second preset threshold, alternatively, heat transfer temperature difference be greater than the second pre-set interval right end point value, The aperture for then controlling electric expansion valve reduces with the reduction of heat transfer temperature difference;
If first the result is that: the degree of superheat is less than the first preset threshold, alternatively, a left side of the degree of superheat less than the first pre-set interval Endpoint value;Second the result is that: heat transfer temperature difference be greater than the second preset threshold, alternatively, heat transfer temperature difference be greater than the second pre-set interval the right side Endpoint value, the then aperture for controlling electric expansion valve reduce with the reduction of the degree of superheat.
Table can be used to be described further above-mentioned implementation.In table 1, the reference standard of the degree of superheat is first default Threshold value, the reference standard of heat transfer temperature difference are the second preset threshold.In table 2, the reference standard of the degree of superheat is the first pre-set interval, is changed The reference standard of the hot temperature difference is the second pre-set interval.And Δ t2 represents the degree of superheat;δ represents the first preset threshold;Δ t1 representative is changed The hot temperature difference, ε represent the second preset threshold;[A, B] represents the first pre-set interval;[α, β] represents the second pre-set interval, and EXV generation Table electric expansion valve.
Table 1
Δt1< ε Δt1 Δt1> ε
Δt2> δ It opens greatly, is adjusted by the degree of superheat It opens greatly, is adjusted by the degree of superheat EXV is not adjusted
Δt2 EXV is not adjusted EXV is not adjusted It turns down, is adjusted by heat transfer temperature difference
Δt2< δ EXV is not adjusted EXV is not adjusted It turns down, is controlled by the degree of superheat
Table 2
Δt1< α Δt1=[α, β] Δt1> β
Δt2> B It opens greatly, is adjusted by the degree of superheat It opens greatly, is adjusted by the degree of superheat EXV is not adjusted
Δt2=[A, B] EXV is not adjusted EXV is not adjusted It turns down, is adjusted by heat transfer temperature difference
Δt2< A EXV is not adjusted EXV is not adjusted It turns down, is controlled by the degree of superheat
It should be noted that heat transfer temperature difference is smaller, the performance of unit is higher, and is carried out based on the degree of superheat to electric expansion valve Adjust it is higher than the priority that electric expansion valve is adjusted based on heat transfer temperature difference, be exemplified by Table 1, when unit heat transfer temperature difference not Greater than the second preset threshold and when the degree of superheat is not more than the first preset threshold, the operating condition of unit is normal, i.e. electric expansion valve Aperture caused by flow through the cold medium flux of unit and unit performance and can maintain the state of a stable equilibrium, then do not need Electric expansion valve is adjusted.But if heat transfer temperature difference remains unchanged, the degree of superheat raises to above the first preset threshold, then controls Electric expansion valve processed is opened greatly according to the raising of the degree of superheat.If heat transfer temperature difference is greater than the second preset threshold, and the degree of superheat at this time Equal to the first preset threshold, illustrate that the degree of superheat is relatively stable, then controls electric expansion valve and turned down according to the reduction of heat transfer temperature difference. If heat transfer temperature difference is greater than the second preset threshold, and the degree of superheat is less than the first preset threshold, that is to say, that the two is unstable Under state, then according to above-mentioned priority, controls electric expansion valve and turned down according to the reduction of the degree of superheat.
The aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference as a result,.With only consider the degree of superheat this because Element is compared, and can systematically assess two kinds of factors of heat transfer characteristic and the degree of superheat of unit, after comprehensive descision, selects suitable adjust The mode of electric expansion valve, the cold medium flux after adjusting enable to the degree of superheat and heat transfer temperature difference to be in suitable range It is interior, Performance And Reliability (especially at low temperatures) when unit is run can be improved as a result,.
Fig. 3 shows a kind of unit, and for unit for executing method shown in above-described embodiment, unit includes: mainboard (in figure It is not shown) and electric expansion valve 1;
Mainboard is connect with electric expansion valve 1, for determining the degree of superheat and heat transfer temperature difference of unit;According to the degree of superheat and change The hot temperature difference adjusts the aperture of electric expansion valve 1.
In one possible implementation, unit further include: air-breathing temperature sensing package 2, low pressure sensor 3, defrost temperature sensing package 4, tracheae and tracheae temperature sensing package 5, water outlet temperature sensing package 6, liquid pipe and liquid pipe temperature sensing package 7 and water inlet temperature sensing package 8,
Air-breathing temperature sensing package 2 is connect with low pressure sensor 3;
Low pressure sensor 3, for detecting pressure of inspiration(Pi), wherein pressure of inspiration(Pi) is for determining pressure of inspiration(Pi) saturation temperature;
Mainboard, with air-breathing temperature sensing package 2, low pressure sensor 3, tracheae temperature sensing package 5, water outlet temperature sensing package 6, liquid pipe temperature sensing package 7 and Water inlet temperature sensing package 8 is separately connected, for determining the degree of superheat according to suction temperature and pressure of inspiration(Pi) saturation temperature;Alternatively, according to Suction temperature and defrost tube temperature degree determine the degree of superheat;And according to tracheae temperature, leaving water temperature, liquid pipe temperature and water inlet temperature It spends and determines heat transfer temperature difference.
In one possible implementation, mainboard, is also used to compare the degree of superheat and the first preset threshold or first are default The size relation in section obtains the first result;And compare the big of heat transfer temperature difference and the second preset threshold or the second pre-set interval Small relationship obtains the second result;The aperture of electric expansion valve 1 is adjusted according to the first result and the second result.
In one possible implementation, unit further include: four-way valve 9, evaporator 10, high pressure sensor 11, high pressure Switch 12, compressor 13, low tension switch 14, vapour divide 15,
The S hydraulic fluid port of four-way valve 9 is connected to air-breathing temperature sensing package 2, C hydraulic fluid port is connected to evaporator 10, D hydraulic fluid port is connected to high pressure biography Sensor 11, E hydraulic fluid port are connected to tracheae 5;
Evaporator 10 is connected to defrost temperature sensing package 4;
Electric expansion valve 1 is between defrost temperature sensing package 4 and liquid pipe 7;
High pressure sensor 11, high-voltage switch gear 12, compressor 13, low tension switch 14, vapour points 15 and low pressure sensor 3 are successively It is linked in sequence.
The aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference.With only consideration this factor phase of the degree of superheat Than can systematically assess two kinds of factors of heat transfer characteristic and the degree of superheat of unit, after comprehensive descision, select suitable to adjust electronics The mode of expansion valve, the cold medium flux after adjusting enable to the degree of superheat and heat transfer temperature difference to be in suitable range, by This, can be improved Performance And Reliability (especially at low temperatures) when unit is run.
Fig. 4 shows a kind of control device of electric expansion valve, which, should for executing method shown in fig. 1 or fig. 2 Device includes:
Determining module 401, for determining the degree of superheat and heat transfer temperature difference of unit;
Adjustment module 402, for adjusting the aperture of electric expansion valve according to the degree of superheat and heat transfer temperature difference.
In one possible implementation, determining module 401 are also used to obtain suction temperature and pressure of inspiration(Pi) saturation temperature Degree, the degree of superheat of unit is determined according to suction temperature and pressure of inspiration(Pi) saturation temperature;Alternatively, obtaining suction temperature and defrost tube temperature Degree, the degree of superheat of unit is determined according to suction temperature and defrost tube temperature degree;And it obtains tracheae temperature, liquid pipe temperature, go out water temperature Degree, inflow temperature;The heat transfer temperature difference of unit is determined according to tracheae temperature, liquid pipe temperature, leaving water temperature, inflow temperature.
In one possible implementation, adjustment module 402 are also used to compare the degree of superheat and the first preset threshold or the The size relation of one pre-set interval obtains the first result;And compare heat transfer temperature difference and the second preset threshold or the second preset areas Between size relation, obtain the second result;The aperture of electric expansion valve is adjusted according to the first result and the second result.
In one possible implementation, adjustment module 402, if be also used to first the result is that: the degree of superheat is greater than the One preset threshold, alternatively, the degree of superheat is greater than the right end point value of the first pre-set interval;Second the result is that: heat transfer temperature difference is less than second Preset threshold, alternatively, left end point value of the heat transfer temperature difference less than the second pre-set interval;The aperture of electric expansion valve is then controlled with overheat The increase of degree and increase;If first the result is that: the degree of superheat is less than or equal to the first preset threshold, alternatively, the degree of superheat is located at the Left end point value in one pre-set interval or less than the first pre-set interval;Second the result is that: heat transfer temperature difference less than the second preset threshold, Alternatively, left end point value of the heat transfer temperature difference less than the second pre-set interval;The aperture for then controlling electric expansion valve is constant;If the first knot Fruit is: the degree of superheat is greater than the first preset threshold, alternatively, the degree of superheat is greater than the right end point value of the first pre-set interval;Second the result is that: Heat transfer temperature difference is equal to second threshold, alternatively, heat transfer temperature difference is located in the second pre-set interval, then control the aperture of electric expansion valve with The increase of the degree of superheat and increase;If first the result is that: the degree of superheat be less than or equal to the first preset threshold, alternatively, degree of superheat position In the left end point value in the first pre-set interval or less than the first pre-set interval;Second the result is that: it is default that heat transfer temperature difference is equal to second Threshold value, alternatively, heat transfer temperature difference is located in the second pre-set interval, then the aperture for controlling electric expansion valve is constant;If the first result Be: the degree of superheat is greater than the first preset threshold, alternatively, the degree of superheat is greater than the right end point value of the first pre-set interval;Second the result is that: change The hot temperature difference is greater than second threshold, alternatively, heat transfer temperature difference is greater than the right end point value of the second pre-set interval, then controls electric expansion valve Aperture is constant;If first the result is that: the degree of superheat be equal to the first preset threshold, alternatively, the degree of superheat is located in the first pre-set interval; Second the result is that: heat transfer temperature difference be greater than the second preset threshold, alternatively, heat transfer temperature difference be greater than the second pre-set interval right end point value, The aperture for then controlling electric expansion valve reduces with the reduction of heat transfer temperature difference;If first the result is that: the degree of superheat is pre- less than first If threshold value, alternatively, left end point value of the degree of superheat less than the first pre-set interval;Second the result is that: it is default that heat transfer temperature difference is greater than second Threshold value then controls the aperture of electric expansion valve with the degree of superheat alternatively, heat transfer temperature difference is greater than the right end point value of the second pre-set interval Reduce and reduces.
The aperture of electric expansion valve is adjusted according to the degree of superheat and heat transfer temperature difference.With only consideration this factor phase of the degree of superheat Than can systematically assess two kinds of factors of heat transfer characteristic and the degree of superheat of unit, after comprehensive descision, select suitable to adjust electronics The mode of expansion valve, the cold medium flux after adjusting enable to the degree of superheat and heat transfer temperature difference to be in suitable range, by This, can be improved Performance And Reliability (especially at low temperatures) when unit is run.
It should be noted that, in this document, the terms "include", "comprise" or its any other variant are intended to non-row His property includes, so that the process, method, article or the device that include a series of elements not only include those elements, and And further include other elements that are not explicitly listed, or further include for this process, method, article or device institute it is intrinsic Element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that including being somebody's turn to do There is also other identical elements in the process, method of element, article or device.
The serial number of the above embodiments of the invention is only for description, does not represent the advantages or disadvantages of the embodiments.
Through the above description of the embodiments, those skilled in the art can be understood that above-described embodiment side Method can be realized by means of software and necessary general hardware platform, naturally it is also possible to by hardware, but in many cases The former is more preferably embodiment.Based on this understanding, technical solution of the present invention substantially in other words does the prior art The part contributed out can be embodied in the form of software products, which is stored in a storage medium In (such as ROM/RAM, magnetic disk, CD), including some instructions are used so that a mobile terminal (can be mobile phone, computer, clothes Business device, air conditioner or the network equipment etc.) execute method described in each embodiment of the present invention.
The embodiment of the present invention is described above in conjunction with figure, but the invention is not limited to above-mentioned specific realities Mode is applied, the above mentioned embodiment is only schematical, rather than restrictive, and those skilled in the art exist Under enlightenment of the invention, without breaking away from the scope protected by the purposes and claims of the present invention, many shapes can be also made Formula, all of these belong to the protection of the present invention.

Claims (15)

1. a kind of control method of electric expansion valve, which is characterized in that the described method includes:
Determine the degree of superheat and heat transfer temperature difference of unit;
The aperture of electric expansion valve is adjusted according to the degree of superheat and the heat transfer temperature difference.
2. the method according to claim 1, wherein determining the degree of superheat and heat transfer temperature difference of unit, comprising:
Suction temperature and pressure of inspiration(Pi) saturation temperature are obtained, is determined according to the suction temperature and the pressure of inspiration(Pi) saturation temperature The degree of superheat of unit;Alternatively, suction temperature and defrost tube temperature degree are obtained, it is true according to the suction temperature and the defrost tube temperature degree Determine the degree of superheat of unit;
And
Obtain tracheae temperature, liquid pipe temperature, leaving water temperature, inflow temperature;According to the tracheae temperature, the liquid pipe temperature, institute State leaving water temperature, the inflow temperature determines the heat transfer temperature difference of unit.
3. according to the method described in claim 2, it is characterized in that, being saturated temperature according to the suction temperature and the pressure of inspiration(Pi) The degree of superheat for determining unit is spent, is realized by following formula:
The degree of superheat=suction temperature-pressure of inspiration(Pi) saturation temperature.
4. according to the method described in claim 2, it is characterized in that, being determined according to the suction temperature and the defrost tube temperature degree The degree of superheat of unit, is realized by following formula:
The degree of superheat=suction temperature-defrost tube temperature degree.
5. according to the method described in claim 2, it is characterized in that, according to the tracheae temperature, the liquid pipe temperature, it is described go out Coolant-temperature gage, the inflow temperature determine heat transfer temperature difference, are realized by following formula:
6. the method according to claim 1, wherein adjusting electricity according to the degree of superheat and the heat transfer temperature difference The aperture of sub- expansion valve includes:
The size relation for comparing the degree of superheat and the first preset threshold or the first pre-set interval, obtains the first result;And
The size relation for comparing the heat transfer temperature difference and the second preset threshold or the second pre-set interval obtains the second result;
The aperture of the electric expansion valve is adjusted according to first result and second result.
7. according to the method described in claim 6, it is characterized in that, adjusting institute according to first result and second result The aperture for stating electric expansion valve includes:
If described first the result is that: the degree of superheat is greater than first preset threshold, alternatively, the degree of superheat be greater than it is described The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be less than second preset threshold, alternatively, The heat transfer temperature difference is less than the left end point value of second pre-set interval;The aperture of the electric expansion valve is then controlled with the mistake The increase of temperature and increase;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the degree of superheat position In the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: the heat exchange The temperature difference is less than second preset threshold, alternatively, the heat transfer temperature difference is less than the left end point value of second pre-set interval;Then control The aperture for making the electric expansion valve is constant;
If described first the result is that: the degree of superheat is greater than first preset threshold, alternatively, the degree of superheat be greater than it is described The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be equal to the second threshold, alternatively, described Heat transfer temperature difference is located in second pre-set interval, then control the aperture of the electric expansion valve with the increase of the degree of superheat and Increase;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the degree of superheat position In the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: the heat exchange The temperature difference is equal to second preset threshold and then controls the electricity alternatively, the heat transfer temperature difference is located in second pre-set interval The aperture of sub- expansion valve is constant;
If described first the result is that: the degree of superheat is greater than first preset threshold, alternatively, the degree of superheat be greater than it is described The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than the second threshold, alternatively, described Heat transfer temperature difference is greater than the right end point value of second pre-set interval, then the aperture for controlling the electric expansion valve is constant;
If described first the result is that: the degree of superheat is equal to first preset threshold, alternatively, the degree of superheat be located at it is described In first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, alternatively, the heat exchange The temperature difference is greater than the right end point value of second pre-set interval, then controls the aperture of the electric expansion valve with the heat transfer temperature difference Reduce and reduces;
If described first the result is that: the degree of superheat is less than first preset threshold, alternatively, the degree of superheat be less than it is described The left end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, alternatively, The heat transfer temperature difference is greater than the right end point value of second pre-set interval, then controls the aperture of the electric expansion valve with the mistake The reduction of temperature and reduce.
8. a kind of unit, which is characterized in that the unit is for method described in any one of right of execution 1 to power 7, the machine Group includes: mainboard and electric expansion valve;
The mainboard is connect with the electric expansion valve, for determining the degree of superheat and heat transfer temperature difference of unit;According to the overheat Degree and the heat transfer temperature difference adjust the aperture of electric expansion valve.
9. unit according to claim 8, which is characterized in that the unit further include: air-breathing temperature sensing package, low pressure sensing Device, defrost temperature sensing package, tracheae and tracheae temperature sensing package, water outlet temperature sensing package, liquid pipe and liquid pipe temperature sensing package and water inlet temperature sensing package,
The air-breathing temperature sensing package is connect with the low pressure sensor;
The low pressure sensor, for detecting pressure of inspiration(Pi), wherein the pressure of inspiration(Pi) is for determining pressure of inspiration(Pi) saturation temperature Degree;
The mainboard, with the air-breathing temperature sensing package, low pressure sensor, tracheae temperature sensing package, water outlet temperature sensing package, liquid pipe temperature sensing package and into Talent for swimming thermometer bulb is separately connected, for determining the degree of superheat according to suction temperature and the pressure of inspiration(Pi) saturation temperature;Alternatively, The degree of superheat is determined according to the suction temperature and defrost tube temperature degree;
And heat transfer temperature difference is determined according to tracheae temperature, leaving water temperature, liquid pipe temperature and inflow temperature.
10. unit according to claim 8, which is characterized in that
The mainboard is also used to the size relation of the degree of superheat described in comparison and the first preset threshold or the first pre-set interval, obtains First result;And the size relation of the heat transfer temperature difference and the second preset threshold or the second pre-set interval, obtain second As a result;The aperture of the electric expansion valve is adjusted according to first result and second result.
11. unit according to claim 8, which is characterized in that the unit further include:
Four-way valve, evaporator, high pressure sensor, high-voltage switch gear, compressor, low tension switch, vapour point,
The S hydraulic fluid port of the four-way valve is connected to the air-breathing temperature sensing package, C hydraulic fluid port is connected to the evaporator, D hydraulic fluid port is connected to institute High pressure sensor is stated, E hydraulic fluid port is connected to the tracheae;
The evaporator is connected to the defrost temperature sensing package;
The electric expansion valve is between the defrost temperature sensing package and the liquid pipe;
The high pressure sensor, the high-voltage switch gear, the compressor, the low tension switch, the vapour divides and the low pressure Sensor is successively linked in sequence.
12. a kind of control device of electric expansion valve, which is characterized in that described device is for described in 1 to 7 any one of right of execution Method, described device includes:
Determining module, for determining the degree of superheat and heat transfer temperature difference of unit;
Adjustment module, for adjusting the aperture of electric expansion valve according to the degree of superheat and the heat transfer temperature difference.
13. device according to claim 12, which is characterized in that
The determining module is also used to obtain suction temperature and pressure of inspiration(Pi) saturation temperature, according to the suction temperature and described Pressure of inspiration(Pi) saturation temperature determines the degree of superheat of unit;Alternatively, suction temperature and defrost tube temperature degree are obtained, according to the air-breathing temperature Degree and the defrost tube temperature degree determine the degree of superheat of unit;
And
Obtain tracheae temperature, liquid pipe temperature, leaving water temperature, inflow temperature;According to the tracheae temperature, the liquid pipe temperature, institute State leaving water temperature, the inflow temperature determines the heat transfer temperature difference of unit.
14. device according to claim 12, which is characterized in that
The adjustment module is also used to the size relation of the degree of superheat described in comparison and the first preset threshold or the first pre-set interval, Obtain the first result;And the size relation of the heat transfer temperature difference and the second preset threshold or the second pre-set interval, it obtains Second result;The aperture of the electric expansion valve is adjusted according to first result and second result.
15. device according to claim 14, which is characterized in that
The adjustment module, if be also used to described first the result is that: the degree of superheat be greater than first preset threshold, or Person, the degree of superheat are greater than the right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be less than institute The second preset threshold is stated, alternatively, the heat transfer temperature difference is less than the left end point value of second pre-set interval;Then control the electronics The aperture of expansion valve increases with the increase of the degree of superheat;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the degree of superheat position In the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: the heat exchange The temperature difference is less than second preset threshold, alternatively, the heat transfer temperature difference is less than the left end point value of second pre-set interval;Then control The aperture for making the electric expansion valve is constant;
If described first the result is that: the degree of superheat is greater than first preset threshold, alternatively, the degree of superheat be greater than it is described The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be equal to the second threshold, alternatively, described Heat transfer temperature difference is located in second pre-set interval, then control the aperture of the electric expansion valve with the increase of the degree of superheat and Increase;
If described first the result is that: the degree of superheat be less than or equal to first preset threshold, alternatively, the degree of superheat position In the left end point value in first pre-set interval or less than first pre-set interval;Described second the result is that: the heat exchange The temperature difference is equal to second preset threshold and then controls the electricity alternatively, the heat transfer temperature difference is located in second pre-set interval The aperture of sub- expansion valve is constant;
If described first the result is that: the degree of superheat is greater than first preset threshold, alternatively, the degree of superheat be greater than it is described The right end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than the second threshold, alternatively, described Heat transfer temperature difference is greater than the right end point value of second pre-set interval, then the aperture for controlling the electric expansion valve is constant;
If described first the result is that: the degree of superheat is equal to first preset threshold, alternatively, the degree of superheat be located at it is described In first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, alternatively, the heat exchange The temperature difference is greater than the right end point value of second pre-set interval, then controls the aperture of the electric expansion valve with the heat transfer temperature difference Reduce and reduces;
If described first the result is that: the degree of superheat is less than first preset threshold, alternatively, the degree of superheat be less than it is described The left end point value of first pre-set interval;Described second the result is that: the heat transfer temperature difference be greater than second preset threshold, alternatively, The heat transfer temperature difference is greater than the right end point value of second pre-set interval, then controls the aperture of the electric expansion valve with the mistake The reduction of temperature and reduce.
CN201810689042.9A 2018-06-28 2018-06-28 Control method and control device of electronic expansion valve and unit Active CN108981101B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810689042.9A CN108981101B (en) 2018-06-28 2018-06-28 Control method and control device of electronic expansion valve and unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810689042.9A CN108981101B (en) 2018-06-28 2018-06-28 Control method and control device of electronic expansion valve and unit

Publications (2)

Publication Number Publication Date
CN108981101A true CN108981101A (en) 2018-12-11
CN108981101B CN108981101B (en) 2020-06-05

Family

ID=64539434

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810689042.9A Active CN108981101B (en) 2018-06-28 2018-06-28 Control method and control device of electronic expansion valve and unit

Country Status (1)

Country Link
CN (1) CN108981101B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110986253A (en) * 2019-11-15 2020-04-10 珠海格力电器股份有限公司 Electronic expansion valve control method, compressor control system and air conditioner
CN111121290A (en) * 2019-12-19 2020-05-08 宁波奥克斯电气股份有限公司 Control method and control device of electronic expansion valve and heat pump water heater
WO2021218272A1 (en) * 2020-04-26 2021-11-04 青岛海尔空调电子有限公司 Method for controlling opening degree of expansion valve of air conditioning system
CN113742833A (en) * 2021-09-17 2021-12-03 上海美控智慧建筑有限公司 Air conditioner room setting method and device and electronic equipment
CN115265012A (en) * 2022-07-08 2022-11-01 珠海格力电器股份有限公司 Electronic expansion valve opening control method, system and unit
CN115493295A (en) * 2022-09-26 2022-12-20 珠海格力电器股份有限公司 Control method and system of hot water unit and computer readable storage medium

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003156260A (en) * 2001-11-20 2003-05-30 Fujitsu General Ltd Control method for air-conditioner
JP2005069655A (en) * 2003-08-28 2005-03-17 Matsushita Electric Ind Co Ltd Multi-type air conditioner
JP2012132578A (en) * 2010-12-20 2012-07-12 Panasonic Corp Refrigerating cycle device
CN103808010A (en) * 2012-11-15 2014-05-21 珠海格力电器股份有限公司 Quasi-two-stage compression heat pump water heater and control method thereof
CN104949276A (en) * 2015-06-24 2015-09-30 海信(山东)空调有限公司 Air conditioner running state self-detecting method and system
CN105371545A (en) * 2014-07-31 2016-03-02 青岛海尔空调器有限总公司 An air conditioner and a refrigerant circulation quantity adjusting method for a refrigeration system thereof
CN105423498A (en) * 2015-12-21 2016-03-23 珠海格力电器股份有限公司 Control method of air conditioning system and air conditioning system
CN106595141A (en) * 2016-12-12 2017-04-26 重庆美的通用制冷设备有限公司 Electronic expansion valve control method and device and refrigerating system

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003156260A (en) * 2001-11-20 2003-05-30 Fujitsu General Ltd Control method for air-conditioner
JP2005069655A (en) * 2003-08-28 2005-03-17 Matsushita Electric Ind Co Ltd Multi-type air conditioner
JP2012132578A (en) * 2010-12-20 2012-07-12 Panasonic Corp Refrigerating cycle device
CN103808010A (en) * 2012-11-15 2014-05-21 珠海格力电器股份有限公司 Quasi-two-stage compression heat pump water heater and control method thereof
CN105371545A (en) * 2014-07-31 2016-03-02 青岛海尔空调器有限总公司 An air conditioner and a refrigerant circulation quantity adjusting method for a refrigeration system thereof
CN104949276A (en) * 2015-06-24 2015-09-30 海信(山东)空调有限公司 Air conditioner running state self-detecting method and system
CN105423498A (en) * 2015-12-21 2016-03-23 珠海格力电器股份有限公司 Control method of air conditioning system and air conditioning system
CN106595141A (en) * 2016-12-12 2017-04-26 重庆美的通用制冷设备有限公司 Electronic expansion valve control method and device and refrigerating system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110986253A (en) * 2019-11-15 2020-04-10 珠海格力电器股份有限公司 Electronic expansion valve control method, compressor control system and air conditioner
CN110986253B (en) * 2019-11-15 2022-04-29 珠海格力电器股份有限公司 Electronic expansion valve control method, compressor control system and air conditioner
CN111121290A (en) * 2019-12-19 2020-05-08 宁波奥克斯电气股份有限公司 Control method and control device of electronic expansion valve and heat pump water heater
CN111121290B (en) * 2019-12-19 2021-11-09 宁波奥克斯电气股份有限公司 Control method and control device of electronic expansion valve and heat pump water heater
WO2021218272A1 (en) * 2020-04-26 2021-11-04 青岛海尔空调电子有限公司 Method for controlling opening degree of expansion valve of air conditioning system
CN113742833A (en) * 2021-09-17 2021-12-03 上海美控智慧建筑有限公司 Air conditioner room setting method and device and electronic equipment
CN115265012A (en) * 2022-07-08 2022-11-01 珠海格力电器股份有限公司 Electronic expansion valve opening control method, system and unit
CN115265012B (en) * 2022-07-08 2024-01-12 珠海格力电器股份有限公司 Electronic expansion valve opening control method, system and unit
CN115493295A (en) * 2022-09-26 2022-12-20 珠海格力电器股份有限公司 Control method and system of hot water unit and computer readable storage medium

Also Published As

Publication number Publication date
CN108981101B (en) 2020-06-05

Similar Documents

Publication Publication Date Title
CN108981101A (en) Control method and control device of electronic expansion valve and unit
KR101551242B1 (en) Cascade floating intermediate temperature heat pump system
US9250001B2 (en) Control of an expansion valve regulating refrigerant to an evaporator of a climate control system
KR101106383B1 (en) Freezing apparatus
US8484990B2 (en) Optimization of air cooled chiller system operation
EP2270405B1 (en) Refrigerating device
US9121631B2 (en) Air conditioner and method of operating an air conditioner
US9982925B2 (en) Air conditioner and method of controlling an air conditioner
CN109373497B (en) Refrigerant quantity adjusting method, device and system of temperature adjusting equipment and air conditioner
US20060162358A1 (en) Superheat control by pressure ratio
CN109405379B (en) Control method for refrigeration electronic expansion valve
CN108474594B (en) Refrigerating device
US20100324742A1 (en) Control system for an expansion valve regulating refrigerant to an evaporator of a climate control system
CN104006445A (en) Multi-connected air conditioner and control method thereof
CN112665112B (en) Air conditioner, control method thereof and readable storage medium
US10107531B2 (en) Method for controlling a chiller system
WO2021058193A1 (en) A method for controlling suction pressure of a vapour compression system
KR101336720B1 (en) Air conditioning system
CN108662798A (en) Water chilling unit and control method and device thereof
CN106594964B (en) Control method for controlling operation of air conditioning system and air conditioning system
EP2434232A2 (en) Control of a transcritical vapor compression system
CN112611041B (en) Air conditioning unit and electronic expansion valve control method
KR20170095616A (en) Air conditioner and a method for controlling the same
RU2735041C1 (en) Method of suction pressure control, based on cooling object under the biggest load
KR102177952B1 (en) Air conditioner

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant