CN105972860B - Multi-line system and its valve body control method for crossing cold loop - Google Patents

Multi-line system and its valve body control method for crossing cold loop Download PDF

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Publication number
CN105972860B
CN105972860B CN201610285059.9A CN201610285059A CN105972860B CN 105972860 B CN105972860 B CN 105972860B CN 201610285059 A CN201610285059 A CN 201610285059A CN 105972860 B CN105972860 B CN 105972860B
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Prior art keywords
heat
exchanging component
flow path
heat exchange
compressor
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CN105972860A (en
Inventor
罗彬�
李元阳
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Midea Group Co Ltd
Guangdong Midea HVAC Equipment Co Ltd
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Midea Group Co Ltd
Guangdong Midea HVAC Equipment Co Ltd
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/003Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/20Disposition of valves, e.g. of on-off valves or flow control valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/005Arrangement or mounting of control or safety devices of safety devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2500/00Problems to be solved
    • F25B2500/28Means for preventing liquid refrigerant entering into the compressor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

The invention discloses a kind of multi-line system and its valve body control methods of cold loop excessively, the described method comprises the following steps: obtaining the discharge superheat of compressor;When discharge superheat is less than the first preset value, if the outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is less than first outlet target superheat degree, aperture is carried out to second throttle and turns control down;When the aperture regulation of second throttle is to minimum aperture, if the outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is less than first outlet target superheat degree, then minimum aperture is carried out to turn amendment down, and continue to turn control down to second throttle progress aperture, until the discharge superheat of compressor is greater than the second preset value.This method is when compressor has back liquid risk, by adjusting the aperture of second throttle, not only excessive refrigerant can have been limited and returned to compressor, but also time liquid risk that the return-air degree of superheat reduces compressor can be improved, to improve the refrigeration effect of system and the safety of operation.

Description

Multi-line system and its valve body control method for crossing cold loop
Technical field
The present invention relates to the valve body control methods that cold loop is crossed in air-conditioning technical field more particularly to a kind of multi-line system And a kind of multi-line system.
Background technique
The main refrigeration mode of multi-line system can simultaneously utilize system condensation heat and heat of evaporation, realize simultaneously refrigeration with Heating, substantially increases system energy efficiency.In multi-line system, outdoor unit can be distributed liquid state refrigerant by part flow arrangement To the indoor unit with different refrigeration, heating needs, wherein part flow arrangement was provided with cold loop.
When multi-line system is run with main refrigeration mode or pure refrigeration mode, when refrigeration indoor unit outlet superheat degree too It is small, or supercooling circuit outlet refrigerant is more and the gas in the smaller exit to refrigeration indoor unit of outlet superheat degree generate compared with When strong cooling effect, the air entry that the easy to carry liquid of return-air returns to compressor will lead to, at this time the discharge superheat of system It is lower, to influence the safe operation of system.
Summary of the invention
The present invention is directed to solve at least some of the technical problems in related technologies.For this purpose, of the invention One purpose is to propose to cross the valve body control method of cold loop in a kind of multi-line system, and this method has back liquid wind in compressor When dangerous, by adjusting second throttle aperture to suitable aperture, can not only limit excessive refrigerant and return to compressor, also Time liquid risk that the return-air degree of superheat reduces compressor can be improved, to improve the refrigeration effect of system and the safety of operation.
It is another object of the present invention to propose a kind of multi-line system.
In order to achieve the above objectives, one aspect of the present invention embodiment proposes the valve body that cold loop is crossed in a kind of multi-line system Control method, the multi-line system include outdoor unit, part flow arrangement and multiple indoor units, and the outdoor unit includes compressor, The part flow arrangement includes the first heat-exchanging component and the second heat-exchanging component, and the first heat exchange flow path of first heat-exchanging component goes out First throttle valve is set between the entrance of first heat exchange flow path of mouth and second heat-exchanging component, second heat-exchanging component Second throttle is set between the entrance of second heat exchange flow path of the outlet and second heat-exchanging component of the first heat exchange flow path, institute The entrance for stating the outlet of the second heat exchange flow path of the second heat-exchanging component and the second heat exchange flow path of first heat-exchanging component is connected to, The heat exchange flow path of first heat-exchanging component and the heat exchange flow path of second heat-exchanging component constitute the cold loop excessively, the side Method is the following steps are included: obtain the discharge superheat of the compressor;When the discharge superheat of the compressor is pre- less than first If when value, if the outlet superheat degree of the second heat exchange flow path of first heat-exchanging component is less than first outlet target superheat degree, Aperture then is carried out to the second throttle and turns control down;When the aperture regulation of the second throttle is to minimum aperture, such as The outlet superheat degree of second heat exchange flow path of the first heat-exchanging component described in fruit is less than the first outlet target superheat degree, then to institute It states minimum aperture to carry out turning amendment down, according to the second of first heat-exchanging component the heat exchange outlet superheat degree of flow path and described First outlet target superheat degree continues to turn control down to second throttle progress aperture, until the exhaust of the compressor Temperature is greater than the second preset value, wherein second preset value is greater than first preset value.
The valve body control method that cold loop is crossed in multi-line system according to an embodiment of the present invention, obtains compressor first Discharge superheat, when the discharge superheat of compressor is less than the first preset value, if the second heat exchange stream of the first heat-exchanging component The outlet superheat degree on road is less than first outlet target superheat degree, then carries out aperture to second throttle and turn control down, when the second section When flowing the aperture regulation of valve and arriving minimum aperture, if the second of the first heat-exchanging component exchange heat flow path outlet superheat degree less than first The export goal degree of superheat then carries out minimum aperture to turn amendment down, with going out according to the second of the first heat-exchanging component the heat exchange flow path Temperature of making a slip of the tongue and first outlet target superheat degree continue to turn control down to second throttle progress aperture, until the exhaust of compressor The degree of superheat is greater than the second preset value.This method is when compressor has back liquid risk, by the aperture for quickly adjusting second throttle To suitable aperture, it can not only limit excessive refrigerant and return to compressor, the return-air degree of superheat can also be improved and reduce compressor Return liquid risk, to reach better refrigeration effect and safer operating status.
According to one embodiment of present invention, when the discharge superheat of the compressor is less than the first preset value, judgement There is back liquid risk in the compressor.
According to one embodiment of present invention, by the way that the current minimum aperture of the second throttle is subtracted default aperture Threshold value to the minimum aperture to carry out turning amendment down.
According to one embodiment of present invention, the multi-line system carries out work under main refrigeration mode or pure refrigeration mode Make.
In order to achieve the above objectives, another aspect of the present invention embodiment proposes a kind of multi-line system, comprising: outdoor unit, The outdoor unit includes compressor;Multiple indoor units;Part flow arrangement, the part flow arrangement include that the first heat-exchanging component and second changes Hot component, the first heat exchange flow path of the outlet and second heat-exchanging component of the first heat exchange flow path of first heat-exchanging component First throttle valve, the outlet of the first heat exchange flow path of second heat-exchanging component and second heat-exchanging component are set between entrance The second heat exchange flow path entrance between second throttle is set, the outlet of the second heat exchange flow path of second heat-exchanging component with The entrance connection of second heat exchange flow path of first heat-exchanging component, the heat exchange flow path of first heat-exchanging component and described second The heat exchange flow path composition of heat-exchanging component is described to cross cold loop;Control module, the control module is for obtaining the compressor Discharge superheat, and the of first heat-exchanging component is judged when the discharge superheat of the compressor is less than the first preset value Whether the outlet superheat degree of two heat exchange flow paths is less than first outlet target superheat degree, wherein if first heat-exchanging component The outlet superheat degree of second heat exchange flow path is less than first outlet target superheat degree, and the control module is then to the second throttle It carries out aperture and turns control down, and when the aperture regulation of the second throttle is to minimum aperture, if the first heat exchange group Part second heat exchange flow path outlet superheat degree be less than the first outlet target superheat degree, the control module then to it is described most Small guide vane carries out turning amendment down, according to the outlet superheat degree and described first of the second of first heat-exchanging component the heat exchange flow path The export goal degree of superheat continues to turn control down to second throttle progress aperture, until the discharge superheat of the compressor Greater than the second preset value, wherein second preset value is greater than first preset value.
Multi-line system according to an embodiment of the present invention, by the discharge superheat of control module acquisition compressor, and The outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is judged when the discharge superheat of compressor is less than the first preset value Whether first outlet target superheat degree is less than, wherein if the outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is small In first outlet target superheat degree, control module then carries out aperture to second throttle and turns control down, and in second throttle When aperture regulation is to minimum aperture, if the outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is less than first outlet mesh The degree of superheat is marked, control module then carries out minimum aperture to turn amendment down, according to the second of the first heat-exchanging component the heat exchange flow path Outlet superheat degree and first outlet target superheat degree continue to turn control down to second throttle progress aperture, until the row of compressor The gas degree of superheat is greater than the second preset value.The system is when compressor has back liquid risk, by quickly adjusting opening for second throttle Degree can not only limit excessive refrigerant and return to compressor, can also improve the return-air degree of superheat and reduce compression to suitable aperture Machine returns liquid risk, to reach better refrigeration effect and safer operating status.
According to one embodiment of present invention you, when the discharge superheat of the compressor is less than the first preset value, institute It states control module and judges that the compressor has back liquid risk.
According to one embodiment of present invention, the control module is by by the current minimum aperture of the second throttle Default aperture threshold value is subtracted to carry out turning amendment down to the minimum aperture.
According to one embodiment of present invention, the multi-line system carries out work under main refrigeration mode or pure refrigeration mode Make.
Detailed description of the invention
Above-mentioned and/or additional aspect and advantage of the invention will become from the following description of the accompanying drawings of embodiments Obviously and it is readily appreciated that, wherein
Fig. 1 is the structural schematic diagram of the multi-line system of an implementation according to the present invention;
Fig. 2 is the process that the valve body control method of cold loop is crossed in multi-line system according to an embodiment of the invention Figure;And
Fig. 3 crosses the process of the valve body control method of cold loop in the multi-line system of a specific example according to the present invention Figure.
Appended drawing reference: outdoor unit 10, part flow arrangement 20, multiple indoor units 30, compressor 101, the first heat-exchanging component 201, Second heat-exchanging component 202, first throttle valve 203 and second throttle 204.
Specific embodiment
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning to end Same or similar label indicates same or similar element or element with the same or similar functions.Below with reference to attached The embodiment of figure description is exemplary, it is intended to is used to explain the present invention, and is not considered as limiting the invention.
With reference to the accompanying drawings come describe the multi-line system proposed according to embodiments of the present invention and its cross cold loop valve body Control method.
Fig. 1 is the structural schematic diagram of the multi-line system of an implementation according to the present invention.As shown in Figure 1, the system includes: Outdoor unit 10, part flow arrangement 20, multiple indoor units 30 and control module (not specifically illustrated in figure).
Wherein, outdoor unit 10 includes compressor 101.Part flow arrangement 20 includes the first heat-exchanging component 201 and the second heat exchange group Part 202, the outlet of the first heat exchange flow path and the entering for the first heat exchange flow path of the second heat-exchanging component 202 of the first heat-exchanging component 201 First throttle valve 203, the outlet of the first heat exchange flow path of the second heat-exchanging component 202 and the second heat-exchanging component 202 are set between mouthful Second heat exchange flow path entrance between be arranged second throttle 204, the second heat-exchanging component 202 second heat exchange flow path outlet It is connected to the entrance of the second heat exchange flow path of the first heat-exchanging component 201, the heat exchange flow path of the first heat-exchanging component 201 and the second heat exchange The heat exchange flow path of component 202 constituted cold loop.
As shown in Figure 1, first throttle valve 203 is shown in a fully open operation when multi-line system is run with pure refrigeration mode, from The high temperature gas-liquid mixture that the gas-liquid separator of part flow arrangement 20 comes out, successively by the first heat-exchanging component 201 and the second heat exchange Component 202.The refrigerant come out from the first heat exchange flow path of the second heat-exchanging component 202, a part are expanded by second throttle 204 Evaporation absorbs the heat of the first heat exchange flow path of the first heat-exchanging component 201 and the second heat-exchanging component 202, eventually enters into outdoor unit 10 low-voltage tube, another part enter refrigeration indoor unit by the throttle valve for the indoor unit that freezes, outdoor unit 10 are entered after absorbing heat Low-voltage tube.
When multi-line system is run with main refrigeration mode, the gas-liquid separator of part flow arrangement 20 will be from the height of outdoor unit 10 The high temperature gas-liquid mixture that pressure pipe enters is divided into highly pressurised liquid and high pressure gas, wherein highly pressurised liquid passes through the first heat-exchanging component 201 supercoolings, high pressure gas enters heating indoor unit, after heating indoor unit heat release, with the liquid flowed out from the first heat-exchanging component 201 Enter the second heat-exchanging component 202 after the mixing of body refrigerant.The refrigerant come out from the first heat exchange flow path of the second heat-exchanging component 202, one Part after the first heat-exchanging component 201 and the second heat-exchanging component 202 with from refrigeration indoor unit come out refrigerant mix after, entrance The low-voltage tube of outdoor unit 10, another part enter refrigeration indoor unit by the throttle valve for the indoor unit that freezes, the sky to freeze to needs Between freeze.
In embodiments of the present invention, when multi-line system is worked under main refrigeration mode or pure refrigeration mode, control Module is used to obtain the discharge superheat DSH of compressor 101, and in the discharge superheat DSH of compressor less than the first preset value A When, judge whether the outlet superheat degree SHm3 of the second heat exchange flow path of the first heat-exchanging component 201 is less than first outlet target superheat Spend B, wherein if the outlet superheat degree SHm3 of the second heat exchange flow path of the first heat-exchanging component 201 is less than first outlet target mistake Temperature B, control module then carries out aperture to second throttle 204 and turns control down, and arrives in the aperture regulation of second throttle 204 When minimum aperture, if the outlet superheat degree SHm3 of the second heat exchange flow path of the first heat-exchanging component 201 is less than first outlet target Degree of superheat B, control module then carry out minimum aperture to turn amendment down, according to the second of the first heat-exchanging component 201 the heat exchange flow path Outlet superheat degree SHm3 and first outlet target superheat degree B continue to second throttle 204 carry out aperture turn control down, up to The discharge superheat DSH of compressor is greater than the second preset value C, wherein the second preset value C is greater than the first preset value A, and first is default Value A, first outlet target superheat degree B and the second preset value C can be demarcated according to the actual situation.In embodiments of the present invention, when When the discharge superheat DSH of compressor 101 is less than the first preset value A, control module judges that compressor 101 has back liquid risk. Specifically, when multi-line system is worked under main refrigeration mode or pure refrigeration mode, control module obtains compressor 101 Discharge superheat DSH, and DSH < A is judged whether there is, if there is DSH < A, then illustrate that compressor has back liquid risk.In order to meet The refrigeration demand of refrigeration indoor unit, the throttle valve adjustment for the indoor unit that freezes is as far as possible according to adjusting rule when operating normally, at this time By adjusting the aperture of second throttle 204 compressor 101 can be made to restore biggish discharge superheat DSH again, to protect The safe and stable operation of card system.
When the aperture to second throttle 204 is adjusted, control module will be according to the second of the first heat-exchanging component 201 The outlet superheat degree SHm3 and first outlet target superheat degree B of heat exchange flow path carry out PI to second throttle 204 (Proportional Integral, proportional integration) is adjusted, in adjustment process, if control module judges SHm3 < B, and control Molding block then turns the aperture of second throttle 204 down, to reduce low pressure, improves the return-air degree of superheat of outdoor unit 10.Such as The aperture of fruit second throttle 204 is transferred to minimum aperture, still remains SHm3 < B, although then illustrating second throttle 204 Aperture has been transferred to minimum aperture, but for cold loop excessively, the aperture of second throttle 204 or larger, mistake cold loop Can by low temperature refrigerant flow or too many, but second throttle 204 cannot be completely closed again.Because for main system Multi-line system under cold mode, the refrigerant for heating indoor unit need just return to outdoor unit 10 by second throttle 204, and Refrigeration indoor unit needs part flow arrangement 20 to have certain degree of superheat, that is, needs the second heat exchange flow path of the first heat-exchanging component 201 There is certain degree of superheat in exit, just has the sky that the refrigerant of enough degree of supercooling SCm2 enters refrigeration indoor unit to freeze to needs Between freeze, it is therefore desirable to little by little adjust second throttle 204 aperture.
Specifically, control module first carries out turning amendment down to the minimum aperture of second throttle 204, to obtain than minimum The smaller aperture of aperture, can be improved SHm3, often turn primary minimum aperture down, and SHm3 can be improved a bit.
According to one embodiment of present invention, control module is by subtracting the current minimum aperture of second throttle 204 Aperture threshold value a is preset to carry out turning amendment down to minimum aperture, wherein a is smaller value, such as a can be 1.That is, When control module carries out turning amendment down to the minimum aperture of second throttle 204, revised minimum aperture=current minimum aperture- Default aperture threshold value a.
Then, control module according to SHm3 and B continue to second throttle 204 carry out aperture turn control down, when SHm3 again It is secondary when reaching B, judge whether the discharge superheat DSH of compressor 101 is greater than the second preset value C.If the exhaust of compressor 101 Degree of superheat DSH is greater than the second preset value C, it is ensured that compressor 101 is without liquid risk is returned, and system can be transported at this time with safety and stability Row, in this way under the premise of system can be with safe and stable operation, control module stablizes the aperture of second throttle 204 current PI adjusting is carried out to second throttle 204 compared with small guide vane, or according to operating condition variation;If the discharge superheat of compressor 101 DSH is less than or equal to the second preset value C, illustrates that the discharge superheat DSH of compressor 101 is still unsatisfactory for the peace of compressor assembly Full service condition, control module continues to carry out turning amendment down to the minimum aperture of second throttle 204, until meeting DSH > C. The multi-line system limits excessive refrigerant and returns to compressor as a result, while reducing compression by improving the return-air degree of superheat Machine returns liquid risk, to improve the refrigeration effect of system and the safety of operation.
It should be noted that the outlet superheat degree SHm3=Tm3-Tps3 of the second heat exchange flow path of the first heat-exchanging component 201, Wherein, Tm3 is the outlet temperature of the second heat exchange flow path of the first heat-exchanging component 201, and Tps3 is the of the first heat-exchanging component 201 The corresponding saturation temperature of outlet pressure of two heat exchange flow paths;Degree of supercooling SCm2=Tps2-Tm2 before 204 valve of second throttle, In, Tps2 is the outlet temperature of the first heat exchange flow path of the second heat-exchanging component 202, and Tm2 is the first of the second heat-exchanging component 202 to change The corresponding saturation temperature of the outlet pressure of hot flowpath.
In conclusion multi-line system according to an embodiment of the present invention, the exhaust of compressor is obtained by control module Temperature, and judge that when the discharge superheat of compressor is less than the first preset value, the second heat exchange flow path of the first heat-exchanging component goes out Whether temperature of making a slip of the tongue is less than first outlet target superheat degree, wherein if the outlet of the second heat exchange flow path of the first heat-exchanging component The degree of superheat is less than first outlet target superheat degree, and control module then carries out aperture to second throttle and turns control down, and second When the aperture regulation of throttle valve is to minimum aperture, if the outlet superheat degree of the second heat exchange flow path of the first heat-exchanging component is less than the The one export goal degree of superheat, control module then carry out minimum aperture to turn amendment down, to change according to the second of the first heat-exchanging component The outlet superheat degree and first outlet target superheat degree of hot flowpath continue to turn control down to second throttle progress aperture, until pressure The discharge superheat of contracting machine is greater than the second preset value.The system is when compressor has back liquid risk, by quickly adjusting the second section The aperture of valve is flowed to suitable aperture, can not only be limited excessive refrigerant and be returned to compressor, can also improve the return-air degree of superheat That reduces compressor returns liquid risk, to reach better refrigeration effect and safer operating status.
Fig. 2 is the process that the valve body control method of cold loop is crossed in multi-line system according to an embodiment of the invention Figure.
As shown in Figure 1, multi-line system includes outdoor unit, part flow arrangement and multiple indoor units, outdoor unit includes compressor, Part flow arrangement includes the first heat-exchanging component and the second heat-exchanging component, the outlet and second of the first heat exchange flow path of the first heat-exchanging component First throttle valve is set between the entrance of the first heat exchange flow path of heat-exchanging component, and the first heat exchange flow path of the second heat-exchanging component goes out Second throttle, the second heat exchange of the second heat-exchanging component are set between the entrance of second heat exchange flow path of mouth and the second heat-exchanging component The outlet of flow path is connected to the entrance of the second heat exchange flow path of the first heat-exchanging component, the heat exchange flow path of the first heat-exchanging component and second The heat exchange flow path of heat-exchanging component constituted cold loop.
As shown in Fig. 2, in multi-line system cross cold loop valve body control method the following steps are included:
S1 obtains the exhaust of compressor when multi-line system is worked under main refrigeration mode or pure refrigeration mode Degree of superheat DSH.
S2, when the discharge superheat DSH of compressor is less than the first preset value A, if the second of the first heat-exchanging component changes The outlet superheat degree SHm3 of hot flowpath is less than first outlet target superheat degree B, then carries out aperture to second throttle and turn control down.
According to one embodiment of present invention, when the discharge superheat DSH of compressor is less than the first preset value A, judgement There is back liquid risk in compressor.
S3, when the aperture regulation of second throttle is to minimum aperture, if the second heat exchange flow path of the first heat-exchanging component Outlet superheat degree SHm3 be less than first outlet target superheat degree B, then minimum aperture is carried out turning amendment down, to change according to first The outlet superheat degree SHm3 and first outlet target superheat degree B of second heat exchange flow path of hot component continue to carry out second throttle Aperture turns control down, until the discharge superheat DSH of compressor is greater than the second preset value C, wherein the second preset value C is greater than the One preset value A, the first preset value A, first outlet target superheat degree B and the second preset value C can be demarcated according to the actual situation.
Specifically, when multi-line system is worked under main refrigeration mode or pure refrigeration mode, the row of compressor is obtained Gas degree of superheat DSH, and DSH < A is judged whether there is, if there is DSH < A, then illustrate that compressor has back liquid risk.In order to meet system The refrigeration demand of cold indoor unit, the throttle valve adjustment for the indoor unit that freezes according to adjusting rule when operating normally, at this time may be used as far as possible The compressor 101 is set to restore biggish discharge superheat DSH again with the aperture by adjusting second throttle, to guarantee system Safe and stable operation.
When the aperture to second throttle is adjusted, go out to make a slip of the tongue according to the second of the first heat-exchanging component the heat exchange flow path Temperature SHm3 and first outlet target superheat degree B carries out PI (Proportional Integral, ratio product to second throttle Point) adjust, in adjustment process, if it is determined that SHm3 < B, then turn the aperture of second throttle down, to reduce low pressure, Improve the return-air degree of superheat of outdoor unit.If the aperture of second throttle is transferred to minimum aperture, SHm3 < B is still remained, is said Although bright be transferred to minimum aperture for the aperture of second throttle, for crossing for cold loop, the aperture of second throttle Or it is larger, cross cold loop can by cold medium flux or too many, but second throttle 204 cannot be closed completely again It closes.Because the refrigerant for heating indoor unit needs to return to room by second throttle for the multi-line system under main refrigeration mode Outer machine, and the indoor unit that freezes needs part flow arrangement to have certain outlet superheat degree, that is, the second of the first heat-exchanging component is needed to exchange heat There is certain degree of superheat in the exit of flow path, and the refrigerant for just having enough degree of supercooling SCm2 enters refrigeration indoor unit to needs Freeze in the space of refrigeration, it is therefore desirable to little by little adjust the aperture of second throttle 204.
In particular, it is desirable to first carry out turning amendment down to the minimum aperture of second throttle, to obtain than minimum aperture more Small aperture, can be improved SHm3, often turn primary minimum aperture down, and SHm3 can be improved a bit.
According to one embodiment of present invention, by the way that the current minimum aperture of second throttle is subtracted default aperture threshold value A is to carry out minimum aperture to turn amendment down.Wherein, a is smaller value, such as a can be 1.That is, to second throttle When minimum aperture carries out turning amendment down, revised minimum aperture=current minimum aperture-presets aperture threshold value a.
Then, continued to turn control down to second throttle progress aperture according to SHm3 and B, when SHm3 reaches B again, be sentenced Whether the discharge superheat DSH of disconnected compressor is greater than the second preset value C.If the discharge superheat DSH of compressor is greater than second Preset value C, it is ensured that compressor without return liquid risk, at this time system can with safe and stable operation, in this way system can be safe Under the premise of stable operation, the aperture of second throttle is stablized currently compared with small guide vane, or is changed according to operating condition to second Throttle valve carries out PI adjusting;If being less than or equal to the second preset value C by the discharge superheat DSH of compressor, illustrate compressor Discharge superheat DSH be still unsatisfactory for the safe operating conditions of compressor assembly, continue the minimum aperture to second throttle It carries out turning amendment down, until meeting DSH > C.This method limit excessive refrigerants to return to compressor as a result, while by mentioning The high return-air degree of superheat reduces time liquid risk of compressor, to improve the refrigeration effect of system and the safety of operation.
It should be noted that the outlet superheat degree SHm3=Tm3-Tps3 of the second heat exchange flow path of the first heat-exchanging component 201, Wherein, Tm3 is the outlet temperature of the second heat exchange flow path of the first heat-exchanging component 201, and Tps3 is the of the first heat-exchanging component 201 The corresponding saturation temperature of outlet pressure of two heat exchange flow paths;Degree of supercooling SCm2=Tps2-Tm2 before 204 valve of second throttle, In, Tps2 is the outlet temperature of the first heat exchange flow path of the second heat-exchanging component 202, and Tm2 is the first of the second heat-exchanging component 202 to change The corresponding saturation temperature of the outlet pressure of hot flowpath.
Further, to make those skilled in the art better understand the present invention, Fig. 3 be according to the present invention one specifically show The flow chart of the valve body control method of cold loop is crossed in the multi-line system of example.As shown in figure 3, method includes the following steps:
S101 obtains the exhaust of compressor when multi-line system is worked under main refrigeration mode or pure refrigeration mode Degree of superheat DSH, and judge whether DSH < A.
S102, if it is determined that DSH < A, illustrates that compressor has back liquid risk, initialize the aperture of second throttle.
S103 carries out PI adjusting to second throttle according to SHm3 and B, if SHm3 < B, carries out to second throttle Aperture turns control down.
S104, when the aperture regulation of second throttle is to minimum aperture, if still SHm3 < B, to minimum aperture It carries out turning amendment down, revised minimum aperture=current minimum aperture-presets aperture threshold value a.
S105 continues to turn control down to second throttle progress aperture according to SHm3 and B.
S106 judges whether DSH > C when SHm3 reaches B again, if so, illustrating that compressor without liquid risk is returned, is held Row step S107, if not;Illustrate that compressor still has back liquid risk, executes step S104.
S107 stablizes the aperture of second throttle currently compared with small guide vane, or throttled according to operating condition variation to second Valve carries out PI adjusting.
In conclusion crossing the valve body control method of cold loop in multi-line system according to an embodiment of the present invention, obtain first The discharge superheat for taking compressor, when the discharge superheat of compressor is less than the first preset value, if the first heat-exchanging component The outlet superheat degree of second heat exchange flow path is less than first outlet target superheat degree, then carries out aperture to second throttle and turn control down System, when the aperture regulation of second throttle arrives minimum aperture, if the second heat exchange flow path of the first heat-exchanging component is made a slip of the tongue out Temperature is less than first outlet target superheat degree, then carries out turning amendment down to minimum aperture, according to the second of the first heat-exchanging component The outlet superheat degree and first outlet target superheat degree of heat exchange flow path continue to turn control down to second throttle progress aperture, until The discharge superheat of compressor is greater than the second preset value.This method is when compressor has back liquid risk as a result, by adjusting second The aperture of throttle valve can not only limit excessive refrigerant and return to compressor, and can also reduce compressor returns liquid risk, thus The refrigeration effect of raising system and the safety of operation.
In the description of the present invention, it is to be understood that, term " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" "inner", "outside", " up time The orientation or positional relationship of the instructions such as needle ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " be orientation based on the figure or Positional relationship is merely for convenience of description of the present invention and simplification of the description, rather than the device or element of indication or suggestion meaning must There must be specific orientation, be constructed and operated in a specific orientation, therefore be not considered as limiting the invention.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or Implicitly include at least one this feature.In the description of the present invention, the meaning of " plurality " is at least two, such as two, three It is a etc., unless otherwise specifically defined.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc. Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be mechanical connect It connects, is also possible to be electrically connected;It can be directly connected, can also can be in two elements indirectly connected through an intermediary The interaction relationship of the connection in portion or two elements, unless otherwise restricted clearly.For those of ordinary skill in the art For, the specific meanings of the above terms in the present invention can be understood according to specific conditions.
In the present invention unless specifically defined or limited otherwise, fisrt feature in the second feature " on " or " down " can be with It is that the first and second features directly contact or the first and second features pass through intermediary mediate contact.Moreover, fisrt feature exists Second feature " on ", " top " and " above " but fisrt feature be directly above or diagonally above the second feature, or be merely representative of First feature horizontal height is higher than second feature.Fisrt feature can be under the second feature " below ", " below " and " below " One feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example Point is included at least one embodiment or example of the invention.In the present specification, schematic expression of the above terms are not It must be directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be in office It can be combined in any suitable manner in one or more embodiment or examples.In addition, without conflicting with each other, the skill of this field Art personnel can tie the feature of different embodiments or examples described in this specification and different embodiments or examples It closes and combines.
Although the embodiments of the present invention has been shown and described above, it is to be understood that above-described embodiment is example Property, it is not considered as limiting the invention, those skilled in the art within the scope of the invention can be to above-mentioned Embodiment is changed, modifies, replacement and variant.

Claims (8)

1. crossing the valve body control method of cold loop in a kind of multi-line system, which is characterized in that the multi-line system includes room Outer machine, part flow arrangement and multiple indoor units, the outdoor unit include compressor, the part flow arrangement include the first heat-exchanging component and Second heat-exchanging component, the outlet and the first heat exchange of second heat-exchanging component of the first heat exchange flow path of first heat-exchanging component First throttle valve is set between the entrance of flow path, and the outlet of the first heat exchange flow path of second heat-exchanging component is changed with described second Second throttle is set between the entrance of the second heat exchange flow path of hot component, the second heat exchange flow path of second heat-exchanging component It exports and is connected to the entrance of the second heat exchange flow path of first heat-exchanging component, the heat exchange flow path of first heat-exchanging component and institute The heat exchange flow path for stating the second heat-exchanging component constituted cold loop, the described method comprises the following steps:
Obtain the discharge superheat of the compressor;
When the discharge superheat of the compressor is less than the first preset value, if the second heat exchange stream of first heat-exchanging component The outlet superheat degree on road is less than first outlet target superheat degree, then carries out aperture to the second throttle and turn control down;
When the aperture regulation of the second throttle is to minimum aperture, if the second heat exchange flow path of first heat-exchanging component Outlet superheat degree be less than the first outlet target superheat degree, then the minimum aperture is carried out turning amendment down, according to institute The outlet superheat degree and the first outlet target superheat degree for stating the second heat exchange flow path of the first heat-exchanging component continue to described the Two throttle valves carry out aperture and turn control down, until the discharge superheat of the compressor is greater than the second preset value, wherein described the Two preset values are greater than first preset value.
2. crossing the valve body control method of cold loop in multi-line system according to claim 1, which is characterized in that when described When the discharge superheat of compressor is less than the first preset value, judge that the compressor has back liquid risk.
3. crossing the valve body control method of cold loop in multi-line system according to claim 1 or 2, which is characterized in that logical It crosses and the current minimum aperture of the second throttle is subtracted into default aperture threshold value to carry out turning amendment down to the minimum aperture.
4. crossing the valve body control method of cold loop in multi-line system according to claim 1, which is characterized in that described more On-line system works under main refrigeration mode or pure refrigeration mode.
5. a kind of multi-line system characterized by comprising
Outdoor unit, the outdoor unit include compressor;
Multiple indoor units;
Part flow arrangement, the part flow arrangement include the first heat-exchanging component and the second heat-exchanging component, and the of first heat-exchanging component First throttle valve is set between the entrance of first heat exchange flow path of the outlet and second heat-exchanging component of one heat exchange flow path, it is described It is set between the entrance of second heat exchange flow path of the outlet and second heat-exchanging component of the first heat exchange flow path of the second heat-exchanging component Set second throttle, the outlet and the second heat exchange of first heat-exchanging component of the second heat exchange flow path of second heat-exchanging component The entrance of flow path is connected to, and the heat exchange flow path of first heat-exchanging component and the heat exchange flow path of second heat-exchanging component constitute supercooling Circuit;
Control module, the control module are used to obtain the discharge superheat of the compressor, and in the exhaust of the compressor Judge whether the outlet superheat degree of the second heat exchange flow path of first heat-exchanging component is less than when the degree of superheat is less than the first preset value First outlet target superheat degree, wherein if the outlet superheat degree of the second heat exchange flow path of first heat-exchanging component is less than the The one export goal degree of superheat, the control module then carry out aperture to the second throttle and turn control down, and described second When the aperture regulation of throttle valve is to minimum aperture, if the outlet superheat degree of the second heat exchange flow path of first heat-exchanging component is small In the first outlet target superheat degree, the control module then carries out turning amendment down to the minimum aperture, according to The outlet superheat degree of second heat exchange flow path of the first heat-exchanging component and the first outlet target superheat degree continue to described second Throttle valve carries out aperture and turns control down, until the discharge superheat of the compressor is greater than the second preset value, wherein described second Preset value is greater than first preset value.
6. multi-line system according to claim 5, which is characterized in that when the discharge superheat of the compressor is less than When one preset value, the control module judges that the compressor has back liquid risk.
7. multi-line system according to claim 5 or 6, which is characterized in that the control module passes through described second The current minimum aperture of throttle valve subtracts default aperture threshold value to carry out turning amendment down to the minimum aperture.
8. multi-line system according to claim 5, which is characterized in that the multi-line system is in main refrigeration mode or pure It works under refrigeration mode.
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