CN105980793A - Device for the thermal conditioning of a motor vehicle passenger compartment and/or component - Google Patents
Device for the thermal conditioning of a motor vehicle passenger compartment and/or component Download PDFInfo
- Publication number
- CN105980793A CN105980793A CN201480075433.1A CN201480075433A CN105980793A CN 105980793 A CN105980793 A CN 105980793A CN 201480075433 A CN201480075433 A CN 201480075433A CN 105980793 A CN105980793 A CN 105980793A
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- Prior art keywords
- heat exchanger
- heat
- compressor
- cryogenic fluid
- entrance
- Prior art date
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Links
- 230000003750 conditioning effect Effects 0.000 title claims abstract description 5
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 4
- 239000012530 fluid Substances 0.000 claims description 96
- 239000006200 vaporizer Substances 0.000 claims description 13
- 239000012071 phase Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 7
- 239000007791 liquid phase Substances 0.000 claims description 7
- 230000008878 coupling Effects 0.000 claims description 2
- 238000010168 coupling process Methods 0.000 claims description 2
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 239000002826 coolant Substances 0.000 abstract 1
- 239000013529 heat transfer fluid Substances 0.000 abstract 1
- 238000004378 air conditioning Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000875 corresponding effect Effects 0.000 description 3
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 2
- FXRLMCRCYDHQFW-UHFFFAOYSA-N 2,3,3,3-tetrafluoropropene Chemical compound FC(=C)C(F)(F)F FXRLMCRCYDHQFW-UHFFFAOYSA-N 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B5/00—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
- F25B5/04—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity arranged in series
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/005—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/39—Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/23—Separators
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Air-Conditioning For Vehicles (AREA)
Abstract
The invention relates to a device for thermally conditioning a motor vehicle passenger compartment and/or component, which comprises a coolant circuit (1) able to cool the air (F) bound for the passenger compartment of a vehicle using an evaporator (E2) and a heat-transfer fluid circuit (4) able to cool said component of the motor vehicle. A flap (8) is positioned upstream of the evaporator (E2) to regulate the flow of air (Fa) passing through the evaporator (E2).
Description
Technical field
The present invention relates to a kind of for motor vehicles main cabin and/or the heat regulating device of parts (such as battery).
Background technology
This kind of device known in the art includes cryogenic fluid loop, and it includes that can be formed as condenser first changes
Hot device, can be formed as vaporizer the second heat exchanger, can be formed as the 3rd heat exchanger of vaporizer, the first compressor,
Two compressoies, the first pressure relief mechanism, the second pressure relief mechanism, for classify cryogenic fluid liquid and gas discrete device, with
And cryogenic fluid can be made along the device of at least one looped cycle, described loop passes in succession through First Heat Exchanger, the first decompression
Component, the 3rd heat exchanger and discrete device, subsequently, the liquid phase of the cryogenic fluid obtained from discrete device is by the second decompression structure
Part, the second heat exchanger and the first compressor, then by the second compressor, and the gas phase of the cryogenic fluid obtained from discrete device
Directly by the second compressor.
This kind of device also include heat exchanging fluid circuit, it includes that the 3rd heat exchanger, the 3rd heat exchanger can make heat exchange stream
Heat between body and cryogenic fluid swaps;Heat exchanging fluid circuit includes that the 4th heat exchanger, the 4th heat exchanger can make
Heat exchange is carried out between cryogenic fluid and the battery of motor vehicles;Heat exchanging fluid circuit includes the 5th heat exchange forming radiator
Device, pump and can at least one makes the device that heat exchanging fluid circulates according in following operator scheme:
-the first operator scheme, wherein, heat exchanging fluid flows along the first loop, described first loop pass in succession through pump,
Four heat exchangers and the 3rd heat exchanger,
-the second operator scheme, wherein, heat exchanging fluid flows along second servo loop, described second servo loop pass in succession through pump, the
Four heat exchangers and the 5th heat exchanger,
Second heat exchanger is contained in air stream circulation canal, and the circulation of described air is toward vehicle passenger cabin, the second heat exchanger energy
Enough make to carry out between cryogenic fluid and air stream heat exchange.
First Heat Exchanger and the 5th heat exchanger are commonly disposed to the front of motor vehicles.Second exchanger and passage are such as
Belong to heating, ventilate and/or air-conditioning equipment (also referred to as H.V.A.C. (heating, heating ventilation and air-conditioning)).
During operation, the second heat exchanger can make by the cooled (air for main cabin of the air stream of above-mentioned passage
Regulation).Further, the 4th heat exchanger can make battery be cooled.
Can be in the region of First Heat Exchanger and the 5th heat exchange from the heat of removal for the air stream of main cabin or battery
The region of device is discharged.Specifically, according to the temperature of vehicle outer air, transporting can from the heat exchanging fluid of the heat of battery removal
With:
-by the 3rd heat exchanger, this heat being delivered to cryogenic fluid loop, then cryogenic fluid loop is changed by first
Hot device by the air outside this heat dissipation to vehicle,
-or by the 5th heat exchanger, this heat is directly discharged in extraneous air.
According to demand with temperature or the humidity condition of extraneous air, it is necessary to second heat exchanger and fourth is independently variable and changes
The cooling power level of hot device.
To this end, based on current structure, theoretically, it is necessary to speed and second compression of first compressor are independently variable
The speed of device, or change the cubic metre of the such as second compressor, in order to realize second and the 4th cooling power institute of heat exchanger
Desired specification, this is difficult to technically.
Summary of the invention
Especially, it is an object of the present invention to provide a kind of simplicity for this problem, effective, economic solution party
Case.
To this end, the present invention proposes a kind of for motor vehicles main cabin and/or the heat regulating device of parts, comprising:
Cryogenic fluid loop, it First Heat Exchanger including being formed as condenser, it is possible to be formed as the of vaporizer
Two heat exchangers, it is possible to be formed as the 3rd heat exchanger of vaporizer, the first compressor, the second compressor, the first pressure relief mechanism, second
Pressure relief mechanism, for separating the discrete device of liquid and gas of cryogenic fluid and cryogenic fluid can be made along at least one
The device of looped cycle, described loop passes in succession through First Heat Exchanger, the first pressure relief mechanism, the 3rd heat exchanger and discrete device,
Subsequently, from the liquid phase of the cryogenic fluid of discrete device generation by the second pressure relief mechanism, the second heat exchanger and the first compressor, and
Then by the second compressor, from the gas phase of the cryogenic fluid of discrete device generation directly by the second compressor,
Heat exchanging fluid circuit, it includes the 3rd heat exchanger so that the 3rd heat exchanger can exchange heat exchanging fluid and cryogenic fluid
Between heat, can exchange between cryogenic fluid and motor vehicle component heat the 4th heat exchanger, can be formed as scattered
5th heat exchanger of hot device, pump and can be according at least one and the device that makes heat exchanging fluid circulate, institute in following operator scheme
State operator scheme to include:
-the first operator scheme, wherein heat exchanging fluid extends successively through along the first circuit cycle, described first loop
Pump, the 4th heat exchanger and the 3rd heat exchanger,
-the second operator scheme, wherein heat exchanging fluid circulates along second servo loop, and described second servo loop extends successively through
Pump, the 4th heat exchanger and the 5th heat exchanger,
Second heat exchanger is contained in the circulation canal of the air stream that vehicle passenger cabin is led in expectation, and the second heat exchanger can be handed over
Change the heat between cryogenic fluid and air stream, it is characterised in that the second heat exchanger includes controlling shunting device (controlled
Branching means), it can make being diverted at least partially beyond the second heat exchanger of described air stream.
Preferably, the temperature at the air of the second heat exchanger mixed downstream is substantially equal to design temperature.
In this way, use for different operating situation have constant cubic metre compressor and use with
In the case of the compressor that identical speed (but, this speed can change according to aforesaid operations situation) rotates, by changing
By the air stream of the second exchanger, it is possible to achieve the institute for cooling power of both the second heat exchanger and the 4th heat exchanger
Desired specification.
According to a feature of the present invention, shunting device includes being positioned at the second heat exchanger relative to the flow direction of air stream
Upstream, the valve member that is positioned in flow channel.
This technical scheme simple possible, with low cost, reliable and take less space.
In this case, valve member can with control device be associated, control device can control valve component position with adjust
The flow saving the air stream by the second heat exchanger and the air flow not passing through the second heat exchanger being split, and,
It is preferably so that the temperature of the air of the mixed downstream at the second heat exchanger is equal to design temperature.
Further, the discrete device of the liquid and gas separating cryogenic fluid can include bottle.
Further, each compressor can include Rotating input shaft, and the power shaft of said two compressor is for rotating
Coupling, in order to driven at the same speed.
According to another feature of the invention, cryogenic fluid loop includes:
-between the outlet and the entrance of First Heat Exchanger of the second compressor extend Part I,
-the Part II that extends between the outlet and the cryogenic fluid entrance of the 3rd heat exchanger of First Heat Exchanger, this is the years old
Two parts have the first pressure relief mechanism,
-export the entrance with the discrete device of the liquid and gas separating cryogenic fluid at the cryogenic fluid of the 3rd heat exchanger
Between extend Part III,
-export the Part IV extended between the entrance of the second heat exchanger, this Part IV at the first of discrete device
There is the second pressure relief mechanism,
-the second heat exchanger outlet with the entrance of the second compressor between extend Part V,
-the first compressor outlet with the entrance of the second compressor between extend Part VI, this Part VI bag
Include branch,
-export, at the second of discrete device, the Part VII extended between branch,
Heat exchanging fluid circuit includes:
-the 3rd heat exchanger heat exchanging fluid export and the entrance of pump between extend Part I, this Part I bag
Include branch,
-between the entrance of delivery side of pump and the 4th heat exchanger extend Part II,
-between the outlet and the first path of valve (such as control valve) of the 4th heat exchanger extend Part III,
-between second path and the heat exchanging fluid entrance of the 3rd heat exchanger of valve extend Part IV,
-between the 3rd path and the entrance of the 5th heat exchanger of valve extend Part V,
-the 5th heat exchanger outlet with branch between extend Part VI.
Preferably, the parts of motor vehicles are batteries.
Further, First Heat Exchanger can make to carry out between cryogenic fluid and air heat exchange.
In the same fashion, the 5th heat exchanger can make to carry out between heat exchanging fluid and air heat exchange.
The invention still further relates to a kind of motor vehicles, it is characterised in that it includes the device of the above-mentioned type.
Accompanying drawing explanation
The following description be given in non-limiting example mode by reading, and combine accompanying drawing, it is better understood with
The present invention and other details, features and advantages of the present invention, in the accompanying drawings:
-Fig. 1 is the schematic diagram of the heat regulating device according to prior art;
-Fig. 2 is enthalpy entropy (Mollier) figure of the operation in the cryogenic fluid loop of the device illustrating Fig. 1;
-Fig. 3 corresponds to the diagram of Fig. 1, and it illustrates according to one embodiment of present invention.
Detailed description of the invention
Fig. 1 shows the device of the thermal conditioning of a kind of main cabin for motor vehicles of the prior art and/or battery.
This device includes cryogenic fluid loop 1, comprising: outside being formed as condenser and cryogenic fluid can being made with vehicle
Carry out the First Heat Exchanger E1 of heat exchange between portion's air, be formed as vaporizer and cryogenic fluid and outside vehicle can be made
Carry out the second heat exchanger E2 of heat exchange between air, be formed as vaporizer and can make cryogenic fluid and heat exchanging fluid it
Between carry out the 3rd heat exchanger E3 of heat exchange, and the first compressor C1, the second compressor C2, the first pressure relief mechanism D1,
Two pressure relief mechanism D2 and for separating the discrete device that form is bottle B of liquid and gas of cryogenic fluid.
First Heat Exchanger E1 is generally arranged at the front of vehicle.Second heat exchanger E2 generally falls into heating, ventilates and/or empty
Adjust device (also referred to as H.V.A.C. (heat, ventilate and air-conditioning)).
Second heat exchanger E2 is specifically located in the circulating line 2 of air stream F, and described pipeline 2 is in the main cabin of vehicle
In open wide, described air stream is as shown by arrow F.
Cryogenic fluid loop 1 specifically includes:
-Part I P1, it extends between the outlet and the entrance of First Heat Exchanger E1 of the second compressor C2,
-Part II P2, it prolongs between outlet and the cryogenic fluid entrance of the 3rd heat exchanger E3 of First Heat Exchanger E1
Stretching, this Part II P2 is provided with the first pressure relief mechanism D1,
-Part III P3, its extension between cryogenic fluid outlet and the entrance of bottle B of the 3rd heat exchanger E3,
-Part IV P4, its extension between the first outlet and the entrance of the second heat exchanger E2 of bottle B, the 4th
P4 is divided to have the second pressure relief mechanism D2,
-Part V P5, it is extension between outlet and the entrance of the first compressor C1 of the second heat exchanger E2,
-Part VI P6, it is extension between outlet and the entrance of the second compressor C2 of the first compressor C1, and the 6th
Part P6 includes branch X,
Part VII P7, it extends between the second outlet and the branch X of bottle B.
Cryogenic fluid for example, R-134a (1,1,1,2-tetrafluoroethane) or R-1234yf (2,3,3,3-tetrafluoropropene) class
Type.
Described device also includes heat exchanging fluid circuit 4, and this fluid reflux 4 includes: make between heat exchanging fluid and cryogenic fluid
Carry out the 3rd heat exchanger E3 of heat exchange, it is possible to make to carry out between cryogenic fluid and the battery of motor vehicles the of heat exchange
Four heat exchanger E4, are formed as the 5th heat exchanger E5 of radiator, pump P, and three-way valve V (such as electromagnetic valve (solenoid
valve))。
Heat exchanging fluid circuit 4 specifically includes:
-Part I P'1, its extension between heat exchanging fluid outlet and the entrance of pump P of the 3rd heat exchanger E3, this is first years old
Part P'1 includes branch X',
-Part II P'2, it is extension between outlet and the entrance of the 4th heat exchanger E4 of pump P,
-Part III P'3, it prolongs between the outlet and the first path 5 of valve V (such as electromagnetic valve) of the 4th heat exchanger E4
Stretch,
-Part IV P'4, it extends between the second path 6 and the heat exchanging fluid entrance of the 3rd heat exchanger E3 of valve V,
-Part V P'5, it extends between the 3rd path 7 and the entrance of the 5th heat exchanger E5 of valve V,
-Part VI P'6, it extends between the outlet and branch X' of the 5th heat exchanger E5,
-heat exchanging fluid e.g. ethanol water (glycolic water).
During operation, cryogenic fluid circulates in a loop, this loop pass in succession through First Heat Exchanger E1 (condenser),
First pressure relief mechanism D1, the 3rd heat exchanger E3 (vaporizer) and bottle B, from the liquid phase of the cryogenic fluid of bottle B generation subsequently
By the second pressure relief mechanism D2, the second heat exchanger E2 (vaporizer) and the second compressor C1, then pass through the second compressor C2, from
The gas phase of the cryogenic fluid that bottle B produces is directly by the second compressor C2.
Enthalpy-entropy diagram at Fig. 2 shows corresponding thermodynamic cycle.In this figure, abscissa is the enthalpy H of cryogenic fluid, vertical
Coordinate is the pressure P of cryogenic fluid.
It is shown in the cryogenic fluid circulation 1 shown in enthalpy-entropy diagram and Fig. 1 by the point of i1 to i10 labelling, in order to reason
Solve.Phase (the liquid phase of cryogenic fluid;Biphase, i.e. liquid gas coexists;Gas phase) also illustrate on figure, also show that the different step of circulation
(evaporate, condense, compress, reduce pressure).
For heat exchanging fluid circuit 4, corresponding fluids is with following cycle of modes:
-in the first mode of operation, heat exchanging fluid along the first looped cycle, this first loop pass in succession through pump P, the 4th
Heat exchanger E4 and the 3rd heat exchanger E3, the most again by pump P.Here, open first path 5 and second path 6 of valve V, and
Close the 3rd path 7 of valve closing V,
-in this second mode of operation, heat exchanging fluid along the second looped cycle, this second loop pass in succession through pump P, the 4th
Heat exchanger E4 and the 5th heat exchanger E5, the most again by pump P.Here, open first path 5 and the 3rd path 7 of valve V, and
Close the second path 6 of valve closing V.
By this way, in the first mode of operation, battery is cooled down by the 4th heat exchanger E4 (vaporizer), moves from battery
The heat gone out is transferred to cryogenic fluid loop 1 by the 3rd heat exchanger E3.
Differently, in this second mode of operation, battery is cooled down by the 4th heat exchanger E4 (vaporizer), but, from battery
The heat of removal is discharged in the air outside vehicle by the 5th heat exchanger E5 (radiator).
Meanwhile, regardless of the operator scheme of heat exchanging fluid circuit 4, by the passage for the main cabin split shed at vehicle
In air F by second heat exchanger E2 (vaporizer) cool down, Btu utilization First Heat Exchanger E1 (condenser) is discharged into vehicle
In outer air.
Table 1 below shows the theoretical property example of several operating mode.For every kind of operating mode, it is shown that the first compressor C1 cube
Volume, the theoretical cubic metre of the second compressor C2, the temperature of extraneous air, thermal power (the such as basis of the second heat exchanger E2
The air-conditioning power of user's instruction) and the thermal power (power needed for cooling battery) of the 4th heat exchanger E4.It should be noted that two compressions
Device C1, C2 rotate with identical speed, and described speed can change as the case may be.It should be noted that to realize under every kind of operating mode
Specific thermal power level, it is necessary to change the second compressor C2 cubic metre (assume for all operations situation, first
The cubic metre of compressor C1 keeps constant).Technically, it is difficult to change the cubic metre of compressor during operation.
Cubic metre CP1 [cm3] | 10.3 | 10.3 | 10.3 | 10.3 |
Cubic metre CP2 [cm3] | 24.7 | 36.8 | 26.1 | 35.5 |
Air-conditioning power [W] | 2330 | 2325 | 2342 | 1717 |
The cooling power [W] of battery | 3306 | 4478 | 2867 | 2867 |
Table 1
It is within the contemplation of the invention that by providing a kind of device similar with said apparatus to overcome this defect, but wherein, valve
Component 8 is installed in the passage 2 of recycled air stream F, and described air stream F leads to main cabin, and this valve member 8 is along air stream
The direction of F is arranged on the upstream of the second heat exchanger E2, as shown in Figure 3.
The Angle Position of valve member 8 is controlled, in order to regulate (and the therefore cooled) air by the second heat exchanger E2
Flow the flow (flow rate) of Fa, and regulation is redirected and does not passes through the flow of the air stream Fb of the second heat exchanger E2.
Valve member 8 preferably moves, at the first extreme position, all air stream F between the first extreme position and the second extreme position
Being redirected and do not pass through the second heat exchanger E2, at the second extreme position, all air stream F pass through the second heat exchanger E2.Valve
Component 8 also can occupy all centre positions between the two extreme position.Preferably, perform the thermal conditioning according to the present invention
The control of device, so that the temperature at the air of the mixed downstream of the second heat exchanger E2 is equal to design temperature.
Table 2 below shows the example corresponding essentially to above-mentioned operating mode, in other words, these examples consist essentially of
Two heat exchanger E2 and the 4th heat exchanger E4 are required or the identical thermal power level specified, and the cubic metre of the first compressor C1 is also
Identical.Further, in the example that these are different, the rotating speed of two compressoies C1, C2 is identical, but this speed can root
Change according to operational circumstances, as described above.
Except the information having shown that in table 1, table 2 includes an indicated value, and it does not pass through the second heat exchange with being redirected
Device E2 air stream is correlated with relative to the mass percent of total air stream.Therefore, numerical value 0% represents that all air stream F are by second
Exchanger E2, numerical value 20% represent valve member 8 be positioned such that the 20% of the mass flow of air stream F be redirected and not
By the second heat exchanger E2 (therefore, the 80% of this mass flow passes through the second heat exchanger E2).
Table 2
It should be noted that the present invention only by change valve member 8 position, just can make device be easily adapted to different size or
Operating mode, in other words, makes device be applicable to the second heat exchanger E2 (for regulating the air in main cabin) and the 4th heat exchanger E4 (for cold
But battery) different thermal power level, and compressor C1, C2 have constant cubic metre (can be according to operation identical
Situation and change) rotate under speed.
Claims (10)
1. for motor vehicles main cabin and/or a device for the thermal conditioning of parts, comprising:
Cryogenic fluid loop (1), it includes to be formed as the First Heat Exchanger (E1) of condenser, can being formed as vaporizer
Second heat exchanger (E2), the 3rd heat exchanger (E3) of vaporizer, the first compressor (C1), the second compressor can be formed as
(C2), the first pressure relief mechanism (D1), the second pressure relief mechanism (D2), for separating the discrete device of liquid and gas of cryogenic fluid
And cryogenic fluid can be made to pass in succession through described First Heat Exchanger along the device of at least one circuit cycle, described loop (B)
(E1), described first pressure relief mechanism (D1), described 3rd heat exchanger (E3) and described discrete device (B), subsequently, from described separation
The liquid phase of the cryogenic fluid that device (B) produces by before described second compressor (C2) by described second pressure relief mechanism
(D2), described second heat exchanger (E2) and described first compressor (C1), the cryogenic fluid produced from described discrete device (B)
Gas phase directly passes through described second compressor (C2),
Heat exchanging fluid circuit, it includes described 3rd heat exchanger (E3), so that described 3rd heat exchanger (E3) can exchange described
Heat between heat exchanging fluid and described cryogenic fluid, the described cryogenic fluid described parts with described motor vehicles can be exchanged
Between heat the 4th heat exchanger (E4), the 5th heat exchanger (E5) of radiator, pump (P) can be formed as and change described in can making
Hot fluid is according at least one device being circulated in following operator scheme:
-the first operator scheme, wherein, described heat exchanging fluid along the first looped cycle, this first loop pass in succession through pump (P),
4th heat exchanger (E4) and the 3rd heat exchanger (E3),
-the second operator scheme, wherein, described heat exchanging fluid is along the second looped cycle, and this second loop passes in succession through described pump
(P), described 4th heat exchanger (E4) and described 5th heat exchanger (E5),
Described second heat exchanger (E2) is accommodated in the circulation being expected in the described main cabin of described vehicle open air stream (F)
In passage (2), described second heat exchanger (E2) can exchange heat between described cryogenic fluid and described air stream (F), and it is special
Levying and be, described second heat exchanger (E2) includes controlled shunting device (8), and this controlled shunting device can be by air stream (F)
(Fb) is diverted to beyond described second heat exchanger (E2) at least partially.
Device the most according to claim 1, it is characterised in that described shunting device includes valve member (8), this valve member position
In the upstream of described second heat exchanger (E2) relative to the flow direction of described air stream (F), it is positioned at described air stream (F)
In flow channel (2).
Device the most according to claim 2, it is characterised in that described valve member (8) is associated with control member, described control
Component processed can the position of control valve component (8), in order to adjust air stream (Fa) by the second heat exchanger (E2) flow, with
And it is divided to the flow of air stream (Fb) beyond the second heat exchanger (E2).
4. according in claims 1 to 3 described device, it is characterised in that for separating the described of described cryogenic fluid
The described discrete device of liquid phase and described gas phase includes bottle (B).
5. according in Claims 1-4 described device, it is characterised in that each compressor (C1, C2) includes rotating defeated
Enter axle, the described power shaft of said two compressor (C1, C2) in terms of rotation be coupling, in order at the same speed by
Drive.
6. according in claim 1 to 5 described device, it is characterised in that described cryogenic fluid loop (1) including:
-Part I (P1), it is between the outlet and the entrance of described First Heat Exchanger (E1) of described second compressor (C2)
Extend,
The cryogenic fluid of-Part II (P2), its outlet at described First Heat Exchanger (E1) and described 3rd heat exchanger (E3)
Extending between entrance, described Part II (P2) is provided with described first pressure relief mechanism (D1),
-Part III (P3), it exports at the cryogenic fluid of described 3rd heat exchanger (E3) and is used for separating described cryogenic fluid
Described liquid phase and described gas phase described discrete device (B) entrance between extend,
-Part IV (P4), it is between the first outlet and the entrance of described second heat exchanger (E2) of described discrete device (B)
Extending, described Part IV (P4) is provided with described second pressure relief mechanism (D2),
-Part V (P5), it is between the outlet and the entrance of described first compressor (C1) of described second heat exchanger (E2)
Extend,
-Part VI (P6), it is between the outlet and the entrance of described second compressor (C2) of described first compressor (C1)
Extending, described Part VI (P6) includes branch (X),
-Part VII (P7), its extension between the second outlet and the described branch (X) of described discrete device (B),
Described heat exchanging fluid circuit (4) including:
-Part I (P'1), it exports between the entrance of described pump (P) at the heat exchanging fluid of described 3rd heat exchanger (E3)
Extending, described Part I (P'1) includes branch (X'),
-Part II (P'2), it extends between the outlet and the entrance of described 4th heat exchanger (E4) of described pump (P),
-Part III (P'3), it extends between outlet and the first path (5) of valve (V) of described 4th heat exchanger (E4),
Described valve (V) e.g. Controlled valve,
-Part IV (P'4), its heat exchanging fluid in second path (6) of described valve (V) with described 3rd heat exchanger (E3) enters
Extend between Kou,
-Part V (P'5), it prolongs between the 3rd path (7) and the entrance of described 5th heat exchanger (E5) of described valve (V)
Stretch,
-Part VI (P'6), it extends between outlet and the described branch (X') of described 5th heat exchanger (E5).
7. according in claim 1 to 6 described device, it is characterised in that the described parts of described motor vehicles are electricity
Pond.
8. according in claim 1 to 7 described device, it is characterised in that described First Heat Exchanger (E1) can exchange
Heat between described cryogenic fluid and described air.
9. according in claim 1 to 8 described device, it is characterised in that described 5th heat exchanger (E5) can exchange
Heat between described heat exchanging fluid and described air.
10. motor vehicles, it is characterised in that it includes according in claim 1 to 9 described device.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1362724A FR3015012B1 (en) | 2013-12-16 | 2013-12-16 | DEVICE FOR THERMALLY CONDITIONING A CAR AND / OR AN ORGAN OF A MOTOR VEHICLE |
FR1362724 | 2013-12-16 | ||
PCT/EP2014/076280 WO2015090943A1 (en) | 2013-12-16 | 2014-12-02 | Device for the thermal conditioning of a motor vehicle passenger compartment and/or component |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105980793A true CN105980793A (en) | 2016-09-28 |
Family
ID=50624689
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201480075433.1A Pending CN105980793A (en) | 2013-12-16 | 2014-12-02 | Device for the thermal conditioning of a motor vehicle passenger compartment and/or component |
Country Status (4)
Country | Link |
---|---|
CN (1) | CN105980793A (en) |
DE (1) | DE112014005711T5 (en) |
FR (1) | FR3015012B1 (en) |
WO (1) | WO2015090943A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019001351A1 (en) * | 2017-06-27 | 2019-01-03 | 杭州三花研究院有限公司 | Thermal management system |
CN109398026A (en) * | 2018-09-11 | 2019-03-01 | 蔚来汽车有限公司 | Electric automobile and air conditioning system thereof |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3056289B1 (en) * | 2016-09-16 | 2018-09-28 | Valeo Systemes Thermiques | THERMAL MANAGEMENT CIRCUIT FOR MOTOR VEHICLE |
FR3057343B1 (en) * | 2016-10-12 | 2019-06-21 | Valeo Systemes Thermiques | MEANS FOR MASKING FOR AIR CONDITIONING SYSTEM EXCHANGER |
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2013
- 2013-12-16 FR FR1362724A patent/FR3015012B1/en active Active
-
2014
- 2014-12-02 DE DE112014005711.8T patent/DE112014005711T5/en not_active Withdrawn
- 2014-12-02 WO PCT/EP2014/076280 patent/WO2015090943A1/en active Application Filing
- 2014-12-02 CN CN201480075433.1A patent/CN105980793A/en active Pending
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US4972992A (en) * | 1988-07-11 | 1990-11-27 | Robert Bosch Gmbh | Device for heating passenger spaces in power vehicles |
US5134859A (en) * | 1991-03-29 | 1992-08-04 | General Electric Company | Excess refrigerant accumulator for multievaporator vapor compression refrigeration cycles |
FR2876323A1 (en) * | 2004-10-12 | 2006-04-14 | Renault Sas | DEVICE AND METHOD FOR CONTROLLING THE TEMPERATURE OF THE HABITACLE OF A MOTOR VEHICLE |
CN102548780A (en) * | 2009-08-07 | 2012-07-04 | 雷诺股份公司 | System for the overall control of heat for electrically propelled motor vehicle |
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WO2019001351A1 (en) * | 2017-06-27 | 2019-01-03 | 杭州三花研究院有限公司 | Thermal management system |
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CN109398026A (en) * | 2018-09-11 | 2019-03-01 | 蔚来汽车有限公司 | Electric automobile and air conditioning system thereof |
Also Published As
Publication number | Publication date |
---|---|
FR3015012B1 (en) | 2016-09-02 |
DE112014005711T5 (en) | 2016-09-15 |
WO2015090943A1 (en) | 2015-06-25 |
FR3015012A1 (en) | 2015-06-19 |
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