CN106482433A - Air-cooled separating refrigerating equipment - Google Patents
Air-cooled separating refrigerating equipment Download PDFInfo
- Publication number
- CN106482433A CN106482433A CN201610950635.7A CN201610950635A CN106482433A CN 106482433 A CN106482433 A CN 106482433A CN 201610950635 A CN201610950635 A CN 201610950635A CN 106482433 A CN106482433 A CN 106482433A
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- air
- evaporimeter
- heat exchanger
- hypothermia
- compressor
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- 239000003507 refrigerant Substances 0.000 claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 230000002631 hypothermal effect Effects 0.000 claims description 47
- 239000000203 mixture Substances 0.000 claims description 27
- 238000005057 refrigeration Methods 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 17
- 230000008676 import Effects 0.000 claims description 7
- 230000007704 transition Effects 0.000 claims description 6
- 239000006200 vaporizer Substances 0.000 claims description 2
- 206010021113 Hypothermia Diseases 0.000 claims 20
- 238000010025 steaming Methods 0.000 claims 1
- 238000003860 storage Methods 0.000 description 11
- 238000009835 boiling Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 238000009833 condensation Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 208000011580 syndromic disease Diseases 0.000 description 1
- 210000005239 tubule Anatomy 0.000 description 1
- 239000012808 vapor phase Substances 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
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D19/00—Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors
- F25D19/003—Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors with respect to movable containers
-
- 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
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D2201/00—Insulation
- F25D2201/30—Insulation with respect to sound
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Other Air-Conditioning Systems (AREA)
Abstract
The present invention provides a kind of air-cooled separating refrigerating equipment, including compressor, hot end heat exchanger and blower fan, it is characterized in that, also include outdoor machine shell, the compressor, the hot end heat exchanger and the blower fan are arranged in the outdoor machine shell, and the blower fan is arranged between the compressor and the hot end heat exchanger, is provided with air channel between the blower fan and the compressor, the hot end heat exchanger adopts heat regenerator, and the heat regenerator has refrigerant pipeline and heat-exchanging water pipeline；Air-supply passage is provided with the interior locker, the air-supply passage is provided with air inlet and air outlet, and circulating fan and the cool end heat exchanger is provided with the air-supply passage.Realize ease of use and versatility is improved, and improve user's comfort and experience property.
Description
Technical field
The present invention relates to refrigeration plant, more particularly to a kind of air-cooled separating refrigerating equipment.
Background technology
At present, refrigeration plant（Refrigerator, refrigerator etc.）It is widely used in daily life.Traditional family expenses system
Cool equipment is divided into storing compartment and cabin using single body structure, casing, and the part such as compressor, condenser and fan is arranged on
In cabin, storing compartment is used for storing to be frozen or refrigeration article.In actual use, the compressor operating in cabin
Noise and heat will be produced, cause user's comfort of refrigeration plant in prior art and experience property poor；Meanwhile, storing
Compartment is arranged in same casing, and user needs to configure multiple independent refrigeration plants to meet refrigeration storing in not chummery
Need, cause the ease of use of refrigeration plant and versatility in prior art relatively low.
Content of the invention
The technical problem to be solved is：A kind of air-cooled separating refrigerating equipment is provided, realizes raising split type
The ease of use of refrigeration plant and versatility, and improve user's comfort and experience property.
The present invention provide technical scheme be, a kind of air-cooled separating refrigerating equipment, including compressor, hot end heat exchanger and
Blower fan, it is characterised in that also include outdoor machine shell, the compressor, the hot end heat exchanger and the blower fan are arranged on described
In outdoor machine shell, the blower fan is arranged between the compressor and the hot end heat exchanger, the blower fan and the compressor
Between be provided with air channel, the hot end heat exchanger adopts heat regenerator, the heat regenerator have refrigerant pipeline and
Heat-exchanging water pipeline；Air-supply passage is provided with the interior locker, the air-supply passage is provided with air inlet and air outlet, institute
State in air-supply passage and be provided with circulating fan and the cool end heat exchanger.
The air-cooled separating refrigerating equipment that the present invention is provided, by using split-type structural be divided into outdoor machine shell and multiple solely
Vertical indoor locker, the part such as compressor, condenser and throttling arrangement are disposed in the outdoor in casing, as outdoor machine shell is arranged
The noise produced in outside, compressor and heat will not produce impact to indoor, can effectively improve the use of user
Comfortableness and experience property；Also, due to adopting multiple independent indoor lockers, user can be as needed by different interiors
Locker is placed in different rooms, realizes improving ease of use and the versatility of separating refrigerating equipment.In addition, will pressure
Contracting machine, condenser and blower fan are arranged on same air channel, and the wind that sufficiently can be produced using blower fan is while to compressor and condensation
Device is radiated, the heat transfer effect of general increase compressor and condenser, improves the heat exchange efficiency of refrigeration system, improves energy profit
With rate.
Description of the drawings
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
Accompanying drawing to be used needed for technology description is had to be briefly described, it should be apparent that, drawings in the following description are these
Some bright embodiments, for those of ordinary skill in the art, without having to pay creative labor, acceptable
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structure principle chart of the air-cooled separating refrigerating apparatus embodiments of the present invention.
Fig. 2 is the schematic diagram of the air-cooled separating refrigerating apparatus embodiments of the present invention.
Fig. 3 is the structure principle chart of off-premises station in the air-cooled separating refrigerating apparatus embodiments of the present invention.
Fig. 4 is the structure principle chart of indoor locker in the air-cooled separating refrigerating apparatus embodiments of the present invention.It is embodied as
Mode
Purpose, technical scheme and advantage for making the embodiment of the present invention is clearer, below in conjunction with the embodiment of the present invention
Accompanying drawing, is clearly and completely described to the technical scheme in the embodiment of the present invention, it is clear that described embodiment is this
Bright a part of embodiment, rather than whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art are not having
There is the every other embodiment obtained under the premise of making creative work, belong to the scope of protection of the invention.
As shown in Figure 1-Figure 3, the air-cooled separating refrigerating equipment of the present embodiment adopts split-type structural, including outdoor machine shell
101 and multiple independent indoor lockers 102, outdoor machine shell 101 is placed on the outside of wall 100, and indoor locker 102 is put
Put in the inner side of wall 100, wherein, the compressor 1 of refrigeration system, condenser 2, throttling arrangement and blower fan（Not shown）Deng part
It is disposed in the outdoor in casing 101, and the cold end evaporimeter of refrigeration system is arranged in corresponding interior locker 102.
Specifically, the air-cooled separating refrigerating equipment of the present embodiment in actual use, as compressor 1 is arranged on
In outside outdoor machine shell 101, compressor 1 runs the noise of generation and heat will not produce impact to indoor, can be effective
Improve the comfortableness that uses indoors of user, improve user experience.Simultaneously as using multiple independent indoor lockers
102, used in indoor locker 102 can be placed as required on different rooms, realize single compressor 1 and meet not having sexual intercourse
Between freezing or chilled goods demand.According to user's needs, the interior locker 102 can be horizontal counter body or vertical counter
Body or wall-mounted cabinet.Preferably, it is preferred that in order to make full use of the condensation heat of hot end heat exchanger 2, hot end heat exchanger 2 is adopted
Heat regenerator, is provided with heat-storing material 20 in hot end heat exchanger 2, also, hot end heat exchanger 2 with refrigerant pipeline 21 and is changed
Hot water line 22, and wherein, refrigerant pipeline 21 is connected in refrigerating circuit and conveys refrigerant, and the confession then with outside of heat-exchanging water pipeline 22
Water end (W.E.) connects, and extraneous water is entered in heat-exchanging water pipeline 22 carries out heat exchange formation hot water, realizes making full use of the heat energy of condensation,
Improve energy utilization rate；And due to being provided with heat-storing material 20 in hot end heat exchanger 2, when shutting down, heat-storing material 20 still can
Heat water is enough provided.
Wherein, for air-supply passage 1020 is provided with indoor locker 102, air-supply passage 1020 is with air outlet 1021
With air inlet 1022, circulating fan 103 in the air-supply passage 1020, is additionally provided with, room can be realized using circulating fan 103
Air circulation flow in interior locker 102, to improve the temperature distribution evenness in indoor locker 102.
In addition, constituting recovery type heat refrigeration plant room for outdoor machine shell 101, compressor 1, condenser 2 and blower fan 10
Outer machine, the compressor 1, the condenser 2 and the blower fan 10 are arranged in the outdoor machine shell 101, and the blower fan 10 sets
Put between the compressor 1 and the condenser 2, between the blower fan 10 and the compressor 1, be provided with air channel（Do not mark
Note）.Specifically, compressor 1, condenser 2 and blower fan 10 are arranged on same straight line, and blower fan 10 is blown from 2 side air draught of condenser
To compressor 1, the lift problem of blower fan was both considered, can guarantee that the radiating effect of compressor and condenser again, reached energy-conservation mesh
's.Blower fan 10 is radiated to condenser 2 during 2 air draught of blower fan Wei Yu condenser 2 and compressor 1 between, meanwhile, blower fan 10 can be from cold
The peripheral air draught of condenser 2, the then wind-warm syndrome for blowing out are relatively low, and the radiating effect that gives after compressor 1 is preferable.Further, the room
The upper surface of outer cage 101 is formed with domatic 1011, is provided with fan housing between the blower fan 10 and the outdoor machine shell 101
1012, the fan housing 1012 constitutes the air channel with the bottom surface of the outdoor machine shell 101, two side and domatic 1011, it is preferred that
The fan housing 1012 is arc-shaped structure, and the air channel is sequentially formed with air channel along the blower fan 10 to 1 direction of the compressor
Divergent segment（Unmarked）With air channel converging transition（Unmarked）；Wherein, along the blower fan 10 to 1 direction of the compressor, the wind
The area of section of road divergent segment is gradually increased, and the area of section of the air channel converging transition is gradually reduced, the air channel divergent segment
The length W1 ratio of length W2 and the air channel converging transition is 1：（3-5）.Specifically, the cross section of air quantity is first become ambassador's wind by air channel
It is diffused on whole duct cross-section, then air channel reduced cross-sectional, when now wind speed is gradually increasing and blows to 1 surface of compressor,
Wind speed increases the coefficient of heat transfer on 1 surface of compressor more than the wind speed that blower fan 10 is exported.
Based on technique scheme, optionally, in order to the high and refrigeration performance of energy utilization rate is improved, expand cryogenic temperature area
Between to improve versatility, the interior locker 102 is divided into low hypothermia locker and profound hypothermia locker, and cold end evaporimeter is divided into
Low hypothermia evaporimeter 4 and profound hypothermia evaporimeter 5, are provided with the low hypothermia evaporimeter 4, the depth in the low hypothermia locker
The profound hypothermia evaporimeter 5 is provided with low temperature locker；And the refrigeration system also includes gas-liquid separator 3, the first backheat
Device 7 and heat exchanger 6；The first capillary 71 and first product heat cal rod 72 of mutual heat exchange is provided with first regenerator 7,
The outlet of the condenser 2 is connected with the import of the gas-liquid separator 3；The gas outlet of the gas-liquid separator 3 and the heat
The first heat exchanger channels connection of exchanger 6, first heat exchanger channels are by the second capillary 82 and the profound hypothermia evaporimeter 5
Import connection；The liquid outlet of the gas-liquid separator 3 is entered by first capillary 71 and the low hypothermia evaporimeter 4
Mouth connection, the outlet of the low hypothermia evaporimeter 4 are connected with the second heat exchanger channels of the heat exchanger 6, second heat exchange
The outlet of passage and profound hypothermia evaporimeter 5 is connected with the import of the compressor 1 by first product heat cal rod 72 respectively.Specifically
, cold-producing medium compresses the superheated refrigerant gas for forming high temperature, high pressure through compressor 1, and refrigerant gas enter condenser 2 and enter
Row condensation, the dew-point temperature using high low boiling point refrigerant in cold-producing medium are different, are formed rich in height boiling after refrigerant gas condensation
The point refrigerant liquid and two phase refrigerant rich in low boiling point refrigerant gas, the cold-producing medium enter gas-liquid separator 3 and carry out point
From.Liquid phase refrigerant rich in higher boiling cold-producing medium is exported from the liquid outlet of gas-liquid separator 3, is throttled via the first capillary 71
Afterwards, enter into after low hypothermia evaporimeter 4 carries out heat exchange to form two phase refrigerant and enter in heat exchanger 6 further heat exchange and become saturation
Refrigerant gas, the first product heat cal rod 72 that subsequent refrigerant gas are entered in the first regenerator 7, the first product heat cal rod 72 and first mao
Tubule 71 carries out heat exchange；After vapor phase refrigerant is introduced into the cold of the cold-producing medium that heat exchanger 6 absorbs 4 output of low hypothermia evaporimeter
Liquid phase refrigerant is formed, and liquid phase refrigerant forms gas after 5 heat exchange of profound hypothermia evaporimeter is entered after the throttling of the second capillary 81
Cryogen is flowed in the first product heat cal rod 72, finally, and the refrigerant gas in the first product heat cal rod 72 are transmitted back to compressor 1.Excellent
Choosing, the present embodiment multi-temperature zone cooling cycle system also includes the second regenerator 8, is provided with mutually in second regenerator 8
Second capillary 81 of heat exchange and the second product heat cal rod 82, the outlet of the profound hypothermia evaporimeter 5 and the second heat exchanger channels
It is connected with the first product heat cal rod 72 by the second product heat cal rod 82 respectively.Specifically, the gas system for being formed after 5 heat exchange of profound hypothermia evaporimeter
The cold-producing medium of cryogen and the conveying of the second heat exchanger channels is entered in the second product heat cal rod 82 of the second regenerator 8, the second product heat cal rod 82
Carry out after heat exchange with the second capillary 81, can more added with the temperature that can freeze of reduction profound hypothermia evaporimeter 5, obtain more
The refrigeration of low temperature, and more effectively using energy consumption, improve efficiency.Specifically, two evaporimeters are configured with corresponding time
Hot device, regenerator can recycle the cold of cold-producing medium in return-air improve the energy utilization rate of system, also without complicated control
Processing procedure sequence, it is ensured that also ensure that the performance of product while product cost.
In actual use, low hypothermia evaporimeter 4 is used for refrigeration or the freezing of routine, and for profound hypothermia evaporimeter
5 in addition to it can be used in conventional freezing, can also realize cryogenic refrigeration, coordinate different cold-producing mediums realize large span temperature
The refrigeration of degree scope, the present embodiment multi-temperature zone cooling cycle system adopt mix refrigerant, and the mix refrigerant includes multiple
Cold-producing medium, for example：The mix refrigerant is the mixture of R600a and R290；Or, the mix refrigerant be R600 and
The mixture of R290；Or, the mix refrigerant is the mixture of R600a and R600；Or, the mix refrigerant is
The mixture of R600a and R170；Or, the mix refrigerant is the mixture of R290 and R170；Or, the hybrid refrigeration
Agent is the mixture of R600a, R290 and R170.Different storage warm areas can be formed by different non-public boiling mix refrigerants,
Working medium is to R600a/R290：Can achieve -18 ~ -30 DEG C of storage warm areas and -30 ~ -40 DEG C of storage warm areas；Working medium is to R600/R290：
Can achieve -6 ~ -18 DEG C of storage warm areas and -30 ~ -40 DEG C of storage warm areas；Working medium is to R600/R600a：Can achieve 0 ~ 9 DEG C of storage temperature
Area and -6 ~ -12 DEG C of storage warm areas；Working medium is to R600a/R170：Can achieve -18 ~ -30 DEG C of storage warm areas and -40 ~ -60 DEG C of storages
Warm area；Working medium is to R290/R170：Can achieve -20 ~ -40 DEG C of storage warm areas and -40 ~ -60 DEG C of storage warm areas etc..
Wherein, according to the setting of varying number warm area, low hypothermia evaporimeter 4 and profound hypothermia evaporimeter 5 can all adopt many
Individual sub- evaporimeter is constituted, and can be applied in combination in the way of using serial or parallel connection between sub- evaporimeter.In addition, relevant heat exchange
Its performance entity of device 6 can be using heat-exchangers of the plate type or casing type heat exchanging.
By the cold-producing medium of gaseous state in gas-liquid separator and liquid is delivered in different evaporimeters respectively, gaseous refrigerant
Agent carries out the refrigeration of profound hypothermia through over-heat-exchanger by being transported in profound hypothermia evaporimeter, and liquid refrigerant is through capillary section
Entering into after stream carries out the refrigeration of low hypothermia in low hypothermia evaporimeter, and in order to effectively widen temperature range, steams from low hypothermia
Sending out the cold-producing medium exported in device carries out heat exchange by heat exchange with the cold-producing medium entered in low hypothermia evaporimeter, so that shallow
The cryogenic temperature of cryogenic vaporizer is lower, realizes the effect of multi-temperature zone refrigeration, and without the need for the control program using complexity, and hot
Exchanger can effectively improve efficiency, reducing energy consumption, and realization improves the high and refrigeration property of separating refrigerating equipment energy utilization rate
Can, expand cryogenic temperature interval to improve versatility.
Finally it should be noted that：Above example only in order to technical scheme to be described, rather than a limitation；Although
With reference to the foregoing embodiments the present invention is described in detail, it will be understood by those within the art that：Which still may be used
To modify to the technical scheme described in foregoing embodiments, or equivalent is carried out to which part technical characteristic；
And these modification or replace, do not make appropriate technical solution essence depart from various embodiments of the present invention technical scheme spirit and
Scope.
Claims (10)
1. a kind of air-cooled separating refrigerating equipment, including refrigeration system and blower fan, the refrigeration system includes that compressor, hot junction are changed
Hot device, throttling arrangement and cool end heat exchanger, it is characterised in that also include outdoor machine shell, the compressor, the hot end heat exchanger
It is arranged in the outdoor machine shell with the blower fan, the blower fan is arranged between the compressor and the hot end heat exchanger,
Air channel is provided between the blower fan and the compressor, the hot end heat exchanger adopts heat regenerator, the heat accumulating type
Heat exchanger has refrigerant pipeline and heat-exchanging water pipeline；Air-supply passage is provided with the interior locker, the air-supply passage sets
Air inlet and air outlet is equipped with, in the air-supply passage, is provided with circulating fan and the cool end heat exchanger.
2. air-cooled separating refrigerating equipment according to claim 1, it is characterised in that the compressor, the blower fan and
The condenser is arranged on the same line.
3. air-cooled separating refrigerating equipment according to claim 1, it is characterised in that the upper surface shape of the outdoor machine shell
Become to have domatic, between the blower fan and the outdoor machine shell, be provided with fan housing, the bottom surface of the fan housing and the outdoor machine shell, two
Side wall and the domatic composition air channel.
4. air-cooled separating refrigerating equipment according to claim 3, it is characterised in that the fan housing is arc-shaped structure,
The air channel is sequentially formed with air channel divergent segment and air channel converging transition along the blower fan to the compressor direction；Wherein, along institute
Blower fan is stated to the compressor direction, the area of section of the air channel divergent segment is gradually increased, the section of the air channel converging transition
Area is gradually reduced.
5. air-cooled separating refrigerating equipment according to claim 4, it is characterised in that the air channel divergent segment and the wind
The length ratio of road converging transition is 1：（3-5）.
6. according to the arbitrary described air-cooled separating refrigerating equipment of claim 1-5, it is characterised in that the interior locker
It is divided into low hypothermia locker and profound hypothermia locker, the cold end evaporimeter is divided into low hypothermia evaporimeter and profound hypothermia evaporimeter,
The low hypothermia evaporimeter is provided with the low hypothermia locker, is provided with profound hypothermia steaming in the profound hypothermia locker
Send out device；The throttling arrangement includes the first capillary and the second capillary, the refrigeration system also include gas-liquid separator, first
Regenerator and heat exchanger；First capillary and first backheat of mutual heat exchange is provided with first regenerator
Pipe, the outlet of the condenser are connected with the import of the gas-liquid separator；The gas outlet of the gas-liquid separator and the heat
The first heat exchanger channels connection of exchanger, first heat exchanger channels are by second capillary and the profound hypothermia evaporimeter
Import connection, the import of the liquid outlet of the gas-liquid separator by first capillary and the low hypothermia evaporimeter
Connection, the outlet of the low hypothermia evaporimeter are connected with the second heat exchanger channels of the heat exchanger, second heat exchanger channels
Outlet with the profound hypothermia evaporimeter connects first product heat cal rod respectively, and first product heat cal rod connects the compressor
Import.
7. separating refrigerating equipment according to claim 6, it is characterised in that also include the second regenerator, described second
Second capillary and second product heat cal rod of mutual heat exchange, second heat exchanger channels and the depth is provided with regenerator
The outlet of cryogenic vaporizer connects second product heat cal rod respectively, and second product heat cal rod is connected with first product heat cal rod.
8. separating refrigerating equipment according to claim 6, it is characterised in that the low hypothermia evaporimeter include multiple simultaneously
Join the sub- evaporimeter of the multiple low hypothermia for arranging, or, the low hypothermia evaporimeter includes multiple multiple low hypothermia being arranged in series
Sub- evaporimeter；The profound hypothermia evaporimeter includes the sub- evaporimeter of multiple multiple profound hypothermias being arranged in parallel, or, the profound hypothermia
Evaporimeter includes the sub- evaporimeter of multiple multiple profound hypothermias being arranged in series.
9. separating refrigerating equipment according to claim 6, it is characterised in that the separating refrigerating equipment is using mixing
Cold-producing medium, the mix refrigerant include multiple cold-producing mediums.
10. separating refrigerating equipment according to claim 9, it is characterised in that the mix refrigerant be R600a and
The mixture of R290；Or, the mix refrigerant is the mixture of R600 and R290；Or, the mix refrigerant is
The mixture of R600a and R600；Or, the mix refrigerant is the mixture of R600a and R170；Or, the mixing system
Cryogen is the mixture of R290 and R170；Or, the mix refrigerant is the mixture of R600a, R290 and R170.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610950635.7A CN106482433A (en) | 2016-10-27 | 2016-10-27 | Air-cooled separating refrigerating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610950635.7A CN106482433A (en) | 2016-10-27 | 2016-10-27 | Air-cooled separating refrigerating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106482433A true CN106482433A (en) | 2017-03-08 |
Family
ID=58273075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610950635.7A Pending CN106482433A (en) | 2016-10-27 | 2016-10-27 | Air-cooled separating refrigerating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106482433A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109556213A (en) * | 2018-12-06 | 2019-04-02 | 广东西屋康达空调有限公司 | A kind of split-type wind-cooled module machine |
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| CN109556213A (en) * | 2018-12-06 | 2019-04-02 | 广东西屋康达空调有限公司 | A kind of split-type wind-cooled module machine |
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Application publication date: 20170308 |