CN209877698U - High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid - Google Patents

High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid Download PDF

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Publication number
CN209877698U
CN209877698U CN201920543255.0U CN201920543255U CN209877698U CN 209877698 U CN209877698 U CN 209877698U CN 201920543255 U CN201920543255 U CN 201920543255U CN 209877698 U CN209877698 U CN 209877698U
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China
Prior art keywords
heat exchange
chamber
pressure
cavity
radiator
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Expired - Fee Related
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CN201920543255.0U
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Chinese (zh)
Inventor
郑纪明
陈风章
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Shanghai Runshuang Refrigeration Equipment Engineering Co Ltd
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Shanghai Runshuang Refrigeration Equipment Engineering Co Ltd
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Abstract

The utility model discloses a high-efficient heat transfer type fluorine refrigerating system based on force supplies liquid, include through the pipeline communicate in proper order radiator, compressor, the oil separation chamber that forms the return circuit, condensation structure, refrigeration medium storage structure is owing to the high pressure chamber that the condensation structure is linked together, the low pressure circulation chamber in intercommunication high pressure chamber and the muddy sap cavity that is linked together with high pressure chamber and low pressure circulation chamber respectively constitute, it is linked together with the radiator to mix sap cavity, radiator and compressor are linked together through low pressure circulation chamber. The cooling oil and the refrigerating medium in the utility model can be separated and circulated until being completely separated, thus improving the recovery efficiency of the cooling oil; the heat exchange medium can drive the blades to rotate, so that the heat exchange effect is improved; the high-pressure liquid refrigeration medium in the high-pressure cavity is introduced into the low-pressure circulation cavity, so that the forced circulation of the refrigeration medium can be promoted, the refrigeration effect is better, and the energy consumption ratio can be effectively improved.

Description

High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid
Technical Field
The utility model relates to the technical field of refrigeration, specifically a high-efficient heat transfer type fluorine refrigerating system based on force supplies liquid.
Background
Refrigeration is achieved by circulating a refrigerant in a closed system, changing state continuously, and obtaining low temperature. Taking a refrigerator as an example, a compressor sucks low-temperature low-pressure freon gas from an evaporator, compresses the low-temperature low-pressure freon gas into high-temperature high-pressure freon gas, then flows through a thermostatic expansion valve (capillary tube), is throttled into low-temperature low-pressure freon gas-liquid two-phase objects, then the low-temperature low-pressure freon liquid absorbs heat from indoor air in the evaporator to become the low-temperature low-pressure freon gas, and the low-temperature low-pressure freon gas is sucked by the compressor. After the indoor air passes through the evaporator, heat is released, and the temperature of the air is reduced. The refrigerant continuously takes away the heat of the indoor air through repeated cycles of compression, condensation, throttling and evaporation, thereby reducing the temperature of the room.
The structure in the prior art mainly adopts a high-pressure direct liquid supply mode, and has lower energy consumption.
Disclosure of Invention
An object of the utility model is to provide a high-efficient heat transfer type fluorine refrigerating system based on force supplies liquid to solve the problem that provides among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a high-efficient heat transfer type fluorine refrigerating system based on force supplies liquid, includes and communicates radiator, compressor, oil separating chamber, condensation structure, the refrigeration medium storage structure that forms the return circuit through the pipeline in proper order, the refrigeration medium stores the structure and constitutes owing to the high pressure chamber that the condensation structure is linked together, the low pressure circulation chamber that communicates high pressure chamber and the muddy liquid chamber that is linked together with high pressure chamber and low pressure circulation chamber respectively, it is linked together to mix liquid chamber and radiator, radiator and compressor are linked together through low pressure circulation chamber.
Furthermore, the radiator is a refrigeration medium passing structure formed by bending a snake-shaped copper-based pipeline, and two ends of the radiator are respectively communicated with the low-pressure circulation cavity and the liquid mixing cavity.
Furthermore, the oil separation cavity and the compressor are communicated in two directions to form circulation.
Further, the condensation structure comprises a heat exchange medium circulation structure and a heat exchange flow guide structure, and the heat exchange flow guide structure is respectively communicated with the oil separation cavity and the high-pressure cavity.
Furthermore, the heat exchange medium circulating structure is formed by a liquid inlet pipe and a liquid outlet pipe which penetrate through two sides of the shell; the heat exchange flow guide structure comprises a spiral guide pipe, the spiral guide pipe is a spiral copper-based material pipeline, and two ends of the spiral guide pipe penetrate through two side walls of the shell respectively and are communicated with the oil separation cavity and the high-pressure cavity respectively.
Furthermore, a rotational flow mechanism for promoting heat exchange through rotation is further arranged in the shell, the rotational flow mechanism is formed by fixedly connecting a plurality of groups of blades between two groups of parallel opposite gaskets, and the end faces of the gaskets are rotatably connected with the inner wall of the shell through rotating bearings.
Furthermore, the high-pressure cavity is respectively communicated with the liquid mixing cavity and the low-pressure circulating cavity.
Compared with the prior art, the beneficial effects of the utility model are that: the incompletely separated part of the cooling oil and the refrigerating medium is circularly pumped into the compressor and is separated and circulated again until the cooling oil and the refrigerating medium are completely separated, so that the recovery efficiency of the cooling oil can be improved; after the heat medium enters the shell, the blades and the gaskets can be driven to rotate in the shell through the rotating bearing, so that the heat exchange medium is promoted to be contacted with the spiral conduit, and the heat exchange effect is improved; the high-pressure liquid refrigeration medium in the high-pressure cavity is introduced into the low-pressure circulation cavity, so that the forced circulation of the refrigeration medium which is not completely gasified in the low-pressure circulation cavity can be promoted, the refrigeration medium is mixed with the refrigeration medium which directly enters the liquid mixing cavity in the high-pressure cavity and then enters the radiator for refrigeration, the refrigeration effect is better due to the design, and the energy consumption ratio can be effectively improved.
Drawings
FIG. 1 is a schematic connection diagram of a high efficiency heat exchange type fluorine refrigeration system based on forced liquid supply.
Fig. 2 is a schematic structural diagram of a condensation mechanism in a high-efficiency heat exchange type fluorine refrigeration system based on forced liquid supply.
Fig. 3 is a schematic structural diagram of a swirling mechanism in a forced liquid supply-based efficient heat exchange type fluorine refrigeration system.
In the figure: 1-radiator, 2-compressor, 3-liquid mixing cavity, 4-oil separation cavity, 5-condensation structure, 51-shell, 52-spiral conduit, 53-liquid inlet pipe, 54-liquid outlet pipe, 55-rotary bearing, 56-blade, 57-gasket, 6-high pressure cavity and 7-low pressure circulation cavity.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Example 1
Referring to fig. 1, in an embodiment of the present invention, an efficient heat exchange type fluorine refrigeration system based on forced liquid supply includes a heat sink 1, a compressor 2, an oil separation chamber 4, a condensation structure 5, and a refrigeration medium storage structure sequentially connected through a pipeline to form a loop, where the refrigeration medium storage structure includes a high pressure chamber 6 connected to the condensation structure 5, a low pressure circulation chamber 7 connected to the high pressure chamber 6, and a liquid mixing chamber 3 respectively connected to the high pressure chamber 6 and the low pressure circulation chamber 7, the liquid mixing chamber 3 is connected to the heat sink 1, and the heat sink 1 is connected to the compressor 2 through the low pressure circulation chamber 7.
The heat radiator 1 is a refrigeration medium passing structure formed by bending a snake-shaped copper-based pipeline, two ends of the heat radiator 1 are respectively communicated with the low-pressure circulation cavity 7 and the liquid mixing cavity 3, the refrigeration medium enters the heat radiator 1 through the liquid mixing cavity 3, the refrigeration medium can return to the low-pressure circulation cavity 7 through the heat radiator 1 after heat exchange vaporization, wherein the refrigeration medium which is not completely subjected to heat exchange vaporization sinks and circulates into the liquid mixing cavity 3, heat exchange is repeatedly carried out, and the vaporization part is extracted through the compressor 2.
The compressor 2 guides the vaporized refrigeration medium into the oil separation cavity 4, the vaporized refrigeration medium and the cooling oil are separated in the oil separation cavity 4, the refrigeration medium and the cooling oil are layered through different densities and are respectively pumped out, the refrigeration medium enters the condensation structure 5 through a pipeline, and the part, which is not completely separated, of the cooling oil and the refrigeration medium in the oil separation cavity 4 is circularly pumped into the compressor 2 and is separated and circulated again until the cooling oil and the refrigeration medium are completely separated, so that the recovery efficiency of the cooling oil can be improved.
The condensation structure 5 comprises a heat exchange medium circulation structure and a heat exchange flow guide structure, the heat exchange flow guide structure is respectively communicated with the oil separation cavity 4 and the high-pressure cavity 6, the heat exchange circulation structure is wrapped in an accommodating space on the periphery of the heat exchange flow guide structure and comprises an opening for the heat exchange medium to enter and exit, so that the high-temperature gasified refrigeration medium can be subjected to heat exchange, the condensed refrigeration medium is liquefied, the subsequent pressurization circulation is facilitated, the waste heat can be effectively recovered, and the energy-saving and environment-friendly effects are achieved.
The high-pressure cavity 6 is respectively communicated with the liquid mixing cavity 3 and the low-pressure circulation cavity 7, so that a high-pressure liquid refrigeration medium in the high-pressure cavity 6 is introduced into the low-pressure circulation cavity 7, the refrigeration medium which is not completely gasified in the low-pressure circulation cavity 7 can be pushed to be forced to circulate, and is mixed with the refrigeration medium which directly enters the liquid mixing cavity 3 from the high-pressure cavity 6, and then enters the radiator 1 for refrigeration. The design has better refrigeration effect and can effectively improve the energy consumption ratio.
Example 2
Referring to fig. 2-3, in the embodiment of the present invention, a high efficiency heat exchange type fluorine refrigeration system based on forced liquid supply, on the basis of embodiment 1, the heat exchange medium circulation structure is formed by penetrating a liquid inlet pipe 53 and a liquid outlet pipe 54 through two sides of a shell 51, the heat exchange medium enters the shell 51 through the liquid inlet pipe 53, and is discharged through the liquid outlet pipe 54 after heat exchange, the heat exchange flow guide structure includes a spiral conduit 52, the spiral conduit 52 is a spiral copper-based pipeline, two ends of the spiral conduit 52 respectively penetrate through two side walls of the shell 51, and are respectively communicated with an oil separation chamber 4 and a high pressure chamber 6; a rotational flow mechanism for promoting heat exchange through rotation is further arranged in the shell 51, the rotational flow mechanism is formed by fixedly connecting a plurality of groups of blades 56 between two groups of parallel opposite gaskets 57, and the end faces of the gaskets 57 are rotatably connected with the inner wall of the shell 51 through rotating bearings 55.
Thus, after the heat exchange medium enters the housing 51, the heat exchange medium can drive the blades 56 and the gaskets 57 to rotate in the housing 51 through the rotating bearing 55, so that the heat exchange medium is promoted to contact with the spiral conduit 52, and the heat exchange effect is improved.
The utility model discloses a theory of operation is: the incompletely separated part of the cooling oil and the refrigerating medium is circularly pumped into the compressor 2 and is separated and circulated again until the cooling oil and the refrigerating medium are completely separated, so that the recovery efficiency of the cooling oil can be improved; after the heat medium enters the shell 51, the heat medium can drive the blades 56 and the gaskets 57 to rotate in the shell 51 through the rotating bearing 55, so that the contact between the heat exchange medium and the spiral conduit 52 is promoted, and the heat exchange effect is improved; the high-pressure liquid refrigeration medium in the high-pressure cavity 6 is introduced into the low-pressure circulation cavity 7, so that the forced circulation of the incompletely gasified refrigeration medium in the low-pressure circulation cavity 7 can be promoted, the incompletely gasified refrigeration medium is directly mixed with the refrigeration medium in the liquid mixing cavity 3 directly entering the high-pressure cavity 6 and then enters the radiator 1 for refrigeration, the refrigeration effect is better due to the design, and the energy consumption ratio can be effectively improved.
The utility model discloses the standard part that uses all can purchase from the market, and dysmorphism piece all can be customized according to the description with the record of drawing of description, and the concrete connection mode of each part all adopts conventional means such as ripe bolt, rivet, welding among the prior art, and machinery, part and equipment all adopt prior art, and conventional model, including circuit connection adopts conventional connection mode among the prior art, does not detailed here again.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.

Claims (6)

1. The utility model provides a high-efficient heat transfer type fluorine refrigerating system based on forced liquid supply, includes through the pipeline in proper order intercommunication form return circuit radiator (1), compressor (2), oil separating chamber (4), condensation structure (5), refrigeration medium storage structure, its characterized in that, refrigeration medium storage structure is owing to high-pressure chamber (6) that condensation structure (5) are linked together, the low pressure circulation chamber (7) of intercommunication high-pressure chamber (6) and mix liquid chamber (3) with high-pressure chamber (6) and low pressure circulation chamber (7) respectively be linked together and constitute, it is linked together to mix liquid chamber (3) and radiator (1), radiator (1) and compressor (2) are linked together through low pressure circulation chamber (7).
2. The high-efficiency heat exchange type fluorine refrigerating system based on the forced liquid supply is characterized in that the radiator (1) is a refrigerating medium passing structure formed by bending a snake-shaped copper-based pipeline, and two ends of the radiator (1) are respectively communicated with the low-pressure circulation cavity (7) and the liquid mixing cavity (3).
3. The high-efficiency heat exchange type fluorine refrigerating system based on the forced liquid supply as claimed in claim 1, wherein the two-way communication between the inside of the oil separation chamber (4) and the compressor (2) forms a circulation.
4. The high-efficiency heat exchange type fluorine refrigerating system based on the forced liquid supply as recited in claim 1, wherein the condensing structure (5) comprises a heat exchange medium circulating structure and a heat exchange flow guiding structure, and the heat exchange flow guiding structure is respectively communicated with the oil separation chamber (4) and the high pressure chamber (6).
5. The high-efficiency heat exchange type fluorine refrigerating system based on forced liquid supply is characterized in that the heat exchange medium circulating structure is formed by a shell (51) penetrating through a liquid inlet pipe (53) and a liquid outlet pipe (54) from two sides; the heat exchange flow guide structure comprises a spiral guide pipe (52), the spiral guide pipe (52) is a spiral copper-based material pipeline, and two ends of the spiral guide pipe (52) penetrate through two side walls of the shell (51) respectively and are communicated with the oil separation cavity (4) and the high-pressure cavity (6) respectively.
6. The high-efficiency heat exchange type fluorine refrigerating system based on the forced liquid supply as recited in claim 5, characterized in that a rotational flow mechanism for promoting the heat exchange through the rotation is further arranged in the shell (51), the rotational flow mechanism is composed of a plurality of groups of blades (56) fixedly connected between two groups of parallel opposite gaskets (57), and the end surfaces of the gaskets (57) are rotatably connected with the inner wall of the shell (51) through a rotating bearing (55).
CN201920543255.0U 2019-04-22 2019-04-22 High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid Expired - Fee Related CN209877698U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920543255.0U CN209877698U (en) 2019-04-22 2019-04-22 High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920543255.0U CN209877698U (en) 2019-04-22 2019-04-22 High-efficient heat exchange type fluorine refrigerating system based on force supplies liquid

Publications (1)

Publication Number Publication Date
CN209877698U true CN209877698U (en) 2019-12-31

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Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

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Granted publication date: 20191231

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