CN210801709U - Single-machine secondary throttling regenerative refrigeration cycle system - Google Patents
Single-machine secondary throttling regenerative refrigeration cycle system Download PDFInfo
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- CN210801709U CN210801709U CN201921592983.7U CN201921592983U CN210801709U CN 210801709 U CN210801709 U CN 210801709U CN 201921592983 U CN201921592983 U CN 201921592983U CN 210801709 U CN210801709 U CN 210801709U
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Abstract
The utility model discloses a unit secondary throttle backheating formula refrigeration cycle system, including compressor I, condenser I, drier-filter I, backheating heat exchanger I, first choke valve I, second choke valve I and evaporimeter I. The refrigerating medium is divided into two paths through a three-way valve after passing through a compressor I, a condenser I and a drying filter I, the first path enters a high-temperature end of a regenerative heat exchanger I and then enters an evaporator I for refrigeration after passing through a first throttle valve I, the second path enters a low-temperature end of the regenerative heat exchanger I after passing through a second throttle valve I, the refrigerating medium completes heat exchange through the regenerative heat exchanger I, and an outlet end of the first path of evaporator I and a low-temperature heat exchange outlet end of the second path of regenerative heat exchanger I are connected with an air suction port of the compressor I after converging through the three-way valve. Compared with the prior art, the system further improves the liquid supercooling degree in front of the throttle valve, and simultaneously reduces the air suction temperature of the compressor, so that the air suction specific volume is reduced, and the unit refrigerating capacity of the compressor is improved.
Description
Technical Field
The utility model relates to a refrigeration technology field, concretely relates to unit secondary throttle backheat formula refrigeration cycle system.
Background
The single-machine vapor compression refrigeration cycle equipment mainly comprises four parts: the compressor, the condenser, the throttling device and the evaporator are closely matched to cool the box body. The condenser and the evaporator are heat exchange parts, the condenser is used as a heat release part to exchange heat with ambient air, and the evaporator is used as a heat absorption refrigeration part to exchange heat with a refrigeration space. The main working principle is as follows: the refrigerant is compressed into high-temperature high-pressure gas by a compressor, the high-temperature high-pressure gas is released by a condenser to form low-temperature high-pressure liquid, the low-temperature high-pressure liquid is throttled and depressurized by a throttling device to form low-temperature low-pressure liquid, the low-temperature low-pressure liquid is gasified by an evaporator to absorb heat to form normal-temperature low-pressure gas, the normal-temperature low-pressure gas returns to the compressor again, and the circulation.
Due to the influence of the clearance volume of the compressor and other factors, the refrigerating capacity of the compressor is greatly reduced when the pressure ratio of the refrigerating system is too high, and the power consumption is increased along with the reduction. Even when the evaporation temperature is reduced, the suction ratio volume of the compressor is gradually increased, and the compressor does not discharge air and refrigerate any more after the suction ratio volume of the compressor is increased to a certain degree, so that the refrigeration efficiency becomes zero.
In the traditional regenerative refrigeration cycle in the prior art, cold steam at the outlet of an evaporator and liquid at the outlet of a condenser exchange heat, and although the method improves the supercooling degree before throttling, the method also improves the suction temperature and the suction volume ratio of a compressor. More advanced, the traditional single-stage auto-cascade refrigeration cycle uses mixed working medium, and a gas-liquid separator is arranged to realize the purpose of low evaporation temperature, so that the evaporation temperature is reduced, the suction ratio volume of the compressor is increased, the refrigeration capacity of the compressor is correspondingly reduced, and the manufacturing cost and the later maintenance cost of the product are increased.
According to the above problems in the prior art, the company developed a single-machine secondary throttling regenerative refrigeration cycle system.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a unit secondary throttle backheat formula refrigeration cycle system, this system pass through secondary throttle and backheat formula refrigeration cycle, compare prior art and further improved the liquid super-cooled rate before the main throttle valve, reduced the compressor temperature of breathing in simultaneously, and then make the specific volume reduction of breathing in, improved the unit refrigeration capacity of compressor.
In order to achieve the above object, the utility model discloses a technical solution is:
the first scheme is as follows:
a single-machine secondary throttling regenerative refrigeration cycle system comprises: compressor I, condenser I, drier-filter I, backheat heat exchanger I, first choke valve I, second choke valve I and evaporimeter I. I gas vent of compressor is connected with condenser I, condenser I is connected with drier-filter I, drier-filter I export is divided into two the tunnel through the three-way valve.
The first path is connected with a high-temperature heat exchange inlet end of the regenerative heat exchanger I, and a high-temperature heat exchange outlet end of the regenerative heat exchanger I is connected with the first throttle valve I and is connected with an inlet end of the evaporator I after being throttled by the first throttle valve I. Meanwhile, the second path is connected with a second throttle valve I, throttled by the second throttle valve I and then connected with the low-temperature heat exchange inlet end of the regenerative heat exchanger I. After the refrigeration working medium completes heat exchange through the first regenerative heat exchanger, the outlet end of the first path of evaporator I and the low-temperature heat exchange outlet end of the second path of regenerative heat exchanger I are connected with the air suction port of the compressor I after converging through a three-way valve.
Further, the second throttle valve I is provided with an electromagnetic valve for controlling the opening and closing of the second throttle valve I.
Scheme II:
a single-machine secondary throttling regenerative refrigeration cycle system comprises: the system comprises a compressor II, a condenser II, a drying filter II, a regenerative heat exchanger II, a first throttle valve II, a second throttle valve II and an evaporator II. The air outlet of the compressor II is connected with a condenser II, the condenser II is connected with a drying filter II, and the outlet of the drying filter II is divided into two paths through a three-way valve.
The first path is connected with a high-temperature heat exchange inlet end of the regenerative heat exchanger II, a high-temperature heat exchange outlet end of the regenerative heat exchanger II is connected with the first throttling valve II, and the high-temperature heat exchange outlet end of the regenerative heat exchanger II is connected with an inlet end of the evaporator II after being throttled by the first throttling valve II. Meanwhile, the second path is connected with the inlet end of a second throttling valve II, and the second throttling valve II plays a throttling role. And after the refrigeration working medium completes heat exchange through the second regenerative heat exchanger II, the low-temperature heat exchange outlet end of the second regenerative heat exchanger II is connected with an air suction port of the compressor II.
Further, the second throttle valve II is provided with an electromagnetic valve for controlling the opening and closing of the second throttle valve II.
The third scheme is as follows:
a single-machine secondary throttling regenerative refrigeration cycle system comprises: the system comprises a compressor III, a condenser III, a drying filter III, a heat regenerator III with two high-temperature heat exchanging ends, a first throttling valve III, a second throttling valve III and an evaporator III. The air outlet of the compressor III is connected with a condenser III, the condenser III is connected with a drying filter III, and the outlet of the drying filter III is divided into two paths through a three-way valve.
The first path is connected with a first high-temperature heat exchange inlet end of a regenerative heat exchanger III, and a first high-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with a first throttling valve III, throttled by the first throttling valve III and then connected with an inlet end of an evaporator III. Meanwhile, the second path is connected with a second high-temperature heat exchange inlet end of the regenerative heat exchanger III, a second high-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with an inlet end of a second throttling valve III, and the second throttling valve III plays a throttling role. And after the refrigeration working medium completes heat exchange through the regenerative heat exchanger III, the low-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with an air suction port of the compressor III.
Further, the second throttle valve iii is provided with an electromagnetic valve for controlling the opening and closing of the second throttle valve iii.
Compared with the prior art the utility model discloses the beneficial effect who has:
(1) the utility model discloses the mode through the twice throttle of first choke valve and second choke valve among the regenerative refrigeration cycle process has improved the liquid super-cooled rate before first choke valve is the main throttle valve promptly, and then has improved the refrigerating output of whole circulation, has increased refrigerating system's work efficiency.
(2) The utility model discloses because the existence of second choke valve makes the inspiratory temperature of compressor reduce, and then makes the specific volume of breathing in reduce, has guaranteed that the compressor also has certain inspiratory capacity when very low evaporating temperature to guarantee the refrigerating output of compressor, use in the practical application the utility model discloses refrigeration cycle system single compressor also can reach very low refrigerating temperature.
(3) Compared with the mixed working medium used by the prior art, the utility model discloses only use single refrigeration working medium and get rid of vapour and liquid separator, reduced the manufacturing cost of product, also reduced corresponding equipment maintenance cost and after-sale rate simultaneously.
Drawings
FIG. 1 is a schematic structural diagram of an embodiment.
FIG. 2 is a schematic structural diagram of the second embodiment.
FIG. 3 is a schematic diagram of the third embodiment.
Detailed Description
The technical solution of the present invention is described in detail with reference to the accompanying drawings.
The first embodiment is as follows:
as shown in fig. 1, a single-machine secondary throttling regenerative refrigeration cycle system includes: the air conditioner comprises a compressor I11, a condenser I21, a drying filter I31, a regenerative heat exchanger I41, a first throttle valve I51, a second throttle valve I61 and an evaporator I71. The specific I11 gas vent of compressor is connected with condenser I21, and condenser I21 is connected with drier-filter I31, and more specific refrigerant compresses into high temperature high pressure gas through compressor I11, is becoming medium temperature high pressure liquid through condenser I21 condensation, then passes through drier-filter I31 drying filtration, and drier-filter I31 export is divided into two the tunnel through the three-way valve.
The first path is connected with a high-temperature heat exchange inlet end of the regenerative heat exchanger I41, a high-temperature heat exchange outlet end of the regenerative heat exchanger I41 is connected with a first throttle valve I51, and the high-temperature heat exchange outlet end is connected with an inlet end of an evaporator I71 after being throttled by the first throttle valve I51. Meanwhile, the second path is connected with a second throttle valve I61, throttled by the second throttle valve I61 and then connected with the low-temperature heat exchange inlet end of the regenerative heat exchanger I41. The medium-temperature high-pressure liquid refrigerant is throttled by the second throttling valve I61 and then changed into low-temperature low-pressure liquid, and the low-temperature low-pressure liquid cools the condensed liquid in the regenerative heat exchanger I41 in front of the first throttling valve I51, so that the supercooling degree of the first throttling valve I51, namely the liquid in front of the main throttling valve, is improved, the refrigerating capacity of the whole cycle is improved, and the working efficiency of the refrigerating system is improved. After the refrigeration working medium completes heat exchange through the heat regenerator I41, the outlet end of the first path of evaporator I71 and the low-temperature heat exchange outlet end of the second path of heat regenerator I41 are connected with the air suction port of the compressor I11 after converging through a three-way valve, circulation is completed, and the refrigeration purpose is achieved through the reciprocating circulation in the process.
Further, an electromagnetic valve is installed on the second throttle valve I61, the electromagnetic valve is used for controlling the opening and closing of the second throttle valve I61, whether the second throttle valve I61 works or not is determined by the suction temperature of the compressor I11, and the second electromagnetic valve I61 is started again when the suction temperature is higher than a set value, so that the working efficiency of the cycle is improved.
Furthermore, pipelines for connecting all parts in the refrigeration working medium loop are connected in a copper pipe welding mode.
Embodiment one compares with the heat transfer with the liquid of traditional backheating formula refrigeration cycle with the cold steam of evaporimeter export and condenser export, because second choke valve I61 exists, makes the inspiratory temperature of compressor I11 reduce, and then makes the specific volume of breathing in reduce, has guaranteed that compressor I11 also has certain amount of breathing in when very low evaporating temperature to guarantee compressor I11's refrigerating capacity, use in the practical application the utility model discloses refrigeration cycle system single compressor also can reach very low refrigerating temperature.
Example two:
as shown in fig. 2, a single-machine secondary throttling regenerative refrigeration cycle system includes: the system comprises a compressor II 12, a condenser II 22, a drying filter II 32, a regenerative heat exchanger II 42, a first throttling valve II 52, a second throttling valve II 62 and an evaporator II 72. The exhaust port of the specific compressor II 12 is connected with the condenser II 22, the condenser II 22 is connected with the drying filter II 32, the specific refrigerating medium is compressed into high-temperature high-pressure gas through the compressor II 12, the high-temperature high-pressure gas is condensed into medium-temperature high-pressure liquid through the condenser II 22, then the medium-temperature high-pressure liquid is dried and filtered through the drying filter II 32, and the outlet of the drying filter II 32 is divided into two paths through a three-way valve.
The first path is connected with the high-temperature heat exchange inlet end of the second regenerative heat exchanger 42, the high-temperature heat exchange outlet end of the second regenerative heat exchanger 42 is connected with the first throttling valve II 52, and the high-temperature heat exchange outlet end of the second regenerative heat exchanger is connected with the inlet end of the second evaporator 72 after being throttled by the first throttling valve II 52. Meanwhile, the second path is connected with the inlet end of a second throttling valve II 62, and the second throttling valve II 62 plays a throttling role and changes the medium-temperature high-pressure liquid refrigerating working medium into a low-temperature low-pressure liquid refrigerating working medium. The outlet end of the second throttling valve II 62 and the outlet end of the first evaporator II 72 are connected with the low-temperature heat exchange inlet end of the regenerative heat exchanger II 42 after being converged by the three-way valve, and the converged refrigeration working medium cools the condensed liquid in the regenerative heat exchanger II 42 in front of the first throttling valve II 52, so that the supercooling degree of the first throttling valve II 52, namely the liquid in front of the main throttling valve, is improved, the refrigerating capacity of the whole cycle is improved, and the working efficiency of the refrigerating system is increased. After the refrigeration working medium completes heat exchange through the regenerative heat exchanger II 42, the low-temperature heat exchange outlet end of the regenerative heat exchanger II 42 is connected with the air suction port of the compressor II 12, circulation is completed, and the refrigeration purpose is achieved through the reciprocating circulation in the process.
Further, a solenoid valve is installed on the second throttle valve II 62, the solenoid valve is used for controlling the opening and closing of the second throttle valve II 62, whether the second throttle valve II 62 works or not is determined by the suction temperature of the compressor II 12, and the second solenoid valve II 62 is started again when the suction temperature is higher than a set value, so that the working efficiency of the cycle is improved.
Furthermore, pipelines for connecting all parts in the refrigeration working medium loop are connected in a copper pipe welding mode.
Embodiment two is compared with the heat transfer with the liquid of the cold steam of evaporimeter export and condenser export with traditional backheating formula refrigeration cycle, because second choke valve II 62 exists, makes the inspiratory temperature of compressor II 12 reduce, and then makes the specific volume of breathing in reduce, has guaranteed that compressor II 12 also has certain amount of breathing in when very low evaporating temperature to guarantee the refrigerating output of compressor II 12, use in the practical application the utility model discloses refrigeration cycle system single compressor also can reach very low refrigerating temperature.
Example three:
as shown in fig. 3, a single-machine secondary throttling regenerative refrigeration cycle system includes: the system comprises a compressor III 13, a condenser III 23, a drying filter III 33, a regenerative heat exchanger III 43 with two high-temperature heat exchange ends, a first throttle valve III 53, a second throttle valve III 63 and an evaporator III 73. The air outlet of the compressor III 13 is connected with the condenser III 23, the condenser III 23 is connected with the drying filter III 33, the more specific refrigerating medium is compressed into high-temperature high-pressure gas through the compressor III 13, the high-temperature high-pressure gas is condensed into medium-temperature high-pressure liquid through the condenser III 23, then the medium-temperature high-pressure liquid is dried and filtered through the drying filter III 33, and the outlet of the drying filter III 33 is divided into two paths through a three-way valve.
The first path is connected with a first high-temperature heat exchange inlet end of the regenerative heat exchanger III 43, a first high-temperature heat exchange outlet end of the regenerative heat exchanger III 43 is connected with a first throttling valve III 53, and the first high-temperature heat exchange outlet end is connected with an inlet end of an evaporator III 73 after being throttled by the first throttling valve III 53. Meanwhile, the second path is connected with a second high-temperature heat exchange inlet end of the regenerative heat exchanger III 43, a second high-temperature heat exchange outlet end of the regenerative heat exchanger III 43 is connected with an inlet end of a second throttling valve III 63, and the second throttling valve III 63 plays a throttling role to change the medium-temperature high-pressure liquid refrigerating working medium into a low-temperature low-pressure liquid refrigerating working medium. The outlet end of the first path of evaporator III 73 is connected with the low-temperature heat exchange inlet end of the regenerative heat exchanger III 43 after being converged by the three-way valve with the outlet end of the second path of second throttling valve III 63, the converged refrigerant cools the condensed liquid in the regenerative heat exchanger III 43 in front of the first path of first throttling valve III 53, and simultaneously cools the liquid in front of the second throttling valve III 63, so that the supercooling degree of the liquid in front of the first throttling valve III 53, namely the main throttling valve, is improved, the supercooling degree of the liquid in front of the second throttling valve III 63 is also improved, the refrigerating capacity of the whole cycle is improved, and the working efficiency of the refrigerating system is increased. After the refrigeration working medium completes heat exchange through the regenerative heat exchanger III 43, the low-temperature heat exchange outlet end of the regenerative heat exchanger III 43 is connected with the air suction port of the compressor III 13, circulation is completed, and the refrigeration purpose is achieved through the reciprocating circulation in the process.
Further, an electromagnetic valve is installed on the second throttle valve III 63, the electromagnetic valve is used for controlling the opening and closing of the second throttle valve III 63, whether the second throttle valve III 63 works or not is determined by the suction temperature of the compressor III 13, and the second electromagnetic valve III 63 is started again when the suction temperature is higher than a set value, so that the working efficiency of the cycle is improved.
Furthermore, pipelines for connecting all parts in the refrigeration working medium loop are connected in a copper pipe welding mode.
Embodiment three and traditional backheating formula refrigeration cycle carry out the heat transfer with the cold steam of evaporimeter export and the liquid of condenser export and compare, because second choke valve III 63 exists, make the inspiratory temperature of compressor III 13 reduce, and then make the inspiratory specific volume reduce, guaranteed that compressor III 13 also has certain amount of breathing in when very low evaporating temperature to guarantee compressor III 13's refrigerating capacity, use in the practical application the utility model discloses refrigeration cycle system single compressor also can reach very low refrigerating temperature.
Parts which are not described in the three embodiments can be realized by adopting or referring to the prior art.
Of course, the above description is not intended to limit the present invention, and the present invention is not limited to the above examples, and the changes, modifications, additions or substitutions made by those skilled in the art within the scope of the present invention should also belong to the protection scope of the present invention.
Claims (6)
1. A single-machine secondary throttling regenerative refrigeration cycle system is characterized by comprising: the system comprises a compressor I, a condenser I, a drying filter I, a regenerative heat exchanger I, a first throttle valve I, a second throttle valve I and an evaporator I;
an exhaust port of the compressor I is connected with a condenser I, the condenser I is connected with a drying filter I, and an outlet of the drying filter I is divided into two paths through a three-way valve;
the first path is connected with a high-temperature heat exchange inlet end of a regenerative heat exchanger I, and a high-temperature heat exchange outlet end of the regenerative heat exchanger I is connected with a first throttle valve I, throttled by the first throttle valve I and then connected with an inlet end of an evaporator I;
the second path is connected with a second throttle valve I, throttled by the second throttle valve I and then connected with the low-temperature heat exchange inlet end of the regenerative heat exchanger I;
after the refrigeration working medium completes heat exchange through the first regenerative heat exchanger, the outlet end of the first path of evaporator I and the low-temperature heat exchange outlet end of the second path of regenerative heat exchanger I are connected with the air suction port of the compressor I after converging through a three-way valve.
2. The single-machine secondary throttling regenerative refrigeration cycle system according to claim 1, wherein the second throttle valve I is provided with a solenoid valve for controlling the opening and closing of the second throttle valve I.
3. A single-machine secondary throttling regenerative refrigeration cycle system is characterized by comprising: the system comprises a compressor II, a condenser II, a drying filter II, a regenerative heat exchanger II, a first throttle valve II, a second throttle valve II and an evaporator II;
the air outlet of the compressor II is connected with a condenser II, the condenser II is connected with a drying filter II, and the outlet of the drying filter II is divided into two paths through a three-way valve;
the first path is connected with a high-temperature heat exchange inlet end of a regenerative heat exchanger II, and a high-temperature heat exchange outlet end of the regenerative heat exchanger II is connected with a first throttle valve II, throttled by the first throttle valve II and then connected with an inlet end of an evaporator II;
the second path is connected with the inlet end of a second throttling valve II, and the second throttling valve II plays a throttling role;
and after the refrigeration working medium completes heat exchange through the second regenerative heat exchanger II, the low-temperature heat exchange outlet end of the second regenerative heat exchanger II is connected with an air suction port of the compressor II.
4. The single-machine secondary throttling regenerative refrigeration cycle system according to claim 3, wherein the second throttling valve II is provided with a solenoid valve for controlling the opening and closing of the second throttling valve II.
5. A single-machine secondary throttling regenerative refrigeration cycle system is characterized by comprising: the system comprises a compressor III, a condenser III, a drying filter III, a regenerative heat exchanger III with two high-temperature heat exchange ends, a first throttling valve III, a second throttling valve III and an evaporator III;
the air outlet of the compressor III is connected with a condenser III, the condenser III is connected with a drying filter III, and the outlet of the drying filter III is divided into two paths through a three-way valve;
the first path is connected with a first high-temperature heat exchange inlet end of a regenerative heat exchanger III, and a first high-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with a first throttling valve III, throttled by the first throttling valve III and then connected with an inlet end of an evaporator III;
the second path is connected with a second high-temperature heat exchange inlet end of a regenerative heat exchanger III, a second high-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with an inlet end of a second throttling valve III, and the second throttling valve III plays a throttling role;
and after the refrigeration working medium completes heat exchange through the regenerative heat exchanger III, the low-temperature heat exchange outlet end of the regenerative heat exchanger III is connected with an air suction port of the compressor III.
6. The single-machine secondary throttling regenerative refrigeration cycle system according to claim 5, wherein the second throttle valve III is provided with a solenoid valve for controlling the opening and closing of the second throttle valve III.
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| CN110595116A (en) * | 2019-09-24 | 2019-12-20 | 青岛澳柯玛超低温冷冻设备有限公司 | Single-machine secondary throttling regenerative refrigeration cycle system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110595116A (en) * | 2019-09-24 | 2019-12-20 | 青岛澳柯玛超低温冷冻设备有限公司 | Single-machine secondary throttling regenerative refrigeration cycle system |
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Address after: 266510 No. 315, Bay Road, Huangdao District, Shandong, Qingdao Patentee after: Qingdao Aucma biomedical Co., Ltd Address before: 266510 No. 315, Bay Road, Huangdao District, Shandong, Qingdao Patentee before: Qingdao Aucma ultra low temperature refrigeration equipment Co., Ltd |