CN203116358U - Heat pump for deep supercooled liquid collecting tube liquid phase distribution with good distribution effect - Google Patents
Heat pump for deep supercooled liquid collecting tube liquid phase distribution with good distribution effect Download PDFInfo
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- CN203116358U CN203116358U CN201320045537.0U CN201320045537U CN203116358U CN 203116358 U CN203116358 U CN 203116358U CN 201320045537 U CN201320045537 U CN 201320045537U CN 203116358 U CN203116358 U CN 203116358U
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- collector tube
- producing medium
- subcooler
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Abstract
有较好分配效果的深度过冷集液管液相分配的热泵包括压缩机、冷凝器、蒸发器，其特征在于，在蒸发器和冷凝器之间设置有深度过冷器，冷凝器至深度过冷器的主回路具有支回路，该支回路经过该深度过冷器后连接在压缩机的低压吸气侧，从冷凝器出来的制冷剂一部分流入所述支回路，所述支回路的制冷剂流经该支回路中的支回路膨胀阀后与主回路中流经深度过冷器的制冷剂进行热交换，然后所述支回路的气态制冷剂流入到压缩机的低压吸气侧，主回路中流经深度过冷器的制冷剂被冷却为具有较大过冷度的液相，以至于制冷剂经过主回路中的主回路膨胀阀后呈液相分配到蒸发器各个回路。
The heat pump for the liquid phase distribution of the deep subcooling header with better distribution effect includes a compressor, a condenser, and an evaporator. It is characterized in that a deep subcooler is arranged between the evaporator and the condenser, and the condenser reaches the depth The main circuit of the subcooler has a branch circuit, which is connected to the low-pressure suction side of the compressor after passing through the deep subcooler. Part of the refrigerant coming out of the condenser flows into the branch circuit, and the refrigeration of the branch circuit After the refrigerant flows through the branch circuit expansion valve in the branch circuit, it exchanges heat with the refrigerant flowing through the deep subcooler in the main circuit, and then the gaseous refrigerant in the branch circuit flows into the low-pressure suction side of the compressor, and the main circuit The refrigerant flowing through the deep subcooler is cooled to a liquid phase with a large subcooling degree, so that the refrigerant is distributed to each circuit of the evaporator in liquid phase after passing through the main circuit expansion valve in the main circuit.
Description
Technical field
The utility model relates to heat pump.
Background technology
If entering into the cold-producing medium of evaporimeter is two-phase, then may exist cold-producing medium in the different circuit of coil pipe, to distribute uneven problem.Therefore, how to improve that the distribution effects of cold-producing medium in evaporimeter is a problem that needs to be resolved hurrily in the industry in the heat pump.
The utility model content
The purpose of this utility model is to provide a kind of has the degree of depth of better distribution effects to cross the heat pump that cold collector tube liquid phase is distributed.
For the degree of depth that better distribution effects is arranged that realizes described purpose is crossed the heat pump that cold collector tube liquid phase is distributed, comprise compressor, condenser, evaporimeter, be characterized in, between evaporimeter and condenser, be provided with degree of depth subcooler, condenser to the major loop of degree of depth subcooler has Zhi Huilu, this Zhi Huilu is through being connected the low pressure air suction side of compressor behind this degree of depth subcooler, a cold-producing medium part of coming out from condenser flows into described Zhi Huilu, the cold-producing medium of described Zhi Huilu flow through behind the Zhi Huilu expansion valve among this Zhi Huilu with major loop in the flow through cold-producing medium of degree of depth subcooler carry out heat exchange, the gaseous refrigerant of described Zhi Huilu flow into the low pressure air suction side of compressor then, the cold-producing medium of the degree of depth of flowing through in major loop subcooler is cooled to the liquid phase that has than big supercooling degree, is assigned to each loop of evaporimeter to such an extent as to be liquid phase behind the major loop expansion valve in the cold-producing medium process major loop.
Because single-phase refrigerant is distributed in each loop of evaporator coil, so distribution effects is good.
In the preferred embodiment of described heat pump, described cold-producing medium is assigned to each loop of evaporimeter by liquor collecting system, and described liquor collecting system comprises heating mode collector tube, refrigeration mode collector tube, many capillaries and Duo Gen coil circuit pipe; The heating mode collector tube inserts the refrigeration mode collector tube, has the heating mode entrance, and the end of refrigeration mode collector tube has the refrigeration mode outlet; Capillary inserts the coil circuit pipe, entrance capillaceous is inserted in the heating mode collector tube, the outlet of coil circuit pipe is inserted in the refrigeration mode collector tube, under refrigeration mode, the cold-producing medium that comes out from the heat exchange coil of evaporimeter is through each coil circuit pipe, and then enter into the refrigeration mode collector tube, flow to major loop from the refrigeration mode outlet then; Under heating mode, liquid phase refrigerant flows out from the major loop expansion valve, enters into heating mode collector tube entrance, and then is assigned to capillary, and cold-producing medium is assigned to every loop pipe then, enters into the heat exchange coil of evaporimeter at last.
Aforementioned collector tube have take up room little, the characteristics of compact conformation.
Description of drawings
Fig. 1 is the system block diagram of heat pump among the utility model embodiment, and what system block diagram showed is the signal simplified block diagram of flow of refrigerant under heating mode.
Fig. 2 is the front view of liquor collecting system among the utility model embodiment.
Fig. 3 is the left view of liquor collecting system among the utility model embodiment.
Fig. 4 is the right view of liquor collecting system among the utility model embodiment.
The specific embodiment
Simplification heats shown in the schematic diagram as Fig. 1, and heat pump comprises compressor 12, condenser 13, degree of depth subcooler 14 and evaporimeter 11, and cold-producing medium flows between compressor 12, condenser 13, degree of depth subcooler 14 and evaporimeter 11, and circulation heats.
Major loop between condenser 13 and the degree of depth subcooler 14 has Zhi Huilu 23, this Zhi Huilu 23 guides cold-producing medium to the Zhi Huilu expansion valve, the cold-producing medium of Zhi Huilu 23 is behind the Zhi Huilu expansion valve, again with major loop in carry out heat exchange through the cold-producing medium in the degree of depth subcooler 14, so that the cold-producing medium in the major loop carries out degree of depth cooling, be to have the very liquid phase of big supercooling degree so that enter into the cold-producing medium of major loop expansion valve, its outlet still is liquid phase, in case cold-producing medium is single-phase, the effect that its distribution enters into evaporimeter 11 will improve greatly.On the other hand, after cold-producing medium among the Zhi Huilu 23 and degree of depth subcooler 14 carried out heat exchange, owing to be evaporated, its steam pressure was directed into the low pressure air suction side of compressor 12, reduce even enter the major loop flow of evaporimeter 11 like this, thereby reduced the pressure drop of cold-producing medium in evaporimeter 11.
Therefore, the effect that improves the cold-producing medium distribution effects and reduce the pressure drop of cold-producing medium in evaporimeter 11 has been played in the acting in conjunction of degree of depth subcooler 14 and Zhi Huilu 23 really.
To shown in Figure 4, the liquor collecting system of crossing cold collector tube liquid phase distribution for the degree of depth has heating mode collector tube 101, refrigeration mode collector tube 102, capillary 113 and coil circuit pipe 114, collector end cap 105, refrigeration mode outlet 106 and heating mode entrance 107 as Fig. 2.Heating mode collector tube 101 inserts refrigeration mode collector tube 102, and capillary 113 inserts coil circuit pipe 114, and the entrance of capillary 113 is inserted in the heating mode collector tube 101, and the outlet of coil circuit pipe 114 is inserted in the refrigeration mode collector tube 102.End at refrigeration mode collector tube 102 is provided with refrigeration mode outlet 106.
Under refrigeration mode, the cold-producing medium that comes out from heat exchange coil passes through each coil circuit pipe 114, and then enters into refrigeration mode collector tube 102, flows to liquid pipeline from refrigeration mode outlet 106 then.
Under heating mode, liquid refrigerant flows out from the major loop expansion valve, enters into heating mode entrance 107, and then is assigned to capillary 114, and cold-producing medium enters into every loop pipe 113 then.
Claims (2)
1. there is the degree of depth of better distribution effects to cross the heat pump that cold collector tube liquid phase is distributed, comprise compressor, condenser, evaporimeter, it is characterized in that, between evaporimeter and condenser, be provided with degree of depth subcooler, condenser to the major loop of degree of depth subcooler has Zhi Huilu, this Zhi Huilu is through being connected the low pressure air suction side of compressor behind this degree of depth subcooler, a cold-producing medium part of coming out from condenser flows into described Zhi Huilu, the cold-producing medium of described Zhi Huilu flow through behind the Zhi Huilu expansion valve among this Zhi Huilu with major loop in the flow through cold-producing medium of degree of depth subcooler carry out heat exchange, the gaseous refrigerant of described Zhi Huilu flow into the low pressure air suction side of compressor then, the cold-producing medium of the degree of depth of flowing through in major loop subcooler is cooled to the liquid phase that has than big supercooling degree, is assigned to each loop of evaporimeter to such an extent as to be liquid phase behind the major loop expansion valve in the cold-producing medium process major loop.
2. heat pump as claimed in claim 1 is characterized in that, described cold-producing medium is assigned to each loop of evaporimeter by liquor collecting system, and described liquor collecting system comprises heating mode collector tube, refrigeration mode collector tube, many capillaries and Duo Gen coil circuit pipe; The heating mode collector tube inserts the refrigeration mode collector tube, has the heating mode entrance, and the end of refrigeration mode collector tube has the refrigeration mode outlet; Capillary inserts the coil circuit pipe, entrance capillaceous is inserted in the heating mode collector tube, the outlet of coil circuit pipe is inserted in the refrigeration mode collector tube, under refrigeration mode, the cold-producing medium that comes out from the heat exchange coil of evaporimeter is through each coil circuit pipe, and then enter into the refrigeration mode collector tube, flow to major loop from the refrigeration mode outlet then; Under heating mode, liquid phase refrigerant flows out from the major loop expansion valve, enters into heating mode collector tube entrance, and then is assigned to capillary, and cold-producing medium is assigned to every coil circuit pipe then, enters into the heat exchange coil of evaporimeter at last.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320045537.0U CN203116358U (en) | 2013-01-28 | 2013-01-28 | Heat pump for deep supercooled liquid collecting tube liquid phase distribution with good distribution effect |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320045537.0U CN203116358U (en) | 2013-01-28 | 2013-01-28 | Heat pump for deep supercooled liquid collecting tube liquid phase distribution with good distribution effect |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203116358U true CN203116358U (en) | 2013-08-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320045537.0U Expired - Fee Related CN203116358U (en) | 2013-01-28 | 2013-01-28 | Heat pump for deep supercooled liquid collecting tube liquid phase distribution with good distribution effect |
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|---|---|
| CN (1) | CN203116358U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104266416A (en) * | 2014-09-29 | 2015-01-07 | 特灵空调系统(中国)有限公司 | Multi-split air conditioner throttling and super-cooling control mechanism |
| 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 |
-
2013
- 2013-01-28 CN CN201320045537.0U patent/CN203116358U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104266416A (en) * | 2014-09-29 | 2015-01-07 | 特灵空调系统(中国)有限公司 | Multi-split air conditioner throttling and super-cooling control mechanism |
| 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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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130807 Termination date: 20220128 |