CN205066233U - Heat pump heating system and heat pump water heater - Google Patents
Heat pump heating system and heat pump water heater Download PDFInfo
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- CN205066233U CN205066233U CN201520802685.1U CN201520802685U CN205066233U CN 205066233 U CN205066233 U CN 205066233U CN 201520802685 U CN201520802685 U CN 201520802685U CN 205066233 U CN205066233 U CN 205066233U
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title abstract description 9
- 239000003507 refrigerant Substances 0.000 claims abstract description 50
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 230000001502 supplementing effect Effects 0.000 claims description 23
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000007791 liquid phase Substances 0.000 description 20
- 238000000034 method Methods 0.000 description 19
- 230000008569 process Effects 0.000 description 16
- 239000012071 phase Substances 0.000 description 13
- 239000012808 vapor phase Substances 0.000 description 11
- 238000001704 evaporation Methods 0.000 description 7
- 238000007599 discharging Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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Abstract
The utility model relates to a heat pump heating system and heat pump water heater, heat pump heating system includes major loop (1), the tonifying qi increases enthalpy branch road (2) and hydrojet branch road (3), major loop (1) includes compressor (11) that connect gradually along refrigerant flow direction, condenser (12), first throttling part (13) and evaporimeter (14), the tonifying qi increases enthalpy branch road (2) and hydrojet branch road (3) one end and all connects on main loop (1) between condenser (12) and first throttling part (13), the other end that the tonifying qi increases enthalpy branch road (2) and hydrojet branch road (3) all is connected with the tonifying qi mouth of compressor (11), be used for to compressor (11) make-up the double-phase refrigerant of gas-liquid. The utility model discloses a heat pump heating system can the reliability of lift system when the low temperature operation.
Description
Technical field
The utility model relates to technical field of heat pumps, particularly relates to a kind of heat pump heating and Teat pump boiler.
Background technology
Teat pump boiler is a kind of heat by absorbing in low-temperature heat source, and carries out compressed action to it and be converted to high temperature heat, thus to the equipment that the water of user side heats.As shown in Figure 1, the main circulation loop of general Teat pump boiler comprises compressor 1a, condenser 2a, the first expansion valve 5a and evaporimeter 6a, and condenser 2a is connected with user side, and evaporimeter 6a is connected with extraneous low-temperature heat source, and cold-producing medium circulates in main circulation loop.Operationally, the liquid phase refrigerant flowing through evaporimeter 6a carries out heat exchange by internal-external temperature difference and the external world, liquid phase refrigerant absorbs heat in the process of evaporation, and be converted into the vapor phase refrigerant of low-temp low-pressure, again after compressor 1a compresses, the vapor phase refrigerant being converted into HTHP flows through condenser 2a, and heat exchange is carried out with the water be stored in water heater in condenser 2a, the temperature of water is raised in the process, vapor phase refrigerant is converted into liquid phase refrigerant simultaneously, after the first expansion valve 5a step-down, be supplied to evaporimeter 6a further.
The Teat pump boiler of this routine can meet the instructions for use of user under general operating mode, when but if winter, ambient temperature was lower, the heat exchange amount of evaporimeter 6a side can reduce, and the internal circulating load of cold-producing medium is reduced, thus causes the heating capacity of compressor sharply to decline.Thus occurred in prior art that tonifying Qi as shown in Figure 1 increases enthalpy formula Teat pump boiler, its principle is that the liquid phase refrigerant produced through condenser 2a is divided into two branch roads, wherein a road enters first entrance of heat exchanger 4a after the second expansion valve 3a, with separately lead up to the liquid phase refrigerant that the second entrance directly enters heat exchanger 4a and carry out heat exchange, then fill in compressor 1a by exporting from heat exchanger 4a the vapor phase refrigerant flowed out, the liquid phase refrigerant of cooling is further supplied to evaporimeter 6a further after the first expansion valve 5a step-down.
This kind effectively can improve the heating capacity of unit under worst cold case and efficiency with the Teat pump boiler that tonifying Qi increases enthalpy branch road, but when stable running status do not set up by tonifying Qi increasing enthalpy branch road, the functional reliability of whole system is poor.
Utility model content
The purpose of this utility model proposes a kind of heat pump heating and Teat pump boiler, can promote the reliability of heat pump heating when cold operation.
For achieving the above object, the utility model first aspect provides a kind of heat pump heating, comprise: major loop, tonifying Qi increases enthalpy branch road and hydrojet branch road, described major loop comprises the compressor connected successively along flow of refrigerant direction, condenser, first throttle parts and evaporimeter, one end that described tonifying Qi increases enthalpy branch road and described hydrojet branch road is all connected on the described major loop between described condenser and described first throttle parts, described tonifying Qi increases enthalpy branch road and is all connected with the gas supplementing opening of described compressor with the other end of described hydrojet branch road, for supplementing gas-liquid two-phase cold-producing medium to described compressor.
Further, described tonifying Qi increases enthalpy branch road and the shared gas supplementing opening of described hydrojet branch road.
Further, be provided with in described hydrojet branch road for the hydrojet magnetic valve of hydrojet branch road described in break-make and the 3rd throttle part for adjusting supplementary refrigerant amount.
Further, described 3rd throttle part is expansion valve or capillary.
Further, also comprise economizer, to realize described major loop and the heat exchange wherein of described tonifying Qi increasing enthalpy branch road, described tonifying Qi increases enthalpy branch road and is provided with for the tonifying Qi magnetic valve of tonifying Qi increasing enthalpy branch road described in break-make and the second section stream unit for adjusting supplementary refrigerant amount, and described tonifying Qi magnetic valve and second section stream unit are positioned at the upstream of described economizer.
Further, described economizer is plate type heat exchanger 23, first entrance A of described economizer is connected with the outlet of described condenser with described tonifying Qi magnetic valve by described second section stream unit, second entrance B of described economizer is directly connected with the outlet of described condenser, first outlet C of described economizer is connected with the gas supplementing opening of described compressor, and the second outlet D of described economizer is connected with the entrance of described first throttle parts.
Further, one end of described hydrojet branch road is connected to second of described first throttle parts and described economizer and exports between D, and the other end is connected with the gas supplementing opening of described compressor.
For achieving the above object, the utility model second aspect provides a kind of Teat pump boiler, comprises the heat pump heating described in above-described embodiment.
Based on technique scheme, the heat pump heating of the utility model embodiment, enthalpy branch road and hydrojet branch road is increased by arranging tonifying Qi in systems in which simultaneously, when system can be made to work under worst cold case, system works reliability is improved when tonifying Qi increases when stable running status do not set up by enthalpy branch road, namely when worst cold case makes cold-producing medium internal circulating load in systems in which lower, compressor air-discharging amount is lower, when causing delivery temperature higher, hydrojet branch road provides appropriate gas-liquid two-phase cold-producing medium to compressor, cold-producing medium can absorb heat in the process of vaporization, thus the temperature of compressor air-discharging end is reduced in safe range, and then improve system in cryogenic high pressure contracting than the reliability under operating mode, and can also increase with tonifying Qi the internal circulating load increasing cold-producing medium together with enthalpy branch road to a certain extent, thus improve heating capacity and efficiency, finally realize system can operate efficiently and stably under worst cold case.
Accompanying drawing explanation
Accompanying drawing described herein is used to provide further understanding of the present utility model, and form a application's part, schematic description and description of the present utility model, for explaining the utility model, is not formed improper restriction of the present utility model.In the accompanying drawings:
Fig. 1 is the principle schematic of tonifying Qi enthalpy increasing heat pump heating in prior art;
Fig. 2 is the principle schematic of an embodiment of the utility model heat pump heating;
Fig. 3 is the principle schematic of another embodiment of the utility model heat pump heating.
Description of reference numerals
1a-compressor; 2a-condenser; 3a-second expansion valve; 4a-heat exchanger; 5a-first expansion valve; 6a-evaporimeter;
1-major loop; 2-tonifying Qi increases enthalpy branch road; 3-hydrojet branch road; 11-compressor; 12-condenser; 13-first throttle parts; 14-evaporimeter; 21-tonifying Qi magnetic valve; 22-second section stream unit; 23-plate type heat exchanger; 23A-first entrance; 23B-second entrance; 23C-first exports; 24D-second exports; 31-hydrojet magnetic valve; 32-the 3rd throttle part.
Detailed description of the invention
Below describe the utility model in detail.In the following paragraphs, the different aspect of embodiment is defined in more detail.The each side of restriction like this can combine with any other one aspect or many aspects, not may be combined with unless explicitly stated otherwise.Especially, be considered to preferred or favourable any feature and one or morely can be considered to preferred or favourable feature with other.
Terms such as " first ", " second " that occur in the utility model is only for convenience of description, to distinguish the different building blocks with same names, does not represent successively or primary-slave relation.
The utility model first proposed a kind of heat pump heating, and heat pump heating can by absorbing the heat in low-temperature heat source, and carries out compressed action to it and be converted to high temperature heat, uses for user side.As shown in Figures 2 and 3, this kind of heat pump heating comprises: major loop 1, tonifying Qi increase enthalpy branch road 2 and hydrojet branch road 3, major loop 1 comprises the compressor 11, condenser 12, first throttle parts 13 and the evaporimeter 14 that connect successively along flow of refrigerant direction (arrow direction), one end that tonifying Qi increases enthalpy branch road 2 and hydrojet branch road 3 is all connected on the major loop 1 between condenser 12 and first throttle parts 13, tonifying Qi increases enthalpy branch road 2 and is all connected with the gas supplementing opening of compressor 11 with the other end of hydrojet branch road 3, for supplementing gas-liquid two-phase cold-producing medium to compressor 11.
The heat pump heating of the utility model embodiment, enthalpy branch road and hydrojet branch road is increased by arranging tonifying Qi in systems in which simultaneously, when system can be made to work under worst cold case, system works reliability is improved when tonifying Qi increases when stable running status do not set up by enthalpy branch road, namely when worst cold case makes cold-producing medium internal circulating load in systems in which lower, compressor air-discharging amount is lower, when causing delivery temperature higher, hydrojet branch road provides appropriate gas-liquid two-phase cold-producing medium to compressor, cold-producing medium can absorb heat in the process of vaporization, thus the temperature of compressor air-discharging end is reduced in safe range, and then improve system in cryogenic high pressure contracting than the reliability under operating mode, and can also increase with tonifying Qi the internal circulating load increasing cold-producing medium together with enthalpy branch road to a certain extent, thus improve heating capacity and efficiency, finally realize system can operate efficiently and stably under worst cold case.
The tonifying Qi arranged in embodiment above increases enthalpy branch road 2 and hydrojet branch road 3 can share a gas supplementing opening.This set form makes heat pump heating of the present utility model only need improve loop structure, and without the need to changing the structure of compressor 11, as long as a gas supplementing opening is offered in the position of pressing chamber corresponding in compressor 11; And this set form also can simplify loop structure, thus save pipeline.
Below in conjunction with the embodiment shown in Fig. 2 and Fig. 3, the structure of the utility model heat pump heating is described in detail.This system comprises three chief components: major loop 1, tonifying Qi increase enthalpy branch road 2 and hydrojet branch road 3, sets forth here by the annexation between the concrete composition of each branch road and each branch road.
In major loop 1, compressor 11, condenser 12, first throttle parts 13 are connected along flow of refrigerant direction successively with evaporimeter 14, the air inlet of compressor 11 is connected with evaporimeter 14, exhaust outlet is connected with condenser 12, and cold-producing medium circulates according to arrow indicated direction in major loop 1.In addition, in major loop 1, can also the additional device such as magnetic valve or filter be set as required.
One end that tonifying Qi increases enthalpy branch road 2 is connected between condenser 12 and first throttle parts 13, the other end is connected with the gas supplementing opening of compressor 11, for supplementing cold-producing medium to compressor 11, the cold-producing medium supplemented here is generally vapor phase refrigerant, wherein also may be mixed with a small amount of liquid phase refrigerant.Further, heat pump heating also comprises economizer, to realize major loop 1 and the heat exchange wherein of tonifying Qi increasing enthalpy branch road 2, tonifying Qi increases enthalpy branch road 2 and is provided with for the tonifying Qi magnetic valve 21 of break-make tonifying Qi increasing enthalpy branch road 2 and the second section stream unit 22 for adjusting supplementary refrigerant amount, tonifying Qi magnetic valve 21 and second section stream unit 22 are positioned at the upstream of economizer, and the upstream mentioned here is that the flow direction of reference cold-producing medium defines.Preferably, second section stream unit 22 is arranged near economizer.
In one embodiment, economizer is plate type heat exchanger 23, first entrance 23A of economizer is connected with the outlet of tonifying Qi magnetic valve 21 with condenser 12 by second section stream unit 22, second entrance 23B of economizer is directly connected with the outlet of condenser 12, first outlet 23C of economizer is connected with the gas supplementing opening of compressor 11, and the second outlet 23D of economizer is connected with the entrance of first throttle parts 13.The operation principle of the economizer of this employing plate type heat exchanger 23 form is that a road cold-producing medium absorbs heat by self throttling thus another road cold-producing medium is cooled further, such absorption heat Hou mono-road cold-producing medium forms vapor phase refrigerant, and by the gas supplementing opening of compressor 11 for major loop 1 provides more cold-producing medium to circulate, a cooled road cold-producing medium continues to be supplied to evaporimeter 14 after first throttle parts 13 step-down further.
In another embodiment, economizer is flash vessel, first entrance of economizer is connected with the outlet of condenser with tonifying Qi magnetic valve by second section stream unit successively, and the first outlet of economizer is connected with the gas supplementing opening of compressor, and the second outlet of economizer is connected with the entrance of first throttle parts.Flash vessel can realize gas-liquid separation, and its operation principle is reduced the boiling point of liquid phase refrigerant, and such Partial Liquid Phase cold-producing medium just becomes vapor phase refrigerant and is evaporated.
For the economizer of above-mentioned two types, overall work target is consistent, the liquid refrigerant flowed out from condenser 12 can be cooled further owing to adopting the economizer of plate type heat exchanger 23 form, thus when flowing through evaporimeter 14, the temperature difference of liquid refrigerant and outside air can be increased further, in the process of evaporation, more how extra heat is absorbed from outside air to make liquid refrigerant, thus use in the process of condenser 12 pairs of water heating, this shows, the economizer of plate type heat exchanger 23 form can reach more excellent effect in performance.
One end of hydrojet branch road 3 is connected to second of first throttle parts 13 and economizer and exports between 23D, and the other end is connected with the gas supplementing opening of compressor 11.And be provided with in hydrojet branch road 3 for the hydrojet magnetic valve 31 of break-make hydrojet branch road 3 and the 3rd throttle part 32 for adjusting supplementary gas-liquid two-phase refrigerant amount.In this connected mode, gas-liquid two-phase cold-producing medium in hydrojet branch road 3 is taken from by the further cooled liquid phase refrigerant of economizer, object can play better cooling down effect to the exhaust end of compressor 11 after being that liquid phase refrigerant that temperature is lower is injected into the middle pressure chamber of compressor 11.In addition, those skilled in the art, also can from the position acquisition liquid phase refrigerant of the outlet of condenser 12 without economizer when designing hydrojet branch road 3.
The first throttle parts 13 adopted in this heat pump heating, second section stream unit 22 or the 3rd throttle part 32 can select capillary, see Fig. 2, also can select expansion valve, see Fig. 3.In general, liquid phase refrigerant pressure after throttling can reduce suddenly, and forms gas-liquid two-phase cold-producing medium.
After the structure having understood the utility model heat pump heating, need to be described its operation principle further, can in depth dissect the technique effect that each parts can reach in the process described simultaneously, the arrow marked in Fig. 2 and Fig. 3 is used for the flow direction of cold-producing medium in expression loop.
When heat pump heating is started working, the vapor phase refrigerant of the HTHP of discharging from the exhaust outlet of compressor 11 after condenser 12, by with water heat exchange to be heated after, temperature reduces, and is converted into liquid phase refrigerant.
After liquid phase refrigerant flows out from the outlet of condenser 12, be divided into 1. and 2. two streams, stream liquid phase refrigerant is 1. by after tonifying Qi magnetic valve 21, at second section stream unit 22, place is subject to throttling action, the gas-liquid two-phase cold-producing medium that formation temperature is further reduced, then enter from the first entrance 23A of economizer, absorb the heat from stream liquid phase refrigerant 2.;
Stream liquid phase refrigerant 2. directly enters from the second entrance 23B of economizer, and release heat is excessively cold further, and after leaving economizer, 3. this road liquid phase refrigerant is divided into again and 4. two streams;
3. stream enters evaporimeter 14 after first throttle parts 13 throttling, and the heat absorbing outside air evaporates, and the vapor phase refrigerant forming low-temp low-pressure enters the air inlet of compressor 11, completes the circulation of major loop 1;
Stream, 4. after hydrojet magnetic valve 31, carries out throttling cooling by the 3rd throttle part 32, forms gas-liquid two-phase cold-producing medium, after the vapor phase refrigerant that 1. itself and stream are formed is converged, enters from the gas supplementing opening of compressor 11.Wherein, the essence of 1. being supplemented cold-producing medium by stream is that tonifying Qi increases enthalpy process, and the essence of 4. supplementing cold-producing medium by stream is hydrojet process.
When heat pump heating is in worst cold case, the heat exchange amount of evaporimeter 14 side and outside air can reduce, the amount of the vapor phase refrigerant formed by evaporation is reduced, circulating mass of refrigerant correspondingly in major loop 1 reduces, because the compressed action of now compressor 11 does not reduce, the heat part conduction that compressor 11 acting is produced gives a small amount of cold-producing medium, heat is changed in remainder branch makes the temperature of compressor 11 exhaust end raise, thus cause the heating capacity of compressor 11 sharply to decline, and delivery temperature continues the too high limit delivery temperature easily exceeding compressor 11, destroy the steady-working state of lubricating oil, thus damage is caused to the structure of compressor 11.
In order to promote the heating capacity of heat pump heating, the tonifying Qi of setting up in major loop 1 increases enthalpy branch road 2, for pressing chamber to fill into more gaseous refrigerant in compressor 11, which adds the internal circulating load of cold-producing medium in major loop 1, thus the heat making compressor 11 produce in same acting situation has just been shared, and then reduce delivery temperature; And economizer can make the liquid refrigerant flowed out from condenser 12 cool further, thus when flowing through evaporimeter 14, the temperature difference of liquid refrigerant and outside air can be increased further, in the process of evaporation, more how extra heat is absorbed from outside air to make liquid refrigerant, thus tonifying Qi increases the cryogenic property that enthalpy branch road 2 can promote heat pump heating, and it could the reliability of basic maintenance system after stable.In the process of heat pump heating system works, increase the temperature that air compensation can reduce compressor 11 exhaust end further, and improve system heating capacity, and environment temperature is lower, tonifying Qi increases the delivery temperature that enthalpy branch road 2 more can reduce compressor 11, and correspondingly the raising of heating capacity and efficiency is also more obvious, that is, condensation temperature one timing, evaporating temperature is lower, and the performance improvement arranging tonifying Qi increasing enthalpy branch road 2 pairs of systems is more obvious.
And do not set up in the process of plateau when tonifying Qi increasing enthalpy branch road 2 has just been started working, in practice can by the cold temperature difference of mistake before and after economizer, one or several of increasing in the temperature rise value of enthalpy branch road 2 and outlet air temperature judges to compare with the threshold value of setting in tonifying Qi, to judge that tonifying Qi increases enthalpy branch road 2 and whether is in unsteady state, such as occur tonifying Qi maybe cannot to reach predetermined air compensation, when causing excessive discharge temperature (such as reaching more than 110 DEG C) or protection, just need to connect hydrojet branch road 3, hydrojet branch road 3 be by throttling after gas-liquid two-phase cold-producing medium directly spray in compressor 11 and press chamber, the effect of two aspects can be played: the first sprays into appropriate gas-liquid two-phase cold-producing medium in compressor 11 inside, liquid phase refrigerant is in the process of gasification, heat can be absorbed, thus the delivery temperature of compressor 11 is reduced within safe range, stable exhaust, it two is the internal circulating loads that can increase cold-producing medium to a certain extent, ensures that compressor 11 reliably operates, the overall performance of heat pump heating is got a promotion.
The workflow of the heat pump heating of the utility model above-described embodiment may be summarized to be: when environment temperature is lower than design temperature, that is when heat pump heating is in worst cold case, connect tonifying Qi simultaneously and increase enthalpy branch road 2 and hydrojet branch road 3, for jointly supplementing gas-liquid two-phase cold-producing medium to compressor 11.Further, when the delivery temperature of compressor 11 is lower than design temperature, turn off hydrojet branch road 3.
For the heat pump heating shown in Fig. 2 and Fig. 3, tonifying Qi increasing enthalpy branch road 2 can being connected by opening tonifying Qi magnetic valve 21, connecting hydrojet branch road 3 by opening hydrojet magnetic valve 31.Because the increase of air compensation can play a role in improving to the heating capacity of heat pump heating and efficiency, thus in the process of heat pump heating system works, according to circumstances air compensation can be regulated.
In above-mentioned flow process, if increase the air compensation of enthalpy branch road 2 pairs of compressors 11 for increasing tonifying Qi, just by increasing the aperture of second section stream unit 22, can meanwhile reduce the aperture of first throttle parts 13 to reduce the amount entering the cold-producing medium of evaporimeter 14; Otherwise, just can perform contrary operation to first throttle parts 13 and second section stream unit 22.
When environment temperature is higher than setting value, when namely evaporating temperature is higher, cold-producing medium just can absorb more heat in evaporation process, can form more cold-producing medium and circulate in major loop 1, thus carries out tonifying Qi with regard to not needing tonifying Qi to increase enthalpy branch road 2.In practical operation, tonifying Qi increasing enthalpy branch road 2 can be turned off by closing tonifying Qi magnetic valve 21.
In addition, when the air compensation that tonifying Qi increases enthalpy branch road 2 is certain, if for the amount increasing the gas-liquid two-phase cold-producing medium that hydrojet branch road 3 pairs of compressors 11 supplement, just can increase the aperture of the 3rd throttle part 32, meanwhile reduce the aperture of first throttle parts 13 to reduce the amount entering the cold-producing medium of evaporimeter 14; Otherwise, just can perform contrary operation to first throttle parts 13 and the 3rd throttle part 32.
After increasing enthalpy system stability is set up, just can the heating performance of independent lift heat pump heating, and maintain the reliability of system, thus just without the need to the auxiliary maintenance heating operations of hydrojet branch road 3, now shutoff hydrojet branch road 3 can reduce the energy ezpenditure of system.In practical operation, hydrojet branch road 3 can be turned off by closing hydrojet magnet valve 31.
Secondly, the utility model additionally provides a kind of Teat pump boiler, comprises the heat pump heating described in above-described embodiment.The advantage of this heat pump heating has been set forth in foregoing teachings, thus the water heater that have employed this heat pump heating also has corresponding advantage, this Teat pump boiler can control the delivery temperature of unit when worst cold case, improve reliability when compressor runs with high compression ratio, improve heating capacity and efficiency, the raising of overall performance finally can realize Teat pump boiler and operate efficiently and stably under worst cold case simultaneously.
Above a kind of heat pump heating provided by the utility model and Teat pump boiler are described in detail.Apply specific embodiment herein to set forth principle of the present utility model and embodiment, the explanation of above embodiment just understands method of the present utility model and core concept thereof for helping.Should be understood that; for those skilled in the art; under the prerequisite not departing from the utility model principle, can also carry out some improvement and modification to the utility model, these improve and modify and also fall in the protection domain of the utility model claim.
Claims (8)
1. a heat pump heating, it is characterized in that, comprise: major loop (1), tonifying Qi increases enthalpy branch road (2) and hydrojet branch road (3), described major loop (1) comprises the compressor (11) connected successively along flow of refrigerant direction, condenser (12), first throttle parts (13) and evaporimeter (14), one end that described tonifying Qi increases enthalpy branch road (2) and described hydrojet branch road (3) is all connected on the described major loop (1) between described condenser (12) and described first throttle parts (13), described tonifying Qi increases enthalpy branch road (2) and is all connected with the gas supplementing opening of described compressor (11) with the other end of described hydrojet branch road (3), for supplementing gas-liquid two-phase cold-producing medium to described compressor (11).
2. heat pump heating according to claim 1, is characterized in that, described tonifying Qi increases enthalpy branch road (2) and described hydrojet branch road (3) shares a gas supplementing opening.
3. heat pump heating according to claim 1, it is characterized in that, being provided with in described hydrojet branch road (3) for the hydrojet magnetic valve (31) of hydrojet branch road (3) described in break-make and the 3rd throttle part (32) for adjusting supplementary refrigerant amount.
4. heat pump heating according to claim 3, is characterized in that, described 3rd throttle part (32) is expansion valve or capillary.
5. according to the arbitrary described heat pump heating of Claims 1 to 4, it is characterized in that, also comprise economizer, to realize described major loop (1) and branch road (2) heat exchange wherein of described tonifying Qi increasing enthalpy, described tonifying Qi increases enthalpy branch road (2) and is provided with for the tonifying Qi magnetic valve (21) of tonifying Qi increasing enthalpy branch road (2) described in break-make and the second section stream unit (22) for adjusting supplementary refrigerant amount, and described tonifying Qi magnetic valve (21) and second section stream unit (22) are positioned at the upstream of described economizer.
6. heat pump heating according to claim 5, it is characterized in that, described economizer is plate type heat exchanger (23), first entrance (23A) of described economizer is connected with the outlet of described condenser (12) with described tonifying Qi magnetic valve (21) by described second section stream unit (22), second entrance (23B) of described economizer is directly connected with the outlet of described condenser (12), first outlet (23C) of described economizer is connected with the gas supplementing opening of described compressor (11), second outlet (23D) of described economizer is connected with the entrance of described first throttle parts (13).
7. heat pump heating according to claim 6, it is characterized in that, one end of described hydrojet branch road (3) is connected to second of described first throttle parts (13) and described economizer and exports between (23D), and the other end is connected with the gas supplementing opening of described compressor (11).
8. a Teat pump boiler, is characterized in that, comprises the arbitrary described heat pump heating of claim 1 ~ 7.
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| CN201520802685.1U CN205066233U (en) | 2015-10-15 | 2015-10-15 | Heat pump heating system and heat pump water heater |
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| CN201520802685.1U CN205066233U (en) | 2015-10-15 | 2015-10-15 | Heat pump heating system and heat pump water heater |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105258392A (en) * | 2015-10-15 | 2016-01-20 | 珠海格力电器股份有限公司 | Heat pump heating system, control method and heat pump water heater |
| CN107514814A (en) * | 2017-08-31 | 2017-12-26 | 郑州云宇新能源技术有限公司 | Barber shop's Multifunctional heat pump water heater |
| CN113028679A (en) * | 2021-04-26 | 2021-06-25 | 中国科学院理化技术研究所 | Waste heat recovery heat pump system |
-
2015
- 2015-10-15 CN CN201520802685.1U patent/CN205066233U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105258392A (en) * | 2015-10-15 | 2016-01-20 | 珠海格力电器股份有限公司 | Heat pump heating system, control method and heat pump water heater |
| CN107514814A (en) * | 2017-08-31 | 2017-12-26 | 郑州云宇新能源技术有限公司 | Barber shop's Multifunctional heat pump water heater |
| CN113028679A (en) * | 2021-04-26 | 2021-06-25 | 中国科学院理化技术研究所 | Waste heat recovery heat pump system |
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