CN216114276U - Combined type heat pump heating system - Google Patents
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- CN216114276U CN216114276U CN202121925065.9U CN202121925065U CN216114276U CN 216114276 U CN216114276 U CN 216114276U CN 202121925065 U CN202121925065 U CN 202121925065U CN 216114276 U CN216114276 U CN 216114276U
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- 239000002918 waste heat Substances 0.000 claims abstract description 71
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- 239000006096 absorbing agent Substances 0.000 claims abstract description 40
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Abstract
The utility model discloses a combined heat pump system, which solves the problems of efficiently recovering waste heat and heating return water of a heat supply network in a stepped manner. The return water of the heat supply network sequentially passes through an absorption heat pump absorber (14), a compression heat pump condenser (22) and an absorption heat pump condenser (12), and is finally supplied after peak regulation heating. The waste heat water is returned after being cooled and released through a compression heat pump evaporator (21) and an absorption heat pump evaporator (13) in sequence. The system can increase the outlet temperature of the heat pump to be higher than that of a single absorption heat pump or a compression heat pump under the same return water temperature and waste heat water temperature of the heat supply network, and the energy efficiency of the system is improved. In addition, the free power-applying capacity of the gas, steam and other high-quality heat sources during peak shaving heat supply is effectively utilized in the aspect of economy, and the lower heat supply cost is compared with that of a compression heat pump.
Description
Technical Field
The utility model belongs to the technical field of heat pump heating systems, and particularly relates to a combined type heat pump heating system.
Background
In the future 2050 years of northern towns in China, the heating area reaches about 200 hundred million square meters, and in order to realize low-carbon development, the low-grade waste heat-oriented energy structure transformation is required. The heat energy of the cogeneration and the industrial waste heat is relatively concentrated, but in order to relieve the pressure on the air quality deterioration, the coal-fired power generation or industry is restricted in a core area and is often far away from the urban heat load center, so that the key problem of how to efficiently recover the waste heat and convey the heat energy to the city at low cost is the waste heat as a heating heat source. Analysis shows that long-distance heat delivery and reduction of return water temperature of a heat supply network are main solutions. The absorption heat exchange unit is arranged in the heating station, so that the temperature of return water of a heating network can be reduced, but the temperature resistance and the pressure bearing capacity of the pipeline are limited due to uneven quality of new and old pipelines in old urban areas, and the transformation of some old urban heating stations has practical difficulties of narrow space, property attribution and the like, so that the transformation of all large temperature differences of the existing heating stations in the urban areas is difficult to realize. In order to reduce the change of the operation conditions of the current pipe network and the heating power station as much as possible, fully utilize the current heat network, and configure 25-40% of peak shaving heat sources for urban central heating, the relay energy station can be reconstructed and constructed on the original plant sites of the current heat source plant, a boiler room, a pressure isolation station and the like, and the peak shaving of the urban heat network is combined to reduce the return water temperature.
In the prior art, the heat recovery in the return water of the heat supply network is insufficient, the reduction range of the return water temperature is limited, a large amount of heat energy is still lost in the return water process of the heat supply network, and the energy waste is caused. The heat pump is adopted to recover waste heat, the heat absorption efficiency is not high, and the water temperature at the water outlet of the heat pump system is not obviously improved.
Published patent CN 108167915A 'a large temperature difference heating system and method combined with peak-shaving boiler' proposes a method for reducing the temperature of return water of a heating network by combining a steam-driven absorption heat pump and a compression heat pump, which is characterized in that: and one part of the return water of the heat supply network sequentially passes through the evaporator of the absorption heat pump and the evaporator of the compression heat pump for step cooling, and the other part of the return water of the heat supply network sequentially passes through the condenser of the compression heat pump, the absorber of the absorption heat pump and the condenser for temperature rise, and is further heated by the peak regulating boiler and then is supplied.
SUMMERY OF THE UTILITY MODEL
The technical problem to be solved by the utility model is to overcome the defects of the prior art and provide a combined heat pump heating system, which can more fully recover waste heat and avoid energy waste caused by backwater of a heat supply network in the long-distance conveying process. And simultaneously, the recovered heat is utilized to heat the water step of the heat supply network, so that the temperature rise of the water at the outlet of the heat pump system is higher. Reduce energy consumption and improve the heat energy utilization rate.
The utility model aims to provide a combined heat pump heating system, which solves the problem of insufficient heat recovery of the existing heat pump.
In order to achieve the above effects, the basic concept of the utility model is as follows: a combined heat pump heating system comprises an absorption heat pump, a compression heat pump, a heat supply network water system, a waste heat water system and a driving heat source system;
the driving heat source system includes: a driving heat source supply pipe and a driving heat source recovery pipe; the driving heat source supply pipe is connected with a generator heat source inlet of the absorption heat pump, and a generator heat source outlet of the absorption heat pump is connected with the driving heat source recovery pipe;
the residual heat water system includes: a waste hot water return pipe and a waste hot water supply pipe; the waste heat water return pipe is connected with a heat source inlet of a compression heat pump evaporator, a heat source outlet of the compression heat pump evaporator is connected with a heat source inlet of an absorption heat pump evaporator through a waste heat water return pipe, and a heat source outlet of the absorption heat pump evaporator is connected with a waste heat water supply pipe;
the heat supply network water system comprises: a heat supply network water return pipe and a heat supply network water supply pipe; the heat supply network water return pipe is connected with a cooling liquid inlet of the absorption heat pump absorber, an outlet of the absorption heat pump absorption cooling liquid absorber is connected with a cooling liquid inlet of the compression heat pump condenser through the heat supply network water return pipe, a cooling liquid outlet of the compression heat pump condenser is connected with a cooling liquid inlet of the absorption heat pump condenser through the heat supply network water return pipe, and a cooling liquid outlet of the absorption heat pump condenser is connected with a water supply pipe of the heat supply network water.
Further, still include drive heat source waste heat recovery system, drive heat source waste heat recovery system includes: the heat exchanger is arranged on the driving heat source recovery pipe, an inlet of the heat exchanger is connected with a waste heat water supply pipe through the driving heat source waste heat recovery pipe, and an outlet of the heat exchanger is connected with a waste heat water return pipe through the driving heat source waste heat recovery pipe.
Furthermore, a circulating pump is arranged on the driving heat source waste heat recovery pipe.
Further, an inlet of a waste heat water return pipe is connected with a waste heat source, or connected with a water return system of a previous stage heat supply network, or connected with a water return pipe of the heat supply network; preferably, the inlet of the residual heat water return pipe is connected with a heat supply network water return pipe.
Furthermore, a driving heat source is also communicated in the driving heat source supply and discharge pipe, and the driving heat source is gas, steam or high-temperature hot water.
Furthermore, a peak regulation device is also arranged on the heat supply network water supply pipe.
Further, the peak regulation device is a gas boiler or a steam-water heat exchanger.
Furthermore, the absorption heat pump generator, the absorption heat pump condenser, the absorption heat pump evaporator and the absorption heat pump absorber are of a single-stage or multi-stage structure; the compression type heat pump condenser and the compression type heat pump evaporator are of single-stage or multi-stage structures.
Further, the absorption heat pump is a steam type lithium bromide absorption heat pump.
The technical scheme of the utility model has the following beneficial technical effects:
the utility model discloses a combined heat pump heating system, which solves the problems of efficiently recovering waste heat and heating return water of a heat supply network in a stepped manner. The return water of the heat supply network sequentially passes through the absorption heat pump absorber, the compression heat pump condenser and the absorption heat pump condenser, and is finally supplied out after being further subjected to peak regulation and heating by the gas boiler. The waste heat water returns to the heating side after sequentially passing through the compression heat pump evaporator and the absorption heat pump evaporator for cooling and releasing heat. Compared with the prior patent, the method has the advantages that the working capacity of fuel gas can be fully utilized, the outlet water temperature of the heat pump is further raised, and more residual heat can be recovered in the same heat supply area. Taking 35 ℃ heat supply network backwater as an example, reducing the temperature of the other side residual heat water from 35 ℃ to 20 ℃, adopting the method of the prior patent, because the heat supply network backwater firstly passes through a condenser of a compression heat pump, the inlet water temperature of a suction device of the absorption heat pump is higher, the concentration of dilute solution is higher, in addition, the temperature of a generator is limited by solution corrosion and the like, the temperature of a concentrated solution is up to 165 ℃, the outlet temperature of the condenser is increased to 100 ℃ at most, and adopting the method of the patent, because the heat supply network backwater is firstly advanced into the suction device of the absorption heat pump, the concentration of the dilute solution can be kept in a reasonable range, and after an intermediate heating temperature section is supplemented by the condenser of the compression heat pump, the outlet temperature of the condenser can reach 113 ℃. From another perspective, it is explained that, under the condition that the driving heat source temperature and the low-temperature heat source temperature are not changed, when the temperature of the water inlet of the heat supply network is lower, the required lifting temperature difference (absorber solution temperature-evaporation temperature) of the absorption heat pump is smaller, the required driving temperature difference (generator solution temperature-condensation temperature) can also be smaller, and the water outlet temperature of the heat supply network can be higher.
The system can increase the outlet temperature of the heat pump to be higher than that of a single absorption heat pump or a compression heat pump under the same return water temperature and waste heat water temperature of the heat supply network, and the energy efficiency of the system is improved. In addition, the free power-applying capacity of the gas, steam and other high-quality heat sources during peak shaving heat supply is effectively utilized in the aspect of economy, and the lower heat supply cost is compared with that of a compression heat pump.
(1) The heating side of the heat supply network of the heat pump system is heated in series, and the condenser of the compression heat pump is arranged between the absorber and the condenser of the absorption heat pump, so that the capacity of the absorption heat pump for improving the temperature is fully exerted, the temperature level of the condenser of the compression heat pump is reduced, and the overall energy efficiency of the heat pump system is improved.
(2) The waste heat extraction side of the heat pump system is also connected in series in a stepped mode and used for further cooling the return water of the long heat transmission network, and efficient recycling at a waste heat source end is achieved.
Drawings
Fig. 1 is a schematic view of a structure of a conventional absorption heat pump;
FIG. 2 is a schematic diagram of a prior art compression heat pump;
FIG. 3 is a schematic view of one embodiment of a composite heat pump system of the present invention;
FIG. 4 is a schematic view of another embodiment of the compound heat pump system of the present invention;
reference numerals:
wherein 1-absorption heat pump; 2-a compression heat pump; (ii) a 11-an absorption heat pump generator; 12-absorption heat pump condenser; 13-absorption heat pump evaporator; 14-absorption heat pump absorber; 21-a compression heat pump evaporator; 22-a compression heat pump condenser; 31-heat supply network water return pipe; 32-heat supply network water supply pipe; 41-residual hot water return pipe; 42-residual heat water supply pipe; 43-driving a heat source waste heat recovery pipe; 51-a driving heat source; 52-drive the heat source supply line; 53-drive heat source recovery tube; 6-a heat exchanger; 7-a peak shaving device; 8-circulating pump.
Detailed Description
In the drawings a schematic view of a layer structure according to an embodiment of the utility model is shown. The figures are not drawn to scale, wherein certain details are exaggerated and possibly omitted for clarity. The shapes of various regions, layers, and relative sizes and positional relationships therebetween shown in the drawings are merely exemplary, and deviations may occur in practice due to manufacturing tolerances or technical limitations, and a person skilled in the art may additionally design regions/layers having different shapes, sizes, relative positions, as actually required.
It is to be understood that the embodiments described are only a few embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention. In the description of the present invention, it should be noted that the terms "first", "second", and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In addition, the technical features involved in the different embodiments of the present invention described below may be combined with each other as long as they do not conflict with each other.
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be described in further detail with reference to the accompanying drawings in conjunction with the following detailed description. It should be understood that the description is intended to be exemplary only, and is not intended to limit the scope of the present invention. Moreover, in the following description, descriptions of well-known structures and techniques are omitted so as to not unnecessarily obscure the concepts of the present invention.
Referring to fig. 3, the combined heat pump system provided by the utility model is arranged in a heat supply network heating system so as to recover waste heat water or waste heat of return water of a heat supply network and improve the energy utilization efficiency. It is understood that in other embodiments of the present invention, the compound heat pump system can be used in other applications, such as industrial or agricultural hot water systems, and is not limited herein.
In the embodiment of the utility model, the combined heat pump heating system comprises an absorption heat pump 1, a compression heat pump 2, a heat supply network water system, a waste heat water system and a driving heat source system;
the driving heat source system includes: a driving heat source 51, a driving heat source supply pipe 52, and a driving heat source recovery pipe 53; the driving heat source supply pipe 52 is connected with a heat source inlet of the absorption heat pump generator 11, and a heat source outlet of the absorption heat pump generator 11 is connected with a driving heat source recovery pipe 53;
the residual heat water system includes: a residual heat water return pipe 41 and a residual heat water supply pipe 42; the residual heat water return pipe 41 is connected with a heat source inlet of a compression heat pump evaporator 21, a heat source outlet of the compression heat pump evaporator 21 is connected with a heat source inlet of an absorption heat pump evaporator 13 through the residual heat water return pipe 41, and a heat source outlet of the absorption heat pump evaporator 13 is connected with a residual heat water supply pipe 42;
the heat supply network water system comprises: a heat supply network water return pipe 31 and a heat supply network water supply pipe 32; the heat supply network water return pipe 31 is connected with a cooling liquid inlet of the absorption heat pump absorber 14, a cooling liquid outlet of the absorption heat pump absorber 14 is connected with a cooling liquid inlet of the compression heat pump condenser 22 through the heat supply network water return pipe 31, a cooling liquid outlet of the compression heat pump condenser 22 is connected with a cooling liquid inlet of the absorption heat pump condenser 12 through the heat supply network water return pipe 31, and a cooling liquid outlet of the absorption heat pump condenser 12 is connected with a heat supply network water supply pipe 32.
Under the system structure, the backwater of the heat supply network passes through the absorption heat pump absorber 14, the compression heat pump condenser 22 and the absorption heat pump condenser 12 in sequence, and is supplied after three-stage heating. The waste heat water returns to the heating side after passing through the compression heat pump evaporator 21 and the absorption heat pump evaporator 13 in sequence for cooling and releasing heat. The system can improve the outlet temperature of the heat pump to be higher than that of a single gas absorption heat pump or a single voltage compression heat pump under the same return water temperature and waste heat water temperature of the heat supply network, and improves the energy efficiency of the system.
It should be noted that the heat supply network water return pipe 31 of the present invention must be arranged in the order of connecting the absorption heat pump absorber 14, then connecting the compression heat pump condenser 22, and finally connecting the absorption heat pump condenser 12, and if the connection order is changed, the beneficial effect of increasing the heating temperature of the present invention cannot be achieved.
The connection sequence of the present invention is obtained by comprehensively analyzing the characteristics of the absorption heat pump, and therefore, the characteristics of the absorption heat pump need to be explained and the analysis process of the present invention is clarified.
Referring to fig. 1, a schematic diagram of an absorption heat pump, which uses a working medium pair solution composed of a high boiling point substance and a low boiling point substance to recover and utilize heat energy. The common lithium bromide solution is used, wherein the lithium bromide is an absorbent, the boiling point of the lithium bromide is as high as 1265 ℃, the lithium bromide is a salt substance with strong water absorbability, solid lithium bromide can absorb water vapor, and the lithium bromide solution with higher concentration also has strong water vapor absorption capacity. After the lithium bromide concentrated solution absorbs water vapor, the concentration is reduced to become a dilute solution, and after the water is evaporated and concentrated by heating, the lithium bromide concentrated solution can be recycled. The lithium bromide absorption heat pump takes lithium bromide solution as an absorbent, and achieves the heating purpose by utilizing the process of converting water in a gas-liquid state.
Referring to fig. 1, an absorption heat pump 1 mainly includes four parts: an absorption heat pump generator 11, an absorption heat pump condenser 12, an absorption heat pump evaporator 13, and an absorption heat pump absorber 14. The working process comprises the following steps:
firstly, in the absorption heat pump generator 11, the lithium bromide solution is heated to boiling by the driving heat source medium in the driving heat source supply pipe, so that the water in the lithium bromide solution is evaporated to form high-temperature water vapor, the concentration of the lithium bromide solution losing the water is increased to become a lithium bromide concentrated solution, the lithium bromide concentrated solution flows back to the absorption heat pump absorber 14, and the high-temperature water vapor is conveyed to the absorption heat pump condenser 12.
In the second step, in the absorption heat pump condenser 12, the high-temperature water vapor meets the surface of the heat supply network water return pipe 31 and is condensed, so that a large amount of latent heat is released, the water in the heat supply network water return pipe 31 is heated, and the water temperature in the heat supply network water return pipe 31 is increased. The condensed water enters the absorption heat pump evaporator 13 after throttling.
Thirdly, in the absorption heat pump evaporator 13, the evaporation temperature of water in the evaporator is low, and the water can be saturated and evaporated at 5 ℃ generally, so that the surface temperature of the waste heat water pipe is enough to evaporate the condensed water, the condensed water is evaporated and evaporated on the surface of the waste heat water pipe by heat, and a large amount of heat is absorbed in the evaporation process, so that the temperature of the waste heat water is reduced, and the purpose of recovering heat is achieved. And the water vapor generated after the condensed water is gasified enters an absorber.
Fourthly, in the absorption heat pump absorber 14, the lithium bromide concentrated solution flowing back from the generator is sprayed on the outer surface of the heat supply network water return pipe 31 and meets the water vapor from the absorption heat pump evaporator 13 on the outer surface of the heat supply network water return pipe 31, the lithium bromide concentrated solution absorbs the water vapor, and a large amount of latent heat is released on the outer surface of the heat supply network water return pipe 31 in the process that the water vapor is absorbed and liquefied, so that the water in the heat supply network water return pipe 31 is heated, and the return water temperature of the heat supply network is increased. The concentration of the lithium bromide solution after absorbing the water vapor is reduced to become a lithium bromide dilute solution, the lithium bromide dilute solution flows into the bottom of the absorption heat pump absorber 14 and is pumped into the absorption heat pump generator 11 to be heated by the driving heat source again to boil out moisture, and the lithium bromide dilute solution becomes a concentrated solution after being steamed out and has the capacity of absorbing the water vapor. The whole system is circularly operated in such a way. The return water of the heat supply network is sent out from the outlet of the condenser 12 of the absorption heat pump after passing through the absorber 14 of the absorption heat pump and the condenser 12 for twice temperature rise.
In the absorption heat pump absorber 14, a large amount of cooling liquid is needed to cool the lithium bromide solution due to the large amount of heat released when the lithium bromide solution absorbs water vapor, otherwise, the absorption performance of the lithium bromide solution is inhibited due to the over-high temperature in the absorber, so that the absorption process cannot be performed, and the system efficiency is reduced. The cooling liquid, i.e. the return water of the heat supply network in the return water pipe 31 of the heat supply network, needs to ensure that the temperature of the water in the return water pipe of the heat supply network entering the absorber is not too high. Therefore, the heat supply network backwater is ensured not to be heated before entering the absorber in the process of increasing the temperature of the heat supply network backwater.
In the absorption heat pump evaporator 13, because the interior of the evaporator is negative pressure, the saturated evaporation temperature of water is very low, and the saturated evaporation can be performed at 5 ℃, that is, the evaporator can recover heat from waste heat water with low temperature, so that the temperature of the water in the waste heat water return pipe is reduced, and the normal operation of the evaporator cannot be influenced. And the temperature of the waste heat water is reduced, and the temperature of the generated steam can be reduced, so that the steam with lower temperature enters the absorber, and the working efficiency of the absorber is improved.
In the absorption heat pump condenser 12, in order to increase the temperature of the heat supply network water flowing out of the condenser to a higher level, the temperature of the heat supply network water flowing into the condenser needs to be increased under the condition that the high-temperature steam condition is not changed.
By combining the above analysis, three design ideas are obtained:
1. the temperature of the existing heating network water entering the absorption heat pump absorber 14 is not increased;
2. reducing the temperature of the residual heat water entering the absorption heat pump evaporator 13;
3. raising the temperature of the heat supply network water entering the absorption heat pump condenser 12;
in order to realize the three-point design idea, a compression heat pump 2 (the structure of the compression heat pump is shown in figure 2) is considered to be additionally arranged, the compression heat pump evaporator 21 is used for cooling the residual heat water return water and then sending the residual heat water to the absorption heat pump evaporator, and the compression heat pump condenser 22 is used for heating the heat supply network return water flowing out of the absorption heat pump absorber and then sending the heat supply network return water to the absorption heat pump condenser.
Referring to fig. 3, specifically, a heat supply network water return pipe 31 is directly connected with an absorption heat pump absorber (for realizing that the temperature of the heat supply network water entering the absorber is not increased); the waste heat water return is firstly cooled by a compression heat pump evaporator 21 and then enters an absorption heat pump evaporator 13, namely, a waste heat water return pipe is firstly connected with an inlet of the compression heat pump evaporator 21 and then connected with an outlet of the compression heat pump evaporator and an inlet of the absorption heat pump evaporator (used for reducing the temperature of the waste heat water entering the evaporator); the heat supply network water flowing out of the absorber is heated and then enters the condenser, namely the outlet of the absorption heat pump absorber 14 is connected with the inlet of the compression heat pump condenser 22 through a heat supply network water return pipe 31, and the outlet of the compression heat pump condenser 22 is connected with the absorption heat pump condenser through a heat supply network water return pipe (used for increasing the temperature of the heat supply network water entering the condenser).
The main structure and the constitution mode of the composite heat pump system provided by the utility model are as above.
Another design idea is to connect the compression heat pump 2 and the absorption heat pump 1 in series in a simple combination manner, so that the return water of the heat supply network is heated by the compression heat pump 2 and then enters the absorption heat pump for further heating, but the effect of the series connection manner is not good because the requirement of the absorption heat pump absorber 14 on the working temperature is not considered, the temperature of the return water of the heat supply network heated by the compression heat pump 2 is increased, and then the return water enters the absorption heat pump absorber 14 to inhibit the water absorption process of the lithium bromide solution in the absorber, so that the working efficiency of the whole absorption heat pump 1 is reduced. The simple solution of connecting the compression heat pump 2 and the absorption heat pump 1 in series is therefore disadvantageous. Therefore, a structure that a compression heat pump and an absorption heat pump are directly connected in series cannot be adopted.
In addition, considering that the driving heat source still has a lot of residual heat energy after heating the lithium bromide solution in the generator, if the residual heat energy is not recycled, the residual heat energy will be wasted in the driving heat source recycling pipe.
In order to further improve the heat recovery effect and increase the temperature of the heat supply network, the embodiment of the utility model also comprises a driving heat source waste heat recovery system, wherein the driving heat source waste heat recovery system comprises: the heat exchanger 6 is arranged on the driving heat source recovery pipe 52, the inlet of the heat exchanger is connected with a waste heat water supply pipe through the driving heat source waste heat recovery pipe, and the outlet of the heat exchanger is connected with a waste heat water return pipe through the driving heat source waste heat recovery pipe 43.
In addition, a circulation pump 8 is provided on the driving heat source residual heat recovery pipe 31 to circulate water in the pipe.
According to the embodiment of the utility model, the backwater of the waste heat water system can be selected from various different sources according to the working condition scene of practical application, for example, the inlet of the waste heat water backwater pipe can be connected with a waste heat source, or the inlet of the waste heat water backwater pipe can be connected with the backwater system of the upper-stage heat supply network.
Referring to fig. 4, in another embodiment of the present invention, the waste heat water source may also be derived from the heat supply network water return, that is, a water path branched from the heat supply network water return pipe 31 serves as the waste heat water source, that is, the inlet of the waste heat water return pipe 41 is connected to the heat supply network water return pipe 31. The advantage of adopting this kind of mode is lower at the construction requirement of system, need not look for independent waste heat source, and it is more convenient to set up, utilizes heat supply network water self to can further reduce heat supply network water return water temperature as the waste heat water source simultaneously, reduces the heat energy waste on the way of return water transport.
The choice of the driving heat source can be selected according to the specific application environment, and different heat sources can be selected for industrial application, agricultural application and civil use, and gas, steam or high-temperature hot water is often adopted.
In order to meet the user demand in the peak heating period, a peak regulation device can be arranged on the water supply pipe of the heat supply network. The peak shaving device 7 is used for increasing the heat supply when the user intensively uses the heat.
The peak shaving device 7 can be different devices, for example, the peak shaving device is a gas boiler or a steam-water heat exchanger.
In some extreme areas with energy shortage, in order to improve the heating capacity of the system, the absorption heat pump generator 11, the absorption heat pump condenser 12, the absorption heat pump evaporator 13 and the absorption heat pump absorber 14 can be further arranged into a multi-stage structure; the compression heat pump condenser 22 and the compression heat pump evaporator 21 may be provided in a multistage structure.
For example, in one embodiment, the absorption heat pump 1 may be provided with two or more absorption heat pump generators 11 connected in series, and the driving heat source supply pipe passes through each absorption heat pump generator 11 in turn to more thoroughly absorb the heat of the driving heat source. Two or more than two absorption heat pump condensers 12 connected in series can be arranged in the same way, and the heat supply network water return pipe 31 sequentially passes through each absorption heat pump condenser so as to heat the heat supply network return water more fully. Two or more than two absorption heat pump evaporators 13 which are connected in series can be arranged in the same way, and the waste heat water return pipe 41 sequentially passes through each absorption heat pump evaporator 13, so that the heat recovery of the waste heat water is more sufficient. And two or more absorption heat pump absorbers 14 connected in series, and a heat supply network water return pipe 31 sequentially passes through each absorption heat pump absorber 14 to fully heat the heat supply network water.
Similarly, the compression heat pump can be provided with two or more compression heat pump condensers 22 connected in series, and the heat supply network water return pipe 31 sequentially passes through each compression heat pump condenser 22 so as to fully heat the heat supply network return water. Two or more compression heat pump evaporators 21 connected in series may be provided, and the residual heat water returning pipe 41 may be sequentially passed through each compression heat pump evaporator 21.
Further, there are two main types of the absorption heat pump 1, one is an ammonia absorption heat pump, and the other is a lithium bromide absorption heat pump. The evaporation temperature of the ammonia unit can reach-60, and the ammonia unit is used for a cold storage and is quick-frozen more. And ammonia gas is toxic. When the air is mixed with air to reach a certain concentration, the air is easy to explode when encountering open fire, and the air is dangerous, so that automatic operation cannot be realized without full-automatic equipment generally, and manual operation is required.
The lithium bromide unit uses water as refrigerant, the evaporation temperature is above 0 ℃, the effluent is above 5 ℃, and low-pressure steam or residual heat water can be utilized to recycle waste gas, waste heat, solar energy and low-temperature heat energy. The lithium bromide heat pump is more suitable for recycling heat energy of low-temperature heat sources (such as waste hot water) to prepare required processes or high-temperature heating media (hot water) for heating, and realizes equipment for conveying heat energy from low temperature to high temperature. Therefore, in the embodiment of the present invention, it is preferable that the absorption heat pump is a steam type lithium bromide absorption heat pump.
It is to be understood that the above-described embodiments of the present invention are merely illustrative of or explaining the principles of the utility model and are not to be construed as limiting the utility model. Therefore, any modification, equivalent replacement, improvement and the like made without departing from the spirit and scope of the present invention should be included in the protection scope of the present invention. Further, it is intended that the appended claims cover all such variations and modifications as fall within the scope and boundaries of the appended claims or the equivalents of such scope and boundaries.
Claims (10)
1. A combined heat pump heating system is characterized by comprising an absorption heat pump (1), a compression heat pump (2), a heat supply network water system, a waste heat water system and a driving heat source system;
the driving heat source system includes: a driving heat source supply pipe (52) and a driving heat source recovery pipe (53); the driving heat source supply pipe (52) is connected with a heat source inlet of a generator (11) of the absorption heat pump, and a heat source outlet of the generator (11) of the absorption heat pump is connected with a driving heat source recovery pipe (53);
the residual heat water system includes: a residual heat water return pipe (41) and a residual heat water supply pipe (42); the waste heat water return pipe (41) is connected with a heat source inlet of a compression type heat pump evaporator (21), a heat source outlet of the compression type heat pump evaporator (21) is connected with a heat source inlet of an absorption type heat pump evaporator (13) through the waste heat water return pipe (41), and a heat source outlet of the absorption type heat pump evaporator (13) is connected with a waste heat water supply pipe (42);
the heat supply network water system comprises: a heat supply network water return pipe (31) and a heat supply network water supply pipe (32); the heat supply network water return pipe (31) is connected with a cooling liquid inlet of the absorption heat pump absorber (14), a cooling liquid outlet of the absorption heat pump absorber (14) is connected with a cooling liquid inlet of the compression heat pump condenser (22) through the heat supply network water return pipe (31), a cooling liquid outlet of the compression heat pump condenser (22) is connected with a cooling liquid inlet of the absorption heat pump condenser (12) through the heat supply network water return pipe (31), and a cooling liquid outlet of the absorption heat pump condenser (12) is connected with a heat supply network water supply pipe (32).
2. The combined heat pump heating system of claim 1, further comprising a driving heat source waste heat recovery system, the driving heat source waste heat recovery system comprising: the heat exchanger (6) is arranged on the driving heat source recovery pipe (43), an inlet of the heat exchanger (6) is connected with a waste heat water supply pipe (42) through the driving heat source waste heat recovery pipe (43), and an outlet of the heat exchanger (6) is connected with a waste heat water return pipe (41) through the driving heat source waste heat recovery pipe (43).
3. The combined heat pump heating system according to claim 2, wherein the driving heat source waste heat recovery pipe (43) is provided with a circulating pump (8).
4. The combined heat pump heating system according to claim 1, wherein an inlet of the waste heat water return pipe (41) is connected with a waste heat source, or connected with a water return system of a previous stage heat supply network, or connected with the heat supply network water return pipe (31).
5. The system according to claim 1, wherein a driving heat source (51) is further introduced into the driving heat source supply pipe (52), and the driving heat source is gas, steam or high-temperature hot water.
6. The combined heat pump heating system according to claim 1, wherein a peak shaving device is further provided on the heat supply network water supply pipe (32).
7. The combined heat pump heating system according to claim 1, wherein the peak shaver (7) is a gas boiler or a steam-water heat exchanger.
8. The combined heat pump heating system according to claim 1, wherein the absorption heat pump generator (11), the absorption heat pump condenser (12), the absorption heat pump evaporator (13) and the absorption heat pump absorber (14) are of a single-stage or multi-stage structure.
9. A combined heat pump heating system according to claim 1, characterised in that the compression heat pump condenser (22) and the compression heat pump evaporator (21) are of single-stage or multistage construction.
10. The combined heat pump heating system according to claim 1, wherein the absorption heat pump (1) is a steam-type lithium bromide absorption heat pump.
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| CN113566260A (en) * | 2021-08-17 | 2021-10-29 | 清华大学 | Combined type heat pump heating system and method |
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| CN113566260A (en) * | 2021-08-17 | 2021-10-29 | 清华大学 | Combined type heat pump heating system and method |
| CN113566260B (en) * | 2021-08-17 | 2024-05-07 | 清华大学 | Combined heat pump heating system and method |
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