CN220287387U - Adsorption type steam generation system for generating steam by utilizing residual heat of central air conditioner - Google Patents
Adsorption type steam generation system for generating steam by utilizing residual heat of central air conditioner Download PDFInfo
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- CN220287387U CN220287387U CN202320826837.6U CN202320826837U CN220287387U CN 220287387 U CN220287387 U CN 220287387U CN 202320826837 U CN202320826837 U CN 202320826837U CN 220287387 U CN220287387 U CN 220287387U
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- 238000001179 sorption measurement Methods 0.000 title claims abstract description 154
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 176
- 239000002918 waste heat Substances 0.000 claims abstract description 50
- 229910021536 Zeolite Inorganic materials 0.000 claims description 29
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 29
- 239000010457 zeolite Substances 0.000 claims description 29
- 230000003020 moisturizing effect Effects 0.000 claims description 8
- 238000004321 preservation Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 2
- 229920006395 saturated elastomer Polymers 0.000 description 15
- 238000006243 chemical reaction Methods 0.000 description 13
- 230000001502 supplementing effect Effects 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model relates to an adsorption type steam generation system for generating steam by utilizing waste heat of a central air conditioner, which comprises a waste heat air inlet pipeline, a heat exchanger, an air inlet pipeline, an air compressor, a dryer, an air heater, a hot dry air main pipe, a constant temperature water tank, a pump, a water heater, a water inlet main pipe, an adsorption reactor group, a high-temperature steam main pipe and steam using equipment.
Description
Technical Field
The utility model belongs to the technical field of adsorption heat exchange equipment, and particularly relates to an adsorption type steam generation system for generating steam by utilizing waste heat of a central air conditioner.
Background
With the continuous development of the economic level, the central air conditioner becomes a necessity for some public places, but in the running process, the electric energy consumed by the central air conditioner is huge, and in a large building, the specific gravity of the electric power consumption of the central air conditioner in the total electric power consumption is about 50%. When the central air conditioner works in refrigeration, the condensation heat of the air conditioning system is directly discharged to the atmosphere without utilization, and the value of the condensation heat is about 1.15 to 1.30 times of the refrigerating capacity, so that energy waste is caused, and environmental heat pollution is caused.
The existing central air conditioner waste heat recovery device is used for replacing the traditional energy sources to heat domestic water and the like by recovering part of low-grade waste heat through a heat exchanger, so that heat pollution can be reduced, meanwhile, the heat load of a condenser of an air conditioner water chilling unit can be lightened, power consumption is saved, but the waste heat utilization form of the device is single, and the grade of the recovered waste heat cannot be effectively improved.
The adsorption heat pump is an effective method for generating medium-temperature heat energy by utilizing low-temperature waste heat. The adsorption heat pump has different requirements on the low-temperature heat source temperature due to different adsorbents. The adsorption working substance pair that has been identified so far is zeolite-water. The adsorption reaction is divided into two stages, "steam generation" and "zeolite regeneration". Firstly, high-temperature steam is obtained by introducing low-temperature water at about 80 ℃ into a reactor filled with a zeolite layer. After this stage, the water in the reactor was discharged. And after the water in the reactor is exhausted, introducing 130 ℃ gas into the reactor to carry out zeolite regeneration stage, and circulating in this way. The prior art does not describe the application of the heat pump to the recovery of the residual heat of the central air conditioner.
Disclosure of Invention
In summary, in order to overcome the defects of the prior art, the utility model provides an adsorption type steam generation system for generating steam by utilizing the waste heat of a central air conditioner, which is characterized in that the waste heat of the central air conditioner is recycled and utilized to preheat air, then the preheated air is pressurized, dried and heated to generate hot dry air required by regenerating 13x zeolite, the 13x zeolite in an adsorption reactor of an adsorption heat pump system is subjected to adsorption reaction to generate high-temperature steam, when the 13x zeolite in the adsorption reactor is saturated, the water in the adsorption reactor is emptied and then the hot dry air is introduced into the adsorption reactor, so that the 13x zeolite in the adsorption reactor is regenerated, the waste heat of the central air conditioner is utilized to preheat the air, and the energy consumption required by heating the air can be effectively reduced, and the energy is saved.
In order to solve the technical problems, the technical scheme of the utility model is realized as follows:
an adsorption type steam generation system for generating steam by utilizing waste heat of a central air conditioner, wherein: the adsorption device comprises a waste heat air inlet pipeline, a heat exchanger, an air inlet pipeline, an air compressor, a dryer, an air heater, a hot dry air main pipe, a constant temperature water tank, a pump, a water heater, a water inlet main pipe, an adsorption reactor set, a high-temperature steam main pipe and steam using equipment, wherein the waste heat air inlet pipeline is used for communicating a waste heat air outlet of a central air conditioner with waste heat air inlet of the heat exchanger, the waste heat air outlet of the heat exchanger is emptied, the air inlet pipeline is communicated with air and an air inlet of the heat exchanger, an air outlet of the heat exchanger is communicated with air inlet of the air compressor through a pipeline, an air outlet of the air compressor is communicated with an air inlet of the dryer, an air outlet of the dryer is communicated with an air inlet of the air heater, an air outlet of the air heater is communicated with an air inlet of an adsorption reactor set through the hot dry air main pipe, a water inlet of the adsorption reactor set is communicated with a water outlet of the water heater through a pipeline, a water inlet of the pump is communicated with a water outlet of the constant temperature water tank, a water outlet of the adsorption reactor set is communicated with a water return port of the constant temperature water tank, an air outlet of the adsorption reactor set is communicated with the high-temperature steam using equipment, an air outlet of the adsorption reactor set is communicated with the air outlet of the adsorption reactor set through the high-temperature steam using equipment, and the adsorption layer is arranged in the adsorption layer 13, and the adsorption layer is arranged in the adsorption device is an adsorption layer.
Further, the adsorption reactor group comprises three adsorption reactors, namely a first adsorption reactor, a second adsorption reactor and a third adsorption reactor, wherein the first adsorption reactor is communicated with a hot dry air main pipe through a first air inlet pipeline, a first air inlet valve is arranged on a first air inlet pipeline, the first adsorption reactor is communicated with a high-temperature steam main pipe through a first steam pipeline, a first steam valve is arranged on the first steam pipeline, the first adsorption reactor is communicated with a water inlet main pipe through a first water inlet pipeline, a first water inlet valve is arranged on the first water inlet pipeline, the first adsorption reactor is communicated with a constant-temperature water tank through a first water outlet pipe, a first water diversion valve is arranged on the first water outlet pipe, the second adsorption reactor is communicated with the hot dry air main pipe through a second air inlet pipeline, a second air inlet valve is arranged on the second air inlet pipeline, the second adsorption reactor is communicated with the high-temperature steam main pipe through a second steam pipeline, a second steam valve is arranged on the second steam pipeline, the second adsorption reactor is communicated with a third water inlet valve is arranged on the third water inlet pipeline, the first adsorption reactor is communicated with a third water inlet valve through a third water inlet pipeline, the third adsorption reactor is communicated with the third water inlet pipeline, the first water inlet valve is communicated with the third water inlet pipeline, the third adsorption reactor is communicated with the constant-temperature water tank through a third drain pipe, and a third shunt valve is arranged on the third drain pipe.
Further, the constant temperature water tank communicate the water source through the moisturizing pipeline, moisturizing pipeline be the heat preservation pipeline, be provided with the moisturizing valve on the moisturizing pipeline.
Further, a waste heat air inlet valve is arranged on the waste heat air inlet pipe.
Further, an air filter and an air inlet valve are arranged on the air inlet pipe.
Further, an air inlet main valve is arranged on the hot dry air main pipe.
Further, a water inlet main valve is arranged on a pipeline for communicating the water inlet of the water heater with the water outlet of the pump.
The beneficial effects of the utility model are as follows:
1. the utility model is to recycle and utilize the waste heat of the central air conditioner to preheat the air, then boost and dry the preheated air and heat the preheated air to generate hot dry air required by regenerating the 13x zeolite, the 13x zeolite in the adsorption reactor of the adsorption heat pump system generates adsorption reaction to generate high-temperature steam, when the 13x zeolite in the adsorption reactor is saturated, the water in the adsorption reactor is emptied and then the hot dry air is introduced into the adsorption reactor, so that the 13x zeolite in the adsorption reactor is regenerated, and the waste heat of the central air conditioner is utilized to preheat the air, thereby effectively reducing the energy consumption required by heating the air and saving energy.
2. The utility model can effectively reduce the heat load of the condenser in the air conditioning unit, effectively improve the efficiency of the air conditioning unit, remarkably reduce the power consumption and create economic benefit.
3. The adsorption reactor group comprises a plurality of adsorption reactors which are arranged in parallel, the adsorption reactors are arranged in parallel and can be controlled independently through an air inlet valve and an air inlet valve, the 13x zeolite in the first adsorption reactor can generate adsorption reaction to generate high-temperature steam after being saturated, meanwhile, the 13x zeolite in the first adsorption reactor can generate adsorption reaction to generate high-temperature steam after being saturated, the 13x zeolite in the second adsorption reactor can generate adsorption reaction to generate high-temperature steam after being saturated, the 13x zeolite in the first and second adsorption reactors can generate adsorption reaction to generate high-temperature steam after being saturated, and the 13x zeolite in the second and third adsorption reactors can generate high-temperature steam after being saturated, so the continuous production of the high-temperature steam can be realized by circulating and reciprocating.
4. The utility model has simple structure and convenient use, and utilizes the waste heat generated by the central air conditioner as one of the energy sources for driving the adsorption heat pump system, thereby reducing the environmental heat pollution generated by waste heat emission and reducing the energy source consumed by the adsorption heat pump system.
Drawings
Fig. 1 is a schematic structural view of the present utility model.
Description of the embodiments
The present utility model will be described in further detail with reference to the accompanying drawings.
As shown in fig. 1, an adsorption type steam generation system for generating steam by utilizing waste heat of a central air conditioner comprises a waste heat air inlet pipeline 1, a heat exchanger 3, an air inlet pipeline 4, an air compressor 6, a dryer 7, an air heater 8, a hot dry air main pipe 10, a constant temperature water tank 31, a pump 30, a water heater 28, a water inlet main pipe 27, an adsorption reactor group, a high temperature steam main pipe 17 and steam using equipment 47, wherein the waste heat air inlet pipeline 1 is used for communicating a waste heat air outlet of the central air conditioner with waste heat inlet of the heat exchanger 3, the waste heat air inlet pipeline 1 is provided with a waste heat air inlet valve 2, the waste heat air outlet of the heat exchanger 3 is emptied, the air inlet pipeline 4 is communicated with air inlets of the atmosphere and the heat exchanger 3, and the air inlet pipeline 4 is provided with an air filter 34 and an air inlet valve 5. The air outlet of the heat exchanger 3 is communicated with the air inlet of the air compressor 6 through a pipeline, the air outlet of the air compressor 6 is communicated with the air inlet of the dryer 7, the air outlet of the dryer 7 is communicated with the air inlet of the air heater 8, the air outlet of the air heater 8 is communicated with the air inlet of the adsorption reactor set through a hot dry air main pipe 10, the hot dry air main pipe 10 is provided with an air inlet main valve 9, the water inlet of the adsorption reactor set is communicated with the water outlet of the water heater 28 through a water inlet main pipe 27, the water inlet of the water heater 28 is communicated with the water outlet of the pump 30 through a pipeline, and the pipeline for communicating the water inlet of the water heater 28 with the water outlet of the pump 30 is provided with a water inlet main valve 29. The water inlet of the pump 30 is communicated with the water outlet of the constant temperature water tank 31, the constant temperature water tank 31 is communicated with a water source through a water supplementing pipeline 32, the water supplementing pipeline 32 is a heat preservation pipeline, and a water supplementing valve 33 is arranged on the water supplementing pipeline 32. The outlet of the adsorption reactor group is communicated with the water return port of the constant temperature water tank 31, the air outlet of the adsorption reactor group is communicated with the steam using equipment 47 through the high temperature steam header pipe 17, the adsorption reactor group comprises a plurality of adsorption reactors which are arranged in parallel, an adsorption layer is arranged in the adsorption reactor, and the adsorption layer is a 13x zeolite adsorption layer.
In this embodiment, the adsorption reactor set includes three adsorption reactors, which are respectively a first adsorption reactor 18, a second adsorption reactor 19 and a third adsorption reactor 20, the first adsorption reactor 18 is connected to the hot dry air main pipe 10 through a first air inlet pipe 35, a first air inlet valve 11 is disposed on the first air inlet pipe 35, the first adsorption reactor 18 is connected to the high temperature steam main pipe 17 through a first steam pipe 38, the first steam pipe 38 is provided with a first steam valve 14, the first adsorption reactor 18 is connected to the water inlet main pipe 27 through a first water inlet pipe 41, the first water inlet pipe 41 is provided with a first water inlet valve 21, the first adsorption reactor 18 is connected to the constant temperature water tank 31 through a first water outlet pipe 44, the first water outlet pipe 44 is provided with a first water diversion valve 24, the second adsorption reactor 19 is connected to the hot dry air main pipe 10 through a second air inlet pipe 36, the second air inlet pipe 36 is provided with a second air inlet valve 12, the second adsorption reactor 19 is connected to the high temperature water inlet main pipe 17 through a second steam pipe 39, the first water inlet pipe 41 is connected to the second water inlet pipe 41, the first water inlet valve 41 is connected to the first water inlet pipe 21 through a first water inlet pipe 41, the first water inlet pipe 41 is connected to the first water inlet pipe 45, the first water inlet valve 20 is connected to the first water inlet pipe 45 through a second water inlet pipe 45, the second water inlet valve 37 is connected to the second water inlet pipe 45, the second water inlet pipe 45 is connected to the second water inlet pipe 37 through a second water inlet pipe 45, the second water inlet pipe 45 is connected to the second water inlet pipe 45, and the second water inlet pipe 45 is connected to the high temperature air main pipe 20, the third steam pipeline 40 is provided with a third steam valve 16, the third adsorption reactor 20 is communicated with the water inlet main pipe 27 through a third water inlet pipeline 43, the third water inlet pipeline 43 is provided with a third water inlet valve 23, the third adsorption reactor 20 is communicated with the constant temperature water tank 31 through a third water outlet pipe 46, and the third water outlet pipe 46 is provided with a third water diversion valve 26.
When the air conditioner is used, the waste heat air inlet valve 2, the air inlet valve 5, the air compressor 6, the air heater 8, the air inlet main valve 9, the first air inlet valve 11, the second air inlet valve 12 and the third air inlet valve 13 are opened, waste heat generated by the central air conditioner enters the heat exchanger 3 through the waste heat air inlet pipeline 1, air is filtered through the filter and then enters the heat exchanger 3 through the air inlet pipeline 4, heat in the waste heat is absorbed by the air, the temperature of the air is raised, the waste heat of the central air conditioner is cooled and then discharged, the air is preheated, the preheated air is pressurized by the air compressor 6 and then enters the dryer 7 to be dried, then the heated air is heated by the air heater 8 and then becomes hot dry air, the hot dry air flows along the hot dry air main pipe 10, then enters the first adsorption reactor 18, the second adsorption reactor 19 and the third adsorption reactor 20 through the first air inlet pipeline 35, the second air inlet pipeline 36 and the third air inlet pipeline 37 respectively, 13x zeolite in the three adsorption reactors is desorbed by utilizing the hot dry air, 13x zeolite in the three adsorption reactors is regenerated, the air is completely desorbed, the air is completely, the air is preheated by the air main valve 9, the first heater, the first air heater 6, the compressed air valve 11, the second air inlet valve 11 and the third air inlet valve 25 are stopped, the hot wet air is saturated by the water inlet valve 25, the water is saturated by the hot water, and the hot water is saturated by the hot water in the water heater, and the water heater is saturated by the water through the water heater, and the water heater is saturated by the hot wet air, and the air is saturated by the water.
The pump 30 and the water heater 28 are started, the water inlet main valve 29 and the first water inlet valve 21 are opened, the second water diversion valve 25 and the third water diversion valve 26 are closed, hot water in the constant temperature water tank 31 enters the water heater 28 under the action of the pump 30 and is heated to generate hot water at about 80 ℃, the hot water enters the first adsorption reactor 18 along the water inlet main pipe 27 through the first water inlet pipeline 41, adsorption reaction is carried out on the hot water and 13x zeolite in the first adsorption reactor 18, adsorption heat generated in the adsorption reaction process enables the hot water to evaporate, high-temperature steam is generated, the steam can continuously absorb and emit heat to generate more high-temperature steam with the 13x zeolite, after the steam pressure in the first adsorption reactor 18 reaches a set value, the first air outlet valve is opened, the high-temperature steam enters the steam main pipe along the first steam pipeline 38 and then enters the steam using equipment 47, such as a steam washing equipment, and the steam washing equipment utilizes the high-temperature steam to wash clothes. When the liquid level of the water in the first adsorption reactor 18 reaches the top end of the adsorption layer, the first water inlet valve 21 is closed, the first water diversion valve 24 and the second water inlet valve 22 are opened, the first adsorption reactor 18 discharges water, hot water enters the second adsorption reactor 19, the second adsorption reactor 19 generates adsorption reaction to generate high-temperature steam, the high-temperature steam is provided for the steam using equipment 47, the steam compressor and the air heater 8 are started, the air inlet main valve 9 and the first air inlet valve 11 are opened, hot dry air is fed into the first adsorption reactor 18, desorption reaction is carried out on the 13x zeolite in the first adsorption reactor 18, the 13x zeolite is regenerated, and after the desorption of the 13x zeolite in the first adsorption reactor 18 is completed, the first air inlet valve 11 and the air compressor 6 are closed, and the hot dry air supply is stopped.
When the adsorption of the 13x zeolite in the second adsorption reactor 19 is saturated, the second water inlet valve 22 is closed, the second air inlet valve 12 and the second water dividing valve 25 are opened to desorb the 13x zeolite in the second adsorption reactor 19, the third water inlet valve 23 of the third adsorption reactor 20 is opened, the adsorption reaction is performed by the third adsorption reactor 20 to generate high-temperature steam, when the adsorption of the 13x zeolite in the third adsorption reactor 20 is saturated, the third water inlet valve 23 is closed, the third air inlet valve 13 and the third water dividing valve 26 are opened, the desorption is performed on the 13x zeolite in the third adsorption reactor 20, the first water inlet valve 21 is opened again, the water inlet adsorption reaction of the first adsorption reactor 18 is utilized, and the circulation is sequentially performed to generate the high-temperature steam, so that the continuous generation of the high-temperature steam is ensured, and the high-temperature steam is continuously provided for the steam using equipment 47.
It should be noted that the above-mentioned embodiments are illustrative rather than limiting, and that those skilled in the art can substitute equivalents or other modifications made according to the prior art without departing from the spirit and scope of the present utility model, and are intended to be included in the scope of the claims.
Claims (7)
1. An adsorption type steam generation system for generating steam by utilizing waste heat of a central air conditioner is characterized in that: the device comprises a waste heat air inlet pipeline (1), a heat exchanger (3), an air inlet pipeline (4), an air compressor (6), a dryer (7), an air heater (8), a hot dry air main pipe (10), a constant temperature water tank (31), a pump (30), a water heater (28), a water inlet main pipe (27), an adsorption reactor set, a high temperature steam main pipe (17) and steam using equipment (47), wherein the waste heat air inlet pipeline (1) is used for communicating a waste heat air outlet of a central air conditioner with waste heat air inlet of the heat exchanger (3), a waste heat air outlet of the heat exchanger (3) is emptied, the air inlet pipeline (4) is communicated with the atmosphere and an air inlet of the heat exchanger (3), an air outlet of the heat exchanger (3) is communicated with the air inlet of the air compressor (6) through the pipeline, an air outlet of the air compressor (6) is communicated with the air inlet of the dryer (7), an air outlet of the air heater (7) is communicated with the air inlet of the air heater (8) through the hot dry air main pipe (17), an air outlet of the adsorption reactor set is communicated with the air inlet of the water heater set through the hot dry air main pipe (10), a water inlet of the water heater (28) is communicated with the water outlet of the water heater (28) through the water inlet of the water heater (28), the water inlet of pump (30) intercommunication constant temperature water tank (31) delivery port, the outlet intercommunication constant temperature water tank (31) of adsorption reactor group return water mouth, the gas outlet of adsorption reactor group pass through high temperature steam house steward (17) intercommunication steam and use equipment (47), the adsorption reactor group include a plurality of adsorption reactors of parallelly connected arrangement, the adsorption reactor in be provided with the adsorbed layer, the adsorbed layer be 13x zeolite adsorbed layer.
2. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 1, wherein: the adsorption reactor group comprises three adsorption reactors, namely a first adsorption reactor (18), a second adsorption reactor (19) and a third adsorption reactor (20), wherein the first adsorption reactor (18) is communicated with a hot dry air main pipe (10) through a first air inlet pipeline (35), a first air inlet valve (11) is arranged on the first air inlet pipeline (35), the first adsorption reactor (18) is communicated with a high-temperature steam main pipe (17) through a first steam pipeline (38), a first steam valve (14) is arranged on the first steam pipeline (38), the first adsorption reactor (18) is communicated with a water inlet main pipe (27) through a first water inlet pipeline (41), the first air inlet pipeline (35) is provided with a first water inlet valve (21), the first adsorption reactor (18) is communicated with a constant-temperature water tank (31) through a first water outlet pipe (44), the second adsorption reactor (19) is communicated with a second air inlet valve (36) through a second water inlet pipeline (36), the second adsorption reactor (19) is communicated with a second hot dry air main pipe (17), the utility model provides a second steam valve (15) are provided with on second steam line (39), second adsorption reactor (19) through second intake pipe (42) intercommunication intake manifold (27), second intake pipe (36) on be provided with second water intaking valve (22), second adsorption reactor (19) through second drain pipe (45) intercommunication constant temperature water tank (31), second drain pipe (45) on be provided with second water separator (25), third adsorption reactor (20) through third intake pipe (37) intercommunication hot dry air house steward (10), be provided with third admission valve (13) on third intake pipe (37), third adsorption reactor (20) through third steam line (40) intercommunication high temperature steam house steward (17), third steam line (40) on be provided with third valve (16), third adsorption reactor (20) through third intake pipe (43) intercommunication intake water tank (27), third intake pipe (37) on be provided with third intake pipe (37) intercommunication water separator (26) through third intake pipe (23), third water separator (46) on the drain pipe (37) is provided with third water separator (46).
3. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 2, wherein: the constant temperature water tank (31) communicate the water source through moisturizing pipeline (32), moisturizing pipeline (32) be the heat preservation pipeline, be provided with moisturizing valve (33) on moisturizing pipeline (32).
4. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 1, wherein: the waste heat air inlet pipeline (1) is provided with a waste heat air inlet valve (2).
5. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 1, wherein: an air filter (34) and an air inlet valve (5) are arranged on the air inlet pipeline (4).
6. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 1, wherein: an air inlet main valve (9) is arranged on the hot dry air main pipe (10).
7. The adsorption type steam generating system for generating steam by using waste heat of central air conditioner according to claim 1, wherein: the water inlet of the water heater (28) is communicated with the water outlet of the pump (30), and a water inlet main valve (29) is arranged on the pipeline.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202320826837.6U CN220287387U (en) | 2023-04-14 | 2023-04-14 | Adsorption type steam generation system for generating steam by utilizing residual heat of central air conditioner |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202320826837.6U CN220287387U (en) | 2023-04-14 | 2023-04-14 | Adsorption type steam generation system for generating steam by utilizing residual heat of central air conditioner |
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| CN220287387U true CN220287387U (en) | 2024-01-02 |
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