CN213747089U - Novel heat exchange dehumidification structure - Google Patents

Novel heat exchange dehumidification structure Download PDF

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CN213747089U
CN213747089U CN202021532530.8U CN202021532530U CN213747089U CN 213747089 U CN213747089 U CN 213747089U CN 202021532530 U CN202021532530 U CN 202021532530U CN 213747089 U CN213747089 U CN 213747089U
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air
temperature
type
humidity
dehumidification structure
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魏鸿彬
朱会君
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Do You Have Industrial Chongqing Co ltd
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Do You Have Industrial Chongqing Co ltd
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Abstract

The utility model relates to a heating and ventilation air conditioner field especially relates to novel heat transfer dehumidification structure. The air inlet can realize dehumidification and temperature rise of the air outlet by utilizing the self-temperature-return principle, and can easily realize respective control of temperature and humidity. 1. The single cooling source is utilized to form a heating structure and a heating method, other energy reheating sections are not needed, the total temperature reduction temperature difference of the dehumidification part is close to zero, and the energy consumption is greatly reduced; 2. the structure is simple, 2 meter cooling sections are arranged, the temperature and the humidity can be controlled separately, and the failure rate is low. Protection the four structures and methods listed below illustrate the principles with reference to several structures listed below: type a configuration-plate; type B configuration-liquid circulation; c-type configuration-wheel; d-type structure-heat pipe; the temperature and humidity control is realized by using a self-heating principle without reheating energy consumption, and the temperature and humidity control is the protection content.

Description

Novel heat exchange dehumidification structure
Technical Field
The utility model relates to a heating and ventilation air conditioner field especially relates to novel heat transfer dehumidification structure.
Background
The gradual popularization of modern thermal comfort theory and the influence of humidity in high-temperature and high-humidity areas on comfort and health, people realize that the humidity regulation is important to the improvement of comfort, no dehumidification or fresh air exists, a whole-house comfortable humidity regulation system can quickly enter the family of common people,
a new coronavirus COVID-19 in 2020 is abused globally, and from experts to the public field, the defects of energy conservation and dehumidification are overcome by mixed wind for an all-air system; the traditional dehumidification scheme is easy to mix wind and spread virus and bacteria, and is not easy to realize fresh wind dehumidification and cooling through deep energy-saving dehumidification. If a traditional dehumidification scheme is used for realizing a full fresh air conditioner, an additional heating section is needed to consume a large amount of energy, so that a full air system (VAV or CAV) is caused, the energy consumption is reduced by mixing air generally, and the required effect can be achieved through multiple air mixing cycles, so that the full fresh air conditioner system which is in urgent need of temperature and humidity control and can deeply dehumidify once is introduced into mass consumers;
another disadvantage of the traditional dehumidifier is that the outlet air temperature fluctuates when the dehumidification is started; if the dehumidification amount needs to be increased, the temperature of the evaporation section needs to be reduced, but the air outlet temperature can also be influenced, namely the coupling effect is realized, and the linkage effect is not suitable in the field of comfortable air conditioners.
Therefore, it is necessary to develop an energy-saving, efficient and decoupling dehumidification cooling system.
The basic principle of the conventional dehumidifier commonly used in the market at present is as follows:
stage 1: cooling, wherein a cold source is provided through an evaporator or other modes, and the process cools air to ensure that the air entering is reduced to be below a dew point and the relative humidity of the air exceeds 100 percent, so that condensed water is generated to dehumidify;
and (2) stage: the temperature is increased, because the temperature of the air passing through the evaporator is very low, the process needs to provide a heat source, namely a condenser to increase the temperature, so that the air is heated, the temperature is higher than the dew point, the transmission pipeline is kept dry, the air supply temperature is uncontrollable, and people feel uncomfortable;
the traditional dehumidifier has the following defects:
disadvantage 1: energy consumption, the air is heated by external heat sources such as a condenser and the like in the traditional dehumidifier principle during the heating in the stage 2, and huge energy consumption is brought in the process.
Under the condition of high outdoor humidity, if one-time deep dehumidification is needed to reach the comfortable humidity range of a human body, the temperature of an evaporation section needs to be reduced to be very low, the temperature needs to be reduced to about 13 ℃ once, and then the temperature needs to be increased to 21-26 ℃ in order to keep the air supply temperature to make the human body comfortable, so that the energy consumption is increased; therefore, in order to avoid too high heating energy consumption, most dehumidifiers use a dehumidification method of mixing air for multiple cycles and heating as little as possible.
And (2) disadvantage: the health safety risk caused by mixed air is caused because the traditional dehumidifier carries out annular mixed air dehumidification for many times, which causes virus or bacteria cross infection, and the mixed air for the whole air system solves the defects of energy saving and dehumidification, and breaks against the safety and health of the whole air conditioning.
Disadvantage 3: the independent control of temperature and humidity is not easy to realize, most air conditioning systems are temperature and humidity coupled systems, if temperature and humidity are required to be controlled separately, if an air system in a radiation air conditioning system which is in popularity is required to be decoupled, the existing method mostly adopts a double-cooling-source form of fluorine refrigerant and water refrigerant, but the complexity, the control complexity, the structural complexity and the pipeline installation difficulty of the system are increased;
in a traditional air system, a four-pipe double water source (variable-temperature cold water and variable-temperature hot water) mode is adopted, but due to energy consumption reasons, the designed system has the problems of small dehumidification amount and difficulty in deep dehumidification, energy consumption is increased due to hot water temperature return, and extra energy consumption is also solved by circulating mixed air;
description of the working principle of the traditional dehumidifier:
the working principle is as follows: (primary dehumidification);
if one wants to use this conventional structure for dehumidification, the following conditions are applied:
the assumption is that when the temperature of high-temperature air at 40 ℃ in outdoor summer passes through an outdoor fresh air inlet X4 and then passes through an air filter screen X1 and an evaporator X6, the temperature of the air is reduced to 14 ℃, a large amount of condensed water is generated in the process so as to play a role in dehumidification, the temperature difference power consumption is 26 ℃ during the working principle, and the air after temperature reduction and dehumidification is easy to condense in a pipeline and an air inlet if being directly conveyed due to too high humidity so as to breed bacteria; to avoid this, the air is warmed and the relative humidity is reduced, so the condenser X7 is added, but this process increases the subsequent power consumption.
SUMMERY OF THE UTILITY MODEL
The purpose of the utility model is that: in order to provide a novel heat exchange and dehumidification structure and a method with better effect, the specific purpose is to see a plurality of substantial technical effects of the specific implementation part.
In order to achieve the purpose, the utility model adopts the following technical proposal:
novel heat transfer dehumidification structure, its characterized in that is as follows any one:
the plate type heat exchange dehumidification structure comprises a shell, the shell comprises a sensible heat plate type heat exchanger A4 arranged in the middle, the sensible heat plate type heat exchanger A4 is positioned in the shell, the shell comprises a plate type air inlet A7 and a plate type air outlet A8, and an air return section is arranged below the shell; the air return section is internally provided with a surface air cooler A2 with independent humidity regulation; the plate-type air outlet A8 is provided with an independent temperature adjusting surface air cooler A9;
the liquid circulation type heat exchange and dehumidification structure is characterized by comprising a shell, wherein the left side of the shell comprises a first air inlet B4, and the right side of the shell is provided with a first air outlet B9; a liquid circulation type combined pre-cooling surface cooler B6, a water coil pipe humidity independent adjusting surface cooler I B2, a liquid circulation type combined temperature returning surface cooler B7 and a water coil pipe temperature independent adjusting surface cooler I B10 are arranged in the shell from air inlet to air outlet;
the rotating wheel type heat exchange dehumidification structure is characterized by comprising a shell, wherein a separation baffle is arranged in the middle of the upper portion of the shell, a rotating wheel type air inlet C1 is formed in the left side of the separation baffle, a rotating wheel type air outlet C11 is formed in the right side of the separation baffle, a sensible heat rotating wheel C3 is arranged in the middle of the shell, and a water coil pipe humidity independent adjusting surface cooler II C4 is arranged below the sensible heat rotating wheel C3;
modular heat pipe formula heat transfer dehumidification structure, its characterized in that, modular heat pipe formula heat transfer dehumidification structure contains the casing, and the casing below contains two D4 of air intake, and the top contains two D9 of air outlet, from up distributing in proper order down modular heat pipe formula heat exchanger evaporation zone D5, three D6 of water coil pipe humidity independent control surface cooler, heat exchanger condenser D7, three D11 of water coil pipe temperature independent control surface cooler.
The utility model discloses a further technical scheme lies in, and plate-type air filter A6 is installed to plate-type air intake A7 in the first scheme.
The utility model has the further technical proposal that the first proposal also comprises an air source heat pump A1, the air source heat pump A1 is connected with a surface air cooler A2 with independent humidity regulation through a water mixing or flow regulating device A11; the air source heat pump A1 is connected with the independent temperature regulation surface cooler A9 through a water mixing or flow regulation device A10.
The utility model discloses a further technical scheme lies in, and air intake B4 in the second kind of scheme has arranged air screen two B5.
The utility model discloses a further technical scheme lies in, and power fan two B8 is arranged to air outlet B9 avris in the second scheme.
The utility model has the further technical proposal that the third proposal also comprises an air source heat pump three C7, the air source heat pump three C7 is connected with a water coil pipe humidity independent adjusting surface cooler two C4 through water mixing or a flow adjusting device three C5; the air source heat pump III C7 is connected with a temperature independent adjusting surface cooler C9 for the combined heat pipe type heat exchange dehumidification structure through a water mixing or flow adjusting device seven C8.
The utility model has the further technical proposal that the side of the second D4 air inlet in the fourth proposal contains a four D3 air filter screen; and a power fan D8 is arranged below the air outlet II D9.
The utility model has the further technical proposal that the fourth proposal also comprises four air source heat pumps D1, the four air source heat pumps D1 are connected with a combined water coil pipe humidity independent adjusting surface cooler three D6 through five D13 of water mixing or flow adjusting devices; the air source heat pump four D1 is connected with the water coil pipe through a water mixing or flow regulating device six D10 to independently regulate the temperature of the surface cooler three D11.
The novel heat exchange dehumidification method is characterized in that the novel heat exchange dehumidification structure is utilized, and comprises the following steps;
description of type a structure-plate working principle:
the working principle is as follows: when outdoor high-temperature and high-humidity air in summer passes through the plate-type air inlet A7, the plate-type air filter screen A6 and the plate-type fan A5, the temperature is reduced to relatively low temperature through heat exchange when the air passes through the sensible heat plate-type heat exchanger A4, condensate water is possibly generated at the time, then the air is cooled to be lower than a dew point through the humidity independent adjusting surface air cooler A2 at the time, the relative humidity reaches more than 100%, the air temperature is relatively low, a large amount of condensate water is generated in the process, so that a dehumidification function is achieved, the temperature of the air is controlled through controlling the flow rate of a condensing medium in the humidity independent adjusting surface air cooler by a water mixing or flow adjusting device II A11, the lower the air temperature is, the higher the dehumidification amount is, and the independent control of the humidity is achieved; when the air with the humidity being dehumidified and reaching the comfortable humidity of the human body passes through the sensible heat plate type heat exchanger A4 again, the temperature is gradually increased to be relatively high, then the temperature of the surface air cooler A9 is adjusted independently through the mixed water or flow adjusting device A10, finally the temperature of the air is adjusted to reach the comfortable temperature of the human body of 26 ℃, meanwhile, the temperature can raise the dew point temperature, air is let to enter an air supply pipeline through the plate type air outlet A8, condensation in the pipeline can not be caused, and therefore the independent control of the temperature and the humidity and the energy saving effect are achieved;
description of the type B structure-liquid circulation working principle:
the working principle is as follows: high-temperature and high-humidity air in outdoor summer passes through an air inlet I B4, an air filter screen II B5 and a liquid circulation type combined precooling surface cooler B6, the temperature is reduced in an exchange manner, part of condensed water is possibly generated in the process, the function of pre-dehumidification is achieved, then the air in the surface cooler I B2 is cooled secondarily until the dew point relative humidity reaches 100% and the air temperature reaches a relatively low temperature, the flow rate of a condensing medium in the surface cooler I B2 is independently adjusted by a liquid circulation type water mixing or flow adjusting device B12 or the temperature of the water is changed to control the temperature of the air, when the low-temperature air passes through a liquid circulation type combined type return temperature surface cooler B7, the liquid in the liquid circulation type combined return temperature surface cooler B7 is cooled and then circulated into the liquid circulation type combined type precooling surface cooler B6, and the liquid circulation type combined type return surface cooler B6 and the liquid circulation type return surface cooler B7 are alternately reciprocated and circulated in a reciprocating manner The temperature of the air reaches the relative high temperature, when the humidity is dehumidified, the air reaching the comfortable humidity of the human body is pushed forward again, and passes through the water coil pipe temperature independent adjusting surface cooler I B10, the air temperature is adjusted to be 26 ℃ of the comfortable temperature of the human body, and then the air finally enters the room through the air outlet I B9 by the power provided by the power fan II B8, and negative temperature rise and energy consumption are avoided during the working principle, so that the independent control of the temperature and the humidity and the energy saving effect are achieved;
the C-type structure-wheel principle describes the working principle: when outdoor high-temperature and high-humidity air in summer passes through the runner type air inlet C1, passes through the air filter screen three C2 and passes through the left side of the sensible heat runner C3, the temperature is exchanged and reduced to relatively low temperature at the moment, partial condensed water is possibly generated, the air temperature at the moment of the surface cooler two C4 is subjected to secondary temperature reduction through independent adjustment of the humidity of the water coil pipe and is lower than the dew point, the relative humidity reaches more than 100%, the air temperature is relatively low, a large amount of condensed water is generated in the process, so that the dehumidification function is achieved, the flow rate of a condensing medium in the surface cooler two C4 is independently adjusted through the water mixing or flow adjusting device three C5, the temperature of the air is controlled, the dehumidification amount is higher when the temperature of the cooled air is lower, and the independent control of the humidity is achieved; when the humidity is dehumidified, the air reaching the comfortable humidity of the human body moves upwards again, the temperature gradually rises to a relatively high temperature through the right side C3 of the sensible heat runner, then the temperature of the independent temperature regulation surface air cooler C9 for the combined heat pipe type heat exchange dehumidification structure is regulated through the mixed water or flow regulation device seven C8, finally the temperature of the air is regulated to the comfortable temperature of the human body of 26 ℃, the air runs through the power provided by the power fan C10 of the runner type, and finally the air enters the room through the air outlet C11 of the runner type; during the working principle, no extra heat source is used for heating, so that the independent control of temperature and humidity and the energy-saving effect are achieved, and it needs to be supplemented to explain that in the structure, the temperature independent adjusting surface cooler C9 for the combined heat pipe type heat exchange dehumidification structure can be omitted, the air outlet temperature can be adjusted by changing the rotating speed of the sensible heat runner, and the independent control of the temperature is realized;
d type combination formula heat pipe formula structural principle:
the working principle is as follows: outdoor high-temperature and high-humidity air passes through the air inlet II D4, passes through the air filter screen IV D3, passes through the combined heat pipe type heat exchanger evaporation section D5 at the moment, is subjected to temperature exchange reduction, then passes through the water coil humidity independent adjustment surface air cooler III D6 at the moment, is subjected to secondary temperature reduction which is lower than the dew point relative humidity by more than 100 percent, and reaches the relative low temperature, a large amount of condensed water is generated in the process, so that the dehumidification function is achieved, the temperature of the air is controlled by controlling the flow rate of a condensing medium in the surface air cooler III D6 through water coil humidity independent adjustment by a water mixing or flow adjusting device, when the low-temperature air passes through the heat pipe type combined heat exchanger condenser D7, the liquid in the heat pipe type combined heat exchanger condenser D7 is cooled and then circulated into the combined heat pipe type pre-cooling surface air cooler D5, and the combined heat pipe type pre-cooling surface air cooler D7 and the combined heat pipe type pre-cooling surface air cooler D5 alternately and repeatedly circulate to achieve the temperature transfer exchange, when the air with the humidity reaching the comfortable humidity of the human body is dehumidified and then pushed forward to pass through the water coil pipe temperature independent adjusting surface air cooler again, the air temperature is adjusted to be at the comfortable temperature of the human body of 26 ℃, and then the air finally enters the room through the air outlet II D9 by the power provided by the power fan IV 8; during the working principle, negative temperature rise and energy consumption are avoided, so that the independent control of the temperature and the humidity and the energy-saving effect are achieved.
Adopt above technical scheme the utility model discloses, for prior art have following beneficial effect: 1. the single cooling source is utilized to form a heating structure and a heating method, other energy reheating sections are not needed, the total temperature reduction temperature difference of the dehumidification part is close to zero, and the energy consumption is greatly reduced; 2. the structure is simple, 2 meter cooling sections are arranged, the temperature and the humidity can be controlled separately, and the failure rate is low.
The air conditioning system has a simple structure, realizes all functions by a full cooling surface cooling function section, does not need an energy consumption means of external negative temperature rise, is a system for realizing natural temperature and humidity control and decoupling by a brand new principle, a brand new method and a brand new structure, and realizes one-time brand new air dehumidification and temperature regulation without other temperature rise energy consumption; such a structure and method has the advantages of:
the method has the advantages that: the air conditioner can deeply dehumidify once without repeated reciprocating internal circulation air mixing, can reach the required temperature and humidity by once passing, and is easy to realize a full fresh air conditioner;
2. the structure and the method have the advantages of natural temperature and humidity control, extremely simple control system, capability of realizing better experience by matching with an all-air or all-fresh-air system, and realization of A-level or A + heat comfort level in European standard EN 12521 and international standard ISO 7730 by matching with a radiation air-conditioning system or using an all-fresh-air conditioner;
3. the single cold source or double cold sources can simultaneously realize primary cooling and primary dehumidification, a reheating section is not needed, and the energy-consumption heating principle is not needed, and the device is also a bright spot and a patent gravity center protection spot which are described in detail later;
4. a built-in compressor is not needed, the structure is simple, the number of fault points is small, and the maintenance is almost free;
5. the control principle and the control algorithm are simple, the control logic and the control algorithm are simple, and the deep fusion with the VAV, the radiation air conditioner and the full fresh air conditioner is convenient; the structure is simple, stable and reliable;
6. the energy consumption of the heating section is avoided, and the method enables the dehumidification cooling equipment to save energy.
7. The device is ultra-silent and has no compressor or expansion valve).
Drawings
For further explanation of the present invention, reference is made to the following description taken in conjunction with the accompanying drawings:
FIG. 1 is a schematic diagram of a prior art structure of the utility model;
FIG. 2 is a schematic structural view of a first embodiment of the present invention;
FIG. 3 is a schematic structural view of a second embodiment of the present invention;
FIG. 4 is a schematic structural view of a third embodiment of the present invention;
FIG. 5 is a schematic structural view of a fourth embodiment of the present invention;
wherein: a1 air source heat pump I; a2 humidity independent regulation surface air cooler; a3 board-type heat preservation shell; a4 sensible plate heat exchanger; a5 plate fan; a6 plate air screen; a7 plate type air inlet; a8 plate type air outlet; a9 independently adjusting the temperature of the surface cooler; a10 water mixing or flow regulating device I; a11 mixing water or flow regulating device two.
B1 liquid circulation type air source heat pump; b2 independently adjusting the humidity of the water coil pipe to a first surface cooler; b3 liquid circulation type heat preservation shell; b4 air inlet I; b5 air strainer II; b6 liquid circulating combined precooling surface cooler; b7 liquid circulation type combined type temperature return surface air cooler; b8 power fan II; b9 air outlet I; b10 water coil temperature independent regulation surface cooler I; b11 liquid circulation type frequency conversion low power consumption small water pump G; b12 liquid circulating water mixing or flow regulating device.
C1 rotary wheel type air inlet; c2 air strainer III; c3 sensible heat runner; c4 water coil humidity independent regulation surface air cooler II; c5 water mixing or flow regulating device iii; c6 runner type heat preservation shell; c7 air-source heat pump III; c8 water mixing or flow regulating device seven; c9 is used for the independent temperature regulation surface air cooler of the combined heat pipe type heat exchange dehumidification structure; c10 rotary wheel type power fan; c11 wheel type air outlet.
D1 air-source heat pump four; d2 combined heat pipe type heat preservation shell; d3 air strainer four; d4 air inlet II; d5 combined heat pipe type precooling surface air cooler; d6 water coil humidity independent regulation surface air cooler III; d7 condenser of heat pipe type combined heat exchanger; d8 dynamic fan four; d9 air outlet II; d10 water mixing or flow adjusting device six; d11 water coil temperature independent regulation surface air cooler III; d12 combined heat pipe type high-efficiency heat pipe; d13 mixing water or flow regulating device v.
An X1 air screen; x2 heat preservation shell; an X3 indoor return air inlet; an X4 outdoor fresh air inlet; an X5 compressor; an X6 evaporator; an X7 condenser; an X8 powered fan; and an X9 air outlet.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings and embodiments, which are to be understood as illustrative only and not limiting the scope of the invention. In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", "top", "bottom", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, unless expressly stated or limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, as they may be fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
The patent provides a plurality of parallel schemes, and different expressions belong to an improved scheme based on a basic scheme or a parallel scheme. Each solution has its own unique features. Furthermore, the technical features mentioned in the different embodiments of the invention described below can be combined with each other as long as they do not conflict with each other.
Description of type a structure-plate working principle:
the working principle is as follows: when outdoor high-temperature and high-humidity air in summer passes through the plate-type air inlet A7, the plate-type air filter screen A6 and the plate-type fan A5, the temperature is reduced to relatively low temperature through heat exchange when the air passes through the sensible heat plate-type heat exchanger A4, condensate water is possibly generated at the time, then the air is cooled to be lower than a dew point through the humidity independent adjusting surface air cooler A2 at the time, the relative humidity reaches more than 100%, the air temperature is relatively low, a large amount of condensate water is generated in the process, so that a dehumidification function is achieved, the temperature of the air is controlled through controlling the flow rate of a condensing medium in the humidity independent adjusting surface air cooler by a water mixing or flow adjusting device II A11, the lower the air temperature is, the higher the dehumidification amount is, and the independent control of the humidity is achieved; when the air with the humidity being dehumidified and reaching the comfortable humidity of the human body passes through the sensible heat plate type heat exchanger A4 again, the temperature is gradually increased to be relatively high, then the temperature of the surface air cooler A9 is adjusted independently through the mixed water or flow adjusting device A10, finally the temperature of the air is adjusted to reach the comfortable temperature of the human body of 26 ℃, meanwhile, the temperature can raise the dew point temperature, air is let to enter an air supply pipeline through the plate type air outlet A8, condensation in the pipeline can not be caused, and therefore the independent control of the temperature and the humidity and the energy saving effect are achieved;
description of the type B structure-liquid circulation working principle:
the working principle is as follows: high-temperature and high-humidity air in outdoor summer passes through an air inlet I B4, an air filter screen II B5 and a liquid circulation type combined precooling surface cooler B6, the temperature is reduced in an exchange manner, part of condensed water is possibly generated in the process, the function of pre-dehumidification is achieved, then the air in the surface cooler I B2 is cooled secondarily until the dew point relative humidity reaches 100% and the air temperature reaches a relatively low temperature, the flow rate of a condensing medium in the surface cooler I B2 is independently adjusted by a liquid circulation type water mixing or flow adjusting device B12 or the temperature of the water is changed to control the temperature of the air, when the low-temperature air passes through a liquid circulation type combined type return temperature surface cooler B7, the liquid in the liquid circulation type combined return temperature surface cooler B7 is cooled and then circulated into the liquid circulation type combined type precooling surface cooler B6, and the liquid circulation type combined type return surface cooler B6 and the liquid circulation type return surface cooler B7 are alternately reciprocated and circulated in a reciprocating manner The temperature of the air reaches the relative high temperature, when the humidity is dehumidified, the air reaching the comfortable humidity of the human body is pushed forward again, and passes through the water coil pipe temperature independent adjusting surface cooler I B10, the air temperature is adjusted to be 26 ℃ of the comfortable temperature of the human body, and then the air finally enters the room through the air outlet I B9 by the power provided by the power fan II B8, and negative temperature rise and energy consumption are avoided during the working principle, so that the independent control of the temperature and the humidity and the energy saving effect are achieved;
c-type structure-wheel principle description
The working principle is as follows: when outdoor high-temperature and high-humidity air in summer passes through the runner type air inlet C1, passes through the air filter screen three C2 and passes through the left side of the sensible heat runner C3, the temperature is exchanged and reduced to relatively low temperature at the moment, partial condensed water is possibly generated, the air temperature at the moment of the surface cooler two C4 is subjected to secondary temperature reduction through independent adjustment of the humidity of the water coil pipe and is lower than the dew point, the relative humidity reaches more than 100%, the air temperature is relatively low, a large amount of condensed water is generated in the process, so that the dehumidification function is achieved, the flow rate of a condensing medium in the surface cooler two C4 is independently adjusted through the water mixing or flow adjusting device three C5, the temperature of the air is controlled, the dehumidification amount is higher when the temperature of the cooled air is lower, and the independent control of the humidity is achieved; when the humidity is dehumidified, the air reaching the comfortable humidity of the human body moves upwards again, the temperature gradually rises to a relatively high temperature through the right side C3 of the sensible heat runner, then the temperature of the independent temperature regulation surface air cooler C9 for the combined heat pipe type heat exchange dehumidification structure is regulated through the mixed water or flow regulation device seven C8, finally the temperature of the air is regulated to the comfortable temperature of the human body of 26 ℃, the air runs through the power provided by the power fan C10 of the runner type, and finally the air enters the room through the air outlet C11 of the runner type; during the working principle, no extra heat source is used for heating, so that the independent control of temperature and humidity and the energy-saving effect are achieved, and it needs to be supplemented to explain that in the structure, the temperature independent adjusting surface cooler C9 for the combined heat pipe type heat exchange dehumidification structure can be omitted, the air outlet temperature can be adjusted by changing the rotating speed of the sensible heat runner, and the independent control of the temperature is realized;
d type combination formula heat pipe formula structural principle:
the working principle is as follows: outdoor high-temperature and high-humidity air passes through the air inlet II D4, passes through the air filter screen IV D3, passes through the combined heat pipe type heat exchanger evaporation section D5 at the moment, is subjected to temperature exchange reduction, then passes through the water coil humidity independent adjustment surface air cooler III D6 at the moment, is subjected to secondary temperature reduction which is lower than the dew point relative humidity by more than 100 percent, and reaches the relative low temperature, a large amount of condensed water is generated in the process, so that the dehumidification function is achieved, the temperature of the air is controlled by controlling the flow rate of a condensing medium in the surface air cooler III D6 through water coil humidity independent adjustment by a water mixing or flow adjusting device, when the low-temperature air passes through the heat pipe type combined heat exchanger condenser D7, the liquid in the heat pipe type combined heat exchanger condenser D7 is cooled and then circulated into the combined heat pipe type pre-cooling surface air cooler D5, and the combined heat pipe type pre-cooling surface air cooler D7 and the combined heat pipe type pre-cooling surface air cooler D5 alternately and repeatedly circulate to achieve the temperature transfer exchange, when the air with the humidity reaching the comfortable humidity of the human body is dehumidified and then pushed forward to pass through the water coil pipe temperature independent adjusting surface air cooler again, the air temperature is adjusted to be at the comfortable temperature of the human body of 26 ℃, and then the air finally enters the room through the air outlet II D9 by the power provided by the power fan IV 8; during the working principle, negative temperature rise and energy consumption are avoided, so that the independent control of the temperature and the humidity and the energy-saving effect are achieved.
The utility model relates to a warm logical air conditioner field utilizes from the temperature return principle, realizes the dehumidification and the intensification of air inlet to the air-out to can easily realize controlling respectively of temperature and humidity. 1. The single cooling source is utilized to form a heating structure and a heating method, other energy reheating sections are not needed, the total temperature reduction temperature difference of the dehumidification part is close to zero, and the energy consumption is greatly reduced; 2. the structure is simple, 2 meter cooling sections are arranged, the temperature and the humidity can be controlled separately, and the failure rate is low. Protection the four structures and methods listed below illustrate the principles with reference to several structures listed below: type a configuration-plate; type B configuration-liquid circulation; c-type configuration-wheel; d-type structure-heat pipe; the protection content is realized by only using a self-heating principle without reheating energy consumption and realizing temperature and humidity control.
The foregoing shows and describes the general principles, essential features, and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are intended to illustrate the principles of the invention, and that various changes and modifications may be made without departing from the spirit and scope of the invention, all of which are intended to be covered by the appended claims.

Claims (8)

1. Novel heat transfer dehumidification structure, its characterized in that is as follows any one:
the first scheme is as follows: plate-type heat transfer dehumidification structure: the plate type heat exchange dehumidification structure comprises a shell, the shell comprises a sensible heat plate type heat exchanger (A4) arranged in the middle, the sensible heat plate type heat exchanger (A4) is positioned inside the shell, the shell comprises a plate type air inlet (A7) and a plate type air outlet (A8), and the lower part of the shell comprises an air return section; a humidity independent adjusting surface cooler (A2) is arranged in the air return section; the plate-type air outlet (A8) is provided with an independent temperature adjusting surface cooler (A9);
the second scheme is as follows: liquid circulating heat transfer dehumidification structure: the liquid circulation type heat exchange and dehumidification structure comprises a shell, wherein the left side of the shell comprises a first air inlet (B4), and the right side of the shell is provided with a first air outlet (B9); a liquid circulation type combined precooling surface cooler (B6), a water coil pipe humidity independent adjusting surface cooler I (B2), a liquid circulation type combined temperature returning surface cooler (B7) and a water coil pipe temperature independent adjusting surface cooler I (B10) are arranged in the shell from air inlet to air outlet;
in the third scheme: rotating wheel formula heat transfer dehumidification structure: the rotary wheel type heat exchange dehumidification structure comprises a shell, wherein a separation baffle is arranged in the middle of the upper portion of the shell, a rotary wheel type air inlet (C1) is formed in the left side of the separation baffle, a rotary wheel type air outlet (C11) is formed in the right side of the separation baffle, a sensible heat rotary wheel (C3) is arranged in the middle of the shell, and a water coil pipe humidity independent adjusting surface cooler II (C4) is arranged below the sensible heat rotary wheel (C3);
a fourth scheme: combined heat pipe type heat exchange dehumidification structure: modular heat pipe formula heat transfer dehumidification structure contains the casing, and the casing below contains air intake two (D4), and the top contains air outlet two (D9), from up distributing in proper order down modular heat pipe formula heat exchanger evaporation zone (D5), water coil humidity independent regulation surface cooler three (D6), heat exchanger condenser (D7), water coil temperature independent regulation surface cooler three (D11).
2. A novel heat exchange dehumidification structure according to claim 1, wherein in the first solution the plate air intake (a7) is equipped with a plate air screen (a 6).
3. The novel heat exchange and dehumidification structure as claimed in claim 1, wherein the first solution further comprises a first air source heat pump (a1), the first air source heat pump (a1) is connected to the humidity independent regulation surface air cooler (a2) through a second water mixing or flow regulation device (a 11); the air source heat pump I (A1) is connected with the independent temperature regulation surface cooler (A9) through the water mixing or flow regulation device I (A10).
4. The novel heat exchange dehumidification structure as set forth in claim 1, wherein the first air inlet (B4) in the second scheme is provided with a second air screen (B5).
5. The novel heat exchange and dehumidification structure as claimed in claim 1, wherein a second power fan (B8) is disposed at the side of the first air outlet (B9).
6. The novel heat exchange and dehumidification structure as claimed in claim 1, wherein the third solution further comprises a third air source heat pump (C7), the third air source heat pump (C7) is connected to the second water coil humidity independent adjusting surface air cooler (C4) through a third water mixing or flow adjusting device (C5); and the air source heat pump III (C7) is connected with a temperature independent adjusting surface cooler (C9) for the combined heat pipe type heat exchange dehumidification structure through a water mixing or flow adjusting device VII (C8).
7. The novel heat exchange and dehumidification structure as claimed in claim 1, wherein in the fourth scheme, the side of the second air inlet (D4) comprises a fourth air screen (D3); and a power fan (D8) is arranged below the second air outlet (D9).
8. The novel heat exchange and dehumidification structure as claimed in claim 1, wherein the fourth scheme further comprises an air source heat pump four (D1), the air source heat pump four (D1) is connected to the combined water coil humidity independent regulation surface air cooler three (D6) through a water mixing or flow regulation device five (D13); and the air source heat pump IV (D1) is connected with the water coil pipe temperature independent adjusting surface cooler III (D11) through a water mixing or flow adjusting device VI (D10).
CN202021532530.8U 2020-07-29 2020-07-29 Novel heat exchange dehumidification structure Active CN213747089U (en)

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