CN116404197A - A spray evaporation chamber with functions of humidifier and intercooler and its system - Google Patents

Abstract

The invention provides a spray evaporation chamber and system with the functions of a humidifier and an intercooler, which belong to the technical field of fuel cells. The spray evaporation chamber includes: at least one layer partition, and the layer partition is horizontal in the spray evaporation chamber. Set up, space the spray evaporation chamber up and down into at least two sub-spray evaporation chambers, each sub-spray evaporation chamber is connected, the first layer of sub-spray evaporation chambers has a fluid inlet, and the last layer of sub-spray evaporation chambers has a fluid outlet; The evaporation chamber includes at least two groups of fluid drainage components. The two groups of fluid drainage components are arranged sequentially in the sub-spray evaporation chamber. The two groups of fluid drainage components form an S-shaped fluid channel in the sub-spray evaporation cavity. The fluid passes through the S-shaped fluid channel. S-shaped flow. The invention reduces cost; the internal flow resistance of the spray evaporation chamber system is reduced, and the efficiency of the spray evaporation chamber system is improved; the spray evaporation chamber is only a mechanical structural part, and its stability is higher than that of a film humidifier, and the humidification stability is significantly improved.

Description

A spray evaporation chamber with functions of humidifier and intercooler and its system

technical field

The invention belongs to the technical field of fuel cells, in particular to a spray evaporation chamber with the functions of a humidifier and an intercooler and a system thereof.

Background technique

A proton exchange membrane fuel cell is a chemical reactor in which hydrogen is decomposed into electrons and protons at the anode catalyst layer. Protons are transported across the membrane to the cathode in the form of hydronium ions, react with oxygen to generate water, and exit the flow channel. The transmembrane transport of protons requires the proton exchange membrane to maintain a certain humidity, otherwise it will bring greater proton transfer resistance and affect the power generation efficiency. Therefore, the reaction gas entering the stack is required to have a certain humidity. In addition, in a typical fuel cell system, the air is pressurized and heated in the air compressor, and its temperature is significantly higher than the operating temperature of the fuel cell system. Therefore, an intercooler is needed to cool down the high temperature air.

The related technology discloses a water spray humidification device and control method for a fuel cell system, which includes: a flow channel pipe, an injection part and a swirl part arranged in the flow pipe at intervals along the direction of air flow; the swirl part includes The heating body extending along the air flow direction, and the swirl sheet arranged spirally on the periphery of the heating body in the axial direction; the injection part includes an injection base body with an injection end, the injection base body is provided with an injection flow path, and the injection flow path is connected with a first outlet flow path and the second outlet channel, the outlet structures of the first outlet channel and the second outlet channel are both swirl-shaped and in the opposite direction of rotation, the outlet structure of the second outlet channel is opposite to the direction of rotation of the swirl plate, and the jet flow path A pressure valve structure is arranged inside, and the pressure valve structure is controlled by the pressure of the injection flow path to control the opening and closing of the first outlet flow channel and the second outlet flow channel.

The spray evaporation chamber of the device disclosed in the related art has a simple structure, requires a long evaporation distance, and the residence time of the liquid droplets in the chamber is short and the evaporation is insufficient. Has moving parts, which reduces stability.

Contents of the invention

The invention provides a spray evaporation chamber with the functions of a humidifier and an intercooler, which can solve the problem of the spray evaporation chamber for devices disclosed in the related art. The structure is simple, a long evaporation distance is required, and the residence time of droplets in the chamber is short. , insufficient evaporation. Having moving parts reduces the technical problem of stability.

The technical scheme provided by the present invention is as follows:

In one aspect, a spray evaporation chamber with the functions of a humidifier and an intercooler is provided, and the spray evaporation chamber includes:

At least one layer partition, the layer partition is arranged horizontally in the spray evaporation chamber, and the spray evaporation chamber is spaced up and down into at least two sub-spray evaporation chambers, each sub-spray evaporation chamber is connected, and the first layer of sub-spray There is a fluid inlet on the evaporation chamber, and a fluid outlet on the last layer of spray evaporation chamber;

The sub-spray evaporation chamber includes at least two groups of fluid drainage components, the two groups of fluid drainage components are arranged sequentially in the sub-spray evaporation chamber, and the two groups of fluid drainage components are formed in the sub-spray evaporation chamber An S-shaped fluid channel through which fluid flows in an S-shape.

In an optional embodiment, the two groups of fluid drainage components include a first group of fluid drainage components and a second group of fluid drainage components, and the first group of fluid drainage components and the second group of fluid drainage components are juxtaposed set up;

There is a first fluid channel between the first group of fluid guiding parts, and a second fluid channel between the second group of fluid guiding parts, and between the first group of fluid guiding parts and the second group of fluid guiding parts form a third fluid channel;

The first fluid channel, the second fluid channel and the third fluid channel form the S-shaped fluid channel.

In an optional embodiment, the first group of fluid guiding elements includes a first row of drain fins and a second row of drain fins, and the first row of drain fins and the second row of drain fins Relatively disposed, the first fluid channel is formed between the first row of drain fins and the second row of drain fins.

In an optional embodiment, the first row of drain fins is arranged at a first preset angle in the sub-spray evaporation chamber, and the second row of drain fins is arranged in the sub-spray evaporation chamber It is set at a second preset angle, and the first preset angle is complementary to the second preset angle.

In an optional embodiment, the second row of drain fins further includes flow limiting fins, and the flow restricting fins are located at the connecting head of the second row of drain fins, and are used to restrict the passage of fluid through the lower A fluid channel flows back to the fluid channel, or flows to a fluid channel through the fluid channel.

In an optional embodiment, the flow limiting fins include a connected limiting portion and a draining portion, the limiting portion and the draining portion are connected at a preset angle, and the limiting portion is used for Restrict fluid from flowing back into this fluid channel through the next fluid channel.

In an optional embodiment, the second group of fluid guiding elements includes a third row of drain fins and a fourth row of drain fins, and the third row of drain fins is opposite to the fourth row of drain fins , the third fluid channel is formed between the third row of drain fins and the fourth row of drain fins.

In an optional embodiment, a communication port is provided at the corner of the last group of fluid guiding components in each sub-spray evaporation chamber, and each sub-spray evaporation chamber is connected through the communication port.

In an optional embodiment, a fluid outlet is provided on the spray evaporation chamber of the last layer, and the fluid outlet includes a spray inlet and a gas inlet.

On the other hand, a system of spray evaporation chamber with humidifier and intercooler functions is provided, the system includes any of the spray evaporation chambers with humidifier and intercooler functions described above, and the system also An air compressor is included, and the outlet of the air compressor is connected with the air inlet of the spray evaporation chamber.

The fuel cell system provided by the embodiments of the present invention has at least the following beneficial effects:

The spray evaporation chamber provided by the embodiment of the present invention replaces the expensive perfluorosulfonic acid resin membrane humidifier, which reduces costs; replaces the high-resistance intercooler, reduces the flow resistance in the spray evaporation chamber system, and replaces the high-resistance The intercooler improves the efficiency of the spray evaporation chamber system; cancels the bulky membrane humidifier to increase the volume and mass power density of the fuel cell. The spray evaporation chamber is only a mechanical structural part, and its stability is higher than that of the almost uncontrollable Membrane humidifier, the humidification stability is significantly improved.

Description of drawings

The above and other objects, features and advantages of the present disclosure will become more apparent by describing the exemplary embodiments of the present disclosure in more detail with reference to the accompanying drawings, wherein, in the exemplary embodiments of the present disclosure, the same reference numerals generally represent same parts.

Fig. 1 shows a kind of spray evaporation chamber structure schematic diagram with humidifier and intercooler function;

Fig. 2 shows a kind of schematic diagram of the direction in which the fluid flow in the spray evaporation chamber with the functions of humidifier and intercooler forms a swirl flow;

Fig. 3 shows a schematic diagram of a three-dimensional structure of a spray evaporation chamber with the functions of a humidifier and an intercooler.

Reference signs:

1-layer spacer; 10-fluid drainage assembly; 100-sub-spray evaporation chamber; 110-communication port; 101-first fluid channel; 102-second fluid channel; 103-third fluid channel; 11-first row of drainage fins; 12-second row of drainage fins; 121-limiting fins; 13-third row of drainage fins; 14-fourth row of drainage fins; 104-spray inlet; 105-gas inlet.

Detailed ways

Embodiments of the present disclosure will be described in more detail below with reference to the accompanying drawings. Although embodiments of the present disclosure are shown in the drawings, it should be understood that the present disclosure may be embodied in various forms and should not be limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the disclosure to those skilled in the art.

As used herein, the term "comprise" and its variants mean open inclusion, ie "including but not limited to". The term "or" means "and/or" unless otherwise stated. The term "based on" means "based at least in part on". The terms "one example embodiment" and "one embodiment" mean "at least one example embodiment." The term "another embodiment" means "at least one further embodiment". The terms "first", "second", etc. may refer to different or the same object. Other definitions, both express and implied, may also be included below.

An embodiment of the present invention provides a spray evaporation chamber with the functions of a humidifier and an intercooler, please refer to Figure 1 and Figure 3, the spray evaporation chamber includes:

At least one layer partition 1, the layer partition 1 is horizontally arranged in the spray evaporation chamber, and the spray evaporation chamber is spaced up and down into at least two sub-spray evaporation chambers 100, each sub-spray evaporation chamber 100 is connected, and the first layer of sub-spray evaporation The evaporation chamber 100 has a fluid inlet, and the last layer of spray evaporation chamber 100 has a gas outlet 103;

The sub-spray evaporation chamber 100 includes at least two groups of fluid drainage assemblies 10, the two groups of fluid drainage assemblies 10 are arranged sequentially in the sub-spray evaporation chamber 100, and the two groups of fluid drainage assemblies 10 form an S-shaped fluid channel in the sub-spray evaporation chamber 100 , the fluid flows in an S shape through the S shape fluid channel.

In the spray evaporation chamber provided by the embodiment of the present invention, the high-temperature gas from the air compressor enters the spray evaporation chamber from the fluid inlet on the first layer of the spray evaporation chamber 100, and at the same time mixes the liquid droplets ejected from the high-pressure nozzle, and the gas entrains the liquid droplets First, serpentine flow is performed in the sub-spray evaporation chamber 100 of the lower layer, and a swirl flow is formed between the fluid drainage components 10 at the same time, then enters the sub-spray evaporation chamber 100 of the upper layer for serpentine flow, and finally flows out of the spray evaporation chamber cavity. As it flows, the hot gas is cooled to the fuel cell operating temperature and the humidity is increased to the operating range.

The spray evaporation chamber provided by the embodiment of the present invention will be further explained and described through optional embodiments below.

It should be noted that only the membrane humidifier and intercooler can be replaced at the same time only if it meets the cooling and humidifying requirements of high temperature gas and has low resistance. For cooling and humidification requirements, it is necessary to make the air stay in a limited volume for a long time as much as possible. The spray evaporation chamber provided by the embodiment of the present invention adopts a multi-layer structure, which strengthens the heat exchange of the fluid, increases the length of the gas flow path, and forces the gas to form a swirl flow between the fluid drainage components 10 through the fluid drainage components 10, which greatly increases the The residence time of the gas is shortened, and the heat transfer is enhanced at the same time.

It should be noted that there is at least one layer spacer 1 provided in the embodiment of the present invention. When there is one layer spacer 1, the spray evaporation chamber is divided into two upper and lower sub-spray evaporation chambers 100, and the fluid is sprayed and evaporated through the lower layer. After heat exchange in the chamber 100, it enters the upper layer sub-spray evaporation chamber 100 for further heat exchange and then discharges. A plurality of layer partitions 1 can also be set as required. At this time, the spray evaporation chamber is divided into a plurality of sub-spray evaporation chambers 100, and the gas exchanges heat through the multi-layer sub-spray evaporation chambers 100, which prolongs the heat exchange path of the gas, and in When the volume of the spray evaporation chamber is fixed, the heat exchange area and heat exchange time can be increased by increasing the layer spacer 1, but it is not necessary to increase the volume of the spray evaporation chamber, which reduces the space occupied by the spray evaporation chamber for the fuel cell .

Further, when there is one layer partition 1, the first layer of sub-spray evaporation chamber 100 has a fluid inlet, and the second layer of sub-spray evaporation chamber 100 has a fluid outlet; when there are multiple layer partitions 1, The first layer of sub-spray evaporation chamber 100 has a fluid inlet, and the last layer of sub-spray evaporation chamber 100 has a fluid outlet.

It should be noted that the layer partition plate 1 provided by the embodiment of the present invention is set horizontally, that is, the spray evaporation chamber is evenly divided up and down, so that the water vapor evaporated in the next layer of heat exchange can continue to enter the upper layer to continue the heat exchange, improving the efficiency of the spray evaporation chamber. Thermal efficiency.

In an optional embodiment, two groups of fluid drainage components 10 include a first group of fluid drainage components and a second group of fluid drainage components, and the first group of fluid drainage components and the second group of fluid drainage components are arranged side by side;

There is a first fluid channel 101 between the first group of fluid guiding parts, there is a second fluid channel 102 between the second group of fluid guiding parts, and a third fluid channel is formed between the first group of fluid guiding parts and the second group of fluid guiding parts 103 ; the first fluid channel 101 , the second fluid channel 102 and the third fluid channel 103 form an S-shaped fluid channel.

It should be noted that the first group of fluid guiding elements themselves form the first fluid channel 101 , and the second group of fluid guiding elements themselves form the second fluid channel 102 . When the first group of fluid guiding parts and the second group of fluid guiding parts are arranged side by side and spaced apart, a third fluid channel 103 is formed between the first group of fluid guiding parts and the second group of fluid guiding parts.

In an optional embodiment, the first group of fluid guiding elements includes a first row of drain fins 11 and a second row of drain fins 12, and the first row of drain fins 11 and the second row of drain fins 12 are arranged opposite to each other. A first fluid channel 101 is formed between the first row of drain fins 11 and the second row of drain fins 12 .

For the requirement of low pressure drop, the embodiment of the present invention designs a fin array set of the first row of drain fins 11 and the second row of drain fins 12 to force the fluid to flow in a serpentine shape. A swirl flow is formed between two adjacent fluids, which greatly reduces the resistance loss along the way and reduces the pressure drop.

In an optional embodiment, the first row of drain fins 11 is arranged at a first preset angle in the sub-spray evaporation chamber 100, and the second row of drain fins 12 is arranged at a second preset angle in the sub-spray evaporation chamber 100. The angle is set, and the first preset angle and the second preset angle are complementary.

That is to say, the direction of the first row of drain fins 11 is different from that of the second row of drain fins 12, and the first row of drain fins 11 is set at a first preset angle in the sub-spray evaporation chamber 100, for example, the first The preset angle may be 45°, and the second row of drain fins 12 is arranged in the sub-spray evaporation chamber 100 at a second preset angle, for example, the second preset angle may be 135°. That is, the extension lines of the first row of drain fins 11 and the second row of drain fins 12 intersect instead of being parallel, so that the passing fluid is shaped and limited so that it flows in one flow channel and is connected with other flow channels. Connected to form an S-shaped flow channel, the normal fluid flow path.

In an optional embodiment, the second row of drain fins 12 also includes flow limiting fins 121, and the flow restricting fins 121 are located at the connecting head of the second row of drain fins 12, and are used to restrict the passage of fluid through the next fluid flow. The channel flows back to the fluid channel, or flows through the fluid channel to the next fluid channel.

It can be understood that the reverse flow of the fluid entering the next fluid channel can be prevented from flowing back to the upper channel by setting the flow limiting fins 121. The flow limiting fins 121 are located at the connecting head of the second row of drain fins 12, that is, when After the fluid flows out of the first fluid channel and flows into the second fluid channel, the fluid can only flow to the third fluid channel through the second fluid channel due to the arrangement of the flow limiting fins 121 connected to the head of the second row of drain fins 12 . without reverse flow.

Further, at the head of each fluid channel, a flow-restricting fin 121 will be set to prevent the fluid from flowing backward, and at the tail of each fluid channel, a flow-limiting fin 121 will be set to prevent the fluid from flowing forward to the next flow channel .

Furthermore, in the first column of drain fins 11 and the second row of drain fins 12 in each group of fluid guide parts, a flow limiting fin 121 is provided, and the fluid flow is displayed through the flow limiting fin 121. flow to a fluid or superfluidic channel. That is, the flow limiting fins 121 are set at the head of the first row of drain fins 11 in this fluid channel to prevent the fluid from flowing in the reverse flow channel, that is, to flow to the next fluid channel through this fluid channel; A flow-limiting fin 121 is provided at the tail of the sheet 12 to prevent the fluid from flowing beyond the flow channel, that is, to flow through the current flow channel to the next fluid flow channel.

In an optional embodiment, the restricting fin 121 includes a connected restricting portion and a drainage portion, the restricting portion and the draining portion are connected at a preset angle, and the restricting portion is used to restrict fluid from passing through the next fluid channel Backflow this fluid channel.

As can be seen in Fig. 2, the shape of the drainage fins provided by the embodiments of the present invention are all the same, and the restricting fins 121 include a limiting part to isolate the current fluid flow channel from the adjacent fluid flow channel, so as to prevent the fluid from flowing in reverse or not according to The S-shaped route moves, and flows to the next fluid channel beyond the current fluid channel. Further, the limiting part is connected with the cavity of the spray evaporation chamber.

In an optional embodiment, the second group of fluid guiding elements includes a third row of drain fins 13 and a fourth row of drain fins 14 , and the third row of drain fins 13 is opposite to the fourth row of drain fins 14 , A third fluid channel 103 is formed between the third row of drain fins 13 and the fourth row of drain fins 14 .

It should be noted that the structure of the second group of fluid drainage elements provided by the embodiment of the present invention is the same as that of the first group of fluid drainage elements, and the arrangement is also similar.

Further, in an optional embodiment, the third row of drain fins 13 is arranged at a first preset angle in the sub-spray evaporation chamber 100, and the fourth row of drain fins 14 is arranged at a first preset angle in the sub-spray evaporation chamber 100. The second preset angle is set, and the first preset angle and the second preset angle are complementary.

That is to say, the third row of drain fins 13 is arranged in a different direction from the fourth row of drain fins 14, and the third row of drain fins 13 is arranged at a third preset angle in the sub-spray evaporation chamber 100. For example, the third row of drain fins 13 The preset angle may be 45°, and the fourth column of drain fins 14 is arranged in the sub-spray evaporation chamber 100 at a fourth preset angle, for example, the fourth preset angle may be 135°. That is, the third row of drain fins 13 intersects with the extension line of the fourth row of drain fins 14 instead of being parallel, so that the passing fluid is shaped and limited so that it flows in one flow channel and is connected with other flow channels. Connected to form an S-shaped flow channel, the normal fluid flow path.

In an optional embodiment, the fourth row of drain fins 14 also includes flow limiting fins 121, and the flow restricting fins 121 are located at the connecting head of the fourth row of drain fins 14, and are used to restrict the passage of fluid through the next fluid flow. The channel flows back to the fluid channel, or flows through the fluid channel to the next fluid channel.

It can be understood that the reverse flow of the fluid entering the next fluid channel can be prevented from flowing back to the upper channel by setting the flow limiting fins 121. The flow limiting fins 121 are located at the connecting head of the fourth row of drain fins 14, that is, when After the fluid flows out of the third fluid channel and flows into the fourth fluid channel, the fluid can only flow to the third fluid channel through the fourth fluid channel due to the setting of the fourth row of drain fins 14 connected to the flow limiting fins 121 at the head. without reverse flow.

Further, that is, in the third row of drain fins 13 and the fourth row of drain fins 14 in each group of fluid guide parts, a flow limiting fin 121 is provided, and the fluid reverse direction is displayed through the flow limiting fin 121 flow or superfluid channel flow. That is, the flow-limiting fins 121 are set at the head of the third row of drain fins 13 in this fluid channel to prevent the fluid from flowing in the reverse flow channel, that is, to flow to the next fluid channel through this fluid channel; A flow limiting fin 121 is provided at the tail of the sheet 14 to prevent the fluid from flowing beyond the flow channel, that is, flowing through the current flow channel to the next fluid flow channel.

In an optional embodiment, a communication port 110 is provided at the corner of the last group of fluid drainage components in each sub-spray evaporation chamber 100 , and each sub-spray evaporation chamber 100 is connected through the communication port 110 .

Further, the communication port 110 at the corner is also provided with a fluid drainage assembly, that is, the first row of drainage fins 11 and the second row of drainage fins 12, and the channels between each sub-spray evaporation chamber 100 are designed between layers, and the channels between the channels The design of the drainage fins and the layer partition plate 1 ensures the interlayer flow and the serpentine flow in the sub-spray evaporation chamber 100 .

In an optional embodiment, the last layer of spray evaporation chamber 100 has a fluid outlet, and the fluid outlet includes a spray inlet 104 and a gas inlet 105 .

Further, referring to FIG. 2 , when there is one layer separation plate 1, the upper and lower intervals of the spray evaporation chamber are divided into two sub-spray evaporation chambers 100, wherein the sub-spray evaporation chamber 100 located below is provided with a spray inlet 104 and a gas inlet 105, A gas outlet 103 is provided on the upper sub-spray evaporation chamber 100 .

Further, referring to FIG. 3 , the gas outlet 103 of the spray evaporation chamber provided by the embodiment of the present invention is connected to the fuel cell stack. That is to say, the high-pressure air from the air compressor enters the spray evaporation chamber, and the high-pressure coolant is provided by the high-pressure water pump, and after heat exchange in the spray evaporation chamber, it directly enters the fuel cell stack from the gas outlet 103 .

On the other hand, a system of a spray evaporation chamber with the functions of a humidifier and an intercooler is provided, the system includes any of the above spray evaporation chambers with the functions of a humidifier and an intercooler, and the system also includes an air compressor , the outlet of the air compressor is connected with the air inlet of the spray evaporation chamber.

Having described various embodiments of the present disclosure above, the foregoing description is exemplary, not exhaustive, and is not limited to the disclosed embodiments. Many modifications and alterations will be apparent to those of ordinary skill in the art without departing from the scope and spirit of the described embodiments. The terminology used herein is chosen to best explain the principle of each embodiment, practical application or technical improvement in the market, or to enable other ordinary skilled in the art to understand each embodiment disclosed herein.

Claims (10)

1. A spray evaporation chamber with humidifier and intercooler function, characterized in that, the spray evaporation chamber comprises: At least one layer partition, the layer partition is arranged horizontally in the spray evaporation chamber, and the spray evaporation chamber is spaced up and down into at least two sub-spray evaporation chambers, each sub-spray evaporation chamber is connected, and the first layer of sub-spray There is a fluid inlet on the evaporation chamber, and a fluid outlet on the last layer of spray evaporation chamber; The sub-spray evaporation chamber includes at least two groups of fluid drainage components, the two groups of fluid drainage components are arranged sequentially in the sub-spray evaporation chamber, and the two groups of fluid drainage components are formed in the sub-spray evaporation chamber An S-shaped fluid channel through which fluid flows in an S-shape. 2. The spray evaporation chamber with humidifier and intercooler functions according to claim 1, wherein the two groups of fluid drainage components comprise a first group of fluid drainage components and a second group of fluid drainage components, so The first group of fluid drainage elements and the second group of fluid drainage elements are arranged side by side; There is a first fluid channel between the first group of fluid guiding parts, and a second fluid channel between the second group of fluid guiding parts, and between the first group of fluid guiding parts and the second group of fluid guiding parts form a third fluid channel; The first fluid channel, the second fluid channel and the third fluid channel form the S-shaped fluid channel. 3. The spray evaporation chamber with the functions of humidifier and intercooler according to claim 2, characterized in that, the first group of fluid guides includes a first row of drain fins and a second row of drain fins, The first row of drain fins is opposite to the second row of drain fins, and the first fluid channel is formed between the first row of drain fins and the second row of drain fins. 4. The spray evaporation chamber with humidifier and intercooler functions according to claim 3, characterized in that, the first column of drain fins is arranged at a first preset angle in the sub-spray evaporation chamber , the second row of drain fins is arranged in the sub-spray evaporation chamber at a second preset angle, and the first preset angle and the second preset angle are complementary. 5. The spray evaporation chamber with the functions of humidifier and intercooler according to claim 3, characterized in that, the second row of drain fins also includes flow-limiting fins, and the flow-limiting fins are located at the The connecting head of the second row of drain fins is used to restrict the fluid from flowing back into the fluid channel through the next fluid channel, or from flowing into the previous fluid channel through the current fluid channel. 6. The spray evaporation chamber with the functions of humidifier and intercooler according to claim 5, characterized in that, the restricting fins include connected limiting parts and drainage parts, and the limiting parts and The drainage part is connected at a predetermined angle, and the limiting part is used to restrict fluid from flowing back into the current fluid channel through the next fluid channel. 7. The spray evaporation chamber with the functions of humidifier and intercooler according to claim 3, characterized in that, the second group of fluid guides includes a third row of drain fins and a fourth row of drain fins, The third row of drain fins is opposite to the fourth row of drain fins, and the third fluid channel is formed between the third row of drain fins and the fourth row of drain fins. 8. The spray evaporation chamber with the functions of humidifier and intercooler according to claim 1, wherein a communication port is arranged at the corner of the last group of fluid drainage components of each sub-spray evaporation chamber, and each sub-spray evaporation chamber communicate through the communication port. 9. The spray evaporation chamber with humidifier and intercooler functions according to claim 1, characterized in that the last layer of the spray evaporation chamber has a fluid outlet, and the fluid outlet includes a spray inlet and a gas inlet. 10. A system with a spray evaporation chamber with humidifier and intercooler functions, characterized in that the system comprises the spray evaporation chamber with humidifier and intercooler functions described in any one of claims 1-9 chamber, the system also includes an air compressor, the outlet of the air compressor is connected to the air inlet of the spray evaporation chamber.

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