CN213073456U

CN213073456U - Gas-liquid phase flow heat exchange unit

Info

Publication number: CN213073456U
Application number: CN202022142837.3U
Authority: CN
Inventors: 陈志蓬; 林裕民
Original assignee: Asia Vital Components Co Ltd
Current assignee: Asia Vital Components Co Ltd
Priority date: 2020-09-25
Filing date: 2020-09-25
Publication date: 2021-04-27
Anticipated expiration: 2030-09-25

Abstract

The utility model provides a gas-liquid phase flow heat exchange unit, which comprises a first cover body, a second cover body, a steam outlet and a liquid inlet, wherein the steam outlet and the liquid inlet are communicated with the first cover body and the second cover body; a second cover having a third side and a fourth side, wherein the first and second covers are combined with each other to define a heat exchange space, the heat exchange space is provided with a working fluid and a flow dividing unit, the flow dividing unit is used to divide the heat exchange space into an evaporation area and a water return area, the evaporation area corresponds to the vapor outlet, and the water return area corresponds to the liquid inlet; therefore, the steam-liquid circulation principle is adopted to replace the traditional motor as the driving source of the working fluid, so that the overall size is reduced, and the design and manufacturing cost is reduced.

Description

Gas-liquid phase flow heat exchange unit

Technical Field

The utility model relates to a heat exchange unit and heat exchange module thereof indicate a gas-liquid looks flow heat exchange unit very much.

Background

Due to the development of computing technology, the internal electronic components of various electronic devices or computer equipment generate relatively high temperature during operation, and the high temperature is likely to cause component damage. Therefore, the heat dissipation mechanism is an important and necessary design for maintaining the electronic devices to operate properly. In addition to the general heat dissipation design using a fan to provide airflow for convection cooling or using a heat dissipation device made of a special material for attachment to generate conduction cooling, a water cooling mechanism is also an effective and common heat dissipation design.

The principle of the water-cooling heat dissipation system is that liquid (such as water or coolant) is generally used as a heat dissipation medium, and a continuously operating pump is used to form a continuous circulation in the water cooling system. The liquid flows in closed conduits that are distributed over the surface of the various electronic components (e.g., central processing units) within the system. When a relatively low temperature fluid flows through these relatively high temperature electronic components, it absorbs its heat to slow the temperature rise. Then, the heat is released by the heat exchange between the pipeline and the outside or other heat dissipation mechanisms to reduce the temperature of the liquid, and the liquid returns to the system again for circulation and heat dissipation. However, the water-cooled heat dissipation system must be provided with a pump, otherwise, the pump cannot drive the liquid to flow circularly, and the internal space of the body of a general electronic device or computer equipment is limited due to the certain volume of the pump motor, so that the water-cooled heat dissipation system is difficult to be arranged. In addition, the pump motor also generates heat during operation, so a heat dissipation mechanism of the pump motor needs to be designed additionally, the pump motor is generally dissipated by liquid in a water-cooled heat dissipation system, and in addition, the water cooling device must prevent water leakage carefully, so that electronic components in the electronic equipment are damaged once water leakage occurs.

Therefore, the design and manufacturing cost of the water-cooled heat dissipation system in the electronic device with smaller and smaller internal space is higher and higher, and the solution to the above problem is the direction of efforts required by researchers in this field.

SUMMERY OF THE UTILITY MODEL

An object of the present invention is to omit the motor, reduce the size of the heat exchange unit and the heat dissipation device so as to be installed in the electronic device, and reduce the design and manufacturing cost.

To achieve the above object, the present invention provides a gas-liquid phase flow heat exchange unit, comprising:

the first cover body is provided with a first side, a second side, a steam outlet and a liquid inlet, and the steam outlet and the liquid inlet are arranged in a separated mode and communicated with the first side and the second side;

the first cover body and the second cover body are correspondingly covered to jointly define a heat exchange space to be provided with a working fluid; and

and the shunting unit is arranged in the heat exchange space and divides the heat exchange space into an evaporation area and a water return area, the evaporation area corresponds to the steam outlet, and the water return area corresponds to the liquid inlet.

The gas-liquid phase stream heat exchange unit, wherein: the flow dividing unit is a capillary structure.

The gas-liquid phase stream heat exchange unit, wherein: the capillary structure is provided with a steam space corresponding to the steam outlet, and the steam space is communicated with the steam outlet and the evaporation area.

The gas-liquid phase stream heat exchange unit, wherein: the flow dividing unit is a fin group flow guiding element and is provided with an upper side surface, a lower side surface, a plurality of channels, a plurality of fins and at least one channel, the plurality of fins are provided with two vertical side edges, the adjacent two fins are mutually overlapped or buckled through the adjacent two side edges to form the upper side surface and the lower side surface, the channels are defined between the two adjacent fins, the upper side surface is provided with an opening corresponding to the steam outlet, the opening is communicated with the plurality of channels and the plurality of fins, and the channel is arranged on the lower side surface and penetrates through the plurality of fins and the plurality of channels, so that the water return area is communicated with the evaporation area.

The gas-liquid phase stream heat exchange unit, wherein: the plurality of fins are provided with a steam space corresponding to the opening, the steam space is communicated with the plurality of channels and the opening, and the steam space is communicated with the steam outlet and the evaporation area.

The gas-liquid phase stream heat exchange unit, wherein: the capillary structure layer is arranged between the third side of the second cover body and the lower side surface of the shunt unit.

The gas-liquid phase stream heat exchange unit, wherein: the flow dividing unit is a fin column group flow guiding element and is provided with an upper plate, a plurality of channels and a plurality of fin columns, the fin columns are arranged on the upper plate in an extending mode, the channels are defined between the fin columns, an opening is formed in the upper plate and communicated with the channels and the fin columns, and the water return area is communicated with the evaporation area through the channels.

The gas-liquid phase stream heat exchange unit, wherein: the first connector is jointed with the first cover body or integrally formed with the first cover body, the first connector is provided with a first outlet, a first inlet and an air outlet cavity, the first outlet and the first inlet are respectively communicated with the air outlet cavity, and the first inlet is correspondingly communicated with the steam outlet.

The gas-liquid phase stream heat exchange unit, wherein: the second joint is connected with the first cover body or integrally formed with the first cover body, the second joint is provided with a second outlet, a second inlet and a water return cavity, the second outlet and the second inlet are respectively communicated with the water return cavity, and the second outlet is correspondingly communicated with the liquid inlet.

The gas-liquid phase stream heat exchange unit, wherein: the gas-liquid phase flow heat exchange unit is also connected with a heat dissipation device, the heat dissipation device is provided with a heat dissipation device outlet and a heat dissipation device inlet, the steam outlet and the heat dissipation device inlet are communicated through a first pipe body, and the liquid inlet and the heat dissipation device outlet are communicated through a second pipe body.

By virtue of the utility model discloses this design need not set up the motor, still enables working fluid drive and circulation, can reach the volume that reduces heat exchange unit and heat exchange module to reduce design and manufacturing cost.

Drawings

Fig. 1 is an exploded perspective view of a first embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 2 is a perspective combination view of a first embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 3 is a cross-sectional view of the gas-liquid phase flow heat exchange unit of the present invention taken along line 2A-A;

figure 4 is an exploded perspective view of a second embodiment of the gas-liquid phase flow heat exchange unit of the present invention;

figure 5 is an exploded perspective view of a third embodiment of the gas-liquid phase flow heat exchange unit of the present invention;

figure 6 is another perspective exploded view of a third embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 7 is a combination cross-sectional view of a third embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 8 is a partial cross-sectional view of a third embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 9 is a schematic view of an alternate embodiment of a third embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

FIG. 10 is a schematic view of an alternate embodiment of a third embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

figure 11 is an exploded perspective view of a fourth embodiment of the gas-liquid phase flow heat exchange unit of the present invention;

fig. 12 is an exploded perspective view of a heat sink of a fifth embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

figure 13 is a perspective assembly view of a heat sink of a fifth embodiment of the gas-liquid phase flow heat exchange unit of the present invention;

figure 14 is a perspective combination view of a fifth embodiment of a gas-liquid phase flow heat exchange unit of the present invention;

figure 15 is a partial cross-sectional view of a fifth embodiment of the gas-liquid phase flow heat exchange unit of the present invention.

Description of reference numerals: a gas-liquid phase flow heat exchange unit 1; a first cover 11; a first side 111; a second side 112; a steam outlet 113; a liquid inlet 114; a second cover 12; a third side 121; a fourth side 122; a capillary structure layer 123; a flow dividing unit 13; an upper side surface 31; a lower side 132; a first channel 133; the first fins 134; a channel 135; a vapor space 136; opening 137; fin posts 138; a connecting body 1381; an upper plate 139; a first joint 14; a first outlet 141; a first inlet 142; an air outlet chamber 143; a second joint 15; a second outlet 151; a second inlet 152; a return water chamber 153; a heat exchange space 16; an evaporation zone 161; a water return zone 162; a working fluid 17; a heat sink 2; a heat sink outlet 201; a heat sink inlet 202; a condenser 21; a heat-dissipating fin group 211; a pipe 212; an upper protection plate 213; a lower protective plate 214; a sub-channel 215; a gas collection connector 22; a first through hole 221; a gas collection chamber 222; a water collecting joint 23; the second through-hole 231; a water collection chamber 232; a first pipe 3; a second tubular body 4.

Detailed Description

The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention. The embodiments of the present invention are explained in detail by referring to the drawings and the embodiments herein, and the principle of the present invention is explained.

The above objects, together with the structure and functional characteristics of the invention, will be best understood from the following description of the preferred embodiments when read in connection with the accompanying drawings.

Please refer to fig. 1, fig. 2 and fig. 3, which are an exploded view, an assembled view and a sectional view of fig. 2A-a of the gas-liquid phase flow heat exchange unit according to the first embodiment of the present invention, as shown in the drawings, the gas-liquid phase flow heat exchange unit 1 of the present invention includes a first cover 11, a second cover 12, a splitting unit 13, a first joint 14 and a second joint 15, and in the specific implementation, the gas-liquid phase flow heat exchange unit 1 is attached to a heating element (not shown).

The first cover 11 has a first side 111, a second side 112, a steam outlet 113 and a liquid inlet 114, the first and

second sides

111, 112 are respectively disposed on the upper and lower sides of the first cover 11, and the steam outlet 113 and the liquid inlet 114 are separately disposed and communicated with the first and

second sides

111, 112.

The second cover 12 has a third side 121 and a fourth side 122, the third side 121 and the fourth side 122 are respectively disposed on the upper side and the lower side of the second cover 12, and the first cover 11 and the second cover 12 are correspondingly covered to define a heat exchange space 16 with a working fluid 17.

The flow dividing unit 13 is disposed in the heat exchanging space 16 and divides (divides) the heat exchanging space 16 into an evaporation area 161 and a water returning area 162, the evaporation area 161 corresponds to the steam outlet 113, the water returning area 162 corresponds to the liquid inlet 114, the working fluid 17 evaporates in the evaporation area 161 and flows out from the steam outlet 113, the working fluid 17 condenses outside and flows into the water returning area 162 from the liquid inlet 114, and the working fluid 17 flows back to the evaporation area 161 from the water returning area 162.

The utility model discloses in this reposition of redundant personnel unit 13 can be a capillary structure for separate this steam outlet 113 and this liquid entry 114, this capillary structure can accelerate the working fluid after the condensation and flow back to this evaporating zone 161, and make the fourth side 122 subsides of this second lid 12 when locating heating element, can make this working fluid 17 be heated the evaporation, because this evaporating zone 161 and this return water district 162 are separated by this reposition of redundant personnel unit 13, so can prevent that the working fluid 17 after the evaporation from blockking up this liquid entry 114 or toward this liquid entry 114 refluence.

The first joint 14 is coupled to the first cover 11 or integrally formed with the first cover 11, the first joint 14 has a first outlet 141, a first inlet 142 and an air outlet chamber 143, the first outlet 141 and the first inlet 142 are respectively communicated with the air outlet chamber 143, and the first inlet 142 is correspondingly communicated with the steam outlet 131. In an alternative embodiment, the first joint 14 further has a degassing and filling port (not shown) connected to the gas outlet chamber 143, the degassing and filling port is used for filling a working fluid 17 capable of performing gas-liquid phase change and for pumping out non-condensed gas inside the gas-liquid phase flow heat exchange unit 1, and the degassing and filling port is sealed after the degassing and filling of the working fluid 17 is finished, wherein the working fluid 17 is, for example, pure water, methanol, or the like.

The second joint 15 is coupled to the first cover 11 or integrally formed with the first cover 11, the second joint 15 has a second outlet 151, a second inlet 152 and a water returning chamber 153, the second outlet 151 and the second inlet 152 are respectively communicated with the water returning chamber 153, and the second outlet 151 is correspondingly communicated with the liquid inlet 114.

In an alternative embodiment, the gas-liquid phase flow heat exchange unit 1 can omit the first and

second connectors

14 and 15, and the tube bodies are directly connected to the vapor outlet 113 and the liquid inlet 114 of the first cover 11.

By virtue of the present invention, after the working fluid 17 of the evaporation area 161 is heated and evaporated (hollow arrow in fig. 3), the first cover 11 has the effect of collecting steam, because the evaporated working fluid 17 can be pushed to the position with smaller pressure, so the evaporated working fluid 17 can be pushed to the air outlet chamber 143 of the first joint 14 and flow out from the first outlet 141, on the contrary, the condensed working fluid 17 is pushed by the evaporated working fluid 17 continuously, and can flow into the water collecting chamber 153 from the second inlet 152 of the second joint 15 and flow into the water return area 162, so the working fluid can still be driven to drive and circulate without a motor, the volume of the heat exchange unit can be reduced, and the design and manufacturing cost can be reduced.

Please refer to fig. 4, which is an exploded perspective view of a second embodiment of the gas-liquid phase flow heat exchange unit of the present invention, and refer to fig. 1, fig. 2, and fig. 3, as shown in the figures, part of the structure and functions of this embodiment are the same as those of the first embodiment, and therefore will not be described herein again, but the difference between this embodiment and the first embodiment is that the capillary structure is provided with a steam space 136 corresponding to the steam outlet 113, and the steam space 136 communicates the steam outlet 113 and the evaporation area 161.

Thus, the evaporated working fluid 17 can be rapidly led out to the vertical direction of the vapor outlet 113, and the probability that the evaporated working fluid 17 is blocked at the liquid inlet 114 is reduced.

Please refer to fig. 5, fig. 6, and fig. 7, which are an exploded perspective view, another perspective view, and a combined cross-sectional view of a third embodiment of the gas-liquid phase flow heat exchange unit of the present invention, and refer to fig. 1, fig. 2, and fig. 3, as shown in the figures, part of the structure and functions of this embodiment are the same as those of the first embodiment, and therefore will not be described herein again, but the flow dividing unit 13 of this embodiment selects a fin group flow guiding element for description, which has an upper side 131, a lower side 132, a plurality of channels 133, a plurality of fins 134, and at least one channel 135.

The plural fins 134 have two vertical side edges, and the two adjacent fins 134 are overlapped or buckled to form the upper and lower side surfaces 131, 132 through the two adjacent side edges, the channel 133 is defined between the two adjacent fins 134, the opening 137 is opened on the upper side surface 131 corresponding to the steam outlet 113, the communication is defined between the plural channels 133 and the plural fins 134, the channel 135 is opened on the lower side surface 132, and penetrates through the plural fins 134 and the plural channels 133 to make the water return area 162 communicate with the evaporation area 161. In the embodiment, the slot 135 is illustrated as two slots 135, but not limited thereto, in other embodiments, the number of the slots 135 may be one or more than three, the working fluid 17 condensed by the slot 135 can flow into the plurality of channels 133 quickly and evenly, and the plurality of fins 134 can increase the heat absorption speed of the working fluid 17.

By defining the direction of the opening 137 by the upper side 131 and the plurality of fins 134, the evaporated working fluid 17 can be rapidly led out to the vertical direction of the vapor outlet 113, thereby reducing the probability (arrows in fig. 8) that the evaporated working fluid 17 is blocked at the liquid inlet 114.

In another alternative embodiment, a capillary structure layer 123 is disposed on the third side 121 of the second cover 12, the capillary structure layer 123 is disposed between the flow dividing unit 13 and the second cover 12, and the capillary structure layer 123 enables the condensed working fluid 17 to rapidly flow back to the channel 135 and the plurality of channels 133 (as shown in fig. 9).

In another alternative embodiment, the flow dividing unit 13 may be alternatively configured as a fin-pillar guiding member (as shown in fig. 10) having an upper plate 139, a plurality of channels 133 and a plurality of fin pillars 138, the upper plate 139 is extended with the fin pillars 138, the plurality of fin pillars 138 define the channels 133 therebetween, the upper plate 131 is provided with an opening 137 to communicate with the plurality of channels 133 and the plurality of fin pillars 138, and the plurality of fin pillars 138 are directly formed on the upper plate 139 or are connected to each other through a plurality of connectors 1381, and the plurality of channels 133 enable the water return region 162 to communicate with the evaporation region 161.

Please refer to fig. 11, which is an exploded perspective view of a fourth embodiment of the gas-liquid phase flow heat exchange unit of the present invention, and with reference to fig. 5 to fig. 10, as shown in the figures, part of the structure and functions of the present embodiment are the same as those of the third embodiment, and therefore will not be described herein again, but the difference between the present embodiment and the third embodiment is that the plurality of fins 134 are provided with a steam space 136 corresponding to the opening 137, the steam space 136 communicates with the plurality of channels 133 and the opening 137, and the steam space 136 communicates with the steam outlet 113 and the evaporation area 161.

Referring to fig. 12, 13, 14 and 15, there are shown an exploded perspective view, an assembled perspective view and a partially sectioned view of a heat dissipating device according to a fifth embodiment of the gas-liquid phase flow heat exchanging device of the present invention, with additional reference to fig. 1-12, as shown, the gas-liquid phase flow heat exchange device of the present embodiment has a gas-liquid phase flow heat exchange unit 1, the gas-liquid phase flow heat exchange unit 1 is connected to a heat dissipation device 2, and the structure and function of the gas-liquid phase flow heat exchange unit 1 are the same as those of the first and second embodiments, so that the details will not be described herein, the heat sink 2 has a heat sink outlet 201 and a heat sink inlet 202, and is connected to the steam outlet 113 and the heat sink inlet 202 through a first tube 3, the liquid inlet 114 and the heat sink outlet 201 are connected by a second tube 4.

In the present embodiment, the heat dissipation device 2 includes a condenser 21, a gas collecting joint 22 and a water collecting joint 23. The condenser 21 has a plurality of heat dissipating fin sets 211, the plurality of heat dissipating fin sets 211 are respectively arranged in a stacking interval, and a plurality of pipes 212 are arranged between two adjacent heat dissipating fin sets 211 in parallel. An upper protection plate 213 is disposed on the upper side of the condenser 21, and a lower protection plate 214 is disposed on the lower side of the condenser 21.

The gas collecting connector 22 has a plurality of first through holes 221 and a gas collecting chamber 222, and the heat sink inlet 202 and the plurality of first through holes 221 are respectively communicated with the gas collecting chamber 222, and for the convenience of understanding, the gas collecting connector 22 is shown in a partial cross-sectional view in fig. 11.

The water collecting joint 23 has a plurality of second through holes 231 and a water collecting chamber 232, the heat dissipating device outlet 201 and the plurality of second through holes 231 are respectively communicated with the water collecting chamber, for easy understanding, the water collecting joint 22 is shown in a partial cross-sectional view in fig. 9, one end of the plurality of pipes 212 is inserted into the plurality of first through holes 221 and communicated with the gas collecting chamber 222, and the other end of the plurality of pipes 212 is inserted into the plurality of second through holes 231 and communicated with the water collecting chamber 232, a plurality of sub-channels 215 are respectively arranged inside the plurality of pipes 212 and communicated with the gas collecting chamber 222 and the water collecting chamber 232.

Referring to fig. 15 showing the arrow direction of the working fluid, the working fluid in the heat exchanging space 16 absorbs the heat of the heat generating source and evaporates, and the evaporated working fluid passes through the vapor outlet 113 of the first cover 11, enters the air outlet chamber 143 through the liquid inlet 142 of the first joint 14, and then is transmitted to the heat dissipation device 2 through the first pipe 3 from the first outlet 141.

The evaporated working fluid enters the gas collecting chamber 222 of the gas collecting joint 22 through the heat sink inlet 202 of the heat sink 2, and then the working fluid 17 is transmitted to the water collecting joint 23 through the plurality of pipes 212. In the process that the working fluid 17 passes through the plurality of pipes 212, the heat of the working fluid 17 is absorbed by the plurality of heat dissipation fins 211 and radiated to the external environment to achieve the effect of heat dissipation and temperature reduction, thereby condensing the working fluid 17. Condensed working fluid 17 enters water collection chamber 232 of water collection fitting 23 and is then transported from heat sink outlet 201 through second tube 4 to gas-liquid phase flow heat exchange unit 1.

The condensed working fluid 17 enters the water return chamber 153 through the second inlet 152 of the second joint 15 of the gas-liquid phase flow heat exchange unit 1, and then enters the heat exchange space 16 through the second outlet 151 and the liquid inlet 114 of the first cover 111. Therefore, the working fluid is pushed to continuously circulate through the high-low pressure difference generated by evaporation and condensation of the working fluid.

The foregoing description is intended to be illustrative rather than limiting, and it will be appreciated by those skilled in the art that many modifications, variations or equivalents may be made without departing from the spirit and scope of the invention as defined in the appended claims.

Claims

1. A gas-liquid phase stream heat exchange unit, comprising:

2. A gas-liquid phase stream heat exchange unit according to claim 1 wherein: the flow dividing unit is a capillary structure.

3. A gas-liquid phase stream heat exchange unit according to claim 2 wherein: the capillary structure is provided with a steam space corresponding to the steam outlet, and the steam space is communicated with the steam outlet and the evaporation area.

4. A gas-liquid phase stream heat exchange unit according to claim 1 wherein: the flow dividing unit is a fin group flow guiding element and is provided with an upper side surface, a lower side surface, a plurality of channels, a plurality of fins and at least one channel, the plurality of fins are provided with two vertical side edges, the adjacent two fins are mutually overlapped or buckled through the adjacent two side edges to form the upper side surface and the lower side surface, the channels are defined between the two adjacent fins, the upper side surface is provided with an opening corresponding to the steam outlet, the opening is communicated with the plurality of channels and the plurality of fins, and the channel is arranged on the lower side surface and penetrates through the plurality of fins and the plurality of channels, so that the water return area is communicated with the evaporation area.

5. A gas-liquid phase stream heat exchange unit according to claim 4 wherein: the plurality of fins are provided with a steam space corresponding to the opening, the steam space is communicated with the plurality of channels and the opening, and the steam space is communicated with the steam outlet and the evaporation area.

6. A gas-liquid phase stream heat exchange unit according to claim 4 wherein: the capillary structure layer is arranged between the third side of the second cover body and the lower side surface of the shunt unit.

7. A gas-liquid phase stream heat exchange unit according to claim 4 wherein: the flow dividing unit is a fin column group flow guiding element and is provided with an upper plate, a plurality of channels and a plurality of fin columns, the fin columns are arranged on the upper plate in an extending mode, the channels are defined between the fin columns, an opening is formed in the upper plate and communicated with the channels and the fin columns, and the water return area is communicated with the evaporation area through the channels.

8. A gas-liquid phase stream heat exchange unit according to claim 1 wherein: the first connector is jointed with the first cover body or integrally formed with the first cover body, the first connector is provided with a first outlet, a first inlet and an air outlet cavity, the first outlet and the first inlet are respectively communicated with the air outlet cavity, and the first inlet is correspondingly communicated with the steam outlet.

9. A gas-liquid phase stream heat exchange unit according to claim 8 wherein: the second joint is connected with the first cover body or integrally formed with the first cover body, the second joint is provided with a second outlet, a second inlet and a water return cavity, the second outlet and the second inlet are respectively communicated with the water return cavity, and the second outlet is correspondingly communicated with the liquid inlet.

10. A gas-liquid phase stream heat exchange unit according to claim 1 wherein: the gas-liquid phase flow heat exchange unit is also connected with a heat dissipation device, the heat dissipation device is provided with a heat dissipation device outlet and a heat dissipation device inlet, the steam outlet and the heat dissipation device inlet are communicated through a first pipe body, and the liquid inlet and the heat dissipation device outlet are communicated through a second pipe body.