CN220793092U - Dual heat absorption type steam generating device - Google Patents
Dual heat absorption type steam generating device Download PDFInfo
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- CN220793092U CN220793092U CN202322630197.4U CN202322630197U CN220793092U CN 220793092 U CN220793092 U CN 220793092U CN 202322630197 U CN202322630197 U CN 202322630197U CN 220793092 U CN220793092 U CN 220793092U
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- 230000009977 dual effect Effects 0.000 title claims description 14
- 238000010521 absorption reaction Methods 0.000 title abstract description 7
- 229910052731 fluorine Inorganic materials 0.000 claims abstract description 149
- 239000011737 fluorine Substances 0.000 claims abstract description 149
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims abstract description 138
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 238000010438 heat treatment Methods 0.000 claims abstract description 49
- 125000001153 fluoro group Chemical group F* 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 16
- 238000000605 extraction Methods 0.000 claims description 8
- WCQRWCFGZARAMR-UHFFFAOYSA-N [F].[F] Chemical compound [F].[F] WCQRWCFGZARAMR-UHFFFAOYSA-N 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 238000004321 preservation Methods 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 238000004804 winding Methods 0.000 claims 1
- 239000003507 refrigerant Substances 0.000 description 34
- 230000000694 effects Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000005674 electromagnetic induction Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a double heat absorption type steam generating device, and belongs to the field of steam generating devices. The device mainly comprises a primary water fluorine heat exchange unit, a secondary fluorine heat exchange unit and a tertiary water fluorine heat exchange unit, wherein the primary water fluorine heat exchange unit comprises a fluorine path circulation channel I and a waterway circulation channel I, the secondary fluorine heat exchange unit comprises a fluorine path circulation channel II and a fluorine path circulation channel III, the tertiary water fluorine heat exchange unit comprises a fluorine path circulation channel IV and a waterway circulation channel II, the fluorine path circulation channel I and the fluorine path circulation channel II are respectively connected with a fin evaporator, the fluorine path circulation channel III is communicated with the fluorine path circulation channel IV, the waterway circulation channel I is communicated with the waterway circulation channel II, and the waterway circulation channel II is connected with an electromagnetic heating mechanism. The utility model absorbs the heat in the air twice, so that the equipment can be started in a short time to generate steam, the steam quantity is large, the output is stable, and the steam supply at 150-180 ℃ can be easily realized by matching with the electromagnetic heating mechanism.
Description
Technical Field
The utility model belongs to the field of steam generation device production, and particularly relates to a double heat absorption type steam generation device.
Background
A steam generator is a mechanical device that can heat water into hot water or steam. The steam generator may be classified into a coal-fired steam generator, a gas steam generator, an electric steam generator, etc., according to the type of fuel. The steam generator has a common problem that the energy consumption is high and the use cost is too high.
The Chinese patent with the publication number of CN113375135A discloses an electromagnetic induction type steam generator based on an air source heat pump, which comprises a preheating mechanism, wherein the output end of a water supply pump is fixedly connected with the water inlet end of a water tank type condenser; the input end of the water delivery pump is fixedly connected with the water outlet end of the water tank type condenser; a water inlet at the bottom end of the steam generator is fixedly connected with the output end of the water delivery pump; the preheating mechanism comprises a fan which is fixedly connected to the positioning table; the evaporator is arranged at the rear side of the fan; the input end of the gas-liquid separator is connected with the working medium outlet of the evaporator; the compressor is fixedly connected to the output end of the gas-liquid separator; the input end of the condensing tube of the water tank type condenser is fixedly connected with the output end of the compressor.
The power of the steam generation is reduced in the modes of preheating and secondary heating, so that the phenomenon that excessive heat energy is instantaneously generated and cannot be fully absorbed is reduced, and the energy-saving effect is achieved. However, in the practical use process, the above structure needs to heat the water to 80-95 ℃ through primary heat exchange, and needs to be circulated for multiple times, which can lead to long equipment starting time, and steam generation still needs to be heated again by means of the steam generator, so that the steam is generated after the equipment is started for a long time, the energy-saving effect is poor, and the steam generation effect is unstable.
Disclosure of utility model
The utility model aims to solve the technical problems that: the utility model provides a overcome the not enough of prior art, provides a dual heat absorption formula steam generator, its adopts tertiary heat transfer unit twice to absorb the heat in the air, has realized that just can be with the steam of 130 ℃ of water heating to about 130 ℃ through tertiary heat transfer unit, makes equipment start in the short time can produce steam, and steam volume is big, and the output is stable, and the cooperation electromagnetic heating mechanism again can easily realize 150-180 ℃ steam's supply under the circumstances of extremely energy-conserving.
The double heat absorption type steam generating device comprises a primary water fluorine heat exchange unit, a secondary fluorine heat exchange unit and a tertiary water fluorine heat exchange unit, wherein the primary water fluorine heat exchange unit comprises a fluorine path circulation channel I and a waterway circulation channel I, the secondary fluorine heat exchange unit comprises a fluorine path circulation channel II and a fluorine path circulation channel III, the tertiary water fluorine heat exchange unit comprises a fluorine path circulation channel IV and a waterway circulation channel II, the fluorine path circulation channel I and the fluorine path circulation channel II are respectively connected with a fin evaporator, the fluorine path circulation channel III is communicated with the fluorine path circulation channel IV, the waterway circulation channel I is communicated with the waterway circulation channel II, and the waterway circulation channel II is connected with an electromagnetic heating mechanism.
Preferably, the first-stage water fluorine heat exchange unit comprises a first-stage compressor, a first-stage separator, a first throttle valve and a first water fluorine heat exchanger, wherein a first fluorine path heat exchange channel and a first waterway heat exchange channel are arranged in the first water fluorine heat exchanger, and the first fluorine path circulating channel is a loop formed by the first fluorine path heat exchange channel, the first throttle valve, the fin evaporator, the first-stage separator and the first-stage compressor.
Preferably, the first waterway circulation channel comprises a water pump and a first waterway heat exchange channel, one end of the first waterway heat exchange channel is connected with the water supply system through the water pump, and the other end of the first waterway heat exchange channel is communicated with the second waterway circulation channel.
Preferably, the second-stage fluorine-fluorine heat exchange unit comprises a second-stage compressor, a second-stage separator, a fluorine-fluorine heat exchanger and a second throttle valve, wherein a fluorine-path heat exchange channel II and a fluorine-path heat exchange channel III are arranged in the fluorine-fluorine heat exchanger, and a fluorine-path circulation channel II is a loop formed by the fluorine-path heat exchange channel II, the second throttle valve, the fin evaporator, the second-stage separator and the second-stage compressor.
Preferably, the three-stage water fluorine heat exchange unit comprises a three-stage compressor, a three-stage separator, a water fluorine heat exchanger II and a third throttle valve, wherein a fluorine path heat exchange channel IV and a water path heat exchange channel II are arranged in the water fluorine heat exchanger II, and the fluorine path heat exchange channel III, the three-stage separator, the three-stage compressor, the fluorine path heat exchange channel IV and the third throttle valve are communicated to form a loop.
Preferably, the second waterway circulation channel comprises a second waterway heat exchange channel, one end of the second waterway heat exchange channel is connected with the electromagnetic heating mechanism through a valve, and the other end of the second waterway heat exchange channel is communicated with the first waterway outlet of the first waterway heat exchange channel.
Preferably, the electromagnetic heating mechanism comprises more than one electromagnetic heating barrel, the upper end of the electromagnetic heating barrel is connected with a spherical crown-shaped steam collecting drum through a flange in a sealing manner, a steam outlet pipe is arranged on the upper portion of the steam collecting drum, a water inlet pipe is arranged at the lower end of the electromagnetic heating barrel and is communicated with a waterway heat exchange channel II, a steam exhaust cover corresponding to the steam collecting drum is arranged inside the electromagnetic heating barrel, steam exhaust holes are formed in the steam exhaust cover, an insulating heat preservation layer is wrapped on the outer wall of the electromagnetic heating barrel, an electromagnetic coil is wound outside the insulating heat preservation layer, and a shielding magnetic stripe is adhered outside the electromagnetic coil.
Preferably, a temperature display and a regulating valve for pressure relief are arranged on the steam outlet pipe.
Preferably, a drain pipe is arranged at the bottom of the electromagnetic heating barrel.
Preferably, the electromagnetic heating barrel is provided with a liquid level meter.
Compared with the prior art, the utility model has the beneficial effects that:
1. The utility model utilizes air energy to supplement heat for the first fluorine path heat exchange channel and the second fluorine path heat exchange channel, saves energy and improves heat efficiency, wherein the first fluorine path heat exchange channel can raise the temperature of normal-temperature water in the first waterway heat exchange channel to 40-60 ℃ through primary heat exchange, the second fluorine path heat exchange channel can absorb air heat, and the low-temperature low-pressure refrigerant in the third fluorine path heat exchange channel can be raised to 60 ℃, thereby greatly reducing the workload of the three-stage compressor, improving the temperature raising speed and shortening the equipment starting time;
2. The utility model absorbs the heat in the air twice, realizes that the water can be heated into the steam with the temperature of about 130 ℃ only through the three-stage heat exchange units, enables the equipment to be started in a short time to generate the steam, has large steam quantity and stable output, and can easily realize the supply of the steam with the temperature of 150-180 ℃ under the condition of extremely saving energy by matching with the electromagnetic heating mechanism.
3. The utility model has high heat efficiency and more stable steam generation effect.
Drawings
FIG. 1 is a schematic diagram of a front structure of the present utility model;
FIG. 2 is a schematic diagram of a front structure of the present utility model;
FIG. 3 is a schematic view of the back structure of the present utility model;
FIG. 4 is a schematic view of the external structure of the electromagnetic heating mechanism;
fig. 5 is a schematic view of the internal structure of the electromagnetic heating mechanism.
In the figure, 1, a rack; 2. a fin evaporator; 3. a water fluorine heat exchanger I; 301. an outlet of the fluorine path I; 302. an outlet of the waterway I; 303. an inlet of the waterway I; 304. an inlet of the fluorine path I; 4. a fluorine-fluorine heat exchanger; 401. a second outlet of the fluorine path; 402. a fluorine path three inlet; 403. a third outlet of the fluorine path; 404. a fluorine path II inlet; 5. a water fluorine heat exchanger II; 501. a fluorine path four inlet; 502. an outlet of the waterway II; 503. a second water channel inlet; 504. a fourth outlet of the fluorine path; 6. an electromagnetic heating mechanism; 601. an electromagnetic heating barrel; 602. an insulating layer; 603. an electromagnetic coil; 604. a steam exhaust hood; 605. a steam exhaust hole; 606. a steam collecting drum; 607. a steam outlet pipe; 608. a liquid level gauge; 609. shielding the magnetic stripe; 610. a water inlet pipe; 611. a blow-down pipe; 612. a temperature display; 613. a regulating valve; 7. a primary separator; 8. a first stage compressor; 9. a secondary separator; 10. a secondary compressor; 11. a third stage separator; 12. a three-stage compressor; 13. a first throttle valve; 14. a second throttle valve; 15. and a third throttle valve.
Detailed Description
The utility model is further described below with reference to the accompanying drawings:
The directional terminology referred to in the paragraphs directed to the detailed description is merely for convenience of those skilled in the art in understanding the teachings of the utility model as set forth in the visual orientations illustrated in the accompanying drawings. Unless specifically defined and limited otherwise, the terms "disposed," "mounted," "connected," and the like are to be construed broadly so that one of ordinary skill in the art would understand the meaning of the terms in this disclosure as the case may be.
As shown in fig. 1 to 3, the dual heat absorption type steam generating device comprises a frame 1, wherein a first-stage water-fluorine heat exchange unit, a second-stage fluorine heat exchange unit, a third-stage water-fluorine heat exchange unit and an electromagnetic heating mechanism 6 are installed on the frame 1, the first-stage water-fluorine heat exchange unit comprises a first fluorine path circulation channel and a first waterway circulation channel, the second-stage fluorine heat exchange unit comprises a second fluorine path circulation channel and a third fluorine path circulation channel, the third-stage water-fluorine heat exchange unit comprises a fourth fluorine path circulation channel and a second waterway circulation channel, the first fluorine path circulation channel and the second fluorine path circulation channel are respectively connected with a fin evaporator 2, namely the first fluorine path circulation channel and the second fluorine path circulation channel respectively absorb heat in air, and the first fluorine path circulation channel exchanges heat with the first waterway circulation channel, so that water in the first waterway circulation channel can be heated to 40-60 ℃. The third fluorine path circulating channel is communicated with the fourth fluorine path circulating channel, namely the third fluorine path circulating channel and the fourth fluorine path circulating channel absorb heat in the second fluorine path circulating channel for heat exchange, the first waterway circulating channel is communicated with the second waterway circulating channel, hot water after heat exchange in the first waterway circulating channel enters the second waterway circulating channel and then undergoes heat exchange and temperature rise again with the fourth fluorine path circulating channel to generate steam, at the moment, the steam can reach about 130 ℃, the second waterway circulating channel is connected with the electromagnetic heating mechanism 6, and the steam can be heated to 150-180 ℃ by using a very small amount of electric energy.
Specifically, the first-stage water fluorine heat exchange unit comprises a first-stage compressor 8, a first-stage separator 7, a first throttle valve 13 and a first water fluorine heat exchanger 3, wherein a fluorine path heat exchange channel I and a water path heat exchange channel I are arranged in the first water fluorine heat exchanger 3, and a fluorine path circulation channel I is formed by a loop formed by the fluorine path heat exchange channel I, the first throttle valve 13, the fin evaporator 2, the first-stage separator 7 and the first-stage compressor 8.
The second-stage fluorine heat exchange unit comprises a second-stage compressor 10, a second-stage separator 9, a fluorine heat exchanger 4 and a second throttle valve 14, wherein a fluorine path heat exchange channel II and a fluorine path heat exchange channel III are arranged in the fluorine heat exchanger 4, and a fluorine path circulation channel II is formed by a loop formed by the fluorine path heat exchange channel II, the second throttle valve 14, the fin evaporator 2, the second-stage separator 9 and the second-stage compressor 10.
The three-stage water fluorine heat exchange unit comprises a three-stage compressor 12, a three-stage separator 11, a water fluorine heat exchanger II 5 and a third throttle valve 15, wherein a fluorine path heat exchange channel IV and a waterway heat exchange channel II are arranged in the water fluorine heat exchanger II 5, and a fluorine path circulation channel III is communicated with the fluorine path circulation channel IV, in particular to a loop formed by the communication of the fluorine path heat exchange channel III, the three-stage separator 11, the three-stage compressor 12, the fluorine path heat exchange channel IV and the third throttle valve 15.
The first waterway circulation channel comprises a water pump and a first waterway heat exchange channel, one end of the first waterway heat exchange channel is connected with the water supply system through the water pump, and the other end of the first waterway heat exchange channel is communicated with the second waterway circulation channel. Cold water enters the first waterway heat exchange channel through the first waterway inlet 303 by the water pump, and exchanges heat with the first fluorine heat exchange channel sufficiently, the water temperature after heat exchange can reach 40-60 ℃, and the water after heat exchange enters the second waterway circulation channel through the first waterway outlet 302. Specifically, the second waterway circulation channel comprises a second waterway heat exchange channel, one end of the second waterway heat exchange channel is connected with the electromagnetic heating mechanism 6 through a valve, and the other end of the second waterway heat exchange channel is communicated with the first waterway outlet 302 of the first waterway heat exchange channel.
As shown in fig. 4 and 5, the electromagnetic heating mechanism 6 includes a plurality of parallel electromagnetic heating barrels 601, the upper ends of the electromagnetic heating barrels 601 are connected with upwards convex spherical crown-shaped steam collecting drums 606 through flanges in a sealing manner, steam outlet pipes 607 are arranged on the upper parts of the steam collecting drums 606, temperature displays 612 and regulating valves 613 for pressure relief are arranged on the steam outlet pipes 607, the temperature displays 612 are used for observing the temperature in the electromagnetic heating barrels 601 in real time, and as the temperature of the electromagnetic heating barrels 601 rises, the pressure in the barrels is higher, the regulating valves 613 can relieve the pressure of the electromagnetic heating barrels 601, so that the safety of the device is improved. The electromagnetic heating barrel 601 lower extreme is equipped with inlet tube 610, and every inlet tube 610 is connected with the intake manifold respectively, and intake manifold and water route second export 502 intercommunication on the water route heat transfer passageway second are equipped with the steam extraction hood 604 of the decurrent spherical cap that corresponds with steam drum 606 in the electromagnetic heating barrel 601 inside, has seted up steam extraction hole 605 on the steam extraction hood 604, and steam extraction hood 604 has the separation effect, can play the purpose of gas-liquid separation, separates the water in the steam, and water can flow back to the bucket along steam extraction hood 604, and likewise, the comdenstion water in the steam drum 606 can flow back to the bucket along spherical cap structure. An insulating layer 602 is wrapped on the outer wall of the electromagnetic heating barrel 601, an electromagnetic coil 603 is wound outside the insulating layer 602, a shielding magnetic strip 609 is stuck outside the electromagnetic coil 603, and the shielding magnetic strip 609 prevents a magnetic field from leaking; the electromagnetic heating barrel 601 is provided with a liquid level meter 608, and the bottom of the electromagnetic heating barrel 601 is provided with a drain pipe 611. The electromagnetic coil 603 is connected with a variable frequency controller, the heating temperature of the electromagnetic coil 603 is controlled by the variable frequency controller, and the liquid level in the barrel can be controlled by the liquid level meter 608.
The working principle of the utility model is as follows: the first-stage compressor 8 is filled with refrigerant, the first-stage compressor 8 is electrified and started, the first-stage compressor 8 compresses the refrigerant into high-temperature high-pressure gas, the gas enters the first fluorine path heat exchange channel through the first fluorine path inlet 304, the first fluorine path heat exchange channel exchanges heat with the first waterway heat exchange channel in the first water-fluorine heat exchanger 3, the refrigerant after heat exchange is discharged through the first fluorine path outlet 301, the refrigerant is throttled and depressurized through the first throttle valve 13, the high-temperature high-pressure gaseous refrigerant is converted into liquid low-temperature low-pressure refrigerant, the refrigerant enters the fin evaporator 2, the fan of the fin evaporator 2 is utilized for absorbing heat and cooling, heat in the air is absorbed to form phase change, the low-temperature low-pressure liquid refrigerant is converted into gaseous low-pressure refrigerant, and the gaseous low-pressure refrigerant returns to the first-stage compressor 8 through the first-stage separator 7 for internal circulation in a cycle.
The two-stage compressor 10 is filled with refrigerant, the two-stage compressor 10 is started, the two-stage compressor 10 compresses the refrigerant into high-temperature high-pressure gas, the refrigerant enters the fluorine path heat exchange channel II through the fluorine path second inlet 404, the fluorine path heat exchange channel II exchanges heat with the fluorine path heat exchange channel III in the fluorine-fluorine heat exchanger 4, the refrigerant in the fluorine path heat exchange channel III can reach more than 60 ℃ after heat exchange, the refrigerant after heat exchange in the fluorine path heat exchange channel II is discharged through the fluorine path second outlet 401, the refrigerant is throttled and depressurized through the second throttle valve 14, the high-temperature high-pressure gaseous refrigerant is converted into liquid low-temperature low-pressure refrigerant, the refrigerant enters the fin evaporator 2 again, heat in the air is absorbed, phase change is formed, the low-temperature low-pressure liquid refrigerant is converted into gaseous low-pressure refrigerant, and the low-temperature low-pressure refrigerant returns to the two-stage compressor 10 through the two-stage separator 9, and internal circulation is carried out repeatedly.
The three-stage compressor 12 is filled with refrigerant, the three-stage compressor 12 is started, the three-stage compressor 12 compresses the refrigerant into high-temperature high-pressure gas, the refrigerant enters the fluorine path heat exchange channel IV through the fluorine path four inlet 501, the fluorine path heat exchange channel IV exchanges heat with the water path heat exchange channel II in the water fluorine heat exchanger II 5, the refrigerant after heat exchange is discharged through the fluorine path four outlet 504, the refrigerant is throttled and depressurized through the third throttle valve 15, the high-temperature high-pressure gaseous refrigerant is converted into liquid low-temperature low-pressure refrigerant, the low-temperature low-pressure refrigerant enters the fluorine path circulation channel III through the fluorine path three inlet 402, the fluorine path circulation channel III absorbs heat in the fluorine path heat exchange channel II to form phase change, the low-temperature low-pressure liquid refrigerant is converted into gaseous low-pressure refrigerant, the low-pressure refrigerant enters the three-stage separator 11 through the fluorine path three outlet 403, and returns to the three-stage compressor 12 again after gas-liquid separation, and internal circulation is performed.
Meanwhile, cold water enters the first waterway heat exchange channel through the first waterway inlet 303 through the water pump and is fully exchanged with the first fluorine heat exchange channel, the water temperature after heat exchange can reach 40-60 ℃, the water after heat exchange enters the second waterway heat exchange channel through the first waterway outlet 302 and the second waterway inlet 503, the second waterway heat exchange channel is fully exchanged with the fourth fluorine heat exchange channel, the water temperature after heat exchange can reach about 130 ℃, the water is quickly vaporized to form steam, the steam temperature is about 120-130 ℃, and the steam outlet amount can be adjusted through a control valve in the process.
Hot water or steam from the second waterway heat exchange channel enters the electromagnetic heating barrel 601 through the water inlet pipe 610, the variable frequency controller controls the electromagnetic coil 603 to be electrified, the electromagnetic coil 603 can be electrified to form a magnetic field, the magnetic field can generate a heat source in the electromagnetic heating barrel 601, the heat source can reach 1200 ℃, the temperature of the heat source can be controlled within 200 ℃ through the temperature control of the variable frequency controller in the embodiment, so that steam at about 130 ℃ can be heated to 150-180 ℃ in the electromagnetic heating barrel 601 again, and the steam at about 130 ℃ mainly absorbs heat in the air, so that the consumed electric energy is extremely small when the steam is heated to 150-180 ℃ through the electromagnetic heating, and the energy is greatly saved.
Finally, although the description has been described in terms of embodiments, not every embodiment is intended to include only a single embodiment, and such description is for clarity only, as one skilled in the art will recognize that the embodiments of the disclosure may be combined as appropriate to form other embodiments that will be apparent to those skilled in the art.
Claims (10)
1. A dual endothermic steam generator characterized in that: the device comprises a primary water fluorine heat exchange unit, a secondary fluorine heat exchange unit and a tertiary water fluorine heat exchange unit, wherein the primary water fluorine heat exchange unit comprises a first fluorine path circulation channel and a first waterway circulation channel, the secondary fluorine heat exchange unit comprises a second fluorine path circulation channel and a third fluorine path circulation channel, the tertiary water fluorine heat exchange unit comprises a fourth fluorine path circulation channel and a second waterway circulation channel, the first fluorine path circulation channel and the second fluorine path circulation channel are respectively connected with a fin evaporator (2), the third fluorine path circulation channel is communicated with the fourth fluorine path circulation channel, the first waterway circulation channel is communicated with the second waterway circulation channel, and the second waterway circulation channel is connected with an electromagnetic heating mechanism (6).
2. The dual endothermic steam generating device of claim 1, wherein: the first-stage water fluorine heat exchange unit comprises a first-stage compressor (8), a first-stage separator (7), a first throttle valve (13) and a first water fluorine heat exchanger (3), wherein a first fluorine path heat exchange channel and a first waterway heat exchange channel are arranged in the first water fluorine heat exchanger (3), and the first fluorine path circulation channel is a loop formed by the first fluorine path heat exchange channel, the first throttle valve (13), the fin evaporator (2), the first-stage separator (7) and the first-stage compressor (8).
3. The dual endothermic steam generating device of claim 2, wherein: the first waterway circulation channel comprises a water pump and a first waterway heat exchange channel, one end of the first waterway heat exchange channel is connected with the water supply system through the water pump, and the other end of the first waterway heat exchange channel is communicated with the second waterway circulation channel.
4. The dual endothermic steam generating device of claim 1, wherein: the second-stage fluorine heat exchange unit comprises a second-stage compressor (10), a second-stage separator (9), a fluorine-fluorine heat exchanger (4) and a second throttle valve (14), wherein a fluorine-path heat exchange channel II and a fluorine-path heat exchange channel III are arranged in the fluorine-fluorine heat exchanger (4), and a fluorine-path circulation channel II is a loop formed by the fluorine-path heat exchange channel II, the second throttle valve (14), the fin evaporator (2), the second-stage separator (9) and the second-stage compressor (10).
5. The dual endothermic steam generator of claim 4, wherein: the three-stage water fluorine heat exchange unit comprises a three-stage compressor (12), a three-stage separator (11), a water fluorine heat exchanger II (5) and a third throttle valve (15), wherein a fluorine path heat exchange channel IV and a water path heat exchange channel II are arranged in the water fluorine heat exchanger II (5), and the fluorine path heat exchange channel III, the three-stage separator (11), the three-stage compressor (12), the fluorine path heat exchange channel IV and the third throttle valve (15) are communicated to form a loop.
6. The dual endothermic steam generating device of claim 5, wherein: the second waterway circulation channel comprises a second waterway heat exchange channel, one end of the second waterway heat exchange channel is connected with the electromagnetic heating mechanism (6) through a valve, and the other end of the second waterway heat exchange channel is communicated with a first waterway outlet (302) of the first waterway heat exchange channel.
7. The dual endothermic steam generating device according to any one of claims 1 to 6, wherein: electromagnetic heating mechanism (6) include more than one electromagnetic heating bucket (601), electromagnetic heating bucket (601) upper end has spherical crown-shaped steam collecting drum (606) through flange sealing connection, steam collecting drum (606) upper portion is equipped with out vapour pipe (607), electromagnetic heating bucket (601) lower extreme is equipped with inlet tube (610), inlet tube (610) and water route heat transfer passageway two intercommunication, electromagnetic heating bucket (601) inside be equipped with steam extraction cover (604) corresponding to steam collecting drum (606), steam extraction hole (605) have been seted up on steam extraction cover (604), the outer wall parcel of electromagnetic heating bucket (601) has insulating heat preservation (602), insulating heat preservation (602) outside winding has solenoid (603), solenoid (603) outside paste has shielding magnetic stripe (609).
8. The dual endothermic steam generator of claim 7, wherein: the steam outlet pipe (607) is provided with a temperature display (612) and a regulating valve (613) for pressure relief.
9. The dual endothermic steam generator of claim 7, wherein: a drain pipe (611) is arranged at the bottom of the electromagnetic heating barrel (601).
10. The dual endothermic steam generator of claim 7, wherein: the electromagnetic heating barrel (601) is provided with a liquid level meter (608).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322630197.4U CN220793092U (en) | 2023-09-27 | 2023-09-27 | Dual heat absorption type steam generating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322630197.4U CN220793092U (en) | 2023-09-27 | 2023-09-27 | Dual heat absorption type steam generating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220793092U true CN220793092U (en) | 2024-04-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322630197.4U Active CN220793092U (en) | 2023-09-27 | 2023-09-27 | Dual heat absorption type steam generating device |
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| Country | Link |
|---|---|
| CN (1) | CN220793092U (en) |
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2023
- 2023-09-27 CN CN202322630197.4U patent/CN220793092U/en active Active
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