CN111306963A - Self-evaporation type steam condenser with netted liquid film ball - Google Patents
Self-evaporation type steam condenser with netted liquid film ball Download PDFInfo
- Publication number
- CN111306963A CN111306963A CN202010251157.7A CN202010251157A CN111306963A CN 111306963 A CN111306963 A CN 111306963A CN 202010251157 A CN202010251157 A CN 202010251157A CN 111306963 A CN111306963 A CN 111306963A
- Authority
- CN
- China
- Prior art keywords
- temperature liquid
- low
- pipe
- cylinder body
- inlet pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
- F28D3/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits with tubular conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/04—Auxiliary systems, arrangements, or devices for feeding, collecting, and storing cooling water or other cooling liquid
- F28B9/06—Auxiliary systems, arrangements, or devices for feeding, collecting, and storing cooling water or other cooling liquid with provision for re-cooling the cooling water or other cooling liquid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/06—Spray nozzles or spray pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/08—Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a self-evaporation type steam condenser with a reticular liquid film ball, which comprises an outer cylinder body, wherein an inner cylinder body is arranged in the outer cylinder body, an interlayer is arranged between the outer cylinder body and the inner cylinder body, an upper cover plate is arranged at the top of the outer cylinder body, and a lower bottom plate is arranged at the bottom of the outer cylinder body; a packing area and a spraying device are arranged in the inner cylinder body, the packing area is arranged in the middle of the inner cylinder body, packing is filled in the packing area, and the spraying device is arranged above the packing area; the side of the lower part of the outer barrel is provided with a low-temperature liquid inlet pipe, a steam inlet pipe is arranged above the low-temperature liquid inlet pipe, the side of the upper part of the outer barrel is provided with a high-temperature liquid outlet pipe and a high-temperature liquid inlet pipe, the upper cover plate is provided with a low-pressure steam outlet pipe and an interlayer exhaust pipe, and the lower bottom plate is provided with a low-temperature liquid outlet pipe. The invention has high steam condensation efficiency, no need of external cold source, good energy-saving effect, high heat utilization rate, no heat emission and no heat pollution, and recovers heat energy. Meanwhile, the equipment has compact and reasonable structure, small volume and small occupied area of equipment with equal capacity, and the investment is reduced.
Description
Technical Field
The invention relates to a condenser, in particular to a mesh liquid film ball self-evaporation type steam condenser.
Background
The condenser is a universal device frequently applied in various fields of energy, chemical industry, food, medicine, environmental protection and the like, has various forms such as a shell-tube type, a plate type, a spray type, a jet type and the like, has the characteristics, but always needs a low-temperature cold source (liquid or gas) to cool high-temperature gas to condense the high-temperature gas, the condenser in different forms has great efficiency difference, and the difference of consumables and cost is also great. In addition, much of the cooled heat is not utilized and is discharged to the atmosphere, which causes thermal pollution to the atmosphere.
The steam condenser has various forms, including a direct contact type and a non-contact type, the contact type steam condenser is one of the condensers, and the common realization mode is as follows: (1) cold water is sprayed in from an upper nozzle, steam enters from a side inlet, the steam is fully contacted with the cold water and then condensed into water, and meanwhile, the water flows downwards along a pipe, and part of non-condensed steam can be brought out; (2) the filling type condenser is filled with ceramic ring fillers, the ceramic ring fillers are filled in the condenser, steam enters from the side pipe and contacts with cold water sprayed from the side pipe, after the fillers are wetted by water, the contact area of the cold water and the steam is increased, the steam is condensed into water and flows out along a lower pipeline, and non-condensable gas and an upper pipeline are pumped out by a vacuum pump so as to ensure a certain vacuum degree in the condenser; (3) a water spray plate or sieve plate condenser, aiming at increasing the contact area of cold water and steam. First, the condenser needs to provide a cold source from the outside, and although the steam of the condenser can contact with the cold source, the heat exchange efficiency between the steam and the cold source is still low, and the amount of circulating water is large.
Disclosure of Invention
One technical problem that this aspect of this disclosure solved is that this condenser does not need the additional low temperature cold source to condense vapour into liquid, but uses the energy of higher pressure vapour itself to make partial cold source for condensing low pressure vapour into liquid.
Another aspect of the present disclosure is to provide a condenser that uses a mesh-shaped liquid film ball as a liquid evaporation device, so that a high-temperature liquid is quickly changed into a liquid film to form a large amount of evaporation surface area. The steam injection and suction pump is driven by a small amount of new steam with higher pressure to form vacuum, partial high-temperature liquid is evaporated by the heat of the steam injection and suction pump, the temperature of the residual liquid which is not evaporated is quickly reduced, the cooled low-temperature liquid returns to enter a steam cooling area to cool the low-pressure steam which needs to be condensed, the low-temperature liquid is heated into the high-temperature liquid by the low-pressure steam, the high-temperature liquid enters the high-efficiency reticular liquid film ball evaporator again, and the partial evaporation, partial cooling, circulation and stable circulation are carried out. This cooling process has no heat output, and the produced part of the low pressure steam, i.e. the latent heat of condensation of the steam, is reused. The condenser recovers the discharged waste heat to save energy and reduces the pollution of the waste heat to the environment.
In order to achieve the purpose, the invention adopts the following technical scheme that the invention comprises an outer cylinder body and is technically characterized in that an inner cylinder body is arranged in the outer cylinder body, an interlayer is arranged between the outer cylinder body and the inner cylinder body, an upper cover plate is arranged at the top of the outer cylinder body, and a lower bottom plate is arranged at the bottom of the outer cylinder body;
a packing area and a spraying device are arranged in the inner cylinder body, the packing area is arranged in the middle of the inner cylinder body, packing is filled in the packing area, and the spraying device is arranged above the packing area;
a low-temperature liquid inlet pipe is arranged on the side surface of the lower part of the outer barrel and communicated with the interlayer, a steam inlet pipe is arranged above the low-temperature liquid inlet pipe and communicated with the interlayer, a high-temperature liquid outlet pipe is arranged on the side surface of the upper part of the outer barrel, a high-temperature liquid inlet pipe is arranged above the high-temperature liquid outlet pipe, one end of the high-temperature liquid inlet pipe is connected with the spraying device of the inner barrel, one end of the high-temperature liquid outlet pipe is communicated with the interlayer, and the other end of the high-temperature liquid;
the low-pressure steam exhaust pipe is communicated with the interlayer, the interlayer exhaust pipe is provided with a control valve for the interlayer exhaust pipe, the lower bottom plate is provided with a low-temperature liquid outlet pipe, the low-temperature liquid outlet pipe is provided with a low-temperature liquid outlet control valve, and the low-temperature liquid outlet pipe is communicated with the inner cylinder.
The low-temperature liquid outlet pipe is connected with the low-temperature liquid inlet pipe, a circulating pump and a low-temperature liquid discharge pipe are arranged on the low-temperature liquid outlet pipe, and a low-temperature liquid discharge control valve is arranged on the low-temperature liquid discharge pipe.
The low-temperature liquid inlet pipe and the steam inlet pipe are both provided with a plurality of same liquid inlet pipes, the low-temperature liquid inlet pipes are same in height, and the steam inlet pipes are same in height.
The high-temperature liquid inlet pipe is provided with a high-temperature liquid inlet control valve, the low-temperature liquid inlet pipe is provided with a low-temperature liquid inlet control valve, and the steam inlet pipe is provided with a steam inlet control valve.
The high-temperature liquid outlet pipe is provided with a high-temperature liquid separating pipe, and a high-temperature liquid separating pipe control valve is arranged on the high-temperature liquid separating pipe.
Preferably, the filler in the filler area is a reticular liquid membrane ball, the inside of the sphere of the reticular liquid membrane ball is hollow, and the spherical surface is reticular.
And a low-temperature liquid level indicator and a low-temperature liquid level sensor are arranged on the side surface of the lower part of the inner cylinder body.
And a high-temperature liquid level indicator and a high-temperature liquid level sensor are arranged on the side surface of the upper part of the outer cylinder body and between the high-temperature liquid inlet pipe and the upper cover plate.
And a heat insulation layer is arranged on the outer side of the outer cylinder body.
Compared with the prior art, the invention has the following beneficial effects:
(1) this condenser does not need other low temperature cold source to condense steam into liquid, but relies on the new steam of part higher pressure to pass through the steam injection pump and forms the vacuum, is connected through the low pressure steam outlet duct of pipeline and upper cover plate, makes interior barrel also become vacuum state, and high-temperature water evaporates at once under vacuum state, and the heat of a large amount of high-temperature water has been taken away to the evaporation latent heat, makes unevaporated water rapid cooling become low-temperature water. The condenser utilizes the energy of steam to manufacture a part of cold source to continuously condense the steam into liquid;
(2) netted liquid film ball surface has many nets, has very big surface area on the net surface, and high temperature liquid one contacts the net and forms large tracts of land liquid film in the twinkling of an eye for the surface area maximize that liquid exposes, evaporation area maximize make high temperature liquid rapid evaporation, will not evaporate liquid rapid cooling simultaneously, and high temperature liquid part high efficiency evaporates promptly and becomes low pressure steam, and partial high efficiency cools off and becomes low temperature liquid. Therefore, the evaporation speed is extremely high, the volume is small, the occupied area is small, and the investment is reduced;
(3) netted liquid film ball has been full of interior barrel middle part, and high temperature liquid flows from the liquid distribution pipe on netted liquid film ball upper portion, evenly flows down on liquid film ball net, and quick expansion forms the liquid film, exposes in the evaporation space, because the action of gravity, liquid flows downwards on one side of evaporating for the liquid film surface of evaporation has new liquid always, is equivalent to the stirring certainly of liquid, has guaranteed lasting evaporation efficiency.
(4) The evaporated gas flows upwards in the cavity part of the reticular liquid film ball, and the structure of the reticular liquid film ball ensures that the resistance of the gas is extremely low, thereby being convenient for the evaporation and the extraction of the gas and further improving the evaporation efficiency.
In a word, the invention has high steam condensation efficiency, does not need an external cold source, has good energy-saving effect, recovers heat energy, improves the heat utilization rate, does not generate heat emission, and does not have any heat pollution. Meanwhile, the equipment has compact and reasonable structure, small volume and small occupied area of equipment with equal capacity, and the investment is reduced.
Drawings
FIG. 1 is a schematic overall structure according to one aspect of the present disclosure;
FIG. 2 is a schematic overall structural view of another embodiment according to an aspect of the present disclosure
In the figure: 1-outer cylinder, 2-inner cylinder, 3-interlayer, 4-upper cover plate, 5-lower bottom plate, 6-reticular liquid film ball, 7-spray device, 8-low pressure steam outlet pipe, 9-interlayer exhaust pipe, 81-low pressure steam outlet control valve, 91-interlayer exhaust pipe control valve, 10-low temperature liquid inlet pipe, 11-steam inlet pipe, 101-low temperature liquid inlet control valve, 111-steam inlet control valve, 12-high temperature liquid outlet pipe, 13-high temperature liquid inlet pipe, 131-high temperature liquid inlet control valve, 14-low temperature liquid outlet pipe, 141-low temperature liquid outlet control valve, 15-low temperature liquid level indicator, 16-low temperature liquid level indicator, 17-high temperature liquid level indicator, 18-high temperature liquid level indicator, 19-circulating pump, 20-low temperature liquid discharge pipe, 201-low temperature liquid discharge control valve, 21-insulating layer, 22-high temperature liquid separation pipe and 221-high temperature liquid separation pipe control valve.
Detailed Description
The present invention will be further explained with reference to the embodiments, but the invention is not limited thereto, and the structures, the proportions, the sizes, and the like, which are shown in the drawings, are only used for matching with the disclosure of the specification, so as to be understood and read by those skilled in the art, and are not used for limiting the conditions under which the present invention can be implemented, so that the present invention has no technical essence, and any structural modification, changes in proportion, or adjustments in size, should still fall within the scope covered by the technical contents disclosed in the present invention without affecting the efficacy and the achievable purpose of the present invention. In addition, the terms "upper", "lower", "front", "rear" and "middle" used in the present specification are for clarity of description, and are not intended to limit the scope of the present invention, and the relative relationship between the terms and the relative positions may be changed or adjusted without substantial technical changes.
The first embodiment is as follows:
as shown in fig. 1, the reticular liquid film ball self-evaporation type steam condenser comprises an outer cylinder body 1 and an inner cylinder body 2, wherein a heat insulation layer 21 is arranged on the outer side of the outer cylinder body 1, the inner cylinder body 2 is arranged inside the outer cylinder body 1, an interlayer 3 is arranged between the outer cylinder body 1 and the inner cylinder body 2, an upper cover plate 4 is arranged at the top of the outer cylinder body 1, a lower bottom plate 5 is arranged at the bottom of the outer cylinder body 1, and the inner cylinder body 2 and the interlayer 3 are hermetically connected with the upper cover plate 4 and; a filling area and a spraying device 7 are arranged in the inner cylinder 2, the filling area is arranged in the middle of the inner cylinder 2, filling materials of a reticular liquid film ball 6 are arranged in the filling area, the inside of the ball body of the reticular liquid film ball 6 is hollow, the spherical surface is a hollow net, and the spraying device 7 is arranged above the filling area; the upper cover plate 4 is provided with a low-pressure steam outlet pipe 8 and an interlayer exhaust pipe 9, one end of the low-pressure steam outlet pipe 8 is communicated with the inner cylinder 2, the other end of the low-pressure steam outlet pipe 8 is connected with vacuum equipment, the low-pressure steam outlet pipe 8 is provided with a low-pressure steam outlet control valve 81, the interlayer exhaust pipe 9 is communicated with the interlayer 3, and the interlayer exhaust pipe 9 is provided with an interlayer exhaust pipe control valve 91;
a low-temperature liquid inlet pipe 10 is arranged on the side surface of the lower part of the outer cylinder body 1, the low-temperature liquid inlet pipe 10 is communicated with the interlayer 3, a steam inlet pipe 11 is arranged above the low-temperature liquid inlet pipe 10, the steam inlet pipe 11 is communicated with the interlayer 3, a low-temperature liquid inlet control valve 101 is arranged on the low-temperature liquid inlet pipe 10, a steam inlet control valve 111 is arranged on the steam inlet pipe 11, steam is in direct contact with low-temperature liquid in the interlayer 3 to quickly heat the low-temperature liquid into high-temperature liquid, a plurality of low-temperature liquid inlet pipes 10 and steam inlet pipes 11 are arranged, the low-temperature liquid inlet pipes 10 are the same in height, the steam inlet pipes 11 are the same in height, a high-temperature liquid outlet pipe 12 is arranged on the side surface of the upper part of the outer cylinder body 1, the high-temperature liquid outlet pipe 12 is arranged below the liquid level of the interlayer 3, a high-temperature liquid, The other end is connected with the other end of the high-temperature liquid inlet pipe 13, the high-temperature liquid inlet pipe 13 is provided with a high-temperature liquid inlet control valve 131, the lower bottom plate 5 is provided with a low-temperature liquid outlet pipe 14, the low-temperature liquid outlet pipe 14 is communicated with the inner cylinder 2, and the low-temperature liquid outlet pipe 14 is provided with a low-temperature liquid outlet control valve 141. High temperature liquid flows from spray set 7, flows down from the netted liquid film ball 6 uniform flow in upper portion, and the net of netted liquid film ball 6 is paved with to liquid, and netted liquid film ball 6 has very big water film surface area, because 2 internal pressure of interior barrel are low, high temperature liquid flash evaporation, and the gas of evaporation is discharged through upper portion low pressure steam outlet duct 8, and the liquid of non-evaporation becomes low temperature liquid and discharges from the low temperature drain pipe of 2 bottoms of interior barrel. The low-temperature liquid with different temperatures can be obtained by controlling the pressure inside the inner cylinder body 2 and the liquid inlet amount of the high-temperature liquid.
A low-temperature liquid level indicator 15 and a low-temperature liquid level sensor 16 are arranged on the lower side surface of the inner cylinder body 2, and a high-temperature liquid level indicator 17 and a high-temperature liquid level sensor 18 are arranged on the upper side surface of the outer cylinder body 1 and between the high-temperature liquid inlet pipe 13 and the upper cover plate 4.
This condenser is when moving, low temperature liquid gets into in the intermediate layer 3 through low temperature feed liquor pipe 10, low temperature liquid during upflow with from steam intake pipe 11 steam direct contact, low temperature liquid is heated by steam and continues upflow, high temperature liquid after the heating flows out from high temperature drain pipe 12 and flows into interior barrel 2 through the nozzle from high temperature feed liquor pipe 13, high temperature liquid is spout through spray set 7, from the even flow down of netted liquid film ball 6 in upper portion, the net surface of liquid film ball is covered with to liquid, netted liquid film ball 6 has very big water film surface area, because interior barrel 2 internal pressure is low, barrel 2 flash evaporation in the high temperature liquid gets into, the gas of evaporation is discharged through upper portion low pressure steam outlet pipe 8, unevaporated liquid becomes low temperature liquid and discharges from interior barrel 2 lower part low temperature drain pipe 14. The low-temperature liquid with different temperatures can be obtained by controlling the pressure inside the inner cylinder body 2 and the liquid inlet amount of the high-temperature liquid. The flow of the low-temperature liquid flowing in is controlled by a low-temperature liquid inlet control valve 101; the flow of the inflow steam is controlled by a steam inlet control valve 111; acquiring the water level in the interlayer 3 through a high-temperature liquid level sensor 18; the flow of the high-temperature liquid entering the inner cylinder body 2 is controlled by the high-temperature liquid inlet control valve 131; acquiring the water level of the inner cylinder through a low-temperature liquid level sensor 16; the low-temperature liquid outflow control valve 141 controls the outflow flow rate of the low-temperature liquid; the flow of the discharged steam is controlled by a vacuum device and a low-pressure steam outlet control valve 81 which are connected with the outside of the low-pressure steam outlet pipe 8, so as to control the pressure in the inner cylinder 2; the pressure in the jacket 3 is controlled by the jacket exhaust control valve 91.
Example two:
in combination with the first embodiment, referring to fig. 2, the low-pressure steam outlet pipe 8 is connected to an air extracting device, so that the low-pressure steam can be better exhausted and the pressure in the inner cylinder 2 can be better controlled through the air extracting device. A water distribution pipe is arranged on the low-temperature liquid inlet pipe 10, the low-temperature liquid outlet pipe 14 is connected with the water distribution pipe, a circulating pump 19 and a low-temperature liquid discharge pipe 20 are arranged on the low-temperature liquid outlet pipe 14, and a low-temperature liquid discharge control valve 201 is arranged on the low-temperature liquid discharge pipe 20. The low-temperature water can be discharged for other use, and can also circularly enter the lower part of the interlayer 3 to continuously and repeatedly circulate. This condenser does not need other low temperature cold source, adopts partial steam to do and draws power of penetrating the drive production for high-temperature liquid self evaporates and makes low-temperature liquid, and low-temperature liquid goes the new steam of condensation again. The high-temperature liquid outlet pipe 12 is provided with a high-temperature liquid separating pipe 22, the high-temperature liquid separating pipe 22 is provided with a high-temperature liquid separating pipe control valve 221, and the high-temperature liquid separating pipe 22 can be connected to a boiler to supply water for the boiler.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (9)
1. Netted liquid film ball is from evaporative steam condenser, including outer barrel, its technical characterstic is: an inner barrel is arranged in the outer barrel, an interlayer is arranged between the outer barrel and the inner barrel, an upper cover plate is arranged at the top of the outer barrel, and a lower bottom plate is arranged at the bottom of the outer barrel;
a packing area and a spraying device are arranged in the inner cylinder body, the packing area is arranged in the middle of the inner cylinder body, packing is filled in the packing area, and the spraying device is arranged above the packing area;
a low-temperature liquid inlet pipe is arranged on the side surface of the lower part of the outer barrel and communicated with the interlayer, a steam inlet pipe is arranged above the low-temperature liquid inlet pipe and communicated with the interlayer, a high-temperature liquid outlet pipe is arranged on the side surface of the upper part of the outer barrel, a high-temperature liquid inlet pipe is arranged above the high-temperature liquid outlet pipe, one end of the high-temperature liquid inlet pipe is connected with the spraying device of the inner barrel, one end of the high-temperature liquid outlet pipe is communicated with the interlayer, and the other end of the high-temperature liquid;
the low-pressure steam exhaust pipe is communicated with the interlayer, the interlayer exhaust pipe is provided with a control valve for the interlayer exhaust pipe, the lower bottom plate is provided with a low-temperature liquid outlet pipe, the low-temperature liquid outlet pipe is provided with a low-temperature liquid outlet control valve, and the low-temperature liquid outlet pipe is communicated with the inner cylinder.
2. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: the high-temperature liquid inlet pipe is provided with a high-temperature liquid inlet control valve, the low-temperature liquid inlet pipe is provided with a low-temperature liquid inlet control valve, and the steam inlet pipe is provided with a steam inlet control valve.
3. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1 or 2, wherein: the low-temperature liquid inlet pipe and the steam inlet pipe are both provided with a plurality of same liquid inlet pipes, the low-temperature liquid inlet pipes are same in height, and the steam inlet pipes are same in height.
4. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 3, wherein: the low-temperature liquid outlet pipe is connected with the low-temperature liquid inlet pipe, a circulating pump and a low-temperature liquid discharge pipe are arranged on the low-temperature liquid outlet pipe, and a low-temperature liquid discharge control valve is arranged on the low-temperature liquid discharge pipe.
5. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: the high-temperature liquid outlet pipe is provided with a high-temperature liquid separating pipe, and a high-temperature liquid separating pipe control valve is arranged on the high-temperature liquid separating pipe.
6. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: the filler in the filler area is a reticular liquid membrane ball, the inside of the ball body of the reticular liquid membrane ball is hollow, and the spherical surface is reticular.
7. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: and a low-temperature liquid level indicator and a low-temperature liquid level sensor are arranged on the side surface of the lower part of the inner cylinder body.
8. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: and a high-temperature liquid level indicator and a high-temperature liquid level sensor are arranged on the side surface of the upper part of the outer cylinder body and between the high-temperature liquid inlet pipe and the upper cover plate.
9. The reticulated liquid film sphere self-evaporating steam condenser as claimed in claim 1, wherein: and a heat insulation layer is arranged on the outer side of the outer cylinder body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010251157.7A CN111306963A (en) | 2020-04-01 | 2020-04-01 | Self-evaporation type steam condenser with netted liquid film ball |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010251157.7A CN111306963A (en) | 2020-04-01 | 2020-04-01 | Self-evaporation type steam condenser with netted liquid film ball |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111306963A true CN111306963A (en) | 2020-06-19 |
Family
ID=71151715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010251157.7A Pending CN111306963A (en) | 2020-04-01 | 2020-04-01 | Self-evaporation type steam condenser with netted liquid film ball |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111306963A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114162892A (en) * | 2021-11-30 | 2022-03-11 | 华能营口热电有限责任公司 | Desulfurization slurry flash evaporation heat extraction system capable of preventing slurry blockage and working method thereof |
-
2020
- 2020-04-01 CN CN202010251157.7A patent/CN111306963A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114162892A (en) * | 2021-11-30 | 2022-03-11 | 华能营口热电有限责任公司 | Desulfurization slurry flash evaporation heat extraction system capable of preventing slurry blockage and working method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101191683B (en) | Jet flow circulated sprinkling falling-film evaporator | |
| CN201261726Y (en) | Novel efficient heat pump sea water desalting apparatus | |
| CN201152648Y (en) | Falling film evaporative cooling refrigeration set | |
| CN104456786B (en) | Evaporation cooling and mechanical refrigeration combined integrated air conditioning unit | |
| JP2011011202A (en) | Evaporation type seawater desalination apparatus using phase-change medium | |
| CN103740567B (en) | High-temperature steam cooling system | |
| CN111747468B (en) | Vacuum low-temperature evaporation and concentration system of heat pump | |
| CN100389294C (en) | Second lithium bromide absorption type heat pump for preparing steam by using vertical double-side falling-film absorber | |
| CN107537167A (en) | Evaporating, concentrating and crystallizing system and evaporation process method | |
| CN113237367A (en) | Warm water drainage loop heat pipe cooling device and method utilizing solar energy | |
| CN111306963A (en) | Self-evaporation type steam condenser with netted liquid film ball | |
| KR102059179B1 (en) | Concentration-apparatus for food | |
| CN207270730U (en) | Evaporating, concentrating and crystallizing system | |
| CN211926578U (en) | Self-evaporation type steam condenser with netted liquid film ball | |
| CN108662802A (en) | Green heat pump refrigerating heating system, refrigerating and heating method and air-conditioning | |
| CN206974220U (en) | Evaporate the spraying cooling mechanism of cold refrigeration plant | |
| CN108662915A (en) | The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect | |
| KR890004393B1 (en) | Air cooling type absorption cooler | |
| CN201510766U (en) | Plate-type falling-film evaporator | |
| CN209386840U (en) | A kind of cooling tower of recyclable evaporation water | |
| CN209371575U (en) | A kind of condenser with new gas heat exchanger | |
| CN206184013U (en) | System for utilize air heat pump low temperature evaporative concentration alcohol waste liquid | |
| CN106267870A (en) | A kind of closed circuit economic benefits and social benefits alcohol concentrates unit and method for concentration thereof | |
| CN102230751A (en) | Vacuum evaporation cooling device | |
| CN106927527B (en) | Low-energy-consumption water purifier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |