CN107976087A - Adverse current no-arbitrary pricing double-curve cooling column - Google Patents
Adverse current no-arbitrary pricing double-curve cooling column Download PDFInfo
- Publication number
- CN107976087A CN107976087A CN201711422638.4A CN201711422638A CN107976087A CN 107976087 A CN107976087 A CN 107976087A CN 201711422638 A CN201711422638 A CN 201711422638A CN 107976087 A CN107976087 A CN 107976087A
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- China
- Prior art keywords
- rotating
- tower body
- spray
- tower
- honeycomb
- Prior art date
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/02—Direct-contact trickle coolers, e.g. cooling towers with counter-current only
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
-
- 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
- F28F25/04—Distributing or accumulator troughs
-
- 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
-
- 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
- F28F25/10—Component parts of trickle coolers for feeding gas or vapour
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention provides adverse current no-arbitrary pricing double-curve cooling column, including tower body, V-shaped dehydrater, rotating-spray water distributing trough, rotary jet, honeycomb, anti-wall flow plate, maintenance door, air inlet, into tower water pipe, collecting-tank and wind-collecting cover；V-shaped dehydrater is located at the lower section of tower body；Rotating-spray water distributing trough is located in tower body below V-shaped dehydrater；Rotary jet is in the uniformly distribution straggly of rotating-spray water distributing trough bottom；Heat exchange space is contacted with air inversion for rotating-spray water droplet between rotating-spray water distributing trough and honeycomb；Honeycomb is equipped with below rotating-spray water distributing trough；Air inlet is equipped between honeycomb and collecting-tank, is located at into tower water pipe below air inlet；Wind-collecting cover is arranged at tower body outer wall and along air inlet along setting, and anti-wall flow plate is located under tower body along nozzle surrounding.The present invention advantageous effects be cooling effect stablize, and more preferably, the energy conservation and environmental protection of low-maintenance.
Description
Technical field
Present invention relates to a kind of circulating water cooling tower field, more particularly to adverse current no-arbitrary pricing double-curve cooling column.
Background technology
Cooling tower is that heat exchange is carried out after being contacted using recirculated water with air flow, radiated using steam, convection current heat transfer and
The principles such as radiant heat transfer disperse the water after the waste heat produced in power generator system is cooled through water pump lifting heat-exchange system,
To ensure the normal operation of system.
Domestic and international double-curve cooling column of the prior art, widely used traditional fixation reflex nozzle and high density are filled out
, there is the high-density packing double-curve cooling column of multiple waveforms in material, from the point of view of service condition is developed, reverse-flow filler hyperbola
The cold effect of cooling tower is difficult holding and raising, and the easy aging of filler, fouling when such cooling tower is run, resistance is big, fouling occurs
Cold effect declines obvious afterwards, need to be continuously added substantial amounts of scale remover scale removal, keeps the hydrophily of filler and could maintain cold effect, operation dimension
Protect of high cost.
Adverse current no-arbitrary pricing double-curve cooling column of the present invention operationally, can ensure that and improve cold effect, and operation expense
It is low.
The content of the invention
The object of the present invention is to provide a kind of cooling effect stabilization, and more preferably, the energy conservation and environmental protection adverse current no-arbitrary pricing of low-maintenance
Double-curve cooling column.
According to an aspect of the invention, there is provided adverse current no-arbitrary pricing double-curve cooling column, including the water removal of tower body, V-shaped
Device, rotating-spray water distributing trough, rotary jet, honeycomb, anti-wall flow plate, maintenance door, air inlet, into tower water pipe, collection
Pond and wind-collecting cover；Tower body is wind tubular construction, and V-shaped dehydrater is located at the lower section inside tower body；Rotating-spray water distributing trough position
In tower body below V-shaped dehydrater；Rotary jet is in the uniformly distribution straggly of rotating-spray water distributing trough bottom；Rotating-spray water distribution
Honeycomb is equipped with below groove；It is inverse for rotating-spray water droplet and air between rotating-spray water distributing trough and honeycomb
Flow the heat exchange space of contact；Tower body bottom is equipped with collecting-tank, air inlet is equipped between honeycomb and collecting-tank, into tower
Water pipe is located at below air inlet；Wind-collecting cover is arranged at tower body outer wall and along air inlet along setting, and maintenance door is arranged at tower body
Outer wall；Anti-wall flow plate side is connected to tower body inner wall and is located at water drenching grid beam lower edge, and anti-wall flow plate and tower body side wall are in 30-
60 ° of angles, anti-wall flow plate surface are evenly equipped with multiple osculums.
In some embodiments, V-shaped dehydrater is arranged parallel to each other by multiple V-shaped pieces and formed, and passes through connecting rod
It is fixed.So that water rem oval higher, intensity are high, be unlikely to deform, service life is longer than traditional dehydrater.
In some embodiments, rotary jet include three-point support, lead-type injection pallet, rotating-spray impeller,
Stainless steel wear-resisting shaft, wear-resisting ring, water inlet, nozzle and duplex bearing, water inlet are connected with nozzle, into tower water pipe respectively, tripodia branch
Frame is fixed on rotating-spray water distribution trench bottom, and stainless steel wear-resisting shaft is arranged at the center at three-point support bottom, lead-type injection
Pallet is rotatably disposed in stainless steel wear-resisting shaft by duplex bearing, is provided between duplex bearing and lead-type injection pallet wear-resisting
Circle, water inlet and nozzle may be contained within inclining on three-point support and positioned at the surface of lead-type injection pallet, rotating-spray impeller
Inclined is distributed in the outer shroud week of lead-type injection pallet；Lead-type injection tray surface circumferential direction is evenly equipped with multiple raised arcs and leads
Line, the incline direction of arc conducting wire is with the incline direction of rotating-spray impeller on the contrary, arc conducting wire is close to rotating-spray impeller
One end is between two adjacent rotating-spray impellers.Stainless steel wear-resisting shaft can avoid wearing in continuous operation, remain
The current cracking that rotation spray projects produces uniform fine liquid particles, ensure that the contact area with unsaturated air, imitates cooling
Fruit is stable and improves.Setting straggly can prevent the generation of hollow phenomenon；In addition, the arc conducting wire on lead-type injection pallet can
Play and the water that lead-type is sprayed on pallet is uniformly accumulated into multiple tracks current, improve impact force of the current to injection impeller, improve
The rotating speed of impeller is sprayed, and then current cracking is produced more tiny water droplet, heat exchange efficiency is improved, in addition, arc conducting wire inclines
The incline direction of tilted direction and rotating-spray impeller is on the contrary, arc conducting wire is adjacent positioned at two close to one end of rotating-spray impeller
Between rotating-spray impeller, impact force of the current to injection impeller can be also further improved, improves the rotating speed of rotating-spray impeller,
Improve heat exchange efficiency.
In some embodiments, honeycomb is bonded hexagonal cell shape structure by multiple knee-pieces and plain film
Body, plays air conducting, makes air draught even into tower chamber without producing vortex flow, and fine liquid particles are in the effect of gravity
Lower uniformly falling falls into collecting-tank after carrying out secondary cooling to honeycomb；Wherein multiple knee-pieces are first bonded into multiple hexagonals
Shape honeycomb molded body, then multiple hexagonal cell shape structures successively bonding form, in two adjacent hexagon bees
Plain film is inserted between nest shape structure, plain film can be bonded between hexagonal cell shape structure, and plain film can increase honeycomb
The bearing capacity of shape rectifier.
In some embodiments, wind-collecting cover includes fan-shaped glass steel body, frame and supporting rod, fan-shaped glass steel body side
Tower body is fixed on, fan-shaped glass steel body is arranged in frame, and frame is fixed in supporting rod one end, and the other end is supported in ground.By
This, can form funnelling between fan-shaped glass steel body and ground, improve the efficiency of air inlet inlet air.
In some embodiments, wind-collecting cover is equipped with multiple rolling screen door close to the side of air inlet, and rolling screen door can be adjusted
The intake size of air inlet.Thus when temperature is too low, in order to ensure normal operating temperature in cooling tower, control can be passed through
Part rolling screen door processed is closed, and to control the intake of air inlet, it is normal operating temperature that can ensure the temperature in cooling tower.
In some embodiments, anti-wall flow plate is evenly equipped with multiple sinks, each sink successively from inner side edge to outer side edges
Multiple osculums are inside evenly equipped with, are equipped with drainage trough between two neighboring sink, the inner side edge of the diameter of osculum from anti-wall flow plate
Become larger to the direction of outer side edges.
Brief description of the drawings
Fig. 1 is the structure diagram of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 2 is the structure diagram of the V-shaped dehydrater of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 3 is the side view of the V-shaped dehydrater of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 4 is the rotary jet structure diagram of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 5 is sectional views of the Fig. 4 along A-A directions；
Fig. 6 is the structure diagram of the wind-collecting cover of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 7 is the structure diagram of the honeycomb of adverse current no-arbitrary pricing double-curve cooling column of the present invention；
Fig. 8 is the sectional view of the honeycomb of adverse current no-arbitrary pricing double-curve cooling column of the present invention.
Fig. 9 is the anti-wall flow plate structure schematic diagram of the present invention；
Figure 10 is the anti-wall flow plate side view of the present invention；
Figure 11 is another example structure schematic diagram of anti-wall flow plate of the present invention.
Embodiment
Further detailed description explanation is carried out to technical scheme with reference to specific embodiment.
As shown in figures 1-8, adverse current no-arbitrary pricing double-curve cooling column includes：Tower body 1, V-shaped dehydrater 2, rotating-spray are matched somebody with somebody
Sink 6, rotary jet 8, honeycomb 11, air inlet 14, into tower water pipe 4, maintenance door 35, collecting-tank 15 and wind-collecting cover
5。
Tower body 1 is large-scale housing structure, is specifically wind tubular construction, can be according to builder not in actual construction
With requirement, material of the suitable material as tower body is selected.In certain embodiments of the present invention, when need build Large Towers
When, tower body material is concrete, when needing to build medium-sized tower, and tower body material is fiberglass.
V-shaped dehydrater 2 is located at the middle lower section inside tower body 1, and positioned at the top of rotating-spray water distributing trough in tower 6, V-shaped
Dehydrater 2 can be fixed on 1 inner wall of tower body by frame body, and V-shaped dehydrater 2 is arranged parallel to each other by multiple V-shaped pieces 21
Composition, and fixed by connecting rod 22, specifically connecting rod 22 rushes across each V-shaped piece 21 and is fixed.Rotary jet 8 and bee
It is a space between nest shape rectifier 11, which provides the fine liquid particles that rotary jet sprays and contacted with unsaturated air
Carry out the heat transfer space of heat exchange；Rotating-spray water distributing trough can be fixed by the bracket the middle and lower part for being installed on tower, and be located at V words
Below shape dehydrater, rotating-spray water distributing trough 6 is fixedly installed in the inner wall of tower body 1.In the present embodiment, rotary jet 8 can
Multiple to be arranged to, rotary jet 8 is fixedly installed in 6 bottom of rotating-spray water distributing trough and straggly is uniformly distributed.
It is wear-resisting that rotary jet 8 includes three-point support 81, lead-type injection pallet 82, rotating-spray impeller 83, stainless steel
Axis 84, wear-resisting ring 85, water inlet 86, nozzle 87 and duplex bearing 88, water inlet 86 are connected with nozzle 87, into tower water pipe 4 respectively, and three
Foot support 81 is fixedly installed in 6 bottom of rotating-spray water distributing trough, and stainless steel wear-resisting shaft 84 is fixedly installed on 81 bottom of three-point support
Center, lead-type injection pallet 82 are rotatably mounted to stainless steel wear-resisting shaft 84 by duplex bearing 88, and duplex bearing 88 is with leading
Wear-resisting ring 85 is provided between line style injection pallet 82, water inlet 86 and nozzle 87 may be contained within three-point support 81 and are located to lead
Line style sprays the surface of pallet 82.In the present embodiment, rotating-spray impeller 83 is multiple that rotating-spray impeller 83 is distributed in
In the outer shroud week of lead-type injection pallet 82, specifically, rotating-spray impeller 83 be rectangular configuration, its can weld or it is integral into
Type sprays 82 upper side of pallet in lead-type, and positioned at the edge of lead-type injection pallet 82, the axis of rotating-spray impeller 83
Without the center of lead-type injection pallet 82, in the present embodiment, axis and the rotating-spray leaf of rotating-spray impeller 83
Tangent line at 45 ° angle of the wheel 83 on 82 junction of lead-type injection pallet.Lead-type injection 82 surface circumferential direction of pallet is evenly equipped with
Multiple raised arc conducting wires 821, the incline direction of arc conducting wire 821 is with the incline direction of rotating-spray impeller 83 on the contrary, arc
Shape conducting wire 821 is close to one end of rotating-spray impeller 83 between two adjacent rotating-spray impellers 83.Thus, lead-type sprays
The arc conducting wire penetrated on pallet can be played uniformly accumulates multiple tracks current by the water that lead-type is sprayed on pallet, improves current pair
The impact force of impeller is sprayed, improves the rotating speed of injection impeller, and then current cracking is produced more tiny water droplet, improves heat exchange effect
Rate, in addition, the incline direction of the incline direction of arc conducting wire and rotating-spray impeller on the contrary, arc conducting wire close to rotating-spray leaf
One end of wheel can also further improve impact force of the current to injection impeller, carry between two adjacent rotating-spray impellers
The rotating speed of high rotating-spray impeller, improves heat exchange efficiency
The lower section of rotary jet 8 is equipped with honeycomb 11, and honeycomb 11 can pass through cellular rectification
Device frame is fixedly mounted in tower body 1, and 11 hexagonal honeycomb structure of honeycomb, it is by multiple honeycombs
Knee-piece and plain film are bonded, and honeycomb 11 is uniformly covered with whole honeycomb frame, and air-flow can be made uniform
Enter tower chamber without producing vortex, add the relative velocity of gas liquid interfacial area, the tiny water that rotary jet 8 sprays
Drop does not produce assembly, and water droplet is uniformly distributed whereabouts, and sufficient heat exchange is obtained with unsaturated air.The lower section of honeycomb fashion rectifier rack 11
For air inlet 14, air inlet 14 can be opened in tower body 1, and collecting-tank 15 is arranged in the soil under tower body 1.
While adverse current rotating-spray cooling tower projects current by rotary jet, it is refined into current cracking numerous
Fine liquid particles, the contact area with unsaturated air is added, on the other hand, by the dynamic of the water droplet directive tower chamber of rotating-spray
It can be made sufficiently to contact and perturb with air-flow, exchanged beneficial to the caloic of aqueous vapor, accelerate water droplet cooling velocity, it is thin when injection
Small water droplet, adverse current to honeycomb, collecting-tank is fallen into after carrying out secondary cooling under gravity.Tower intracavitary air-flow
Constantly perturb, add the relative velocity of gas liquid interfacial area, enhance the heat exchange efficiency of adverse current rotating-spray tower, so that reject
Filler.
When cooling tower is run, the saturated moist air in tower is mingled with numerous fine liquid particles, its composition of leading the way of V-shaped dehydrater
Unique hyperspace, flowing resistance is small, effectively controls the vortex phenomenon in tower, avoids the easy drift of fine liquid particles in tower
The problem of outer increase circulation water consume, environmental pollution is avoided, improves the destabilizing factor of tower intracavitary fluidised form, water rem oval obtains
Further improve.
Consolidate in addition, wind-collecting cover 5 includes fan-shaped glass steel body 51, frame 52 and supporting rod 53, fan-shaped 51 side of glass steel body
Due to tower body 1, fan-shaped glass steel body 51 is arranged in frame 52, and frame 52 is fixed in 53 one end of supporting rod, and the other end is supported in
Ground.Thus, funnelling can be formed between fan-shaped glass steel body and ground, improves the efficiency of air inlet inlet air.
Wind-collecting cover 5 is equipped with multiple rolling screen door 54 close to the side of air inlet 14, and rolling screen door 54 can adjust air inlet 14
Intake size.Thus when temperature is too low, in order to ensure normal operating temperature in cooling tower, control unit bundling can be passed through
Curtain door is closed, and to control the intake of air inlet, it is normal operating temperature that can ensure the temperature in cooling tower.
As shown in Figures 9 and 10, anti-wall flow plate 28 is further included, 28 side of anti-wall flow plate is connected to 6 inner wall of tower body and is located at bee
11 lower edge of nest shape rectifier, anti-wall flow plate 28 and 6 side wall of tower body are in 30-60 ° of angle, in the present embodiment, anti-wall flow plate 28 and tower
6 side wall of body is in 40 ° of angles.As shown in figure 11, in another embodiment, 28 surface of anti-wall flow plate is evenly equipped with multiple osculums 281, can
So that current are dripped by osculum 281, prevent waterfall shape current from producing, add the heat exchange area between water droplet and air,
Improve heat exchange efficiency.Anti-wall flow plate 28 is evenly equipped with multiple sinks 282 successively from inner side edge to outer side edges, in each sink 282
Multiple osculums 281 are evenly equipped with, thus, it is possible to make current be more prone to discharge by osculum 281, two neighboring sink 282
Between be equipped with drainage trough 283, thereby, it is possible to which the water in a upper drainage trough is drained into next drainage trough, osculum 281
Direction of the diameter from the inner side edge of anti-wall flow plate 28 to outer side edges become larger, thus, it is possible to drip each osculum 281
The similar size of water droplet, can make that current are decomposed more uniformly, improve heat exchange efficiency.It is anti-thereby, it is possible to solve tradition
Wall flowing plate edge easily forms the current of waterfall shape, and the problem of cause the heat exchange efficiency between air low.Need what is illustrated
It is that the inner side edge of anti-wall flow plate 28 is the side being connected with 6 side wall of tower body, and outer side edges are the side opposite with inner side edge.In addition,
Osculum 281 can also be corresponded in the underface of osculum 281 multiple top fluidization towers are set, top fluidization tower can be consolidated by connecting rod
Dingan County is loaded on the side wall of tower body 6, the tapered structure in top fluidization tower top, and the water droplet thus dripped from osculum 281 strikes top again
When at the top of fluidization tower, the water droplet of smaller, increase and the contact area of air can be broken down into, improves heat exchange efficiency.
The adverse current no-arbitrary pricing double-curve cooling column of the present invention so operates：The pump machine of ON cycle water system, catchments
High-temperature water in pond 15 passes through the water inlet 14 that rotary jet 8 is sent into tower water pipe, then is sprayed by nozzle 87, and high-temperature water falls
On lead-type injection pallet 82, pass through the thrust between high-temperature water and rotating-spray impeller 83 so that lead-type sprays pallet 82
Rotation, and make high-temperature water by rotation spray, rotation spray project water droplet it is uniform, tiny, so as to through honeycomb 11
The unsaturated air of entrance fully carries out heat exchange；The fine liquid particles that rotary jet 8 ejects are in gravity and uniform air flow shadow
Ring lower even drop down and carry out secondary cooling to honeycomb 11, fall into collecting-tank 15, then followed by what water pump output had cooled down
After ring water to each heat transmission equipment, cooling tower is again returned to, is recycled in cycles.
It should be appreciated that although this specification is described according to embodiment, not each embodiment is only only comprising one
Vertical technical solution, this narrating mode of specification is only that those skilled in the art should be by specification for clarity
As an entirety, the technical solutions in the various embodiments may also be suitably combined, formed it will be appreciated by those skilled in the art that
Other embodiment.
Those listed above is a series of to describe illustrating only for possible embodiments of the invention in detail,
They simultaneously are not used to limit the scope of the invention, all to should be included in this without departing from the equivalent embodiment of the present invention or change
Within the protection domain of invention.
Claims (7)
1. adverse current no-arbitrary pricing double-curve cooling column, it is characterised in that it includes tower body, V-shaped dehydrater, rotating-spray water distribution
Groove, rotary jet, honeycomb, anti-wall flow plate, maintenance door, air inlet, into tower water pipe, collecting-tank and wind-collecting cover；Institute
It is wind tubular construction to state tower body, and the V-shaped dehydrater is located at the lower section inside the tower body；The rotating-spray water distributing trough position
Below the V-shaped dehydrater described in tower body；The rotary jet is straggly point uniform in the rotating-spray water distribution trench bottom
Cloth；The honeycomb is equipped with below the rotating-spray water distributing trough；The rotating-spray water distributing trough and cellular rectification
The heat exchange space contacted between device for rotating-spray water droplet with air inversion；The tower body bottom is equipped with the collecting-tank, institute
State and the air inlet is equipped between honeycomb and the collecting-tank, it is described to be located at into tower water pipe below the air inlet；
The wind-collecting cover is arranged at tower body outer wall and along the air inlet along setting, and the maintenance door is arranged at the outer wall of tower body；Institute
Anti-wall flow plate side is stated to be connected to the tower body inner wall and be located at the honeycomb lower edge, the anti-wall flow plate with it is described
Tower body side wall is in 30-60 ° of angle, and the anti-wall flow plate surface is evenly equipped with multiple osculums.
2. adverse current no-arbitrary pricing double-curve cooling column according to claim 1, it is characterised in that the V-shaped dehydrater by
Multiple V-shaped pieces are arranged parallel to each other composition, and are fixed by connecting rod.
3. adverse current no-arbitrary pricing double-curve cooling column according to claim 1, it is characterised in that the rotary jet includes
Three-point support, lead-type injection pallet, duplex bearing, rotating-spray impeller, stainless steel wear-resisting shaft, wear-resisting ring, water inlet and nozzle,
The water inlet respectively with the nozzle, it is described connected into tower water pipe, the three-point support is fixed on the rotating-spray water distribution
Trench bottom, the stainless steel wear-resisting shaft are fixed on the center at three-point support bottom, and the lead-type injection pallet passes through twin shaft
Hold and be rotatably disposed in stainless steel wear-resisting shaft, the wear-resisting ring, institute are provided between duplex bearing and lead-type the injection pallet
State water inlet and nozzle may be contained within three-point support and positioned at the surface of lead-type injection pallet, the rotating-spray
The inclined formula of impeller is distributed in the outer shroud week of lead-type injection pallet；The lead-type injection tray surface circumferential direction is evenly equipped with multiple
Raised arc conducting wire, the incline direction of the arc conducting wire is with the incline direction of rotating-spray impeller on the contrary, the arc is led
Line is close to one end of rotating-spray impeller between two adjacent rotating-spray impellers.
4. adverse current no-arbitrary pricing double-curve cooling column according to claim 1, it is characterised in that the honeycomb by
Multiple knee-pieces and plain film are bonded hexagonal cell shape structure.
5. adverse current no-arbitrary pricing double-curve cooling column according to claim 1, it is characterised in that the wind-collecting cover includes sector
Tower body is fixed in glass steel body, frame and supporting rod, the sector glass steel body side, and fan-shaped glass steel body is arranged at the frame
In frame, frame is fixed in described supporting rod one end, and the other end is supported in ground.
6. adverse current no-arbitrary pricing double-curve cooling column according to claim 5, it is characterised in that the wind-collecting cover is close to inlet air
The side of mouth is equipped with multiple rolling screen door, and the rolling screen door can adjust the intake size of air inlet.
7. adverse current no-arbitrary pricing double-curve cooling column according to claim 1, it is characterised in that the anti-wall flow plate is from inner side
Side is evenly equipped with multiple sinks to outer side edges successively, and multiple osculums are evenly equipped with each sink, two neighboring described
Drainage trough is equipped between sink, the inner side edge of diameter from the anti-wall flow plate of the osculum gradually becomes to the direction of outer side edges
Greatly.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711422638.4A CN107976087A (en) | 2017-12-25 | 2017-12-25 | Adverse current no-arbitrary pricing double-curve cooling column |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711422638.4A CN107976087A (en) | 2017-12-25 | 2017-12-25 | Adverse current no-arbitrary pricing double-curve cooling column |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107976087A true CN107976087A (en) | 2018-05-01 |
Family
ID=62007732
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711422638.4A Withdrawn CN107976087A (en) | 2017-12-25 | 2017-12-25 | Adverse current no-arbitrary pricing double-curve cooling column |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107976087A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109357544A (en) * | 2018-11-15 | 2019-02-19 | 江苏中兴药业有限公司 | A kind of water collection type cooling tower with high cooling efficiency |
| CN109851501A (en) * | 2019-03-20 | 2019-06-07 | 江苏索普（集团）有限公司 | Ethyl acetate integration system is for tower |
| CN110514028A (en) * | 2019-09-09 | 2019-11-29 | 陆洪新 | Adverse current double-curve cooling column |
| CN112833700A (en) * | 2021-01-31 | 2021-05-25 | 厦门金名节能科技有限公司 | Efficient water distribution nozzle for cooling tower |
-
2017
- 2017-12-25 CN CN201711422638.4A patent/CN107976087A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109357544A (en) * | 2018-11-15 | 2019-02-19 | 江苏中兴药业有限公司 | A kind of water collection type cooling tower with high cooling efficiency |
| CN109851501A (en) * | 2019-03-20 | 2019-06-07 | 江苏索普（集团）有限公司 | Ethyl acetate integration system is for tower |
| CN110514028A (en) * | 2019-09-09 | 2019-11-29 | 陆洪新 | Adverse current double-curve cooling column |
| CN112833700A (en) * | 2021-01-31 | 2021-05-25 | 厦门金名节能科技有限公司 | Efficient water distribution nozzle for cooling tower |
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Application publication date: 20180501 |
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