CN201016625Y - Anti-block fluid dispersing means - Google Patents
Anti-block fluid dispersing means Download PDFInfo
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- CN201016625Y CN201016625Y CNU2006200364691U CN200620036469U CN201016625Y CN 201016625 Y CN201016625 Y CN 201016625Y CN U2006200364691 U CNU2006200364691 U CN U2006200364691U CN 200620036469 U CN200620036469 U CN 200620036469U CN 201016625 Y CN201016625 Y CN 201016625Y
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Abstract
The utility model discloses an anti-clogging fluid dispersion apparatus. A blind plate (11) is on the top end of a constant pressure box (13) and a flange (8) is on the bottom end. The constant pressure fluid box (13) top is connected with three to eight fluid inlet tubes, the outer end of which is connected with a dispersion head (12). The fluid inlet tube is connected with a lateral tangent of the dispersion head (12), a top inner cavity is like a reverted cone. The utility model has a good atomization effect, and a long service life. In addition, the utility is difficult to be blocked and is easy to cool and clean. Thereby the utility model can be widely used in petrochemical industry, chemical industry, chemical fiber industry, chemical fertilizer industry, coking industry, metallurgical industry, light industry, biochemical equipment, pharmaceutical equipment, leeching equipment as well as flue duct removal equipment.
Description
Technical field
The utility model relates to block-resistant type fluid dispersal device, especially relates to a kind of block-resistant type fluid dispersal device that extensively applies in industrial civilian circulating water cooling tower, drip washing equipment and the cleaner.
Background technology
The cooling device of packed tower has experienced with bamboo chip, cement grid, the PVC plastics development course as cooling element, no matter these packed towers adopt above-mentioned which kind of cooling element, the cooling element ubiquity of packed tower is aging, distortion, embrittlement, collapse, problems such as obstruction, channel, thereby influence is produced and process equipment, and along with the packed tower growth of running time, clean cooling element and strengthened operating cost, influenced production, particularly used PVC plastics as cooling element, useless PVC plastics after the replacing irregularly can cause severe contamination to environment.
Summary of the invention
It is good that the purpose of this utility model provides a kind of atomizing effect, is convenient to cooling and cleaning, and be difficult for stopping up the block-resistant type fluid dispersal device of long service life.
In order to achieve the above object, the utility model adopts following technical scheme: a kind of block-resistant type fluid dispersal device, and there is blind plate the upper end of weighing apparatus hydraulic fluid case, and there is flange its lower end, the top of weighing apparatus hydraulic fluid case is connected with 3-8 root fluid and enters pipe, and the outer end that every fluid enters pipe is connected with the dispersion head.
Described to disperse the inside of head be cavity body, and this cavity body communicates by the inner chamber that fluid enters Guan Yuheng hydraulic fluid case, and fluid enters pipe and is connected on the outside tangent line that disperses head, and it is tapered to disperse the top inner chamber body of head to be rounding.
Described dispersion head is connected as a single entity by three ones of upper, middle and lower, and its top is cavity cylinder or cavity inverted cone, and the middle part is the cavity cone, and the bottom is cavity cylinder or cavity hemisphere.
Described weighing apparatus hydraulic fluid case is connected as a single entity by the upper and lower, and its inside is cavity body, and the top of weighing apparatus hydraulic fluid case is the cavity cylinder, and the bottom is the cavity Rotary-table.
Described fluid enters pipe and constitutes for the 2-section pipe road, and the 2-section pipe road connects by flange.
The top of weighing apparatus hydraulic fluid case of the present utility model is connected with 3-8 root fluid and enters pipe, the outer end that every fluid enters pipe is connected with the dispersion head, fluid is through weighing apparatus hydraulic fluid case, fluid enters pipe and enters the dispersion head, because fluid enters pipe and is connected on the outside tangent line that disperses head, disperse the top inner chamber body of head to be rounding tapered (delivery port is less), fluid forms the high speed centrifugation motion in weighing apparatus hydraulic fluid case, become spray pattern after disperse head that fluid is separated into small dynamic fluid flow particle shape, be convenient to the effect in cooling tower, playing cooling effect and in drip washing equipment and cleaner, play absorbing medium like this, and because weighing apparatus hydraulic fluid case of the present utility model, fluid enters pipe and disperses head all is the cavity body structure, thereby be difficult for stopping up, because weighing apparatus hydraulic fluid case is by metalwork (carbon steel, cast steel, cast iron, stainless steel etc.) and organic material (engineering plastics, fiberglass, PVC, UPVC etc.) part constitutes, fluid disperses head by metal (carbon steel, cast steel, cast iron, stainless steel etc.) and organic material (engineering plastics, fiberglass, PVC, UPVC etc.) make long service life.
The utility model has the advantages that: atomizing effect is good, and is difficult for stopping up long service life.When it is used for cooling tower, utilization block-resistant type fluid dispersal device is with being the cooling dispersive element, no any filler in the cooling tower, all drawbacks have obtained elimination, operational effect is stable, and the life-span is long, does not have to freeze and extension ice phenomenon, simultaneously because of non-filler, the Tower System resistance reduces, and the shaft power of blower fan necessary electromotor reduces, and is energy-conservation obvious, have good economic benefit and environmental benefit, because block-resistant type fluid dispersal device adopts organic material or metal to make, thereby behind maintain and replace environment is not polluted, utilization block-resistant type fluid dispersal device as cooling element after, cooling effect obviously is better than packed tower, stable, operating cost is low, long service life, be the desirable substitute products of cooling element in the conventional filler tower, meet the national environmental protection product requirement; When it is used for drip washing equipment and cleaner, have the following advantages: 1, resistance is little, and power consumption is low; 2, the rate of recovery or detersive efficiency height; 3, stable nothing maintenance, 4; Economic benefit and environmental benefit are obvious.Tradition drip washing equipment or cleaner are filler equipment, constitute by filler and multilayer column plate in the equipment, its resistance is very big, often in order to overcome SR, all having disposed powerful air blast blows to device bottom, power consumption is big, detersive efficiency (or organic efficiency) is low, uneconomical, also not environmental protection, adopt the utility model block-resistant type fluid dispersal device and and the utility model in the fluid distribution showerhead disperse waste gas and absorbing medium, cancelled the supporting air blast breeze fan of traditional drip washing equipment or cleaner, filler and column plate have been cancelled simultaneously, resistance reduces greatly, and the gas-liquid contact surface is long-pending big, the absorption efficiency height, power consumption reduces greatly, has remarkable economic efficiency and environmental benefit.
Description of drawings
Fig. 1 is the facade structures figure of the utility model block-resistant type fluid dispersal device, is reality of the present utility model simultaneously
Execute example 1,12 top of the dispersion among this embodiment 1 are the cavity cylinder, and the middle part is the cavity cone, the lower cavity cylinder;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is embodiment 2 of the present utility model, and 12 top of the dispersion among this embodiment 2 are the cavity cylinder, and the middle part is the cavity cone, and the bottom is the cavity hemisphere;
Fig. 4 is embodiment 3 of the present utility model, and 12 top of the dispersion among this embodiment 3 are the cavity inverted cone, and the middle part is the cavity cone, and the bottom is the cavity cylinder;
Fig. 5 is the structure chart that the utility model block-resistant type fluid dispersal device is used for Non Packing Atomize Cooling Column.
Fig. 6 is the structure chart that the utility model block-resistant type fluid dispersal device is used for drip washing equipment.
The specific embodiment
Embodiment 1:
The structure of a kind of block-resistant type fluid of the utility model dispersal device as shown in Figure 1 and Figure 2, mainly by weighing apparatus hydraulic fluid case 13, disperse 12, fluid enters pipe and constitutes, there is blind plate 11 upper end of the hydraulic fluid that wherein weighs case 13, there is flange 8 its lower end, the top of weighing apparatus hydraulic fluid case 13 is connected with 4 fluids and enters pipe, and the outer end that every fluid enters pipe is connected with and disperses 12.Disperseing 12 inside is cavity body, and this cavity body communicates by the inner chamber that fluid enters Guan Yuheng hydraulic fluid case 13, and fluid enters pipe and is connected and disperses on 12 the outside tangent line, and it is tapered to disperse a top inner chamber body of 12 to be rounding.Disperse 12 to be connected as a single entity by three ones of upper, middle and lower, its top is cavity cylinder 1, and the middle part is a cavity cone 2, and the bottom is a cavity cylinder 3.Weighing apparatus hydraulic fluid case 13 is connected as a single entity by the upper and lower, and its inside is cavity body, and the top of the hydraulic fluid that weighs case 13 is cavity cylinder 10, and the bottom is a cavity Rotary-table 9.Fluid enters pipe and constitutes for 2-section pipe road 7,4, and 2-section pipe road 7,4 connects by flange 6,5.
Embodiment 2:
Structure such as Fig. 1, shown in Figure 3 of a kind of block-resistant type fluid of the utility model dispersal device: mainly by weighing apparatus hydraulic fluid case 13, disperse 12, fluid enters pipe and constitutes, there is blind plate 11 upper end of the hydraulic fluid that wherein weighs case 13, there is flange 8 its lower end, the top of weighing apparatus hydraulic fluid case 13 is connected with 4 fluids and enters pipe, and the outer end that every fluid enters pipe is connected with and disperses 12.Disperseing 12 inside is cavity body, and this cavity body communicates by the inner chamber that fluid enters Guan Yuheng hydraulic fluid case 13, and fluid enters pipe and is connected and disperses on 12 the outside tangent line, and it is tapered to disperse a top inner chamber body of 12 to be rounding.Disperse 12 to be connected as a single entity by three ones of upper, middle and lower, its top is cavity cylinder 1, and the middle part is a cavity cone 2, the bottom be cavity hemisphere 3 '.Weighing apparatus hydraulic fluid case 13 is connected as a single entity by the upper and lower, and its inside is cavity body, and the top of the hydraulic fluid that weighs case 13 is cavity cylinder 10, and the bottom is a cavity Rotary-table 9.Fluid enters pipe and constitutes for 2-section pipe road 7,4, and 2-section pipe road 7,4 connects by flange 6,5.
Embodiment 3:
Structure such as Fig. 1, shown in Figure 4 of a kind of block-resistant type fluid of the utility model dispersal device: mainly by weighing apparatus hydraulic fluid case 13, disperse 12, fluid enters pipe and constitutes, there is blind plate 11 upper end of the hydraulic fluid that wherein weighs case 13, there is flange 8 its lower end, the top of weighing apparatus hydraulic fluid case 13 is connected with 4 fluids and enters pipe, and the outer end that every fluid enters pipe is connected with and disperses 12.Disperseing 12 inside is cavity body, and this cavity body communicates by the inner chamber that fluid enters Guan Yuheng hydraulic fluid case 13, and fluid enters pipe and is connected and disperses on 12 the outside tangent line, and it is tapered to disperse a top inner chamber body of 12 to be rounding.Disperse 12 to be connected as a single entity by three ones of upper, middle and lower, its top be cavity inverted cone 1 ', the middle part is a cavity cone 2, the bottom is a cavity cylinder 3.Weighing apparatus hydraulic fluid case 13 is connected as a single entity by the upper and lower, and its inside is cavity body, and the top of the hydraulic fluid that weighs case 13 is cavity cylinder 10, and the bottom is a cavity Rotary-table 9.Fluid enters pipe and constitutes for 2-section pipe road 7,4, and 2-section pipe road 7,4 connects by flange 6,5.
In embodiment 1 of the present utility model, embodiment 2, embodiment 3, it is cavity body that fluid disperses 12 inside, and inner surface is a Fluid Surface, and its top is cavity cylinder 1 (or being inverted cone 1 '), and cavity is an inverted cone; The middle part is connected as a single entity for the cavity cylinder 3 (perhaps the cavity hemisphere 3 ') of cone 2 with the bottom, and the outside tangent line of cavity cylinder 3 (or cavity hemisphere 3 ') connects fluid and enters pipe 4, and it is flange 5 that fluid enters pipe 4 outer ends.Constant-pressure fluid case 13 is connected as a single entity by upper cavity cylinder 10 and lower cavity Rotary-table 9, inner surface is Fluid Surface, cavity round platform bottom is a flange 8, cavity round platform top is a blind plate 11 blind firmly cavity cylinders 10, cavity cylinder 10 tops have connected 3-8 root fluid and have entered pipe 7, and fluid is gone into pipe 7 outsides and is flange 6.
As embodiment 1 of the present utility model, embodiment 2, when embodiment 3 is used for cooling tower,
Cooling principle: cooling tower utilization block-resistant type fluid dispersal device is as cooling element, this tower to the pressure requirement of recirculated water is: (1) pressure of return water at tower zero plane place only needs P 〉=0.06Mpa to get final product, (2) the pressure of return water P 〉=0.03Mpa of block-resistant type atomising device place gets final product or in tower, therefore, the utility model requires very low to the recirculated water pressure of return water, under extremely low pressure of return water condition, fluid is through weighing apparatus hydraulic fluid case, fluid enters pipe and enters the dispersion head, fluid forms the high speed centrifugation motion in the dispersion head of low-pressure fluid dispersal device, fluid is separated into small dynamic fluid flow grain under the effect of cooling tower upper end blower fan, forms spray pattern, circulation water smoke is suspended in the cooling tower and carries out heat exchange with air, thereby has reached cooling effect.
See Fig. 5, at the tower body inner top blower fan 14 is installed, the middle part is installed in the utility model block-resistant type fluid dispersal device 15 on the water pipe 16, the bottom is for containing the pond 19 of cooling water, water enters the weighing apparatus hydraulic fluid case of each block-resistant type fluid dispersal device from water pipe 16, disperse head ejection water smoke through fluid at last, after the cooling tower air heat exchange, drop in the pond 19.
When in cooling tower, using, block-resistant type fluid dispersal device 15 is installed on the pipeline 17 of cooling tower of below, recirculated water is under the low pressure effect, weighing apparatus hydraulic fluid case through block-resistant type fluid dispersal device 15, doing high speed centrifugation motion formation diameter by block-resistant type fluid dispersal device 15 in fluid disperses head at last is the vaporific liquid grain of 0.3-1mm, along disperseing an inner surface evenly to spray the height of 3-4 rice, even vaporific liquid grain is suspended in the cooling tower fully and cold air carries out heat exchange, thereby reach cooling, its cooling effect obviously is better than filling cooling tower and other no-padding and spraying cooling towers, stable, expense is low, long service life does not have maintenance substantially, does not stop up.Be used for newly-built and the transformation circulating water cooling tower.
The utility model can be widely used in petrochemical industry, chemical industry, in the circulating water cooling tower of industries such as chemical fibre, chemical fertilizer, coking, metallurgy, light industry, biochemistry, fermentation, pharmacy, sugaring, electric power, the fiberglass packed tower that can be used for newly-built 50-5000 ton, the cooling tower of the concrete tower body of newly-built 500-5000 ton, to pressure of return water require lowly, the pressure of return water at tower zero plane place only needs 〉=0.06Mpa gets final product, perhaps the pressure of return water P 〉=0.03Mpa at atomising device place gets final product in tower; Circulating water pressure only needs P 〉=0.06Mpa to get final product, and perhaps the pressure of return water P≤0.03Mpa at atomising device place gets final product in tower: under the working condition of the mechanical admixture particle diameter≤10mm in the recirculated water, all can use, and can reach desirable cooling effect.
Use the newly built and improved Non Packing Atomize Cooling Column of block-resistant type fluid dispersal device of the present utility model, three principal elements that cool are: the 1. ratio of cooling medium and cooling water inflow, i.e. gas-water ratio; 2. cooling medium and cooling water contacted specific surface area; 3. the time of staying of cooling water in cooling tower.
Non Packing Atomize Cooling Column is owing to used block-resistant type fluid dispersal device as cooling element, be almost void tower in the whole cooling tower, thereby SR greatly reduces in the tower, under the identical situation of blower fan and necessary electromotor power thereof, the Tower System resistance reduces, air quantity increases, and promptly gas-water ratio increases, thereby good cooling results.
Recirculated water is behind block-resistant type fluid dispersal device centrifugal atomizing in the Non Packing Atomize Cooling Column, form contacting of small droplet with cold air, even and under the optimum state that the recirculated water in the packed tower does not stop up at filler, is out of shape, wears out, the filler of flowing through could form moisture film and contact with cold air.Thereby the contacted specific surface area of Non Packing Atomize Cooling Column cooling air and cooling water is greater than the specific area of packed tower.
Recirculated water is ejected into highest point in the tower through behind the centrifugal atomizing in the Non Packing Atomize Cooling Column, assembles for droplet then, is suspended in the tower after the gravity of droplet and blower fan axle power reach relative equilibrium, falls then.Therefore recirculated water falls into the pond and has experienced rising, suspension, three cooling procedures in whereabouts altogether from being ejected into, and the cooling water in the packed tower is to drop in the pond under being scattered afterwards by filler on filler with the form of moisture film, thereby the cooling water time of staying in the Non Packing Atomize Cooling Column is long than packed tower.
By Non Packing Atomize Cooling Column and filling cooling tower cool three principal elements more as can be known, adopt the Non Packing Atomize Cooling Column cooling effect of block-resistant type fluid dispersal device obviously to be better than filling cooling tower.
As embodiment 1 of the present utility model, embodiment 2, when embodiment 3 is used for drip washing equipment or cleaner
The drip washing principle: drip washing equipment or cleaner are as the cycle gas dispersal device with block-resistant type fluid dispersal device, the bottom that is installed in equipment is evenly distributed on waste gas in the equipment, according to different flow, pressure and equipment size design, the fluid of arranging the layer 2-4 varying number in equipment disperses head, fluid disperses a mounting arrangements on separating tube, water fluids such as (or) other soda acids disperses head by fluid, under lower pressure, the small droplet that is dispersed into 0.3-0.5mm fully contacts absorption with the waste gas that block-resistant type fluid dispersal device disperses, washing, the material of water-soluble in the waste gas fluids such as (or) other soda acids is absorbed to greatest extent, tail gas is discharged after reaching emission request.
See Fig. 6, in drip washing (dedusting) device bottom fluid line 20 to be washed is installed, the utility model block-resistant type fluid dispersal device 15 is installed on fluid line to be washed 20, wait to wash fluid flow pressure and the design of drip washing equipment size according to difference, in drip washing equipment, arrange layer 2-4 washing agent fluid line 21, fluid is installed on washing agent fluid line 21 is disperseed 12.Disperse a cleaning solvent that shed in 12 minutes fully to contact solable matter or the dirt particle that absorbs in dissolving air-flow or the vaporific liquid grain, thereby reach washing or washing and recycling effect with the fluid to be washed of fluid dispersal device 15 ejections.
When in drip washing equipment (perhaps cleaner), using, block-resistant type fluid dispersal device 15 is installed in being washed on fluid (comprising gas and the liquid) pipeline 20 of drip washing equipment, disperse 12 to be installed on the washing agent pipeline 21 of drip washing equipment fluid, the fluid that is washed (comprising gas and liquid) is under the low pressure effect, by block-resistant type fluid dispersal device 15 formation uniform air flows or diameter is the vaporific liquid grain of 0.3-1mm, along disperseing an inner surface evenly to spray the height of 3-4 rice, uniform air flow or vaporific liquid grain in drip washing equipment with the washing agent pipeline 21 that is installed in drip washing equipment on fluid disperse the vaporific cleaning solution grain of a 0.3-1mm who shed in 12 minutes to contact, vaporific cleaning solution grain absorbs solable matter or the dirt particle in dissolving air-flow or the vaporific liquid grain, thereby reach washing or washing and recycling, its effect obviously is better than filler drip washing equipment (or dedusting), stable, expense is low, long service life, substantially do not have maintenance, do not stop up.Not only be applied to newly-built and transformation drip washing equipment (cleaner), also be applicable to the flue cleaner.
Claims (5)
1. block-resistant type fluid dispersal device, it is characterized in that: there is blind plate (11) upper end of weighing apparatus hydraulic fluid case (13), there is flange (8) its lower end, and the top of weighing apparatus hydraulic fluid case (13) is connected with 3-8 root fluid and enters pipe, and the outer end that every fluid enters pipe is connected with and disperses head (12).
2. block-resistant type fluid dispersal device according to claim 1, it is characterized in that: disperseing the inside of head (12) is cavity body, this cavity body communicates by the inner chamber that fluid enters Guan Yuheng hydraulic fluid case (13), fluid enters pipe and is connected on the outside tangent line that disperses head (12), and it is tapered that the top inner chamber body of dispersion head (12) is rounding.
3. block-resistant type fluid dispersal device according to claim 1 and 2, it is characterized in that: disperse head (12) to be connected as a single entity by three ones of upper, middle and lower, its top is cavity cylinder (1) or cavity inverted cone (1 '), the middle part is cavity cone (2), and the bottom is cavity cylinder (3) or cavity hemisphere (3 ').
4. block-resistant type fluid dispersal device according to claim 1 and 2, it is characterized in that: weighing apparatus hydraulic fluid case (13) is connected as a single entity by the upper and lower, its inside is cavity body, and the top of weighing apparatus hydraulic fluid case (13) is cavity cylinder (10), and the bottom is cavity Rotary-table (9).
5. block-resistant type fluid dispersal device according to claim 1 and 2 is characterized in that: fluid enters pipe and constitutes for 2-section pipe road (7,4), and 2-section pipe road (7,4) connect by flange (6,5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200364691U CN201016625Y (en) | 2006-12-01 | 2006-12-01 | Anti-block fluid dispersing means |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200364691U CN201016625Y (en) | 2006-12-01 | 2006-12-01 | Anti-block fluid dispersing means |
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| Publication Number | Publication Date |
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| CN201016625Y true CN201016625Y (en) | 2008-02-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2006200364691U Expired - Fee Related CN201016625Y (en) | 2006-12-01 | 2006-12-01 | Anti-block fluid dispersing means |
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| CN (1) | CN201016625Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112871122A (en) * | 2020-12-31 | 2021-06-01 | 哈尔滨工业大学 | Reaction kettle for preparing nano silicon modified steel fibers in large batch and preparation method |
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2006
- 2006-12-01 CN CNU2006200364691U patent/CN201016625Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112871122A (en) * | 2020-12-31 | 2021-06-01 | 哈尔滨工业大学 | Reaction kettle for preparing nano silicon modified steel fibers in large batch and preparation method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080206 Termination date: 20111201 |