CN205099383U - Be applied to atomizing device of polyferric sulfate production process - Google Patents
Be applied to atomizing device of polyferric sulfate production process Download PDFInfo
- Publication number
- CN205099383U CN205099383U CN201520805274.8U CN201520805274U CN205099383U CN 205099383 U CN205099383 U CN 205099383U CN 201520805274 U CN201520805274 U CN 201520805274U CN 205099383 U CN205099383 U CN 205099383U
- Authority
- CN
- China
- Prior art keywords
- orifice
- group
- mist pipe
- production process
- atomization hole
- 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.)
- Active
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a production facility of water treatment agent, a be applied to atomizing device of polyferric sulfate production process, including be responsible for and with be responsible for the atomizing pipe of intercommunication, the lateral wall of atomizing pipe on be provided with at least two sets of atomization hole, every group from top to bottom atomizing hollow shaft in atomization hole edge is to the setting, and is a set of at least the atomization hole slope sets up downwards, and is a set of at least the atomization hole slope upwards sets up, and at least a set of slope sets up downwards atomization hole is located a set of that the slope upwards set up atomization hole's top. Beneficial effect: utilize the slope upwards to form the relative droplet that sprays with the decurrent two sets of atomization hole of slope, the more small -size's that the collision formed between the droplet droplet, increased with material and gaseous area of contact, make the material fully contact and fill the interior gas of reation kettle, but also solved the problem that ordinary spiral atomizer easily blockked up. And the the device preparation is simple and convenient, and easy maintenance can realize mechanized operation, practices thrift artifically in a large number.
Description
Technical field
The utility model relates to the production unit of water conditioner, especially a kind of atomisation unit be applied in bodied ferric sulfate production process.
Background technology
In current domestic inorganic polymer water conditioner, the most widely used is poly aluminium chloride and bodied ferric sulfate.And what mostly adopt in bodied ferric sulfate production process is oxygenant technique, catalytic oxidation technique.Using during catalytic oxidation technique mainly utilizes recycle pump circulation to make liquid fully contact gas, realizes the process that gas-liquid is reacted rapidly.How the process main difficulty of present production bodied ferric sulfate namely realizes gas-liquid mixed to greatest extent, fully contacts, accelerated reaction.
Utility model content
The purpose of this utility model overcomes prior art to there is the defect that gas-liquid can not fully contact, and provides a kind of atomisation unit being applied to bodied ferric sulfate production process.
The utility model solves the technical scheme that its technical problem adopts: a kind of atomisation unit being applied to bodied ferric sulfate production process, comprise supervisor and be responsible for described the mist pipe be communicated with, the sidewall of described mist pipe is provided with at least two group orifices from top to bottom, orifice described in same group is axially arranged along mist pipe, described at least one group, orifice is tilted to lower setting, described at least one group, orifice tilts upward setting, and at least one group of described orifice being tilted to lower setting is positioned at the top of orifice described in a group that tilts upward setting.
As preferably, for effectively promoting that material is sprayed by orifice, described mist pipe closed bottom, and the bottom of mist pipe is provided with towards the tapered protrusion at mist pipe top.
As preferably, described mist pipe sidewall is provided with three groups of orifices, wherein one group of orifice is horizontally disposed with.The droplet utilizing the droplet of horizontally disposed one group of orifice ejection and the two groups of orifices being tilted to down and tilting upward to spray collides further, thus is conducive to forming the less droplet of size.
As preferably, described in horizontally disposed one group, orifice is positioned at the top of orifice described in a group that is tilted to lower setting.
As preferably, the described orifice angle of inclination being tilted to lower setting is 45 °, and the described orifice angle of inclination tilting upward setting is 45 °.
Further, for by unreacted completely material re-start atomization, reaction, described atomisation unit also comprises reactor and recycle pump, described mist pipe is arranged in reactor, described supervisor by Flange joint above reactor, be provided with outlet bottom described reactor, described outlet is communicated with described supervisor by described recycle pump.
Beneficial effect: utilize tilt upward be tilted under two groups of orifices form the droplet of relative injection, the droplet of the smaller szie of formation is collided between droplet, increase the contact area with material and gas, make material fully contact the gas be filled with in reactor, but also solve the susceptible to plugging problem of normal spiral spraying gun.And this device is simple for production, easy to maintenance, can realize mechanized operation, a large amount of saving is artificial.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is supervisor and mist pipe sectional structure schematic diagram;
Fig. 2 is mist pipe sectional structure schematic diagram;
Fig. 3 is supervisor and mist pipe and reactor syndeton schematic diagram;
1. supervisors in figure, 2. mist pipe, 21. orifices, 22. is protruding, 3. reactor, 4. recycle pump.
Embodiment
Embodiment
As illustrated in fig. 1 and 2, a kind of atomisation unit being applied to bodied ferric sulfate production process, the mist pipe 2 comprising supervisor 1 and be communicated with described supervisor 1, the sidewall of described mist pipe 2 is provided with at least two group orifices 21 from top to bottom, described mist pipe 2 closed bottom, and the bottom of mist pipe 2 is provided with towards the tapered protrusion 22 at mist pipe 2 top; Orifice 21 described in same group is axially arranged along mist pipe 2, described at least one group, orifice 21 is tilted to lower setting, described at least one group, orifice 21 tilts upward setting, and at least one group of described orifice 21 being tilted to lower setting is positioned at the top of orifice 21 described in a group that tilts upward setting.
The utility model is mist pipe 2 to be arranged three groups of orifices 21.
One group, the top orifice 21 is horizontally disposed with, and the one group of orifice 21 tilting upward setting is arranged on bottom, and the one group of orifice 21 being tilted to lower setting is arranged on centre.
For by unreacted completely material re-start atomization, reaction, as shown in Figure 3, described atomisation unit also comprises reactor 3 and recycle pump 4, described mist pipe 2 is arranged in reactor 3, described supervisor 1 by Flange joint above reactor 3, be provided with outlet bottom described reactor 3, described outlet is communicated with described supervisor 1 by described recycle pump 4.
Particularly, mist pipe 2 caliber is identical with supervisor's 1 caliber, the total length of mist pipe 2 is 50 ~ 75cm, orifice 21 aperture is 2 ~ 3mm, often organizing orifice 21 quantity is 6 ~ 8, between two adjacent groups orifice 21, spacing is greater than 15cm, and described orifice 21 angle of inclination of setting under described being tilted to is 45 °, and described described orifice 21 angle of inclination tilting upward setting is 45 °.
The utility model, utilize tilt upward be tilted under two groups of orifices 21 form the droplet of relative injection, the droplet of the smaller szie of formation is collided between droplet, and the droplet that the droplet utilizing horizontally disposed one group of orifice 21 to spray and the two groups of orifices 21 being tilted to down and tilting upward spray collides further, be conducive to forming the less droplet of size.Thus the contact area increased with material and gas, make material fully contact the gas be filled with in reactor 3.In reactor 3 unreacted completely material again pass into supervisor 1 through recycle pump 4 and can again carry out being atomized, reacting.
Should be appreciated that specific embodiment described above only for explaining the utility model, and be not used in restriction the utility model.Still be among protection domain of the present utility model by spirit institute's apparent change of extending out of the present utility model or change.
Claims (6)
1. one kind is applied to the atomisation unit of bodied ferric sulfate production process, it is characterized in that: the mist pipe (2) comprising supervisor (1) and be communicated with described supervisor (1), the sidewall of described mist pipe (2) is provided with at least two group orifices (21) from top to bottom, orifice (21) described in same group is axially arranged along mist pipe (2), described at least one group, orifice (21) is tilted to lower setting, described at least one group, orifice (21) tilts upward setting, and at least one group of described orifice (21) being tilted to lower setting is positioned at the top of orifice (21) described in a group that tilts upward setting.
2. the atomisation unit being applied to bodied ferric sulfate production process according to claim 1, it is characterized in that: described mist pipe (2) closed bottom, and the bottom of mist pipe (2) is provided with towards the tapered protrusion (22) at mist pipe (2) top.
3. the atomisation unit being applied to bodied ferric sulfate production process according to claim 1 and 2, it is characterized in that: described mist pipe (2) sidewall is provided with three groups of orifices (21), wherein one group of orifice (21) is horizontally disposed with.
4. the atomisation unit being applied to bodied ferric sulfate production process according to claim 3, is characterized in that: described in horizontally disposed one group, orifice (21) is positioned at the top of orifice (21) described in a group that is tilted to lower setting.
5. the atomisation unit being applied to bodied ferric sulfate production process according to claim 1, it is characterized in that: described orifice (21) angle of inclination being tilted to lower setting is 45 °, described orifice (21) angle of inclination tilting upward setting is 45 °.
6. the atomisation unit being applied to bodied ferric sulfate production process according to claim 1, it is characterized in that: also comprise reactor (3) and recycle pump (4), described mist pipe (2) is arranged in reactor (3), described supervisor (1) is by the top of Flange joint in reactor (3), described reactor (3) bottom is provided with outlet, and described outlet is communicated with described supervisor (1) by described recycle pump (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520805274.8U CN205099383U (en) | 2015-10-16 | 2015-10-16 | Be applied to atomizing device of polyferric sulfate production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520805274.8U CN205099383U (en) | 2015-10-16 | 2015-10-16 | Be applied to atomizing device of polyferric sulfate production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205099383U true CN205099383U (en) | 2016-03-23 |
Family
ID=55515177
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520805274.8U Active CN205099383U (en) | 2015-10-16 | 2015-10-16 | Be applied to atomizing device of polyferric sulfate production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205099383U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112827682A (en) * | 2020-12-31 | 2021-05-25 | 常州大学 | High-efficiency atomization anti-scaling anti-blocking atomizing disc for high-speed rotary atomizer |
-
2015
- 2015-10-16 CN CN201520805274.8U patent/CN205099383U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112827682A (en) * | 2020-12-31 | 2021-05-25 | 常州大学 | High-efficiency atomization anti-scaling anti-blocking atomizing disc for high-speed rotary atomizer |
| CN112827682B (en) * | 2020-12-31 | 2022-01-25 | 常州大学 | High-efficiency atomization anti-scaling anti-blocking atomizing disc for high-speed rotary atomizer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204933772U (en) | A kind of wholecircle sprinkler irrigation mini sprinkler | |
| CN203458973U (en) | Spray pipe device | |
| CN205099383U (en) | Be applied to atomizing device of polyferric sulfate production process | |
| CN204933769U (en) | A kind of irrigation is used without dead angle mini sprinkler | |
| CN203304097U (en) | Shower head type sprayer | |
| CN201140125Y (en) | Atomizing nozzle | |
| CN201253442Y (en) | Spray head of gas fire-extinguishing system | |
| CN204429569U (en) | Sprayer medicine case jet stirrer and spraying machine | |
| CN110343540A (en) | A kind of defoaming injection device and delay coke tower apparatus | |
| CN205020263U (en) | Spiral wind -guiding formula shower nozzle of atomizer | |
| CN203598676U (en) | Conical cylindrical sieve plate | |
| CN215313252U (en) | Ultrahigh pressure water molecule atomizing device | |
| CN201361537Y (en) | Water and powder mixing head | |
| CN211098289U (en) | External desulfurization circulation spraying system | |
| CN209333488U (en) | A kind of high efficiency denitration device being uniformly mixed convenient for flue gas with ammonia | |
| CN209005975U (en) | A kind of spray head suitable for Diseases of Turfgrass prevention and treatment | |
| CN206867967U (en) | A kind of novel desulphurization spray assemblies | |
| CN206219944U (en) | Asphalt foaming apparatus | |
| CN208500357U (en) | Phosphorus pentachloride reaction kettle | |
| CN204411542U (en) | A kind of large angle of flare foam fire-fighting shower nozzle | |
| CN202387608U (en) | Shower nozzle | |
| CN204949367U (en) | Liquid essence atomizing adsorption equipment | |
| CN205868581U (en) | Spray blade water flower structure | |
| CN201431929Y (en) | Agricultural sprayer burner cap | |
| CN205095651U (en) | Scrubbing tower with liquid distributor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek Patentee after: Changzhou city clean environmental protection science and technology limited company Address before: 213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek Patentee before: CHANGZHOU QINGLIU WATER TREATMENT AGENT CO., LTD. |
|
| CU03 | Correction of utility model patent gazette |
Correction item: Patentee|Address Correct: Changzhou clean environmental protection science and technology limited company|213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek False: Changzhou city clean environmental protection science and technology limited company|213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek Number: 36 Volume: 32 |
|
| ERR | Gazette correction |