CN205187900U - Polyferric sulfate apparatus for producing - Google Patents
Polyferric sulfate apparatus for producing Download PDFInfo
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- CN205187900U CN205187900U CN201520843312.9U CN201520843312U CN205187900U CN 205187900 U CN205187900 U CN 205187900U CN 201520843312 U CN201520843312 U CN 201520843312U CN 205187900 U CN205187900 U CN 205187900U
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- nozzle
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- edge
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Abstract
The utility model relates to a polyferric sulfate apparatus for producing, be affiliated to flange, central circular cone and flank otter board including nozzle, edge, center circular cone bottom surface diameter is less than the flange diameter is affiliated to at the edge, the flank otter board be the toper, its one end with the bottom surface of center circular cone is connected, the other end with flange joint is affiliated to at the edge, the nozzle is located the top of center circular cone. Beneficial effect: direct impact forms the not liquid drop of equidimension at central circular cone from nozzle spun material liquid column, drop on the flank otter board with oxygen after fully contacting on, the mesh from the flank otter board drips, can fully lengthen liquid drop and gaseous contact time like this, improves production efficiency. And the the device preparation is simple, and it is convenient to overhaul.
Description
Technical field
The utility model relates to a kind of production equipment of water conditioner, particularly relates to a kind of polymeric ferric sulfate production apparatus.
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.Wherein namely catalytic oxidation technique is by material and the catalytic process of oxygen, how to make the abundant hybrid reaction of gas-liquid, and extend gas-liquid contact time is technological difficulties always, there is no good solution in prior art.
Utility model content
The purpose of this utility model overcomes prior art to there is material and oxygen and be difficult to the short defect of abundant hybrid reaction, gas-liquid contact time, provides a kind of polymeric ferric sulfate production apparatus.
The utility model solves the technical scheme that its technical problem adopts: a kind of polymeric ferric sulfate production apparatus, comprises nozzle, flange is affiliated at edge, center cone and flank web plate, and described center cone basal diameter is less than described edge and is affiliated to flange diameter; Described flank web plate is tapered, and its one end is connected with the bottom surface of described center cone, and Flange joint is affiliated at the other end and described edge; Described nozzle is positioned at the top of described center cone.
As preferably, for reaching better material dispersion effect, described nozzle is positioned at directly over described center cone.
As preferably, on described flank web plate, mesh aperture is 10 ~ 15mm, and between adjacent two mesh, spacing is 20 ~ 25mm.
As preferably, for accretion feed liquid drops in the residence time on web plate, thus extend the duration of contact of drop and gas, the angle between described flank web plate and center cone bottom surface is 120 ~ 135 °.
As preferably, for making to have enough pressure from the material of nozzle ejection, thus be conducive to material and disperse under the effect of center cone, the outlet bore of described nozzle is 0.5 times of its import bore.
As preferably, for making the material of fully reaction again can carry out circulating reaction, described polymeric ferric sulfate production apparatus also comprises reactor and recycle pump, and described edge is affiliated to flange and is arranged in reactor; Described nozzle is positioned at reactor top, and its outlet is positioned at reactor; The outlet of described reactor is communicated with described nozzle inlet by described recycle pump.
Beneficial effect: directly impact the drop forming different size in center cone from the material fluid column of nozzle ejection, drop on flank web plate after fully contacting with oxygen, drip down from the mesh flank web plate, fully can extend the duration of contact of drop and gas like this, enhance productivity.And the preparation of this device is simple, maintenance is convenient.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is the structural representation of preferred embodiment of the present utility model;
Fig. 2 is the utility model device (reactor does not draw) sectional structure schematic diagram;
Fig. 3 is the utility model device (reactor does not draw) vertical view.
Wherein: 1, flange is affiliated at edge, 2. flank web plate, 3. center cone, 4. reactor, 5. nozzle, 6. recycle pump.
Embodiment
Embodiment
As shown in Figures 1 to 3, a kind of polymeric ferric sulfate production apparatus, comprise reactor 4, recycle pump 6, nozzle 5, edge be affiliated to flange 1, center cone 3 and flank web plate 2, described center cone 3 basal diameter is less than described edge and is affiliated to flange 1 diameter; Described flank web plate 2 is tapered, and its one end is connected with the bottom surface of described center cone 3, and the other end and described edge are affiliated to flange 1 and are connected; Described edge is affiliated to flange 1 and is arranged in reactor 4; Described nozzle 5 is positioned at reactor 4 top, and its outlet is positioned at reactor 4; The outlet of described reactor 4 is by described recycle pump 6 and described nozzle 5 inlet communication; Described nozzle 5 is positioned at directly over center cone 3.
Particularly, on described flank web plate 2, mesh aperture is 10 ~ 15mm, and between adjacent two mesh, spacing is 20 ~ 25mm.Angle between described flank web plate 2 and center cone 3 bottom surface is 120 ~ 135 °.The outlet bore of described nozzle 5 is 0.5 times of its import bore; The basal diameter of described center cone 3 is 0.25 times of reactor 4 diameter.
During work, the material fluid column sprayed from nozzle 5 directly impacts the drop forming different size in center cone 3, drop on flank web plate 2 after drop fully contacts with oxygen, drip down from the mesh flank web plate 2, fully can extend the duration of contact of drop and gas like this, in reactor 4 unreacted completely material again enter nozzle 5 through recycle pump 6, again react, ensure that material reaction is complete.
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. a polymeric ferric sulfate production apparatus, it is characterized in that: comprise nozzle (5), flange (1) is affiliated at edge, center cone (3) and flank web plate (2), described center cone (3) basal diameter is less than described edge and is affiliated to flange (1) diameter; Described flank web plate (2) is tapered, and its one end is connected with the bottom surface of described center cone (3), and the other end and described edge are affiliated to flange (1) and are connected; Described nozzle (5) is positioned at the top of described center cone (3).
2. polymeric ferric sulfate production apparatus according to claim 1, is characterized in that: described nozzle (5) is positioned at directly over described center cone (3).
3. polymeric ferric sulfate production apparatus according to claim 1, is characterized in that: the upper mesh aperture of described flank web plate (2) is 10 ~ 15mm, and between adjacent two mesh, spacing is 20 ~ 25mm.
4. polymeric ferric sulfate production apparatus according to claim 1, is characterized in that: the angle between described flank web plate (2) and center cone (3) bottom surface is 120 ~ 135 °.
5. polymeric ferric sulfate production apparatus according to claim 1, is characterized in that: the outlet bore of described nozzle (5) is 0.5 times of its import bore.
6. polymeric ferric sulfate production apparatus according to claim 1, is characterized in that: also comprise reactor (4) and recycle pump (6), and described edge is affiliated to flange (1) and is arranged in reactor (4); Described nozzle (5) is positioned at reactor (4) top, and its outlet is positioned at reactor (4); The outlet of described reactor (4) is by described recycle pump (6) and described nozzle (5) inlet communication.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520843312.9U CN205187900U (en) | 2015-10-28 | 2015-10-28 | Polyferric sulfate apparatus for producing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520843312.9U CN205187900U (en) | 2015-10-28 | 2015-10-28 | Polyferric sulfate apparatus for producing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205187900U true CN205187900U (en) | 2016-04-27 |
Family
ID=55780916
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520843312.9U Active CN205187900U (en) | 2015-10-28 | 2015-10-28 | Polyferric sulfate apparatus for producing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205187900U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911455A (en) * | 2018-09-29 | 2018-11-30 | 四川建筑职业技术学院 | A kind of preparation method and equipment of the sludge substratess material based on multiphase wet oxidation |
-
2015
- 2015-10-28 CN CN201520843312.9U patent/CN205187900U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911455A (en) * | 2018-09-29 | 2018-11-30 | 四川建筑职业技术学院 | A kind of preparation method and equipment of the sludge substratess material based on multiphase wet oxidation |
| CN108911455B (en) * | 2018-09-29 | 2024-04-09 | 四川建筑职业技术学院 | Preparation method and equipment of sludge-based material based on multiphase wet oxidation |
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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 technology Co. Ltd| 213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek False: Changzhou city clean environmental protection technology Co. Ltd| 213144 Jiangsu province Changzhou City Zhonglou District zouqu Town Creek Number: 37 Volume: 32 |