CN209123883U - A kind of polymerization iron sulfate water-purifying agent reaction kettle - Google Patents
A kind of polymerization iron sulfate water-purifying agent reaction kettle Download PDFInfo
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- CN209123883U CN209123883U CN201821681902.6U CN201821681902U CN209123883U CN 209123883 U CN209123883 U CN 209123883U CN 201821681902 U CN201821681902 U CN 201821681902U CN 209123883 U CN209123883 U CN 209123883U
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- cylinder
- dilution
- catalysis
- precipitation
- reaction kettle
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Abstract
The utility model proposes a kind of polymerization iron sulfate water-purifying agent reaction kettles, the utility model includes the catalytic oxidizing equipment successively installed up and down, dilution hydrolysis oxidation unit and settler, catalytic oxidizing equipment carries out catalysis oxidation first, raw material is added from the feed inlet of catalysis cylinder, exhaust gas in production process can be collected from exhaust outlet, prevent exhaust emission.Dilution hydrolysis oxidation unit can be diluted reactant, and polymerization reaction can be hydrolyzed in reactant.Settler can carry out precipitation operation to reactant cotton-shaped after hydrolytic polymerization, and part water can flow into header tank from the filter board of strainer valve, and the reactant finally precipitated can be discharged from discharged orifice.The compact overall structure of the utility model eliminates the transmission device between each process, effectively improves preparation efficiency.
Description
Technical field
The utility model relates to water purification agent production technical field, especially a kind of polymerization iron sulfate water-purifying agent reaction kettle.
Background technique
Water purification agent is mostly molysite high molecular polymer, aluminium salt high molecular polymer, and purifying water effect is significant, is widely used
In life and industry.It is during industrial production water purification agent to need reaction kettle to complete more.Bodied ferric sulfate is common net
Aqua, the preparation process of bodied ferric sulfate needs catalyst oxidation, the operation such as be passed through air oxidation, hydrolytic-polymeric reaction.Purpose
Reaction kettle needs multiple device combination connections, and reaction raw materials need to complete to conduct by transmission device between each device, whole
The volume of equipment is larger, occupies biggish place space, is not suitable for enterprise and carries out middle and small scale production.With regard to problem above, we
A kind of polymerization iron sulfate water-purifying agent reaction kettle has been invented, the catalytic oxidizing equipment successively installed up and down, dilution hydrolysis oxidation are set
Device and settler, the reaction kettle can once complete the preparation work of bodied ferric sulfate.
Utility model content
The utility model proposes a kind of polymerization iron sulfate water-purifying agent reaction kettle, the catalysis oxidation dress successively installed up and down is set
Set, dilute hydrolysis oxidation unit and settler, the reaction kettle can once complete the preparation work of bodied ferric sulfate.
The technical solution of the utility model is achieved in that a kind of polymerization iron sulfate water-purifying agent reaction kettle, include on
Under catalytic oxidizing equipment, the dilution hydrolysis oxidation unit and settler successively installed；The catalytic oxidizing equipment includes bottom
The catalysis cylinder of portion's opening, is equipped with stirring motor at the top of the catalysis cylinder, the main shaft of the stirring motor is connected with downward to be stirred
Axis is mixed, the agitating shaft is equipped with paddle；The top surface of the catalysis cylinder offers feed inlet and exhaust outlet upward；The dilution
Hydrolysis oxidation device includes dilution cylinder, the dilution cylinder up and down, it is described dilution cylinder top opening and catalysis cylinder base opening it
Between be connected with switch valve；The top surface of the dilution cylinder offers liquid inlet port upward；The settler includes precipitation cylinder and sinks
Water collecting tube below the cylinder of shallow lake, the precipitation cylinder up and down, are connected between the top opening of the precipitation cylinder and the base opening for diluting cylinder
Switch valve, the base opening of the precipitation cylinder are equipped with strainer valve, are arranged with filter board in the strainer valve；The precipitation cylinder is along side
The bottom of wall offers discharged orifice outwardly, is equipped with switch valve on the discharged orifice.
Further have, air inlet pipe is installed on the top surface of the dilution cylinder, the air inlet pipe court has multiple branches
Pipe, the branched pipe can be put in dilution cylinder.
Further have, the lower half of the precipitation cylinder is that inclined conical surface cylinder, the discharged orifice are located at the conical surface inwardly
The bottom of cylinder.
Further have, the base opening of the catalysis cylinder is equipped with filter plate, and the catalysis cylinder is along the bottom of side wall towards external-open
Equipped with slag-drip opening, switch valve is installed on the slag-drip opening.
Using above-mentioned technical proposal, the utility model has the following beneficial effects:
The utility model includes the catalytic oxidizing equipment successively installed up and down, dilution hydrolysis oxidation unit and precipitating dress
It sets, catalytic oxidizing equipment carries out catalysis oxidation first, and raw material is added from the feed inlet of catalysis cylinder, and the exhaust gas in production process can be from
Exhaust outlet is collected, and exhaust emission is prevented.Dilution hydrolysis oxidation unit can be diluted reactant, and reactant can be hydrolyzed poly-
Close reaction.Settler can carry out precipitation operation to reactant cotton-shaped after hydrolytic polymerization, and part water can be from the filtering of strainer valve
Cardboard flows into header tank, and the reactant finally precipitated can be discharged from discharged orifice.The compact overall structure of the utility model saves
The transmission device between each process has been removed, preparation efficiency is effectively improved.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the cutting structural schematic diagram of the utility model；
Wherein: 1. catalysis cylinders, 2. stirring motors, 3. agitating shafts, 4. paddles, 5. feed inlets, 6. exhaust outlets, 7. dilutions
Cylinder, 8. switch valves, 9. liquid inlet ports, 10. precipitation cylinders, 11. Water collecting tubes, 12. strainer valves, 13. filter boards, 14. discharged orifices, 15.
Air inlet pipe, 16. branched pipes, 17. filter plates, 18. slag-drip openings.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without creative efforts
Every other embodiment obtained, fall within the protection scope of the utility model.
As depicted in figs. 1 and 2, a kind of polymerization iron sulfate water-purifying agent reaction kettle includes the catalysis oxygen successively installed up and down
Makeup sets, dilutes hydrolysis oxidation unit and settler；The catalytic oxidizing equipment includes the catalysis cylinder 1 of bottom opening, institute
The top for stating catalysis cylinder 1 is equipped with stirring motor 2, and the main shaft of the stirring motor 2 is connected with agitating shaft 3, the stirring downward
Axis 3 is equipped with paddle 4；The top surface of the catalysis cylinder 1 offers feed inlet 5 and exhaust outlet 6 upward；The dilution hydrolysis oxidation
Device includes dilution cylinder 7, and the dilution cylinder 7 up and down, connects between the top opening of the dilution cylinder 7 and the base opening for being catalyzed cylinder 1
It is connected to switch valve 8；The top surface of the dilution cylinder 7 offers liquid inlet port 9 upward；The settler includes precipitation cylinder 10 and sinks
The Water collecting tube 11 of the lower section of shallow lake cylinder 10, the precipitation cylinder 10 up and down, the base opening of the top opening of the precipitation cylinder 10 and dilution cylinder 7 it
Between be connected with switch valve 8, the base opening of the precipitation cylinder 10 is equipped with strainer valve 8, is arranged with filter board in the strainer valve 12
13；The precipitation cylinder 10 offers discharged orifice 14 along the bottom of side wall outwardly, is equipped with switch valve 8 on the discharged orifice 14.
Air inlet pipe 15 is installed, the air inlet pipe 15 is towards having multiple branches on the top surface of the dilution cylinder 7 of the present embodiment
Pipe 16, the branched pipe 16 can be put in dilution cylinder 7.The branched pipe 16 of the air inlet pipe 15 connects with dilution cylinder 7, air inlet pipe 15
Air can be filled with, can to reactant carry out air oxidation, reactant energy hydrolytic polymerization more thoroughly.
The lower half of the precipitation cylinder 10 of the present embodiment is that inclined conical surface cylinder, the discharged orifice 14 are located at conical surface cylinder inwardly
The bottom of body.Reactant after hydrolytic-polymeric reaction can in the conical surface cylinder rapid precipitation, can be smoothly outside from discharged orifice 14
Discharge.
The base opening of the catalysis cylinder 1 of the present embodiment is equipped with filter plate 17, and the catalysis cylinder 1 opens up outwardly along the bottom of side wall
There is slag-drip opening 18, switch valve 8 is installed on the slag-drip opening 18.Solid slag in reactant can be retained on filter plate 17,
Solid slag can be discharged from slag-drip opening 10, and the purity of bodied ferric sulfate can be improved.
The utility model includes the catalytic oxidizing equipment successively installed up and down, dilution hydrolysis oxidation unit and precipitating dress
It sets, catalytic oxidizing equipment carries out catalysis oxidation first, and raw material is added from the feed inlet 5 of catalysis cylinder 1, and the exhaust gas in production process can
It is collected from exhaust outlet 6, prevents exhaust emission.Dilution hydrolysis oxidation unit can be diluted reactant, and reactant can carry out water
Depolymerize reaction.Settler can carry out precipitation operation to reactant cotton-shaped after hydrolytic polymerization, and part water can be from strainer valve 12
Filter board 13 flow into header tank 11, the reactant finally precipitated can discharge from discharged orifice 14.The utility model it is whole
Body is compact-sized, eliminates the transmission device between each process, effectively improves preparation efficiency.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (4)
1. a kind of polymerization iron sulfate water-purifying agent reaction kettle, which is characterized in that include the catalytic oxidizing equipment successively installed up and down,
Dilution hydrolysis oxidation unit and settler；The catalytic oxidizing equipment includes the catalysis cylinder (1) of bottom opening, the catalysis
It is equipped with stirring motor (2) at the top of cylinder (1), the main shaft of the stirring motor (2) is connected with agitating shaft (3) downward, described to stir
Axis (3) are mixed equipped with paddle (4)；The top surface of catalysis cylinder (1) offers feed inlet (5) and exhaust outlet (6) upward；It is described
Dilution hydrolysis oxidation unit include dilution cylinder (7), the dilution cylinder (7) up and down, it is described dilute cylinder (7) top opening with urge
Change and is connected with switch valve (8) between the base opening of cylinder (1)；The top surface of dilution cylinder (7) offers liquid inlet port (9) upward；It is described
Settler includes the Water collecting tube (11) below precipitation cylinder (10) and precipitation cylinder (10), the precipitation cylinder (10) up and down,
It is connected with switch valve (8) between the top opening of the precipitation cylinder (10) and the base opening for diluting cylinder (7), the base opening of the precipitation cylinder (10)
It is equipped with strainer valve (12), is arranged with filter board (13) in the strainer valve (12)；The precipitation cylinder (10) is along the bottom of side wall
Portion offers discharged orifice (14) outwardly, is equipped with switch valve (8) on the discharged orifice (14).
2. a kind of polymerization iron sulfate water-purifying agent reaction kettle according to claim 1, which is characterized in that the dilution cylinder (7)
Top surface on be equipped with air inlet pipe (15), the air inlet pipe (15) is towards having multiple branched pipes (16), the branched pipe (16)
It can put in dilution cylinder (7).
3. a kind of polymerization iron sulfate water-purifying agent reaction kettle according to claim 1, which is characterized in that the precipitation cylinder (10)
Lower half be inclined conical surface cylinder, the discharged orifice (14) are located at the bottom of conical surface cylinder inwardly.
4. a kind of polymerization iron sulfate water-purifying agent reaction kettle according to claim 1, which is characterized in that the catalysis cylinder (1)
Base opening be equipped with filter plate (17), the catalysis cylinder (1) offers slag-drip opening (18), the deslagging along the bottom of side wall outwardly
Switch valve (8) are installed on mouth (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821681902.6U CN209123883U (en) | 2018-10-17 | 2018-10-17 | A kind of polymerization iron sulfate water-purifying agent reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821681902.6U CN209123883U (en) | 2018-10-17 | 2018-10-17 | A kind of polymerization iron sulfate water-purifying agent reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209123883U true CN209123883U (en) | 2019-07-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821681902.6U Active CN209123883U (en) | 2018-10-17 | 2018-10-17 | A kind of polymerization iron sulfate water-purifying agent reaction kettle |
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| CN (1) | CN209123883U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112138551A (en) * | 2020-10-14 | 2020-12-29 | 马鞍山健鼎化工有限公司 | Dissolving device for producing polymeric ferric sulfate and working method |
-
2018
- 2018-10-17 CN CN201821681902.6U patent/CN209123883U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112138551A (en) * | 2020-10-14 | 2020-12-29 | 马鞍山健鼎化工有限公司 | Dissolving device for producing polymeric ferric sulfate and working method |
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