CN209481196U - Produce denitration titanium dioxide acid hydrolysis tank - Google Patents
Produce denitration titanium dioxide acid hydrolysis tank Download PDFInfo
- Publication number
- CN209481196U CN209481196U CN201920043092.XU CN201920043092U CN209481196U CN 209481196 U CN209481196 U CN 209481196U CN 201920043092 U CN201920043092 U CN 201920043092U CN 209481196 U CN209481196 U CN 209481196U
- Authority
- CN
- China
- Prior art keywords
- rotary shaft
- acid hydrolysis
- crossbeam
- auger bar
- hydrolysis tank
- 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
- Mixers Of The Rotary Stirring Type (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
The utility model discloses a kind of production denitration titanium dioxide acid hydrolysis tanks, including agitating device, agitating device includes rabbling mechanism and power mechanism, rabbling mechanism includes rotary shaft, one end transmission connection power mechanism of rotary shaft, the other end of rotary shaft is fixedly connected with stirring rack, it stirs rack and includes at least first crossbeam, first crossbeam is vertically arranged and connect with rotary shaft, the end of first crossbeam is fixedly connected with auger bar, the auger bar is at least arranged two, and auger bar is arranged along the axisymmetrical of rotary shaft.By the structure for changing existing agitating device, existing stirring blade is substituted using multiple auger bars, improve the turbulent condition of solution in acid hydrolysis tank, in the case where guaranteeing mixing effect, the scouring force for reducing and stabilizing solution to ceramic tile layer solves the problems, such as that the clay between existing acid hydrolysis tank surface layer ceramic tile is easily washed and wears away.
Description
Technical field
The utility model relates to titanium white production apparatus field, especially a kind of production denitration titanium dioxide acid hydrolysis tank.
Background technique
Denitration titanium dioxide is anatase thpe white powder, generallys use sulfuric acid process preparation, preparation process flow is substantially are as follows: with titanium
Concentrate or titanium slag are raw material, are required according to acidolysis process, carry out ore grinding to raw material, raw ore are crushed to certain granularity, so
Sulfuric acid decomposition Concentrate titanium sulfate solution is used afterwards, and titanium sulfate solution is purified except after iron, metatitanic acid is precipitated in hydrolysis, by metatitanic acid
Denitration titanium dioxide is made after calcining.
It is prepared in titanium liquid stream journey in raw material acidolysis, the preparation of titanium liquid is carried out in the acid hydrolysis tank of acid-proof ceramic tile, that is, will
Concentration is that the concentrated sulfuric acid of 92-94% is fitted into acid hydrolysis tank and is passed through compressed air, and levigate raw material is added in the case of stirring,
The mixture of raw material and sulfuric acid is heated with steam to lure carrying out for acidolysis main reaction, after main reaction, allows the solid formation of generation
It is cured in acid hydrolysis tank, decomposes raw material further, gained solid formation is substantially by ferrotianium sulfate and a fixed number after decomposition
The sulfuric acid of amount forms, and after solid formation is cooled to certain temperature, is gone out with water logging, and stirred with compressed air, after leaching completely, leaching
The ferric sulphate of solution is reduced into ferrous sulfate by solution iron reduction out.Currently, what domestic titanium powder plant used
The specification of acid hydrolysis tank is in 60-150m3Between, and the trend of oriented enlargement development, this requires acid hydrolysis tanks must have batch
The conditions such as yield is big, production is more stable, to meet needed for modern production.
Existing acid hydrolysis tank can satisfy the requirement that batch output is big, production is stable in hydrolysis procedure substantially, still,
There is also some shortcomings, for example, the agitating device that uses of acid hydrolysis tank execute stir operation when, the service life mistake of stirring blade
Short, whipping process is unstable, and scouring force suffered by the acid-resistant and heat-resistant ceramic tile layer of acid hydrolysis tank is larger and variation is big, does not only result in
Clay between acid hydrolysis tank surface layer ceramic tile, which is easy to be washed, to be worn away, and is also resulted in stirring blade premature failure, is increased and be produced into
This, therefore, it is necessary to improve to existing agitating device.
Utility model content
The goal of the invention of the utility model is: in view of the above problems, providing a kind of production denitration titanium dioxide use
Acid hydrolysis tank substitutes existing stirring blade using multiple auger bars, to change by changing the structure of existing agitating device
The turbulent condition of solution in kind acid hydrolysis tank reduces in the case where guaranteeing mixing effect and stablizing solution washes away ceramic tile layer
Power solves existing existing deficiency.
The technical solution adopted in the utility model is as follows: a kind of production denitration titanium dioxide acid hydrolysis tank, including agitating device,
Agitating device includes rabbling mechanism and power mechanism, and rabbling mechanism includes rotary shaft, one end transmission connection engine of rotary shaft
Structure, the other end of rotary shaft are fixedly connected with stirring rack, and stirring rack includes at least first crossbeam, and first crossbeam and rotary shaft are hung down
Directly it is arranged and connects, the end of first crossbeam is fixedly connected with auger bar, and the auger bar is at least arranged two, and
Auger bar is arranged along the axisymmetrical of rotary shaft.
In the present invention, auger bar is different from common straight blade or curved surface bucket, although single spiral
Mixing effect caused by stirring rod can form more stable turbulent flow not as good as straight blade or curved surface bucket, and solution is stirring
Mix smaller to the scouring force of acid hydrolysis tank ceramic tile layer under state, stirring caused by the auger bar of setting two or two or more
Effect can reach the mixing effect of straight blade or curved surface bucket, but its turbulent flow formed is imitated compared with straight blade or curved surface bucket
Fruit is good, and solution is capable of forming stably eddy flow under stirring, reduces to the scouring force of ceramic tile layer, as a result, acid hydrolysis tank
Clay between surface layer ceramic tile, which is not easy to be washed, to be worn away, and ensure that the anti-corrosion capability of acid hydrolysis tank.
It is preferably carried out scheme as one kind, stirring rack further includes second cross beam and third crossbeam, first crossbeam, second
The end of crossbeam and third crossbeam is in turn connected to form triangle rack, and support plate is connected in the middle part of triangle rack, rotation
The end of axis is fixedly connected with support plate, and auger bar is separately positioned at each endpoint of triangle rack.Pass through setting
Three auger bars guarantee mixing effect, while being more likely formed stable steady flow result, reduce solution and rush to ceramic tile layer
Brushing force.
In the present invention, it protrudes into/stretches out in acid hydrolysis tank for the ease of rabbling mechanism, auger bar passes through connecting plate
It connect with stirring rack, is connected between support plate and connecting plate by incorporating section, be provided with sliding slot, auger bar on incorporating section
End be connected in the sliding slot of incorporating section, and auger bar can be free to slide in sliding slot.By storing auger bar
The occupancy volume of rabbling mechanism is reduced, convenient for rabbling mechanism smoothly protrudes into/stretches out in acid hydrolysis tank.
Further, in order to better implement the auger bar of the utility model, auger bar include helical blade and
Stirring rod, helical blade are welded on stirring rod along the axis direction of stirring rod.The structure can not only guarantee mixing effect, also
Production technology can be simplified, reduce production cost to a certain extent.
In the present invention, it is desirable that the outer diameter of helical blade is 1.2 times to 2 times for stirring shank diameter, to avoid spiral
Blade is excessive and adheres to the precipitate in solution and corrodes helical blade, further ensures that the service life of auger bar.
In conclusion by adopting the above-described technical solution, the beneficial effects of the utility model are: by changing existing stir
The structure for mixing device substitutes existing stirring blade using multiple auger bars, improves the turbulent flow of solution in acid hydrolysis tank
State, in the case where guaranteeing mixing effect, the scouring force for reducing and stabilizing solution to ceramic tile layer solves existing acid hydrolysis tank
Clay between surface layer ceramic tile is easily washed the problem of wearing away.
Detailed description of the invention
Fig. 1 is the production denitration titanium dioxide acid hydrolysis tank structural schematic diagram of the utility model；
Fig. 2 is a kind of auger rod structure schematic diagram of the utility model；
Fig. 3 is Fig. 2 auger bar present invention looks up structural representation；
Fig. 4 is another auger rod structure schematic diagram of the utility model；
Fig. 5 is Fig. 4 auger bar present invention looks up structural representation；
Fig. 6 is the improvement structural schematic diagram of Fig. 4.
Marked in the figure: 1 is acid hydrolysis tank, 2 be rabbling mechanism, and 3 be power mechanism, and 4 be rotary shaft, and 5 be stirring rack, and 6 are
First crossbeam, 7 be auger bar, and 701 be helical blade, and 702 be stirring rod, and 8 be reinforcing rod, and 9 be second cross beam, and 10 be the
Three crossbeams, 11 be support plate, and 12 be connecting plate, and 13 be incorporating section, and 14 be sliding slot.
Specific embodiment
With reference to the accompanying drawing, the utility model is described in detail.
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.
As shown in Figure 1, a kind of production denitration titanium dioxide acid hydrolysis tank 1, including agitating device, agitating device include blender
Structure 2 and power mechanism 3, agitating device are protruded into acid hydrolysis tank 1 by rabbling mechanism 2, and rabbling mechanism includes rotary shaft 4, rotary shaft 4
One end be sequentially connected power mechanism 3, the other end of rotary shaft 4 be fixedly connected stirring rack 5, power mechanism 3 include slow down electricity
Machine and reduction gearbox, since these are all existing common structures, details are not described herein, and as shown in Figures 2 and 3, stirring rack 5 includes
First crossbeam 6, first crossbeam 6 are vertically arranged with rotary shaft 4, and the fixed company in the end of rotary shaft 4 and the middle part of first crossbeam 6
It connects, the end of first crossbeam 6 is fixedly connected with auger bar 7, and auger bar 7 includes helical blade 701 and stirring rod
702, helical blade 701 is welded on stirring rod 702 along the axis direction of stirring rod 702, and auger bar 7 is set as two,
Auger bar 7 is arranged along the axisymmetrical of rotary shaft 4, that is, two ends of first crossbeam 6 are arranged in auger bar 7.For
Reinforce the bonding strength between rotary shaft 4 and first crossbeam 6, is also connected by reinforcing rod 8 between rotary shaft 4 and first crossbeam 6
It connects.Rotary shaft 4 is driven to rotate by power mechanism 3, the rotation of rotary shaft 4 drives first crossbeam 6 to rotate, and is achieved in stirring and makees
Industry.
It is preferably carried out mode as one kind, as shown in Figure 4 and Figure 5, stirring rack 5 includes first crossbeam 6, second cross beam
9 and third crossbeam 10, the end of first crossbeam 6, second cross beam 9 and third crossbeam 10 is in turn connected to form triangle rack, and three
Support plate 11 is connected in the middle part of angular rack, the end of rotary shaft 4 is fixedly connected with support plate 11, and auger bar 7 is distinguished
It is arranged at each endpoint of triangle rack.The rotation of rotary shaft 4 drives support plate 11 to rotate, and is achieved in triangle rack
Rotation.Guarantee mixing effect by three auger bars 7 of setting, while being more likely formed stable steady flow result, reduces
Scouring force of the solution to ceramic tile layer.
In Fig. 4 and embodiment shown in fig. 5, protrudes into/stretch out in acid hydrolysis tank 1 for the ease of rabbling mechanism 2, spiral is stirred
It mixes bar 7 and is connect by connecting plate 12 with stirring rack 5, as shown in fig. 6, stirrup 7 is only with the end of its clamping in Fig. 6
Portion indicates, in order to display structure, is connected between support plate 11 and connecting plate 12 by incorporating section 13, incorporating section can be circle
Cylindrical cylindrical rods are also possible to the rectangular shaft of rectangular configuration, and sliding slot 14 is provided on incorporating section 13, and one end of sliding slot 14 extends
It to the middle part of connecting plate 12, is connected and fixed in order to which auger bar 7 slides at connecting plate 12, or is conveniently located at connecting plate
Auger bar 7 at 12 centers is slid into from connecting plate 12 at incorporating section 13, and the end of auger bar 7 is connected to storage
In the sliding slot 14 in portion 13, and auger bar 7 can be free to slide in sliding slot 14.It 14 slides along the chute the end of auger bar 7
It is dynamic, thus protrudes into/stretch out in acid hydrolysis tank 1 convenient for rabbling mechanism 2.
In the above-described embodiments, it is desirable that the outer diameter of helical blade 701 is 1.2 times to 2 times of 702 diameter of stirring rod, preferably
It is 1.5 times, it is excessive to avoid helical blade 701 and adhere to the precipitate in solution and corrode helical blade 701.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (5)
1. a kind of production denitration titanium dioxide acid hydrolysis tank, including agitating device, agitating device includes rabbling mechanism and power mechanism,
It is characterized in that, rabbling mechanism includes rotary shaft, one end of rotary shaft is sequentially connected power mechanism, and the other end of rotary shaft is fixed
Connection stirring rack, stirring rack include at least first crossbeam, and first crossbeam is vertically arranged and connect with rotary shaft, first crossbeam
End be fixedly connected with auger bar, the auger bar is at least arranged two, and auger bar is along rotary shaft
Axisymmetrical setting.
2. production denitration titanium dioxide acid hydrolysis tank as described in claim 1, which is characterized in that stirring rack further includes the second cross
Beam and third crossbeam, the end of first crossbeam, second cross beam and third crossbeam are in turn connected to form triangle rack, triangle machine
Support plate is connected in the middle part of frame, the end of rotary shaft is fixedly connected with support plate, and auger bar is separately positioned on triangle
At each endpoint of rack.
3. production denitration titanium dioxide acid hydrolysis tank as claimed in claim 2, which is characterized in that auger bar passes through connecting plate
It connect with stirring rack, is connected between support plate and connecting plate by incorporating section, be provided with sliding slot, auger bar on incorporating section
End be connected in the sliding slot of incorporating section, and auger bar can be free to slide in sliding slot.
4. the production denitration titanium dioxide acid hydrolysis tank as described in one of claim 1-3, which is characterized in that auger bar includes
Helical blade and stirring rod, helical blade are welded on stirring rod along the axis direction of stirring rod.
5. production denitration titanium dioxide acid hydrolysis tank as claimed in claim 4, which is characterized in that the outer diameter of helical blade is stirring
1.2 times to 2 times of shank diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920043092.XU CN209481196U (en) | 2019-01-11 | 2019-01-11 | Produce denitration titanium dioxide acid hydrolysis tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920043092.XU CN209481196U (en) | 2019-01-11 | 2019-01-11 | Produce denitration titanium dioxide acid hydrolysis tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209481196U true CN209481196U (en) | 2019-10-11 |
Family
ID=68130792
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920043092.XU Active CN209481196U (en) | 2019-01-11 | 2019-01-11 | Produce denitration titanium dioxide acid hydrolysis tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209481196U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535882A (en) * | 2020-12-02 | 2021-03-23 | 浙江工贸职业技术学院 | Centrifugal oil-water separation device |
-
2019
- 2019-01-11 CN CN201920043092.XU patent/CN209481196U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535882A (en) * | 2020-12-02 | 2021-03-23 | 浙江工贸职业技术学院 | Centrifugal oil-water separation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209481196U (en) | Produce denitration titanium dioxide acid hydrolysis tank | |
| JP2024519671A (en) | Iron removal device for nickel-cobalt-manganese sulfate solution and low-temperature continuous removal method for iron ions in nickel-cobalt-manganese sulfate solution | |
| CN105126673B (en) | A kind of white carbon agitating device | |
| CN208288011U (en) | A kind of synthesis reactor being sufficiently stirred | |
| CN208034992U (en) | A kind of truck mixer | |
| CN209481195U (en) | A kind of acidolysis device producing rutile type titanium white | |
| CN108295796A (en) | A kind of synthesis reactor being sufficiently stirred | |
| CN217221391U (en) | Compound cauldron of graphite alkene modified polyurethane environmental protection fabrics is with supplementary feeding device | |
| CN109395634A (en) | A kind of Activated Carbon Production phosphoric acid mixing arrangement | |
| CN108642275A (en) | A kind of efficient leaching tanks of gold mine ore pulp | |
| CN209490741U (en) | The double helix band blender of batch production prefabrication lightweight wall plate device | |
| CN208912001U (en) | A kind of rubidium cesium salt ore dressing agitating device | |
| CN209740738U (en) | Acidolysis system for producing anatase titanium dioxide | |
| CN112495221A (en) | Ore pulp treatment device | |
| CN207047300U (en) | A kind of electrolytic zinc leaching device | |
| CN206262523U (en) | A kind of sulfonation reaction device for being applied to naphthalene water reducer production | |
| CN207169543U (en) | A kind of mixer for being used to prepare tungsten carbide powder | |
| CN207628374U (en) | A kind of polycarboxylic acids room temperature synthesis device | |
| CN208084670U (en) | A kind of mortar mixer | |
| CN108404953A (en) | Photocatalyst material preparation system | |
| CN204816292U (en) | A device that is used for sulfating roast sediment and sulfuric acid solution stirring to mix | |
| CN221386022U (en) | Liquid preparation tank for producing diquafosol sodium eye drops | |
| CN206715750U (en) | A kind of breast can good liquid production with being sufficiently stirred equipment | |
| CN206417423U (en) | A kind of anti-bridge formation agitating paddle of modifying plastics storage bin hopper | |
| CN207206757U (en) | Air-entrained concrete building block slurry agitator tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |