CN204411784U - For the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology - Google Patents
For the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology Download PDFInfo
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- CN204411784U CN204411784U CN201520073779.XU CN201520073779U CN204411784U CN 204411784 U CN204411784 U CN 204411784U CN 201520073779 U CN201520073779 U CN 201520073779U CN 204411784 U CN204411784 U CN 204411784U
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- storage tank
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- titanium dioxide
- filter press
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Abstract
The utility model discloses a kind of for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, this equipment comprises: for depositing the filtrate storage tank of filter press filtrate; For depositing the flocculant storage tank of flocculant; First blender, described first blender is connected with described filtrate storage tank and described flocculant storage tank respectively; For depositing the aluminum sulfate storage tank of aluminum sulfate; Second blender, described second blender is connected with described aluminum sulfate storage tank with described first blender respectively; And the subsider to be connected with described second blender.Of the present utility model for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, owing to arranging the cause of flocculant storage tank and aluminum sulfate storage tank, be that filtrate adds flocculant and aluminum sulfate by flocculant storage tank and aluminum sulfate storage tank, improve the sinking speed of the titanium dioxide particle in filtrate, thus can enhance productivity to a certain extent.
Description
Technical field
The utility model relates to equipment of industrial product technical field, particularly a kind of for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology.
Background technology
At present, in the technology of chloridising preparing titanium dioxide, the titanium dioxide after coating is coagulation, and wherein containing many salts, the way generally by first washing rear filtration removes salt wherein.But in the filtrate after having filtered, still can contain a certain amount of titanium dioxide particle, this not only adds the loss of titanium dioxide, also improve the difficulty of subsequent treatment.
Usually, utilize the method for adding flocculant in filtrate to reach the object of flocculating setting titanium dioxide particle, but owing to containing relatively large titanium dioxide particle in filtrate, so flocculation process is slow, titanium dioxide particles settling cannot be made at short notice, not only affect normal continuous seepage, and cause great waste.
Utility model content
The utility model is intended to solve one of above-mentioned technical problem of the prior art at least to a certain extent.For this reason, an object of the present utility model is that proposition is a kind of for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, and this filter press filtrate treatment facility be used in Titanium Dioxide Produced by Chloride Procedure production technology can improve the sinking speed of the titanium dioxide particle in filtrate to a certain extent.
According to the utility model embodiment for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, it comprises: for depositing the filtrate storage tank of filter press filtrate; For depositing the flocculant storage tank of flocculant; First blender, described first blender is connected with described filtrate storage tank and described flocculant storage tank respectively; For depositing the aluminum sulfate storage tank of aluminum sulfate; Second blender, described second blender is connected with described aluminum sulfate storage tank with described first blender respectively; And subsider, described subsider is connected with described second blender.
According to the utility model embodiment for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, owing to being provided with the cause of aluminum sulfate storage tank, add aluminum sulfate by aluminum sulfate storage tank, thus improve the sinking speed of the titanium dioxide particle in filtrate.
In addition, according to the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology of the utility model embodiment, following additional technical feature can also be had:
According to embodiments more of the present utility model, described first blender is static mixer.
According to embodiments more of the present utility model, described second blender is static mixer.
According to embodiments more of the present utility model, between described flocculant storage tank and described first blender, be provided with flocculant delivery pump.
Preferably, according to embodiments more of the present utility model, described flocculant delivery pump is variable-flow delivery pump.
According to embodiments more of the present utility model, between described filtrate storage tank and described first blender, be provided with filtrate delivery pump.
Preferably, according to embodiments more of the present utility model, described filtrate delivery pump is variable-flow delivery pump.
According to embodiments more of the present utility model, between described aluminum sulfate storage tank and described second blender, be provided with aluminum sulfate delivery pump.
Preferably, according to embodiments more of the present utility model, described aluminum sulfate delivery pump is variable-flow delivery pump.
According to the utility model embodiment for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, also comprise: wastewater regulation tank, described wastewater regulation tank is connected with described subsider.
Accompanying drawing explanation
Fig. 1 is the schematic diagram for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology according to the utility model embodiment.
Detailed description of the invention
Be described below in detail embodiment of the present utility model, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has element that is identical or similar functions from start to finish.Be exemplary below by the embodiment be described with reference to the drawings, be intended to for explaining the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, it will be appreciated that, term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end " " interior ", " outward ", " clockwise ", orientation or the position relationship of the instruction such as " counterclockwise " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.
In addition, term " first ", " second " only for describing object, and can not be interpreted as instruction or hint relative importance or imply the quantity indicating indicated technical characteristic.Thus, be limited with " first ", the feature of " second " can express or impliedly comprise one or more these features.In description of the present utility model, the implication of " multiple " is at least two, such as two, three etc., unless otherwise expressly limited specifically.
In the utility model, unless otherwise clearly defined and limited, the term such as term " installation ", " being connected ", " connection ", " fixing " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or integral; Can be mechanical connection, also can be electrically connected maybe can communicate with one another; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals or the interaction relationship of two elements.For the ordinary skill in the art, the concrete meaning of above-mentioned term in the utility model can be understood as the case may be.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature it " on " or D score can comprise the first and second features and directly contact, also can comprise the first and second features and not be directly contact but by the other characterisation contact between them.And, fisrt feature second feature " on ", " top " and " above " comprise fisrt feature directly over second feature and oblique upper, or only represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " below " and " below " comprise fisrt feature immediately below second feature and tiltedly below, or only represent that fisrt feature level height is less than second feature.
Below with reference to Fig. 1 describe in detail according to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology.
As shown in Figure 1, filtrate storage tank 1, flocculant storage tank 2, first blender 3, aluminum sulfate storage tank 4, second blender 5 and subsider 6 can be comprised according to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology.
According to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology, filtrate storage tank 1 can be formed as general cylindrical shape, filtrate storage tank 1 can be used for depositing the press filtration filtrate formed through filter press, filtrate wherein can be supplied coupled equipment to complete subsequent treatment simultaneously.
According to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology, flocculant storage tank 2 can be used for the flocculant depositing titanium dioxide particle in sedimentation filtrate, flocculant wherein can be supplied coupled equipment to carry out subsequent treatment operation simultaneously.
According to embodiments more of the present utility model, as shown in Figure 1, first blender 3 is connected with filtrate storage tank 1 and flocculant storage tank 2 respectively, the filtrate that filtrate storage tank 1 can be confessed by such first blender 3 and the flocculant that flocculant storage tank 2 is confessed fully mix, accelerate the sinking speed of the titanium dioxide particle in filtrate to a certain extent, the mixed liquor of filtrate and flocculant is supplied coupled equipment to carry out subsequent treatment operation simultaneously.
According to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology, aluminum sulfate storage tank 4 can be used for depositing the aluminum sulfate can accelerating titanium dioxide particle sinking speed, aluminum sulfate wherein can be supplied coupled equipment to complete subsequent treatment simultaneously.
According to embodiments more of the present utility model, as shown in Figure 1, second blender 5 is connected with aluminum sulfate storage tank 4 with the first blender 3 respectively, the aluminum sulfate that the mixed liquor of the filtrate that the first blender 3 can be confessed by such second blender 5 and flocculant and aluminum sulfate storage tank 4 are confessed fully mixes, the sinking speed of titanium dioxide particle in further quickening filtrate, supplies coupled equipment to carry out subsequent treatment operation by the mixed liquor of filtrate, flocculant and aluminum sulfate simultaneously.
According to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology, subsider 6 can be used for separating titanium white powder particle and clear liquid, the titanium dioxide particle completing flocculating setting is sunken to the bottom of subsider 6 under gravity, clear liquid is peripherally overflow discharge from groove top, completes Separation of Solid and Liquid.
To sum up, according to the utility model embodiment for the filter press filtrate treatment facility 100 in Titanium Dioxide Produced by Chloride Procedure production technology, flocculant and aluminum sulfate is added to filtrate by flocculant storage tank 2 and aluminum sulfate storage tank 4, the first blender 3 and the second blender 5 is utilized filtrate, flocculant and aluminum sulfate fully to be mixed, by the titanium dioxide particle flocculation sedimentation in filtrate, thus accelerate the speed of titanium dioxide particles settling to a certain extent, and then ensure filtrate treatment facility can normally, continuous seepage, enhance productivity.
According to embodiments more of the present utility model, first blender 3 can be static mixer, rely on special construction and the fluid motion of the mixed cell in it, the flocculant that filtrate filtrate storage tank 1 can confessed and flocculant storage tank 2 are confessed fully mixes, not only compact conformation, energy consumption are little, and good mixing property, the sinking speed of the titanium dioxide particle in filtrate can be accelerated to a certain extent, thus enhance productivity.
According to embodiments more of the present utility model, second blender 5 can be static mixer, rely on special construction and the fluid motion of the mixed cell in it, the aluminum sulfate that the filtrate confess the first blender 3 and the mixed liquor of flocculant and aluminum sulfate storage tank 4 are confessed fully mixes, not only compact conformation, and energy consumption is little, and invest little, good mixing property, can accelerate the sinking speed of titanium dioxide particle in mixed liquor further, thus enhance productivity.
According to embodiments more of the present utility model, as shown in Figure 1, flocculant delivery pump 21 is provided with between flocculant storage tank 2 and the first blender 3, according to the content of titanium dioxide particle in filtrate, flocculant in flocculant storage tank 2 is delivered to the first blender 3, ensures that the flocculant entering the first blender 3 has suitable flow.
As preferred embodiment, flocculant delivery pump 21 can be variable-flow delivery pump, such as, flocculant delivery pump 21 can be single acting vane pump, radial plunger pump, axial plunger pump etc., thus, the many factors such as the content of titanium dioxide particle and the flow of filtrate in filtrate can be taken into account consider simultaneously, and regulate the flow of flocculant adaptively, thus regulate the addition entering flocculant in the first blender 3, make the flocculant in the first blender 3 have suitable addition, and then accelerate the sinking speed of titanium dioxide particle.
As preferred embodiment, the addition of flocculant can be 2.5-30L/m
3, but be not limited thereto.Such as, the addition of flocculant can be 10L/m
3.
Thus, titanium dioxide particle flocculation sedimentation ground speed can be accelerated, while enhancing productivity, cost-saving.For the ordinary skill in the art, can consider according to many-sides such as different work condition environments, demand and costs, and determine the addition of flocculant adaptively, to this, the utility model does not make particular determination.
According to embodiments more of the present utility model, as shown in Figure 1, filtrate delivery pump 11 is provided with between filtrate storage tank 1 and the first blender 3, according to the content of titanium dioxide particle in filtrate, filtrate in filtrate storage tank 1 is delivered to the first blender 3, thus makes the filtrate entering the first blender 3 have certain pressure and flow.
As preferred embodiment, filtrate delivery pump 11 can be variable-flow delivery pump, such as, filtrate delivery pump 11 can be single acting vane pump, radial plunger pump, axial plunger pump etc., thus, the many factors such as the content of titanium dioxide particle in filtrate and the mixed of the first blender 3 can be taken into account consider simultaneously, and the flow of filtrate adaptively, thus regulate the amount entering filtrate in the first blender 3, filtrate in first blender 3 and flocculant are matched, and then accelerate the sinking speed of titanium dioxide particle, while enhancing productivity, cost-saving.
According to embodiments more of the present utility model, as shown in Figure 1, aluminum sulfate delivery pump 41 is provided with between aluminum sulfate storage tank 4 and the second blender 5, according to the content of titanium dioxide particle in filtrate, aluminum sulfate in aluminum sulfate storage tank 4 is delivered to the second blender 5, the aluminum sulfate tool pressure in need that guarantee enters in the second blender 5 and flow.
As preferred embodiment, aluminum sulfate delivery pump 41 can be variable delivery pump, such as, aluminum sulfate delivery pump 41 can be single acting vane pump, radial plunger pump, axial plunger pump etc., thus, the many factors such as the flow of mixed liquor in the content of titanium dioxide particle in filtrate and the first blender 3 can be taken into account consider simultaneously, and regulate the flow of aluminum sulfate adaptively, thus regulate the addition entering aluminum sulfate in the second blender 5, make the aluminum sulfate in the second blender 5 have suitable addition, accelerate the sinking speed of titanium dioxide particle further.
As preferred embodiment, according to embodiments more of the present utility model, the addition of aluminum sulfate can be 0.5L/m
3-5L/m
3, but be not limited thereto.Such as, the addition of aluminum sulfate can be 3L/m
3.Thus, titanium dioxide particle flocculation sedimentation ground speed can be accelerated further, while enhancing productivity, cost-saving.For the ordinary skill in the art, can consider according to many-sides such as different work condition environments, demand and costs, and determine the addition of aluminum sulfate adaptively, to this, the utility model does not make particular determination.
According to the utility model embodiment, as shown in Figure 1, filter press filtrate treatment facility also comprises wastewater regulation tank 7, wastewater regulation tank is connected with subsider 6, the water quality of the clear liquid of being discharged by the overflow of subsider 6 top and the water yield are regulated, such as, can regulate the pH value of water, water temperature and discharge capacity etc., thus ensure that conveyance conduit does not normally work by the impact of peak flow change, and then ensure normal continuous seepage, enhance productivity to a certain extent.
In the description of this description, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present utility model or example.In this manual, to the schematic representation of above-mentioned term not must for be identical embodiment or example.And the specific features of description, structure, material or feature can combine in an appropriate manner in any one or more embodiment or example.In addition, the different embodiment described in this description or example can carry out engaging and combining by those skilled in the art.
Although illustrate and described embodiment of the present utility model above, be understandable that, above-described embodiment is exemplary, can not be interpreted as restriction of the present utility model, those of ordinary skill in the art can change above-described embodiment, revises, replace and modification in scope of the present utility model.
Claims (10)
1., for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, it is characterized in that, comprising:
For depositing the filtrate storage tank of filter press filtrate;
For depositing the flocculant storage tank of flocculant;
First blender, described first blender is connected with described filtrate storage tank and described flocculant storage tank respectively;
For depositing the aluminum sulfate storage tank of aluminum sulfate;
Second blender, described second blender is connected with described aluminum sulfate storage tank with described first blender respectively; And subsider, described subsider is connected with described second blender.
2. according to claim 1ly it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, described first blender is static mixer.
3. according to claim 1ly it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, described second blender is static mixer.
4. according to claim 1ly to it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, between described flocculant storage tank and described first blender, be provided with flocculant delivery pump.
5. according to claim 4ly it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, described flocculant delivery pump is variable-flow delivery pump.
6. according to claim 1ly to it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, between described filtrate storage tank and described first blender, be provided with filtrate delivery pump.
7. according to claim 6ly it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, described filtrate delivery pump is variable-flow delivery pump.
8. according to claim 1ly to it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, between described aluminum sulfate storage tank and described second blender, be provided with aluminum sulfate delivery pump.
9. according to claim 8ly it is characterized in that for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology, described aluminum sulfate delivery pump is variable-flow delivery pump.
10. according to claim 1ly it is characterized in that, also comprise for the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology: wastewater regulation tank, described wastewater regulation tank is connected with described subsider.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520073779.XU CN204411784U (en) | 2015-02-02 | 2015-02-02 | For the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520073779.XU CN204411784U (en) | 2015-02-02 | 2015-02-02 | For the filter press filtrate treatment facility in Titanium Dioxide Produced by Chloride Procedure production technology |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106075963A (en) * | 2016-07-18 | 2016-11-09 | 攀钢集团攀枝花钢铁研究院有限公司 | A kind of method purifying titanium liquid |
-
2015
- 2015-02-02 CN CN201520073779.XU patent/CN204411784U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106075963A (en) * | 2016-07-18 | 2016-11-09 | 攀钢集团攀枝花钢铁研究院有限公司 | A kind of method purifying titanium liquid |
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| 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: 650100 Kunming, Xishan District, Yunnan Spring Road, No. 913 Patentee after: Yunnan metallurgy Xin Litai industry company limited Address before: 650100 Kunming, Xishan District, Yunnan Spring Road, No. 913 Patentee before: Yunnan Xinli Nonferrous Metal Co., Ltd. |