CN106082316A - Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement - Google Patents
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement Download PDFInfo
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- CN106082316A CN106082316A CN201610694306.0A CN201610694306A CN106082316A CN 106082316 A CN106082316 A CN 106082316A CN 201610694306 A CN201610694306 A CN 201610694306A CN 106082316 A CN106082316 A CN 106082316A
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/02—Halides of titanium
- C01G23/022—Titanium tetrachloride
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
- C01G23/07—Producing by vapour phase processes, e.g. halide oxidation
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Abstract
The invention discloses a kind of Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement, including: three feed bins；Three weighing apparatus, three weighing apparatus are connected by feed pipeline and three feed bin one_to_one corresponding respectively；Three screen clothes, in each screen cloth is located at the feed pipeline of correspondence and between weighing apparatus and feed bin, feed pipeline is provided with neighbouring screen cloth and gathering hole to be opened/closed；Carrier, the outlet of carrier connects with boiling chloridizing furnace；Batch mixing spiral organ of Corti, batch mixing spiral organ of Corti is located between weighing apparatus and the import of carrier.Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement feeding amount according to embodiments of the present invention is compared with accurate and the more uniform property of batch mixing, feeding is smooth and easy and continues, ensure that the stable and continuous of feed arrangement is run, improve product quality, improve boiling chloridizing furnace fluidized state, material through filtering mixes evenly in batch mixing spiral organ of Corti simultaneously, it is to avoid enters the material in boiling chloridizing furnace and layering occurs.
Description
Technical field
The present invention relates to Titanium Dioxide Produced by Chloride Procedure production technical field, more particularly, to a kind of Titanium Dioxide Produced by Chloride Procedure boiling
Chlorination furnace feed arrangement.
Background technology
In upper deslagging fluidizing chlorination titanium white production, raw material is mainly high titanium slag, rutile and petroleum coke, at boiling chlorine
It is under fluidized state in changing stove and reacts with chlorine.Fluidized bed furnace fluidized state in correlation technique is poor, and material is at fluidized bed furnace
Layering the most easily occur, product quality is poor, and often occurs when production operation returning gas problem, and safety is relatively low.
Summary of the invention
The application is to make following facts and the discovery of problem and understanding based on inventor:
Producing, transporting and during conveying etc., raw material high titanium slag, rutile and petroleum coke are inevitably being infiltrated
Iron filings and oarse-grained impurity.In reaction unit fill process, can often there is stuck conveyor screw in these impurity, blocking
The problems such as charging line, these problems will cause feed arrangement poor continuity, cause discontinuity to feed.The most not only can cause boiling
Rise chlorination furnace fluidized state poor, too increase the miscellaneous content entering reaction unit, reduce the matter of intermediate products and final products
Amount.
Meanwhile, need in process of production to feed to boiling chloridizing furnace continuously, but it is difficult to ensure that three during charging
Plant raw material mix homogeneously, so will cause the material entering in boiling chloridizing furnace that layering occurs, and react bad, reduce further
Intermediate products and the quality of final products
It addition, reacting gas and reacted gas are mainly high temperature, poisonous corrosive gas in chlorination furnace, common
Feeding manner and device do not ensure that furnace gas does not returns in raw material feed bin or feed system, thus cause producing
Operation occurs often return gas.
In view of this, it is contemplated that one of technical problem solved the most to a certain extent in correlation technique.To this end,
The present invention proposes a kind of Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement, and described Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feeds
Device feeding is smooth and easy and continues, and feeding amount is more accurate, it is possible to reduce miscellaneous content and the layering of material entering boiling chloridizing furnace.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to embodiments of the present invention, including: three feed bins；Three titles
Treasure, described three weighing apparatus are connected with described three feed bin one_to_one corresponding by feed pipeline respectively；Three screen clothes, Mei Gesuo
Stating in screen cloth is located at the described feed pipeline of correspondence and between described weighing apparatus and described feed bin, described feed pipeline is provided with
Neighbouring described screen cloth and gathering hole to be opened/closed；Carrier, the outlet of described carrier connects with the reaction chamber of boiling chloridizing furnace；
Batch mixing spiral organ of Corti, described batch mixing spiral organ of Corti is located between the import of described weighing apparatus and described carrier.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement feeding amount according to embodiments of the present invention relatively accurately and batch mixing relatively
Uniformity, feeding is smooth and easy and continues, it is ensured that the stable and continuous of feed arrangement is run, and improves boiling chloridizing furnace fluidized state,
Reduce the miscellaneous content entering reaction unit, improve the quality of intermediate products and final products；Meanwhile, through the material filtered
Batch mixing spiral organ of Corti mix evenly, it is to avoid entering the material in boiling chloridizing furnace and layering occur, reaction effect is good.
It addition, Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to the above embodiment of the present invention can also have as
Lower additional technical characteristic:
According to some embodiments of the present invention, Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement also includes: tramp iron separator, institute
State tramp iron separator to be located between each described feed bin and the described batch mixing spiral organ of Corti of correspondence.
According to some embodiments of the present invention, described tramp iron separator is located between described weighing apparatus and described batch mixing spiral organ of Corti.
According to some embodiments of the present invention, described carrier is connected with described boiling chloridizing furnace by feed lines, institute
State feed lines and at least include tilting upward relative to vertical direction the inclination pipeline section of extension.
According to some embodiments of the present invention, described feed lines includes that two horizontal pipeline sections, described inclination pipeline section are located at
Between two described horizontal pipeline sections.
According to some embodiments of the present invention, described feed lines is provided with the control valve controlling its break-make.
According to some embodiments of the present invention, described carrier includes that two be arranged in parallel, each described carrier divide
Feed lines that Tong Guo be not corresponding is connected with described boiling chloridizing furnace.
According to some embodiments of the present invention, described batch mixing spiral organ of Corti is three grades of spiral organ of Corti, the of described three grades of spiral organ of Corti
One-level spiral organ of Corti, second level spiral organ of Corti and third level spiral organ of Corti are vertically distributed.
According to some embodiments of the present invention, described first order spiral organ of Corti includes two, one of them described first order spiral shell
Spigot is connected with feed bin described in two of which, first order spiral organ of Corti described in other in which and feed bin phase described in other in which
Even.
The additional aspect of the present invention and advantage will part be given in the following description, and part will become from the following description
Obtain substantially, or recognized by the practice of the present invention.
Accompanying drawing explanation
Fig. 1 is the structural representation of Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to embodiments of the present invention；
Fig. 2 is the part-structure signal of Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to embodiments of the present invention
Figure；
Fig. 3 is the knot at the feed lines of Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to embodiments of the present invention
Structure schematic diagram.
Reference:
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100；Boiling chloridizing furnace 200；
Feed bin 10；Weighing apparatus 20；Screen cloth 30；Carrier 40；
Batch mixing spiral organ of Corti 50；First order spiral organ of Corti 51；Second level spiral organ of Corti 52；Third level spiral organ of Corti 53；
Tramp iron separator 60；Feed lines 70；Horizontal pipeline section 71；Tilt pipeline section 72；
Control valve 81；Switch valve 82；Blending bunker 90.
Detailed description of the invention
Embodiments of the invention are described below in detail, and the example of described embodiment is shown in the drawings.Below with reference to
The embodiment that accompanying drawing describes is exemplary, it is intended to is used for explaining the present invention, and is not considered as limiting the invention, ability
Above-described embodiment can be changed, revises, replace and modification by the those of ordinary skill in territory within the scope of the invention.
Describe Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement according to embodiments of the present invention below in conjunction with the accompanying drawings in detail
100。
Referring to figs. 1 through shown in Fig. 3, Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100 according to embodiments of the present invention
Three feed bins, 20, three screen clothes 30 of 10, three weighing apparatus, carrier 40 and batch mixing spiral organ of Corti 50 can be included.Three feed bins 10 points
Can not hold high titanium slag, rutile and petroleum coke.
Specifically, feed bin 10, screen cloth 30, weighing apparatus 20, batch mixing spiral organ of Corti 50 and carrier 40 set gradually.Weigh for three
Device 20 can be connected by feed pipeline and three feed bin 10 one_to_one corresponding respectively.It is to say, three weighing apparatus 20 and three material
Storehouse 10 one_to_one corresponding, each weighing apparatus 20 is connected with corresponding feed bin 10 by feed pipeline.The most defeated for convenience of material
Sending, as it is shown in figure 1, each weighing apparatus 20 can be arranged on the lower section of the feed bin 10 of correspondence, feed pipeline can be arranged by general vertical.
Three screen clothes 30 and three weighing apparatus 20 one_to_one corresponding, each screen cloth 30 is respectively provided in the feed pipeline of correspondence, and is positioned at
Between corresponding weighing apparatus 20 and feed bin 10.
Thus, when material flows out from feed bin 10 and flows to weighing apparatus 20, can be through screen cloth 30, screen cloth 30 can be by material
In large granular impurity filter down, prevent large granular impurity from entering weighing apparatus 20 and be positioned at the parts after weighing apparatus 20, shadow
Ring weigh effect and stuck batch mixing spiral organ of Corti 50 and carrier 40 etc., make feeding to continue, steadily and swimmingly carry out.
Further, more accurate through the material metage filtered, improve the accuracy of charging.
The mesh size of screen cloth 30 can be arranged the most flexibly, when short grained contaminant filter is fallen by needs
Time, it is more relatively small that the mesh size of screen cloth 30 can be arranged；When oarse-grained contaminant filter is fallen by needs, screen cloth 30
It is more relatively large that mesh size then can be arranged.It addition, for improving charging system dispensing more accurately, more uniformly mix,
Weighing apparatus 20 can use Weightlessness balance, to join in batch mixing spiral organ of Corti 50 according to corresponding doses.
Can be provided with the gathering hole of neighbouring corresponding screen cloth 30 on each feed pipeline, gathering hole can open and close.When
Gathering hole, when conveying, can be closed by material, prevents material from flowing out from gathering hole；When Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace enters
When material device 100 does not carry out the conveying of material, gathering hole can be opened, so that the granule foreign being trapped on screen cloth 30 is gone
Remove, prevent granule foreign to be deposited on screen cloth 30, affect the conveying effect of material.
As in figure 2 it is shown, switch valve 82 can be arranged between feed bin 10 and screen cloth 30, when switch valve 82 is opened, feed bin 10
In material can flow to screen cloth 30, when switch valve 82 cuts out, the material in feed bin 10 can not flow to screen cloth 30.When opening
When gathering hole carries out the cleaning of screen cloth 30, switch valve 82 can cut out, easy to operate.Alternatively, switch valve 82 can be hands
Dynamic valve, to facilitate operator to stop the feed of feed bin 10 the most at any time.
Batch mixing spiral organ of Corti 50 may be provided between the import of weighing apparatus 20 and carrier 40, and the outlet of carrier 40 can be with boiling
Chlorination furnace 200 is connected.Material after correct amount can realize mixing in batch mixing spiral organ of Corti 50, then by conveying
Device 40 is delivered in boiling chloridizing furnace 200.Wherein, the mixing uniformity of batch mixing spiral organ of Corti 50 is good, it is ensured that material is entering boiling
Rise before in chlorination furnace 200 and can be uniformly mixed, be beneficial to the reaction in boiling chloridizing furnace 200.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100 according to embodiments of the present invention, by feed bin 10 and title
Screen cloth 30 is set between treasure 20, makes the material flowed out from feed bin 10 can flow to weighing apparatus 20 after the filtration of screen cloth 30 again
With batch mixing spiral organ of Corti 50 etc., it is ensured that the accuracy weighed and the uniformity of batch mixing, feeding is smooth and easy and continues, it is ensured that charging
The stable and continuous of device 100 is run, and improves boiling chloridizing furnace 200 fluidized state, and reduces the miscellaneous of entrance reaction unit
Content, reduces the quality of intermediate products and final products.Meanwhile, the material through filtering mixes more in batch mixing spiral organ of Corti 50
Uniformly, it is to avoid entering the material in boiling chloridizing furnace 200 and layering occur, reaction effect is good.
Preferably, according to some embodiments of the present invention, Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100 also may be used
Including tramp iron separator 60, tramp iron separator 60 may be provided between each feed bin 10 and the batch mixing spiral organ of Corti 50 of correspondence.Tramp iron separator 60 can make
The irony impurity entering this region is held removing, is possible not only to realize the recovery to irony impurity, and achieves material
Further filtration, the impurity in material is less, is more beneficial for reaction.
After Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100 works a period of time, tramp iron separator 60 can gather relatively
Many iron tramps, at this point it is possible to the hand hole opened on tramp iron separator 60, remove the iron tramp of absorption, and this clear operation can be
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement 100 is carried out when not feeding, to ensure safety and the elimination effect of operation.
As in figure 2 it is shown, tramp iron separator 60 may be provided between weighing apparatus 20 and batch mixing spiral organ of Corti 50.Now, tramp iron separator 60 is permissible
After being positioned at screen cloth 30, screen cloth 30 can be as main filter element, and tramp iron separator 60 can use as secondary filter members,
Can improve the de-ferrous effect of tramp iron separator 60, it is to avoid the impact on tramp iron separator 60 of other impurity, meanwhile, tramp iron separator 60 is not susceptible to
Damage.
As shown in figures 1 and 3, according to some embodiments of the present invention, carrier 40 can be by feed lines 70 and boiling
Chlorination furnace 200 is connected, and feed lines 70 at least includes the inclination pipeline section 72 tilting upward extension relative to vertical direction.Namely
Say, when material moves in feed lines 70, there is the motion of one section of extension that is inclined upwardly relative to vertical direction to I haven't seen you for ages,
In feeding process, material can fill up this inclination pipeline section 72, and now material can play certain sealing function, i.e. at feed pipe
Road 70 can be formed material seal structure, prevent the material in boiling chloridizing furnace 200 from returning carrier 40 and preventing feeding process
In there is returning gas, safety improves.
As it is shown on figure 3, feed lines 70 can include two horizontal pipeline sections 71, tilt pipeline section 72 and may be provided in two horizontal pipeline sections
Between 71.Thus, it is possible to ensure that the material seal structure formed during stationarity and the feeding of feeding is more stable, it is ensured that seal effect
Really.
Further, feed lines 70 can be provided with the control valve 81 of its break-make of control.It is to say, on feed lines 70
Can arrange control valve 81, control valve 81 can control conducting and the disconnection of feed lines 70, when control valve 81 is opened, and conveying
Device 40 and boiling chloridizing furnace 200 are in connected state, and when control valve 81 is closed, carrier 40 disconnects with boiling chloridizing furnace 200.
Thus, it is possible to control the carrier 40 feeding to boiling chloridizing furnace 200 easily by control valve 81.Alternatively, control valve 81
Can be electrically-controlled valve, it is also possible to for hand-operated valve.As it is shown on figure 3, control valve 81 can be positioned adjacent to the one of boiling chloridizing furnace 200
On individual horizontal pipeline section 71, with operation and the better tightness of being more convenient for.
As it is shown in figure 1, carrier 40 can include two be arranged in parallel, specifically, two carriers 40 are arranged in parallel
Between batch mixing spiral organ of Corti 50 and boiling chloridizing furnace 200.Each carrier 40 is respectively by corresponding feed lines 70 and boiling
Chlorination furnace 200 is connected.Thus, it is possible not only to improve feeding ability, and two carriers 40 can realize complementation, it is to avoid one
When being damaged, whole device all can not feeding, material conveying effective, stationarity and reliability are higher.
According to some embodiments of the present invention, batch mixing spiral organ of Corti 50 is three grades of spiral organ of Corti.Three grades of spiral organ of Corti include the first order
Spiral organ of Corti 51, second level spiral organ of Corti 52 and third level spiral organ of Corti 53, first order spiral organ of Corti 51, second level spiral organ of Corti 52 and the third level
Spiral organ of Corti 53 is vertically distributed.It is to say, batch mixing spiral organ of Corti 50 is formed as vertically disposed three grades of spiral organ of Corti, thus,
Three grades of batch mixings, batch mixing and feeding performance can be realized good, preferably guarantee that dispensing is accurately and mixing uniform, it is achieved material exists
The purpose of mix homogeneously is admirably achieved before entering carrier 40.
As it is shown in figure 1, according to some embodiments of the present invention, first order spiral organ of Corti 51 can include two, one of them is years old
One-level spiral organ of Corti 51 is connected with two of which feed bin 10, other in which first order spiral organ of Corti 51 and other in which feed bin 10 phase
Even.It is to say, when carrying out first order batch mixing, two of which material first mixes, wherein another material individually enters
Row auger, two kinds of materials of mix homogeneously mix with another material when second level batch mixing again, it is achieved three kinds
The mixing of material, finally when third level batch mixing, three kinds of materials mix again.Thus, it is possible to raising by a relatively large margin mixes
Close effect, make the mixing uniformity of material significantly improve.
In a specific embodiment of the present invention, in one-level batch mixing, rutile and petroleum coke first mix homogeneously,
Then mix with high titanium slag again in two grades of batch mixings, finally mix in three grades of batch mixings, good mixing effect the most simultaneously.
As it is shown in figure 1, also can be provided with blending bunker 90 between carrier 40 and batch mixing spiral organ of Corti 50, blending bunker 90 is located at
Between batch mixing spiral organ of Corti 50 and carrier 40, blending bunker 90 can store through the mixed material of batch mixing spiral organ of Corti 50, and
Material is delivered to further carrier 40, is delivered in boiling chloridizing furnace by 40 materials of carrier.
Blending bunker 90 can play and temporarily stores material and balance batch mixing speed and the carrier of batch mixing spiral organ of Corti 50
The effect of the transfer rate of 40, prevents when the material flowed out in batch mixing spiral organ of Corti 50 enters directly in carrier 40, because of one
Secondary feeding too much causes carrier 40 stuck or a feeding is very few and the situation of zero load occurs, and feed arrangement 100 is permissible
The speed kept in balance carries material in boiling chloridizing furnace, and feeding is evenly and plant running is more steadily reliable.
As it is shown in figure 1, when carrier 40 is two, blending bunker 90 can be two, and with two carriers 40 1
One is corresponding connected.Thus, the material flowed out from batch mixing spiral organ of Corti 50 can enter in different blending bunker 90, and can smoothly
Subsequent delivery is realized in entering into the carrier 40 of correspondence.It is understood that the carrier 40 shown in Fig. 1 and blending bunker
90 are two is only used as example and is described, and in the present invention, the quantity of carrier 40 and blending bunker 90 is not limited to two, also
Can be one or more than two etc., specifically can be configured as required.
In sum, Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace 200 feed arrangement 100 according to embodiments of the present invention has even
Continuous charging, material mix homogeneously, remove impurity removing continuously, prevent the features such as returning charge.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace 200 feed arrangement 100 according to embodiments of the present invention other constitute and
Operation is knowable for the person of ordinary skill of the art, is not described in detail at this.
In describing the invention, it is to be understood that term " " center ", " on ", D score, "front", "rear", " vertically ",
The orientation of the instruction such as " level ", " top ", " end ", " interior ", " outward " or position relationship are to close based on orientation shown in the drawings or position
System, is for only for ease of the description present invention and simplifies description rather than instruction or imply that the device of indication or element must have
Specific orientation, with specific azimuth configuration and operation, be therefore not considered as limiting the invention.
In the present invention, unless otherwise clearly defined and limited, term " install ", " being connected ", " connection ", " fixing " etc.
Term should be interpreted broadly, and connects for example, it may be fixing, it is also possible to be to removably connect, or integral；Can be that machinery connects
Connect, it is also possible to be electrical connection or each other can communication；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, permissible
It is connection or the interaction relationship of two elements of two element internals, unless otherwise clear and definite restriction.For this area
For those of ordinary skill, above-mentioned term concrete meaning in the present invention can be understood as the case may be.
In the description of this specification, reference term " embodiment ", " specific embodiment ", " example " or " concrete example " etc.
Description means to combine this embodiment or example describes specific features, structure, material or feature be contained in the present invention extremely
In a few embodiment or example.In this manual, the schematic representation of above-mentioned term is necessarily directed to identical
Embodiment or example.And, the specific features of description, structure, material or feature can with one or more embodiments in office or
Example combines in an appropriate manner.Additionally, in the case of the most conflicting, those skilled in the art can be by this explanation
Different embodiments or the feature of example and different embodiment or example described in book are combined and combine.
Claims (9)
1. a Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement, it is characterised in that including:
Three feed bins；
Three weighing apparatus, described three weighing apparatus are connected with described three feed bin one_to_one corresponding by feed pipeline respectively；
Three screen clothes, in each described screen cloth is located at the described feed pipeline of correspondence and be positioned at described weighing apparatus and described feed bin it
Between, described feed pipeline is provided with neighbouring described screen cloth and gathering hole to be opened/closed；
Carrier, the outlet of described carrier connects with the reaction chamber of boiling chloridizing furnace；
Batch mixing spiral organ of Corti, described batch mixing spiral organ of Corti is located between the import of described weighing apparatus and described carrier.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 1, it is characterised in that also include: remove
Ironware, described tramp iron separator is located between described feed bin and the described batch mixing spiral organ of Corti of correspondence.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 2, it is characterised in that described tramp iron separator
It is located between described weighing apparatus and described batch mixing spiral organ of Corti.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 1, it is characterised in that described carrier
Being connected with described boiling chloridizing furnace by feed lines, described feed lines at least includes tilting upward relative to vertical direction prolonging
The inclination pipeline section stretched.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 4, it is characterised in that described feed pipe
Road also includes that two horizontal pipeline sections, described inclination pipeline section are located between two described horizontal pipeline sections.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 4, it is characterised in that described feed pipe
Road is provided with the control valve controlling its break-make.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 1, it is characterised in that described carrier
Including two be arranged in parallel, each described carrier is connected with described boiling chloridizing furnace by corresponding feed lines respectively.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 1, it is characterised in that described batch mixing spiral shell
Spigot is three grades of spiral organ of Corti, and the first order spiral organ of Corti of described three grades of spiral organ of Corti, second level spiral organ of Corti and third level spiral organ of Corti are along perpendicular
Straight directional spreding.
Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement the most according to claim 8, it is characterised in that the described first order
Spiral organ of Corti includes two, and one of them described first order spiral organ of Corti is connected with feed bin described in two of which, described in other in which
First order spiral organ of Corti is connected with feed bin described in other in which.
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| CN201610694306.0A CN106082316A (en) | 2016-08-19 | 2016-08-19 | Titanium Dioxide Produced by Chloride Procedure boiling chloridizing furnace feed arrangement |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108675342A (en) * | 2018-06-19 | 2018-10-19 | 河南佰利联新材料有限公司 | A kind of device and method improving titanium white chloride production efficiency |
| CN111908501A (en) * | 2020-08-25 | 2020-11-10 | 攀钢集团攀枝花钢铁研究院有限公司 | Chlorination furnace for fine-fraction titanium-rich material and fluidized bed chlorination process thereof |
| CN113108609A (en) * | 2021-04-26 | 2021-07-13 | 南京艾尔康威物料输送系统有限公司 | Automatic charging system of chlorination furnace and control method thereof |
| CN113351121A (en) * | 2021-06-30 | 2021-09-07 | 蚌埠中瓷纳米科技有限公司 | System and method for continuously conveying solid mixed material into chlorination furnace |
| CN115465887A (en) * | 2022-09-14 | 2022-12-13 | 攀钢集团攀枝花钢铁研究院有限公司 | Charging system for chlorination furnace |
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| CN108675342A (en) * | 2018-06-19 | 2018-10-19 | 河南佰利联新材料有限公司 | A kind of device and method improving titanium white chloride production efficiency |
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| CN111908501B (en) * | 2020-08-25 | 2022-07-19 | 攀钢集团攀枝花钢铁研究院有限公司 | Chlorination furnace for fine-fraction titanium-rich material and fluidized bed chlorination process thereof |
| CN113108609A (en) * | 2021-04-26 | 2021-07-13 | 南京艾尔康威物料输送系统有限公司 | Automatic charging system of chlorination furnace and control method thereof |
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