CN201785203U - Tower tray type chlorination reaction container with detachable bottom - Google Patents
Tower tray type chlorination reaction container with detachable bottom Download PDFInfo
- Publication number
- CN201785203U CN201785203U CN2010205130507U CN201020513050U CN201785203U CN 201785203 U CN201785203 U CN 201785203U CN 2010205130507 U CN2010205130507 U CN 2010205130507U CN 201020513050 U CN201020513050 U CN 201020513050U CN 201785203 U CN201785203 U CN 201785203U
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- furnace
- chlorination reaction
- tower tray
- tray type
- heater
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- Expired - Fee Related
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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model discloses a tower tray type chlorination reaction container with a detachable bottom, which comprises a furnace (1). The container is characterized in that a furnace bottom (2) is connected to the bottom of the furnace (1), a reaction section (3), a transition section (4) and an enlarging section (5) are respectively arranged in an inner cavity of the furnace (1) from top to bottom, a feeding inlet (6) is arranged on the lateral wall of the upper portion of the reaction section (3), a fillet of the inner wall of the transition section (4) is in a smoothly transitional structure, an air outlet (7) is arranged on the top of the furnace (1), and an air inlet (8) is arranged on the furnace bottom (2). The container adopting the design of a tower tray type furnace shape leads chlorination reaction of titanium-rich materials and chlorine to be more sufficient, can prevent powdered materials from being accumulated, solves the problem of difficult cleaning of residue in the furnace by the aid of the design of the detachable bottom, realizes switching over a mode of furnace building with a sieve plate and a mode of furnace building without a sieve plate, realizes multiple functions, improves equipment performance and production efficiency, and enlarges equipment applicable range.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, especially a kind of bottom dismountable tower tray type chlorination reaction container.
Background technology
At present, existing chlorination reaction container has two kinds: a kind of is cylindrical container, and another kind is a horn-type container, cylinder shape reaction segment length, and transition section is short, and the trumpet type conversion zone is short, the transition segment length.Though cylinder shape type of furnace material can be in good boiling state, the transition section weak point makes small particles material be blown conversion zone very soon, can not form good boiling state in situ, and fines easily taken out of by air-flow, and is unfavorable to chlorination reaction.The trumpet type type of furnace, flow line speed is downtrending gradually at transition section, just in time adapt along the tapered characteristics of the height of bed with raw meal particle size, small particles material can still be in good boiling state at transition section, increased the touch opportunity of material and gas, thereby help chlorination reaction, but trumpet type transition section cone angle makes easily powder pile up.And above-mentioned two kinds of type of furnaces, its furnace bottom and body of heater are integral design, and furnace bottom is non-dismountable, and residue is difficult for getting rid of cleaning, scarfing cinder difficulty in the stove after the chlorination reaction.Therefore, do not have both to help the chlorination reaction of portly material and chlorine so far, do not produce powder again and pile up, and can get rid of the container of clearing up slag smoothly, be beneficial to the production of metallurgical industry titanium tetrachloride.
Summary of the invention
The purpose of this utility model is: a kind of bottom dismountable tower tray type chlorination reaction container is provided, and it helps chlorination reaction and does not produce the bottom that residue in the cleaning stove is piled up, can be got rid of smoothly to powder, to overcome the deficiencies in the prior art.
The utility model is achieved in that the dismountable tower tray type chlorination reaction container in bottom, comprises body of heater, is connected with furnace bottom in the bottom of body of heater; The inner chamber of body of heater from top to bottom is respectively conversion zone, transition section and expanding reach; On the sidewall on conversion zone top, be provided with charging opening; The inwall fillet of transition section is the rounding off structure; And be provided with the air outlet at the top of body of heater, on furnace bottom, be provided with inlet mouth.
On the sidewall of expanding reach bottom, be provided with thief hole and temperature-measuring port.
The height of conversion zone is 1.2～3 with the diameter ratio.
The sieve plate that between body of heater and furnace bottom, is equipped with.
Between body of heater and furnace bottom, be connected for flange.
Owing to adopted technique scheme, compared with prior art, the utility model adopts the design of the tower tray type type of furnace, makes the chlorination reaction of rich titanium material and chlorine more abundant, and can prevent the powder accumulation; Dismountable bottom design has solved a scarfing cinder difficult problem in the stove, realizes having sieve plate and no sieve plate to build the switching of stove pattern by the mounting or dismounting sieve plate, realizes multi-use, has improved equipment performance and production efficiency, has enlarged the scope of application of equipment.The utility model is simple in structure, makes easily, and result of use is good.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model.
Embodiment
Embodiment of the present utility model: the structure of bottom dismountable tower tray type chlorination reaction container as shown in Figure 1, during making, produce body of heater 1 earlier, make the inner chamber of body of heater 1 from top to bottom be respectively conversion zone 3, transition section 4 and expanding reach 5, and wherein the height of conversion zone 3 is 1.2～3 with the diameter ratio, the inwall fillet of transition section 4 is made as the rounding off structure, offers charging opening 6 on the sidewall on conversion zone 3 tops; And set out gas port 7 at the top of body of heater 1, on furnace bottom 2, be provided with inlet mouth 8; On the sidewall of expanding reach 5 bottoms, produce thief hole 9 and temperature-measuring port 10; The bottom of body of heater 1 is made as cavity loop stitch orchid, and produce the furnace bottom 2 of band stitch orchid, earlier sieve plate 11 is packed in the groove of body of heater 1 bottom, filling up gasket on the flange face of body of heater 1, be fastenedly connected two circumferential weld flanges of body of heater 1 and furnace bottom 2 with studs and nut, body of heater 1 and furnace bottom 2 are connected as one.
When work, chlorine is entered by the inlet mouth 8 of furnace bottom 2, rich titanium material is entered by the charging opening 6 of the conversion zone 3 of body of heater 1, chlorine enters conversion zone 3 through sieve plate 11, and in the bed of material uniform distribution, simultaneously make bed form good initiation of fluidization state with higher gas speed, the gaseous oxidation thing that chlorination reaction generates is that titanium tetrachloride gases is discharged by furnace roof air outlet 7, and residue is got rid of cleaning by taking furnace bottom 2 apart after the chlorination reaction.
Because the utility model has increased the structure of expanding reach 5, can reduce gas velocity, make fines further with chlorine reaction, and reduce the loss that powder is taken away by air-flow; And the fillet of transition section 4 inwalls is made as the rounding off structure, has avoided inside cone angle to occur, can effectively prevent the powder accumulation; And body of heater 1 adopts split type demountable structure, easy cleaning slag with furnace bottom 2; Conversion zone 3 must have certain altitude, so just can make bed depth satisfy the purpose that furnace charge and chlorine have the sufficient contact reacts time; Between body of heater 1 and the furnace bottom 2 sieve plate 11 is housed, realizes having the switching of sieve plate and no sieve plate, realize multi-use by installing and removing sieve plate 11.
Claims (5)
1. bottom dismountable tower tray type chlorination reaction container comprises body of heater (1), it is characterized in that: be connected with furnace bottom (2) in the bottom of body of heater (1); The inner chamber of body of heater (1) from top to bottom is respectively conversion zone (3), transition section (4) and expanding reach (5); On the sidewall on conversion zone (3) top, be provided with charging opening (6); The inwall fillet of transition section (4) is the rounding off structure; And be provided with air outlet (7) at the top of body of heater (1), on furnace bottom (2), be provided with inlet mouth (8).
2. bottom according to claim 1 dismountable tower tray type chlorination reaction container is characterized in that: be provided with thief hole (9) and temperature-measuring port (10) on the sidewall of expanding reach (5) bottom.
3. bottom according to claim 1 dismountable tower tray type chlorination reaction container is characterized in that: the height of conversion zone (3) is 1.2～3 with the diameter ratio.
4. bottom according to claim 1 dismountable tower tray type chlorination reaction container is characterized in that: the sieve plate (11) that is equipped with between body of heater (1) and furnace bottom (2).
5. according to claim 1 or 4 described bottoms dismountable tower tray type chlorination reaction container, it is characterized in that: between body of heater (1) and furnace bottom (2), be connected for flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205130507U CN201785203U (en) | 2010-09-01 | 2010-09-01 | Tower tray type chlorination reaction container with detachable bottom |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205130507U CN201785203U (en) | 2010-09-01 | 2010-09-01 | Tower tray type chlorination reaction container with detachable bottom |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201785203U true CN201785203U (en) | 2011-04-06 |
Family
ID=43817178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205130507U Expired - Fee Related CN201785203U (en) | 2010-09-01 | 2010-09-01 | Tower tray type chlorination reaction container with detachable bottom |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201785203U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106369613A (en) * | 2016-11-19 | 2017-02-01 | 无锡市智锋金属科技有限公司 | Furnace body structure of incineration furnace |
| CN115725859A (en) * | 2022-11-21 | 2023-03-03 | 河南龙佰智能装备制造有限公司 | Titanium sponge fluidization reaction system and method |
-
2010
- 2010-09-01 CN CN2010205130507U patent/CN201785203U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106369613A (en) * | 2016-11-19 | 2017-02-01 | 无锡市智锋金属科技有限公司 | Furnace body structure of incineration furnace |
| CN115725859A (en) * | 2022-11-21 | 2023-03-03 | 河南龙佰智能装备制造有限公司 | Titanium sponge fluidization reaction system and method |
| CN115725859B (en) * | 2022-11-21 | 2024-03-26 | 河南龙佰智能装备制造有限公司 | Titanium sponge fluidization reaction system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110406 Termination date: 20130901 |