CN203021311U - Boiling chlorination furnace - Google Patents
Boiling chlorination furnace Download PDFInfo
- Publication number
- CN203021311U CN203021311U CN 201220730674 CN201220730674U CN203021311U CN 203021311 U CN203021311 U CN 203021311U CN 201220730674 CN201220730674 CN 201220730674 CN 201220730674 U CN201220730674 U CN 201220730674U CN 203021311 U CN203021311 U CN 203021311U
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- boiling
- chloridizing furnace
- furnace
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Abstract
The utility model discloses a boiling chlorination furnace. The boiling chlorination furnace is mainly composed of a furnace body, a boiling area, a chlorine intake manifold and the like, wherein a petroleum coke charge tube is arranged on the furnace body at the upper part of the boiling area; and a compressed air tube and a nitrogen tube are arranged on the chlorine intake manifold respectively. The boiling chlorination furnace disclosed by the utility model can be used for realizing heat insulation after blowout, and is convenient to operate, low in production cost, beneficial for restarting, and simple in structure.
Description
Technical field
The utility model relates to a kind of boiling chloridizing furnace, belongs to the titanium tetrachloride production technical field.
Background technology
at present, boiling chloridizing furnace is the major equipment of producing titanium tetrachloride, contain calcium in raw material titanium ore due to the boiling chloridizing furnace use, the material of magnesium salts and so on, and boiling chloridizing furnace after stopping chlorine because there is no exothermic heat of reaction, so temperature can descend rapidly, the calcium of molten, magnesium salts can condense into along with the reduction of temperature the lump of rock type, the serious chlorine flow opening that stops up the gas distribution dish, cause and open chlorine skewness after stove next time, can't set up the boiling bed, if after boiling chloridizing furnace stops chlorine, insulation is bad, easily affect the life-span of refractory materials, and the huge consumption that heats up and bring when again opening stove, make production cost increase.Therefore, it is very important that the insulation after the boiling chloridizing furnace blowing out seems, and also there is no the heat preservation technology for the boiling chloridizing furnace blowing out in the prior art.
The utility model content
Be to solve the problem that prior art exists, the utility model provides a kind of boiling chloridizing furnace, can realize comparatively easily the insulation after blowing out, and cost is lower.
The technical solution of the utility model is as described below:
A kind of boiling chloridizing furnace mainly is comprised of body of heater, boiling section, chlorine inlet manifold etc., on the body of heater on boiling section top, the refinery coke filling tube is set, and is respectively equipped with compressed air pipe and nitrogen tube on the chlorine inlet manifold.
Advantage of the present utility model and beneficial effect are: after the boiling chloridizing furnace blowing out, can realize boiling chloridizing furnace is incubated, easy to operate, production cost is low, is conducive to restarting of boiling chloridizing furnace, and simple in structure.
Description of drawings
Fig. 1 is the structural representation of a kind of boiling chloridizing furnace of the utility model;
In figure: 1-body of heater, 2-boiling section, 3-chlorine inlet manifold, 4-refinery coke filling tube, 5-compressed air pipe, 6-nitrogen tube.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, a kind of boiling chloridizing furnace mainly is comprised of body of heater 1, boiling section 2, chlorine inlet manifold 3 etc., on the body of heater 1 on boiling section 2 tops, refinery coke filling tube 4 is set, and is respectively equipped with compressed air pipe 5 and nitrogen tube 6 on chlorine inlet manifold 3.
Boiling chloridizing furnace of the present utility model is after blowing out, the exothermicity of utilizing refinery coke that chlorination process is used to possess, by refinery coke filling tube 4, refinery coke is joined in boiling chloridizing furnace, recycling compressed air pipe 5 and nitrogen tube 6 with pressurized air and nitrogen pass into mix in chlorine inlet manifold 3 after, join again in boiling chloridizing furnace and react with refinery coke, utilize petroleum coke combustion to put and to open the insulation effect of boiling chloridizing furnace and the mobility of boiling section 3, simultaneously can regulate temperature in boiling chloridizing furnace by regulating refinery coke and compressed-air actuated intake.
Claims (1)
1. boiling chloridizing furnace, mainly formed by body of heater (1), boiling section (2), chlorine inlet manifold (3) etc., it is characterized in that on the body of heater (1) on described boiling section (2) top, refinery coke filling tube (4) being set, be respectively equipped with compressed air pipe (5) and nitrogen tube (6) on chlorine inlet manifold (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220730674 CN203021311U (en) | 2012-12-26 | 2012-12-26 | Boiling chlorination furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220730674 CN203021311U (en) | 2012-12-26 | 2012-12-26 | Boiling chlorination furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203021311U true CN203021311U (en) | 2013-06-26 |
Family
ID=48645307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220730674 Expired - Fee Related CN203021311U (en) | 2012-12-26 | 2012-12-26 | Boiling chlorination furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203021311U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103818932A (en) * | 2014-02-28 | 2014-05-28 | 金川集团股份有限公司 | Large sieve-plate boiling chlorination furnace control parameter cold state analog device and application method |
| CN105984895A (en) * | 2015-02-02 | 2016-10-05 | 云南新立有色金属有限公司 | Baking system of boiling chlorination furnace |
| CN106542572A (en) * | 2016-10-24 | 2017-03-29 | 云南冶金新立钛业有限公司 | Bed process is made in the igniting of chlorination furnace |
| CN107892325A (en) * | 2017-11-27 | 2018-04-10 | 攀钢集团钒钛资源股份有限公司 | A kind of low temperature chlorination stove stopping production heat preserving method |
-
2012
- 2012-12-26 CN CN 201220730674 patent/CN203021311U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103818932A (en) * | 2014-02-28 | 2014-05-28 | 金川集团股份有限公司 | Large sieve-plate boiling chlorination furnace control parameter cold state analog device and application method |
| CN103818932B (en) * | 2014-02-28 | 2016-04-13 | 金川集团股份有限公司 | Large-scale have sieve plate boiling chloridizing furnace controling parameters cold-stat e simulation device and using method |
| CN105984895A (en) * | 2015-02-02 | 2016-10-05 | 云南新立有色金属有限公司 | Baking system of boiling chlorination furnace |
| CN106542572A (en) * | 2016-10-24 | 2017-03-29 | 云南冶金新立钛业有限公司 | Bed process is made in the igniting of chlorination furnace |
| CN106542572B (en) * | 2016-10-24 | 2018-01-30 | 云南冶金新立钛业有限公司 | Bed process is made in the igniting of chlorination furnace |
| CN107892325A (en) * | 2017-11-27 | 2018-04-10 | 攀钢集团钒钛资源股份有限公司 | A kind of low temperature chlorination stove stopping production heat preserving method |
| CN107892325B (en) * | 2017-11-27 | 2019-10-11 | 攀钢集团钒钛资源股份有限公司 | A kind of low temperature chlorination furnace halt production heat preserving method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130626 Termination date: 20201226 |