CN204702518U - High-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas - Google Patents
High-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas Download PDFInfo
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- CN204702518U CN204702518U CN201520403177.6U CN201520403177U CN204702518U CN 204702518 U CN204702518 U CN 204702518U CN 201520403177 U CN201520403177 U CN 201520403177U CN 204702518 U CN204702518 U CN 204702518U
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- boiling point
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- burner hearth
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Abstract
The utility model discloses high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas, comprise submerged pump on body of heater and circulation pulp tank, the furnace wall of described body of heater is made up of refractory brick, refractory materials packing layer and carbon steel shell from inside to outside successively, described body of heater is made up of burner hearth and two vertical spray cylinders, described spray cylinder top is provided with spray header, described spray header is communicated with submerged pump on circulation pulp tank by shower, be communicated with burner hearth bottom described spray cylinder, be respectively equipped with inlet mouth and air outlet in the upper end of described two spray cylinders.Compared with prior art, the utility model structure is simply easy to use, solves in Molten salt chlorination furnace production process, carries the problem of a large amount of high-boiling point salt in mixed gas gas secretly, make the TiCl produced
4percentage of product improves, and makes AlCl
3, FeCl
3separate from mixed gas gas Deng high-boiling point salt, separation efficiency is up to 99%.
Description
Technical field
The utility model relates to a kind of mixed gas parting furnace, particularly relates to high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas.
Background technology
In existing Molten salt chlorination furnace production process, one or more levels dust chamber device of whole employing, for separating of the high-boiling point salt in mixed gas gas, but no matter be one-level or multistage dust chamber, all high-boiling point salt in mixed gas gas cannot be separated to more than 90%, by still carrying a large amount of high-boiling point salts in the mixed gas gas of dust chamber, this part high-boiling point salt can deposit in follow-up drip washing condenser system, and enters TiCl with the circulation of system material
4in storage tank, cause TiCl
4degradation, and then affect TiCl
4the operating performance of refining system.
According to statistics, the efficiency that current single-stage dust chamber is separated high-boiling point salt is 35%, namely has the high-boiling point salt of 65% to enter elution circuit groove tank, according to TiCl in elution circuit circulation groove
4liquid sampling analysis finds, AlCl
3content accounts for 35%, FeCl
3content accounts for 56%, and solid content is 200g/L, and boiling point is relative to TiCl
4higher, due to high-boiling point salt too high levels, cause submerged pump and annex serious wear on circulation groove, and can cause fouling in the corresponding double pipe cooler of submerged pump, heat exchange efficiency reduces, and direct influential system balance, finally causes TiCl
4quality product declines.
Utility model content
The purpose of this utility model is just to provide a kind of problem solving a large amount of high-boiling point salt of mixed gas gas entrainment in Molten salt chlorination furnace production process, makes the TiCl produced
4high-boiling point salt parting furnace in the fused salt chlorimation mixed gas that percentage of product improves.
To achieve these goals, the technical solution adopted in the utility model is: high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas, comprise submerged pump on body of heater and circulation pulp tank, the furnace wall of described body of heater is from inside to outside successively by refractory brick, refractory materials packing layer and carbon steel shell composition, described body of heater is made up of burner hearth and two vertical spray cylinders, described spray cylinder top is provided with spray header, described spray header is communicated with submerged pump on circulation pulp tank by shower, be communicated with burner hearth bottom described spray cylinder, inlet mouth and air outlet is respectively equipped with in the upper end of described two spray cylinders,
As preferably, described burner hearth internal diameter is 1.3-4m;
As preferably, described spray cylinder internal diameter is 0.4-1mm;
As preferably, the spacing sprinkler spacing between described two spray cylinders is at 0.2-0.6mm;
As preferably, described burner hearth offers top salt outlet, burner hearth bottom offers bottom salt outlet.
Compared with prior art, the utility model has the advantage of: the utility model structure is simply easy to use, solve in Molten salt chlorination furnace production process, in mixed gas gas, carry the problem of a large amount of high-boiling point salt secretly, make the TiCl produced
4percentage of product improves, and makes AlCl
3, FeCl
3separate from mixed gas gas Deng high-boiling point salt, separation efficiency is up to 99%.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1, body of heater; 2, refractory brick; 3, carbon steel shell; 4, refractory materials packing layer; 5, spray cylinder; 6, spray header; 7, inlet mouth; 8, air outlet; 9, shower; 10, submerged pump on circulation pulp tank; 11, top salt outlet; 12, bottom salt discharge.
Embodiment
The utility model is described in further detail below.
Embodiment: see Fig. 1, high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas, comprise submerged pump 10 on body of heater 1 and circulation pulp tank, the furnace wall of described body of heater 1 is from inside to outside successively by refractory brick 2, refractory materials packing layer 4 and carbon steel shell 3 form, described body of heater 1 is made up of burner hearth and two vertical spray cylinders 5, described spray cylinder 5 top is provided with spray header 6, described spray header 6 is communicated with submerged pump 10 on circulation pulp tank by shower 9, be communicated with burner hearth bottom described spray cylinder 5, inlet mouth 7 and air outlet 8 is respectively equipped with in the upper end of described two spray cylinders 5.
Dust chamber is replaced with high-boiling point salt parting furnace by the utility model, this burner hearth internal diameter 1.3-4m, shell is carbon steel, inner lining refractory block 2 and refractory castable, being furnished with two internal diameters is 0.4-1mm spray cylinder 5, spray cylinder 5 shell is carbon steel, inner lining refractory block 2 and refractory castable, two shower nozzles are respectively installed at spray cylinder 5 top, spacing sprinkler spacing between described two spray cylinders 5 is at 0.2-0.6mm, this spacing makes flue gas effectively be circulated in high-boiling point salt parting furnace, by independently circulating, improve spraying effect, conveniently control in-furnace temperature by spray flux, on pulp tank, submerged pump is by TiCl
4slurry transportation sprays to shower nozzle place, and spray mud amount controls at 4-12t, and high boiling point parting furnace entrance flue gas temperature, at 400-450 DEG C, controls high boiling point parting furnace exit gas temperature at 200-250 DEG C by spray flux.Taken up fused salt in described burner hearth, molten salt composition is KCl, NaCl, MgCl
2; Temperature of molten salt is 300-500 DEG C, at this temperature, and AlCl
3, FeCl
3deng high-boiling point salt can with KCl, NaCl, MgCl
2form complex compound, make AlCl
3, FeCl
3separate from mixed gas gas Deng high-boiling point salt, separation efficiency is up to 99%.
Described burner hearth offers salt outlet, described burner hearth offers top salt outlet 11, burner hearth bottom offers bottom salt outlet, carries out salt discharge, discharged by the impurity of collected inside every 10-24 hour by salt parting furnace top salt outlet 11.According to production production capacity, within every 2-6 month, pass through bottom salt discharge 12 mouthfuls by emptying for the inside fused salt, supplemented the new salt melted by salt adding elephant trunk from top salt adding mouth.
Certain titanium sponge factory of company, original single-stage dust chamber that adopts as high-boiling point salt tripping device, high-boiling point salt separation efficiency average 35%, rear employing high-boiling point salt parting furnace as high-boiling point salt tripping device, high-boiling point salt separation efficiency average 99%, as shown in the table:
Above exhaustive presentation is carried out to high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas provided by the utility model, apply specific case herein to set forth principle of the present utility model and embodiment, the explanation of above embodiment just understands method of the present utility model and core concept thereof for helping; Simultaneously, for one of ordinary skill in the art, according to thought of the present utility model, all will change in specific embodiments and applications, to change of the present utility model and improve will be possible, and design and the scope of accessory claim defined can not be exceeded, in sum, this description should not be construed as restriction of the present utility model.
Claims (5)
1. high-boiling point salt parting furnace in a fused salt chlorimation mixed gas, comprise submerged pump on body of heater and circulation pulp tank, it is characterized in that: the furnace wall of described body of heater is made up of refractory brick, refractory materials packing layer and carbon steel shell from inside to outside successively, described body of heater is made up of burner hearth and two vertical spray cylinders, described spray cylinder top is provided with spray header, described spray header is communicated with submerged pump on circulation pulp tank by shower, be communicated with burner hearth bottom described spray cylinder, be respectively equipped with inlet mouth and air outlet in the upper end of described two spray cylinders.
2. high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas according to claim 1, is characterized in that: described burner hearth internal diameter is 1.3-4m.
3. high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas according to claim 2, is characterized in that: described spray cylinder internal diameter is 0.4-1mm.
4. high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas according to claim 3, is characterized in that: the spacing sprinkler spacing between described two spray cylinders is at 0.2-0.6mm.
5. high-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas according to claim 1, is characterized in that: described burner hearth offers top salt outlet, and burner hearth bottom offers bottom salt outlet.
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CN201520403177.6U CN204702518U (en) | 2015-06-11 | 2015-06-11 | High-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas |
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CN201520403177.6U CN204702518U (en) | 2015-06-11 | 2015-06-11 | High-boiling point salt parting furnace in a kind of fused salt chlorimation mixed gas |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106629832A (en) * | 2016-10-25 | 2017-05-10 | 锦州钛业有限公司 | Method for removing low-melting-point complex in elution tower for producing titanium tetrachloride through fused salt chlorination |
-
2015
- 2015-06-11 CN CN201520403177.6U patent/CN204702518U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106629832A (en) * | 2016-10-25 | 2017-05-10 | 锦州钛业有限公司 | Method for removing low-melting-point complex in elution tower for producing titanium tetrachloride through fused salt chlorination |
CN106629832B (en) * | 2016-10-25 | 2018-03-20 | 锦州钛业股份有限公司 | The minimizing technology of low melting point complex in fused salt chlorimation production titanium tetrachloride eluting column |
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