CN204073483U - Slag sulphur flash distillation plant - Google Patents
Slag sulphur flash distillation plant Download PDFInfo
- Publication number
- CN204073483U CN204073483U CN201420534750.2U CN201420534750U CN204073483U CN 204073483 U CN204073483 U CN 204073483U CN 201420534750 U CN201420534750 U CN 201420534750U CN 204073483 U CN204073483 U CN 204073483U
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- CN
- China
- Prior art keywords
- tank body
- motor
- upper tank
- helical blade
- slag
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model provides a kind of slag sulphur flash distillation plant, it is characterized in that: there is upper tank body, the sidewall of upper tank body is provided with charging aperture, charging aperture is connected with feed pipe, feed pipe is connected with feed hopper, be arranged with one in feed pipe to be connected with motor and to be driven the helical blade charging pusher rotated by motor, the top of upper tank body is provided with gas outlet; The below of upper tank body has the lower tank of a back taper, the bottom of lower tank is discharging opening, discharging opening is connected with discharge nozzle, be equipped with one in discharge nozzle to be connected with motor and to be driven the helical blade discharging pusher rotated by motor, helical blade discharging pusher axially stretch in upper tank body, and the upper end of this axle is provided with the cloth tray of a positive taper, the outer wall of lower tank is provided with electric heater unit.The utility model make use of sulphur and at high temperature can gasify and the feature that slag solid can not gasify, and by high temperature, sulphur is separated from slag.
Description
Technical field
The utility model belongs to a kind of device processed slag.
Background technology
In the slag of high sulfur-bearing, sulphur and slag are mixing, but carrying out separation by methods such as chemistry may pollute, and need to add chemicals, and cost compare is high.Therefore, need a kind of new device, realize sulphur effectively also to separate at low cost from slag.
Utility model content
The utility model provides a kind of slag sulphur flash distillation plant, its objective is the shortcoming solving prior art and exist, and makes the sulphur in slag can low cost and being contamination-freely effectively separated.
The utility model solves the technical scheme that its technical problem adopts:
Slag sulphur flash distillation plant, it is characterized in that: there is upper tank body, the sidewall of upper tank body is provided with charging aperture, charging aperture is connected with feed pipe, feed pipe is connected with feed hopper, be arranged with one in feed pipe to be connected with motor and to be driven the helical blade charging pusher rotated by motor, the top of upper tank body is provided with gas outlet; The below of upper tank body has the lower tank of a back taper, the bottom of lower tank is discharging opening, discharging opening is connected with discharge nozzle, be equipped with one in discharge nozzle to be connected with motor and to be driven the helical blade discharging pusher rotated by motor, helical blade discharging pusher axially stretch in upper tank body, and the upper end of this axle is provided with the cloth tray of a positive taper, the outer wall of lower tank is provided with electric heater unit.
Usefulness of the present utility model is:
The utility model make use of sulphur and at high temperature can gasify and the feature that slag solid can not gasify, by high temperature, sulphur separated from slag and leave upper tank body and lower tank respectively, the helical blade pusher of feed pipe and feed pipe defines conveyor screw dynamic seal (packing), sulfur gas can not be discharged from charging aperture and discharging opening, ensure that it is discharged from gas outlet.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is the utility model structure chart.
Detailed description of the invention
As shown in Figure 1, the utility model is used for separating containing the sulphur in the slag of sulphur, and the utility model has upper tank body 1, and the sidewall of upper tank body 1 is provided with charging aperture 11, and charging aperture 11 is connected with feed pipe 12, and feed pipe 12 is connected with feed hopper 13.Accommodatingly in feed pipe 12 be arranged with its axle 22 and be connected with motor 21 and the helical blade charging pusher 2 being driven rotation by motor 21, external diameter and the feed pipe 12 of helical blade charging pusher 2 are matched in clearance.
The top of upper tank body 1 is provided with gas outlet 14, and gas outlet 14 is connected with escape pipe 15.
The below of upper tank body 1 has the lower tank 4 of a back taper.
The bottom of lower tank 4 is discharging opening 41, and discharging opening 41 is connected with discharge nozzle 42, and discharge nozzle 42 is connected to hopper.Accommodatingly in discharge nozzle 42 be arranged with a helical blade discharging pusher 6, the axle 61 of helical blade discharging pusher 6 is connected again after the output shaft connection reducing gear 51 of a motor 5, thus helical blade discharging pusher 6 can be driven by motor 5 and rotate, external diameter and the discharge nozzle 42 of helical blade discharging pusher 6 are matched in clearance.
The axle 61 of helical blade discharging pusher 6 extends upwardly in upper tank body 1, and the upper end of this axle 61 is provided with the cloth tray 62 of a positive taper.Motor 5 driving shaft 61, makes cloth tray 62 rotate.
The outer wall of lower tank 4 is provided with heating wire 7.
During actual use, heating wire 7 heats lower tank 4 makes the inner wall temperature of lower tank 4 reach more than 450 degree.Being coiled into containing sulphur slag of hopper 13 expects that pusher 2 promotes to input from charging aperture 11 to upper tank body 1, after in the cloth tray 62 that slag drops to positive taper, landing drops on the inwall of lower tank 4 of back taper again, the cloth tray 62 of positive taper rotated make slag can fall more equably lower tank 4 inwall and can not be stacking, guarantee sulphur is wherein subject to high temperature flash distillation and gasifies like this.By flash evaporation, sulphur becomes gas to slag, sulfur gas because gas phase in container body expands the air pressure that produces and from gas outlet 14, escape pipe 15 discharges.
Remaining slag is discharged from discharging opening 41, is released by the helical blade discharging pusher 6 rotated.Due to be back taper lower tank 4 thus slag can ensure fall.
Helical blade charging pusher 2 and helical blade discharging pusher 6 not only can promote solid slag, and due to the external diameter of helical blade charging pusher 2 and feed pipe 12 are matched in clearance, external diameter and the discharge nozzle 42 of helical blade discharging pusher 6 are matched in clearance, add slag wherein, thus form the dynamic seal (packing) of spiral material body, sulfur gas cannot be discharged from feed pipe 12 or discharge nozzle 42, can only discharge from gas outlet 14.
In accompanying drawing, gas trend is dotted arrow, and solid trend is solid arrow.
Claims (1)
1. slag sulphur flash distillation plant, it is characterized in that: there is upper tank body, the sidewall of upper tank body is provided with charging aperture, charging aperture is connected with feed pipe, feed pipe is connected with feed hopper, be arranged with one in feed pipe to be connected with motor and to be driven the helical blade charging pusher rotated by motor, the top of upper tank body is provided with gas outlet; The below of upper tank body has the lower tank of a back taper, the bottom of lower tank is discharging opening, discharging opening is connected with discharge nozzle, be equipped with one in discharge nozzle to be connected with motor and to be driven the helical blade discharging pusher rotated by motor, helical blade discharging pusher axially stretch in upper tank body, and the upper end of this axle is provided with the cloth tray of a positive taper, the outer wall of lower tank is provided with electric heater unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420534750.2U CN204073483U (en) | 2014-09-16 | 2014-09-16 | Slag sulphur flash distillation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420534750.2U CN204073483U (en) | 2014-09-16 | 2014-09-16 | Slag sulphur flash distillation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204073483U true CN204073483U (en) | 2015-01-07 |
Family
ID=52166251
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420534750.2U Expired - Fee Related CN204073483U (en) | 2014-09-16 | 2014-09-16 | Slag sulphur flash distillation plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204073483U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105864743A (en) * | 2016-05-26 | 2016-08-17 | 清华大学 | Pollution discharge, water and energy saving, recovery and separation device and method of steam injection boiler |
| CN106744706A (en) * | 2016-12-06 | 2017-05-31 | 山东阳谷华泰化工股份有限公司 | The process units of insoluble sulfur and the method for production insoluble sulfur |
| CN107324287A (en) * | 2017-07-11 | 2017-11-07 | 四川理工学院 | A kind of high temperature steam desulfurization device |
| CN116625103A (en) * | 2023-07-25 | 2023-08-22 | 湖南华尔特今朝科技有限公司 | Discharging device for flash evaporation equipment |
-
2014
- 2014-09-16 CN CN201420534750.2U patent/CN204073483U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105864743A (en) * | 2016-05-26 | 2016-08-17 | 清华大学 | Pollution discharge, water and energy saving, recovery and separation device and method of steam injection boiler |
| CN106744706A (en) * | 2016-12-06 | 2017-05-31 | 山东阳谷华泰化工股份有限公司 | The process units of insoluble sulfur and the method for production insoluble sulfur |
| CN107324287A (en) * | 2017-07-11 | 2017-11-07 | 四川理工学院 | A kind of high temperature steam desulfurization device |
| CN107324287B (en) * | 2017-07-11 | 2019-05-14 | 四川理工学院 | A kind of high temperature steam desulfurization device |
| CN116625103A (en) * | 2023-07-25 | 2023-08-22 | 湖南华尔特今朝科技有限公司 | Discharging device for flash evaporation equipment |
| CN116625103B (en) * | 2023-07-25 | 2023-09-22 | 湖南华尔特今朝科技有限公司 | Discharging device for flash evaporation equipment |
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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 |
Granted publication date: 20150107 Termination date: 20150916 |
|
| EXPY | Termination of patent right or utility model |