CN204841014U - Sulphide crystallization equipment - Google Patents
Sulphide crystallization equipment Download PDFInfo
- Publication number
- CN204841014U CN204841014U CN201520417837.6U CN201520417837U CN204841014U CN 204841014 U CN204841014 U CN 204841014U CN 201520417837 U CN201520417837 U CN 201520417837U CN 204841014 U CN204841014 U CN 204841014U
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- CN
- China
- Prior art keywords
- tank body
- jar body
- described tank
- shaft
- crystallizer
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Abstract
The utility model relates to a sulphide crystallization equipment, which comprises a tank body, physically be provided with the cover in the top at the jar, top at the jar body, the bottom is equipped with the manhole respectively, it washs the mouth to be equipped with at the top of the jar body, the gas vent, upper portion at the jar body is equipped with the overflow mouth, the solution import, on the jar body, the lower part is equipped with the thermometer mouth respectively, it has concentration analyzer to detect the mouth to open in the lower part of the jar body, steam inlet, bottom at the jar body is equipped with the drain, the discharge gate, the (mixing) shaft is equipped with along the vertical direction in central authorities at the jar body, the one end of (mixing) shaft is passed through the base bearing and is installed in jar body bottom and its other end is continuous with the speed reducer, stirring vane is equipped with to lower part at the (mixing) shaft, be equipped with a complex elastic scraper piece bottom jar body below stirring vane, cooling coil installs in the jar body, has cooling water leg cover at external cover in the jar. This equipment can improve the output of ammonium sulfate and reduce the energy consumption.
Description
Technical field
The utility model relates to crystallizer technical field, is specifically related to a kind of sulfide crystallizer.
Background technology
For a long time, the method for flue gas desulfurization has a lot, more than 100 kinds.Be ammonium sulfate for a kind of situation of ammonia desulfurizing process to be further processed from sending into cyclone after desulfurizing tower is got rid of, cyclone requires higher solid-liquid charge ratio usually, so the ammonium sulfate discharging bottom desulfurizing tower will have higher solid-to-liquid ratio, but be but easily deposited at the bottom of tower when the ammonium sulfate solid-to-liquid ratio bottom desulfurizing tower is higher, damage and stir, cause producing continuously.Another kind of situation adopts vaporation-type sulphur crystalline ammonium device, and steam consumption is large, and energy consumption is high, invests also high.
Utility model content
The purpose of this utility model is to overcome defect of the prior art, design a kind of can improve ammonium sulfate output and reduce the sulfide crystallizer of energy consumption.
For achieving the above object, the technical scheme that the utility model adopts is:
A kind of sulfide crystallizer, it is characterized in that, described equipment comprises tank body, the top of described tank body is provided with cover, at the top of described tank body, bottom is respectively equipped with manhole, Butterworth Hatch is provided with at the top of described tank body, exhaust outlet, overfall is provided with on the top of described tank body, solution inlet port, upper at described tank body, bottom is respectively equipped with thermometer mouth, have concentration analyzer in the bottom of described tank body and detect mouth, steam inlet, sewage draining exit is provided with in the bottom of described tank body, discharging opening, vertically shaft is housed in the central authorities of described tank body, one end of described shaft is arranged on described tank base by base bearing and its other end is connected with the output shaft of reductor by shaft coupling, in the bottom of described shaft, stirring vane is housed, the elastic scraper sheet coordinated with tank base is provided with below described stirring vane, cooling coil is arranged in described tank body, the cooling tube water inlet of described cooling coil, delivery port are separately positioned on bottom, the top of described tank body, have cooling water jecket in the outer cover of described tank body, the bottom of described cooling water jecket, top are respectively equipped with water inlet, the delivery port of chuck cooling water.
Wherein preferred technical scheme is provided with dismountable filter screen at described exhaust outlet.
Preferred technical scheme also has, and the angle of described stirring vane and horizontal direction is 45 °.
Preferred technical scheme also has, and described elastic scraper sheet is arranged on the cross bar vertical with shaft, and described elastic scraper sheet is spring steel plate.
Advantage of the present utility model and beneficial effect are: adopt described sulfide crystallizer to utilize water quench sulfuric acid solution, sulfide is separated out outward further at desulfurizing tower, not only increases output, and also a saving the energy.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model sulfide crystallizer;
Fig. 2 is the A-A sectional view of Fig. 1.
In figure: 1, tank body; 2, water inlet; 3, delivery port; 4, solution inlet port; 5, overfall; 6, Butterworth Hatch; 7, exhaust outlet; 8, water inlet; 9, delivery port; 10, the detection mouth of concentration analyzer; 11, thermometer mouth; 12, manhole; 13, discharging opening; 14, steam inlet; 15, sewage draining exit; 16, stirring vane; 17, key; 18, shaft; 19, cooling coil; 20, cover; 21, shaft coupling; 22, reductor; 23, support; 24, motor; 25, bearing; 26, elastic scraper sheet; 27, filter screen; 28, cross bar.
Detailed description of the invention
Below in conjunction with drawings and Examples, detailed description of the invention of the present utility model is further described.Following examples only for clearly the technical solution of the utility model being described, and can not limit protection domain of the present utility model with this.
As shown in Figure 1: the utility model is a kind of sulfide crystallizer, comprise tank body 1, the top of described tank body 1 is provided with cover 20, at the top of described tank body 1, bottom has manhole 12, Butterworth Hatch 6 is had at the top of described tank body 1, exhaust outlet 7, overfall 5 is had on the top of described tank body 1, solution inlet port 4, upper at described tank body 1, bottom has thermometer mouth 11, the detection mouth 10 of concentration analyzer is had in the bottom of described tank body 1, steam inlet 14, sewage draining exit 15 is had in the bottom of described tank body 1, discharging opening 13, in the central authorities of described tank body 1, shaft 18 is vertically housed, one end of described shaft 18 is arranged on the bottom of described tank body 1 by base bearing 25 and its other end is connected by the output shaft of shaft coupling 21 with reductor 22, in use, reductor 22 is connected with motor 24, reductor 22 is arranged on the upper of described cover 20 by support 23.By key 17, stirring vane 16 is housed in the bottom of described shaft 18, is provided with below described stirring vane 16 and the elastic scraper sheet 26 coordinated bottom tank body 1; Cooling coil 19 is arranged in described tank body 1, the cooling tube water water inlet 8 of described cooling coil 19, delivery port 9 are separately positioned on bottom, the top of described tank body, have cooling water jecket in the outer cover of described tank body 1, the bottom of described cooling water jecket, top have water inlet 2, the delivery port 3 of chuck cooling water.Preferred described stirring vane 16 is 45 ° with the angle of horizontal direction.Preferred described elastic scraper sheet 26 is arranged on the cross bar 28 vertical with shaft 18, and described elastic scraper sheet 26 is spring steel plate.Preferably be provided with dismountable filter screen 27 at described exhaust outlet 7 place.The mode of operation of described ammonium sulphate crystallizer and carrying is: bottom desulfurizing tower, through shurry pump, ammonium sulfate is sent into crystallizer, cooling water is passed in chuck He in tank inner coil pipe, ammonium sulfate is separated out further, and carries out Separation of Solid and Liquid, the solid-to-liquid ratio making crystallizer export ammonium sulfate increases.
The above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art; under the prerequisite not departing from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. a sulfide crystallizer, it is characterized in that, described equipment comprises tank body, the top of described tank body is provided with cover, at the top of described tank body, bottom is respectively equipped with manhole, Butterworth Hatch is provided with at the top of described tank body, exhaust outlet, overfall is provided with on the top of described tank body, solution inlet port, upper at described tank body, bottom is respectively equipped with thermometer mouth, have concentration analyzer in the bottom of described tank body and detect mouth, steam inlet, sewage draining exit is provided with in the bottom of described tank body, discharging opening, vertically shaft is housed in the central authorities of described tank body, one end of described shaft is arranged on described tank base by base bearing and its other end is connected with the output shaft of reductor by shaft coupling, in the bottom of described shaft, stirring vane is housed, the elastic scraper sheet coordinated with tank base is provided with below described stirring vane, cooling coil is arranged in described tank body, the cooling tube water inlet of described cooling coil, delivery port are separately positioned on bottom, the top of described tank body, have cooling water jecket in the outer cover of described tank body, the bottom of described cooling water jecket, top are respectively equipped with water inlet, the delivery port of chuck cooling water.
2. sulfide crystallizer as claimed in claim 1, is characterized in that, be provided with dismountable filter screen at described exhaust outlet.
3. sulfide crystallizer as claimed in claim 1, it is characterized in that, the angle of described stirring vane and horizontal direction is 45 °.
4. sulfide crystallizer as claimed in claim 1, it is characterized in that, described elastic scraper sheet is arranged on the cross bar vertical with shaft, and described elastic scraper sheet is spring steel plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520417837.6U CN204841014U (en) | 2015-06-17 | 2015-06-17 | Sulphide crystallization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520417837.6U CN204841014U (en) | 2015-06-17 | 2015-06-17 | Sulphide crystallization equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204841014U true CN204841014U (en) | 2015-12-09 |
Family
ID=54731613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520417837.6U Expired - Fee Related CN204841014U (en) | 2015-06-17 | 2015-06-17 | Sulphide crystallization equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204841014U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955501A (en) * | 2017-05-27 | 2017-07-18 | 湖北华丹医药科技股份有限公司 | A kind of bulk drug crystallizing tank pharmaceutical preparations temperature detection device |
| CN108624343A (en) * | 2018-06-06 | 2018-10-09 | 江苏联合创业环保有限公司 | Biomass carbonization reaction kettle |
| CN110025972A (en) * | 2019-04-18 | 2019-07-19 | 南京金瀚环保科技有限公司 | Ammonium sulfate equipment of crystallisation by cooling |
| CN115246693A (en) * | 2021-09-01 | 2022-10-28 | 江苏天楹等离子体科技有限公司 | System and method for recovering calcium sulfate in plasma fly ash molten flue gas washing wastewater |
-
2015
- 2015-06-17 CN CN201520417837.6U patent/CN204841014U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955501A (en) * | 2017-05-27 | 2017-07-18 | 湖北华丹医药科技股份有限公司 | A kind of bulk drug crystallizing tank pharmaceutical preparations temperature detection device |
| CN108624343A (en) * | 2018-06-06 | 2018-10-09 | 江苏联合创业环保有限公司 | Biomass carbonization reaction kettle |
| CN110025972A (en) * | 2019-04-18 | 2019-07-19 | 南京金瀚环保科技有限公司 | Ammonium sulfate equipment of crystallisation by cooling |
| CN115246693A (en) * | 2021-09-01 | 2022-10-28 | 江苏天楹等离子体科技有限公司 | System and method for recovering calcium sulfate in plasma fly ash molten flue gas washing wastewater |
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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: 20151209 Termination date: 20160617 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |