CN205061581U - Sulphur ammonium crystallization equipment - Google Patents
Sulphur ammonium crystallization equipment Download PDFInfo
- Publication number
- CN205061581U CN205061581U CN201520775547.9U CN201520775547U CN205061581U CN 205061581 U CN205061581 U CN 205061581U CN 201520775547 U CN201520775547 U CN 201520775547U CN 205061581 U CN205061581 U CN 205061581U
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- CN
- China
- Prior art keywords
- sulphur ammonium
- sulphur
- ammonium
- backflow pipeline
- crystalline ammonium
- Prior art date
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Abstract
The utility model discloses a sulphur ammonium crystallization equipment, including crystallization pump (1), centrifugal separator (2), sulphur ammonium crystallizer tank (3), saturator (4), sulphur ammonium crystallizer tank (3) be connected through main backflow pipeline (7) with saturator (4), sulphur ammonium crystallizer tank (3) and saturator (4) still be equipped with additional backflow pipeline (5), the export and main backflow pipeline (7) the intercommunication of additional backflow pipeline (5). Adopt above -mentioned technical scheme, solved the long -time ejection of compact of sulphur ammonium and leaded to backflow pipeline, the problem of mother liquor area gas from backflow pipeline " against the current " to the centrifugal separator, under the condition of not changing the crystallization pump, increase material loading speed and phegmal reflux improve sulphur ammonium output, reduce the saturator resistance, the labor intensity of because of the operating accident that above -mentioned reason caused, workman is reduced, be particularly suitable for the transformation to current manufacturing equipment, economic benefits clear height.
Description
Technical field
The utility model belongs to the technical field of the ammonium sulfate process in coke-oven gas production.More specifically, the utility model relates to a kind of sulphur crystalline ammonium equipment.
Background technology
At present, coke-oven gas deamination-Spray Saturator method produces the crystallizer tank that thiamine process configures, and has considered the coupling of material loading speed and quantity of reflux and the exhausting problem of backflow mother liquor.But, on equipment in the prior art, be not equipped with corresponding equipment.
For ensureing the continous-stable of saturex operation, corresponding transformation must be carried out to it.
Utility model content
The utility model provides a kind of sulphur crystalline ammonium equipment, its objective is and ensures the continuous of saturex operation and stability.
To achieve these goals, the technical scheme that the utility model is taked is:
Sulphur crystalline ammonium equipment of the present utility model, comprise crystallization pump, whizzer, sulphur crystalline ammonium groove, saturex, described sulphur crystalline ammonium groove is connected by main reflux line with saturex, described sulphur crystalline ammonium groove and saturex are also provided with additional reflow pipeline, and the outlet of described additional reflow pipeline is communicated with main reflux line.
The top drilling of described main reflux line is connected with diffuse channel, and the height of described diffuse channel is higher than the height of saturex.
Described crystallization pump, to the ammonium sulfate liquor pipeline of sulphur crystalline ammonium groove, is the high speed mother liquor inlet pipe be tangentially connected with the junction of sulphur crystalline ammonium groove.
The utility model adopts technique scheme, and solve the long-time discharging of sulphur ammonium and cause reflux line, mother liquor band gas is from reflux line " adverse current " to the problem of whizzer; Under the condition not changing crystallization pump, increase material loading speed and quantity of reflux, improve sulphur ammonium output, reduce saturex resistance; Reduce the work accident because above-mentioned reason causes, reduce labor strength; Be particularly suitable for the transformation to existing processing unit, economic benefit clear height.
Accompanying drawing explanation
Brief description is marked as follows in content shown in accompanying drawing and figure:
Fig. 1 is the structural representation of the sulphur crystalline ammonium groove in the utility model;
Fig. 2 is that Spray Saturator of the present utility model produces position structural representation in sulphur ammonium.
Be labeled as in figure:
1, crystallization pump, 2, whizzer, 3, sulphur crystalline ammonium groove, 4, saturex, 5, additional reflow pipeline, 6, diffuse channel, 7, main reflux line, 8, sulphur ammonium crystal grain, 9, high speed mother liquor inlet pipe.
Embodiment
Contrast accompanying drawing below, by the description to embodiment, embodiment of the present utility model is described in further detail, have more complete, accurate and deep understanding to help those skilled in the art to inventive concept of the present utility model, technical scheme.
Structure of the present utility model as shown in Figure 1 and Figure 2, be a kind of sulphur crystalline ammonium equipment, comprise crystallization pump 1, whizzer 2, sulphur crystalline ammonium groove 3, saturex 4, described sulphur crystalline ammonium groove 3 is connected by main reflux line 7 with saturex 4.
Ammonium sulfate liquor crystallizer tank is that the mother liquor containing sulphur crystalline ammonium bottom sulphur ammonium saturex 4 is pumped to eminence groove tank by a kind of crystallization pump 1 that utilizes.
During work, under the drive of whizzer 2, high speed mother liquor tangentially enters sulphur crystalline ammonium groove 3 by pipeline, and rotate to outlet in sulphur crystalline ammonium groove 3 inner high speed, return saturex 4, sulphur crystalline ammonium precipitates at sulphur crystalline ammonium groove 3.
In order to solve prior art Problems existing and overcome its defect, realize the goal of the invention ensureing the continuous of saturex operation and stability, the technical scheme that the utility model is taked is:
As shown in Figure 1 and Figure 2, sulphur crystalline ammonium equipment of the present utility model, wherein, sulphur crystalline ammonium groove 3 and saturex 4 are also provided with additional reflow pipeline 5, and the outlet of described additional reflow pipeline 5 is communicated with main reflux line 7.
On original crystallizer tank body, identical crystallization reflux line is designed with script in an additional road, is merged on main reflux line.The design that technique scheme of the present utility model changes prior art is not enough, improves material loading speed, can also effectively prevent return line reflux.Utilize existing equipment, practicing every conceivable frugality cost in principle, reaching requirement of the present utility model.
The top drilling of described main reflux line is connected with diffuse channel 6, and the height of described diffuse channel 6 is higher than the height of saturex 4.
At main reflux line top drilling, increase to saturex height, this height is as diffuse channel.
The ammonium sulfate liquor pipeline of described crystallization pump 1 to sulphur crystalline ammonium groove 3 is the high speed mother liquor inlet pipe 8 be tangentially connected with the junction of sulphur crystalline ammonium groove 3.
The utility model is under the situation do not stopped production at crystallization pump, utilizes stand-by facilities to complete transformation.
Effect of the present utility model is:
1, solving the long-time discharging of sulphur ammonium causes reflux line, mother liquor band gas from reflux line " adverse current " to the problem of whizzer;
2, under the condition not changing crystallization pump, increase material loading speed and quantity of reflux, improve sulphur ammonium output, reduce saturex resistance;
3, reduce the work accident because above-mentioned reason causes, reduce labor strength;
4, be particularly suitable for existing technological transformation, economical and practical.
By reference to the accompanying drawings the utility model is exemplarily described above; obvious the utility model specific implementation is not subject to the restrictions described above; as long as have employed the improvement of the various unsubstantialities that method of the present utility model is conceived and technical scheme is carried out; or design of the present utility model and technical scheme directly applied to other occasion, all within protection domain of the present utility model without to improve.
Claims (3)
1. a sulphur crystalline ammonium equipment, comprise crystallization pump (1), whizzer (2), sulphur crystalline ammonium groove (3), saturex (4), described sulphur crystalline ammonium groove (3) is connected by main reflux line (7) with saturex (4), it is characterized in that: described sulphur crystalline ammonium groove (3) and saturex (4) are also provided with additional reflow pipeline (5), and the outlet of described additional reflow pipeline (5) is communicated with main reflux line (7).
2. according to sulphur crystalline ammonium equipment according to claim 1, it is characterized in that: the top drilling of described main reflux line is connected with diffuse channel (6), the height of described diffuse channel (6) is higher than the height of saturex (4).
3. according to sulphur crystalline ammonium equipment according to claim 1, it is characterized in that: described crystallization pump (1), to the ammonium sulfate liquor pipeline of sulphur crystalline ammonium groove (3), is the high speed mother liquor inlet pipe (8) be tangentially connected with the junction of sulphur crystalline ammonium groove (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520775547.9U CN205061581U (en) | 2015-09-30 | 2015-09-30 | Sulphur ammonium crystallization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520775547.9U CN205061581U (en) | 2015-09-30 | 2015-09-30 | Sulphur ammonium crystallization equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061581U true CN205061581U (en) | 2016-03-02 |
Family
ID=55388162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520775547.9U Expired - Fee Related CN205061581U (en) | 2015-09-30 | 2015-09-30 | Sulphur ammonium crystallization equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061581U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105197962A (en) * | 2015-09-30 | 2015-12-30 | 芜湖新兴铸管有限责任公司 | Ammonium sulfate crystallization equipment |
| CN111647444A (en) * | 2019-03-19 | 2020-09-11 | 孝义市鹏飞实业有限公司 | Heavy metal treatment device for desulfurization solution |
-
2015
- 2015-09-30 CN CN201520775547.9U patent/CN205061581U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105197962A (en) * | 2015-09-30 | 2015-12-30 | 芜湖新兴铸管有限责任公司 | Ammonium sulfate crystallization equipment |
| CN111647444A (en) * | 2019-03-19 | 2020-09-11 | 孝义市鹏飞实业有限公司 | Heavy metal treatment device for desulfurization solution |
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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: 20160302 Termination date: 20200930 |