CN211420081U - Condensate tank capable of removing impurities and separating water - Google Patents
Condensate tank capable of removing impurities and separating water Download PDFInfo
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- CN211420081U CN211420081U CN201922176360.8U CN201922176360U CN211420081U CN 211420081 U CN211420081 U CN 211420081U CN 201922176360 U CN201922176360 U CN 201922176360U CN 211420081 U CN211420081 U CN 211420081U
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Abstract
The utility model relates to a can detach impurity and condensate groove of separation water, including barrel, head, baffle one, baffle two, condensate inlet tube, water outlet, contain naphthalene condensate export, spray the liquid export, spray liquid full-flow mouth and light tar inlet tube. The beneficial effects are as follows: the condensate that comes from the primary cooler gets into this utility model device one side of baffle, through static separation detach impurity, isolate the opposite side that the moisture flows to the baffle, mix the even liquid that sprays of mixing through supplementary light tar again, return the primary cooler hypomere circulation and spray, can improve the naphthalene removal effect of primary cooler, reduce the spray pipe and block up the probability, improve and spray the operating efficiency.
Description
Technical Field
The utility model relates to a splitter in the technical field of coal coking, in particular to a condensate tank capable of removing impurities and separating water.
Background
The lower section of the primary cooler has the naphthalene removing function, and the naphthalene condensed on the tube wall of the primary cooler can be dissolved and removed by adopting light coke sprayed by oil circulation. At present, in actual production, a horizontal tank is usually adopted to collect condensate of a primary cooler, a part of light tar is supplemented, and naphthalene is removed by circulating spraying, so that the method has the following defects:
1) in the circulating spraying process, the loss is caused by naphthalene dissolved by tar, so that the proportion of oil and water in the circulating spraying liquid is disordered, the naphthalene dissolving efficiency is reduced, and the naphthalene removing effect is poor;
2) along with the circulation spraying process, more and more naphthalene-containing impurities can be accumulated in the circulation spraying liquid, so that the spraying pipe is easily blocked, and naphthalene removal operation is influenced.
SUMMERY OF THE UTILITY MODEL
For overcoming the prior art defect, the utility model provides a technical problem provides a can detach impurity and the condensate groove of separation water, and the condensate that comes from the primary cooler gets into this utility model device one side of baffle, through static separation detach impurity, separate out the opposite side that the moisture flows to the baffle at all, mix the even liquid that sprays of mixing through supplementary light tar again, return the primary cooler hypomere and circulate and spray, can improve the naphthalene removal effect of primary cooler, reduce the spray line and block up the probability, improve and spray the operating efficiency.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a condensate tank capable of removing impurities and separating water comprises a cylinder body, two end sockets, a first partition plate, a second partition plate, a condensate inlet pipe, a water outlet, a naphthalene-containing condensate outlet, a spray liquid full-flow port and a light tar inlet pipe, and is characterized in that the two end sockets are respectively and fixedly connected with the two ends of the cylinder body to form the condensate tank; the first partition plate is arranged at the left position of the center in the barrel, the other three end parts except the upper end part are fixedly connected with the barrel, and the upper end part is provided with a notch; the second partition plate is arranged on the left side of the first partition plate in the cylinder, the other two end parts except the upper end part and the lower end part are fixedly connected with the cylinder, and the upper end part and the lower end part are provided with notches; the condensate inlet pipe is arranged on the left side of the partition plate II and extends into the lower part of the condensate tank from the upper part of the cylinder, the outlet end of the condensate inlet pipe is L-shaped and horizontal, and the outlet of the condensate inlet pipe is arranged leftwards; the light tar inlet pipe is arranged on the right side of the first partition plate and extends into the lower part of the condensate tank from the upper part of the cylinder body; the naphthalene-containing condensate outlet is horizontally arranged on the left end socket and is lower than the outlet end of the condensate inlet pipe; the water outlet is horizontally arranged on the left end socket, and the position of the water outlet is lower than the upper end part of the second partition plate and higher than the upper end part of the first partition plate; the spraying liquid full flow port is horizontally arranged on the right side sealing head, and the position of the spraying liquid full flow port is lower than the upper end part of the second partition plate and higher than the upper end part of the first partition plate; the spraying liquid outlet is horizontally arranged on the right sealing head and is lower than the outlet end of the light tar inlet pipe.
And the lower end part notch of the second partition plate is lower than the upper end part notch of the first partition plate, and the upper end part notch of the second partition plate is higher than the upper end part notch of the first partition plate.
Compared with the prior art, the beneficial effects of the utility model are that:
1) through static separation, impurities can be removed, and water is separated;
2) the effect of uniformly mixing the spraying liquid is achieved by supplementing the stirring of the light tar inlet pipe without additional stirring equipment;
3) the device of the utility model is a closed system, does not produce waste gas and waste water, and is environment-friendly;
4) the use effect can be achieved only by changing the internal structure of the existing equipment, the structure is perfect and reasonable, the cost is reduced, the investment is less, and the energy consumption is low.
Drawings
Fig. 1 is a schematic view of the structure principle of the present invention;
FIG. 2 is a schematic cross-sectional view taken along line A-A of FIG. 1;
fig. 3 is a schematic diagram of a cross-sectional structure along the direction B-B in fig. 1.
In the figure: 1-cylinder 2-end enclosure 3-partition plate one 4-partition plate two 5-condensate inlet pipe 6-water outlet 7-naphthalene-containing condensate outlet 8-spraying liquid outlet 9-spraying liquid full flow port 10-light tar inlet pipe
Detailed Description
The following description of the embodiments of the present invention will be made with reference to the accompanying drawings:
as shown in fig. 1-3, the condensate tank capable of removing impurities and separating out water according to the present invention comprises a cylinder 1, two end sockets 2, a first partition plate 3, a second partition plate 4, a condensate inlet pipe 5, a water outlet 6, a naphthalene-containing condensate outlet 7, a spray outlet 8, a spray overflow port 9 and a light tar inlet pipe 10, wherein the two end sockets 2 are respectively and fixedly connected with two ends of the cylinder 1 to form the condensate tank; the first partition plate 3 is arranged in the left position of the center in the cylinder body 1, the other three end parts except the upper end part are fixedly connected with the cylinder body 1, and the upper end part is provided with a gap (a gap is reserved between the first partition plate 3 and the inner wall of the upper part of the cylinder body 1) to divide the cylinder body 3 into a left part and a right part; the second partition plate 4 is arranged on the left side of the first partition plate 3 in the barrel 1, the other two end parts except the upper end part and the lower end part are fixedly connected with the barrel 1, and gaps are formed in the upper end part and the lower end part (gaps are reserved between the second partition plate 4 and the inner walls of the upper part and the lower part of the barrel 1); the condensate inlet pipe 5 is arranged on the left side of the partition plate II 4 and extends into the lower part of the condensate tank from the upper part of the cylinder 1, the outlet end of the condensate inlet pipe is L-shaped and horizontal, and the outlet of the condensate inlet pipe is arranged leftwards; the light tar inlet pipe 10 is arranged on the right side of the first partition plate 3 and extends into the lower part of the condensate tank from the upper part of the barrel 1; the naphthalene-containing condensate outlet 7 is horizontally arranged on the left end socket 2 (horizontal discharging), and is lower than the outlet end of the condensate inlet pipe 5; the water outlet 6 is horizontally arranged on the left end enclosure 2, and is lower than the upper end part of the second partition plate 4 and higher than the upper end part of the first partition plate 3; the spraying liquid overflow port 9 is horizontally arranged on the right end enclosure 2, and is lower than the upper end part of the second partition plate 4 and higher than the upper end part of the first partition plate 3; the spraying liquid outlet 8 is horizontally arranged on the right end socket 2 and is lower than the outlet end of the light tar inlet pipe 10.
The lower end part gap of the second partition plate 4 is lower than the upper end part gap of the first partition plate 3, and the upper end part gap of the second partition plate 4 is higher than the upper end part gap of the first partition plate 3.
When in work:
firstly, introducing light tar into the right side of a condensate tank from a light tar inlet pipe 10, pumping the light tar to a lower section circulating spray pipe at the upper part of a primary cooler heat exchange pipe from a spray liquid outlet 8, washing impurities such as tar, naphthalene and the like condensed in coal gas outside the primary cooler heat exchange pipe, and enabling formed condensate to flow into the lower part of the primary cooler;
1) condensate from the lower part of the primary cooler enters from a condensate inlet pipe 5 and enters the left space of a partition plate II 4 in the condensate tank through a horizontal outlet, the liquid level gradually increases along with the increase of the amount of the condensate, and finally the liquid level reaches the gap at the upper end part of the partition plate I3 and flows to the right side of the condensate tank; because the lower end part gap of the second partition plate 4 is lower than the upper end part gap of the first partition plate 3, the left side of the second partition plate 4 has a certain liquid level height; after static separation, impurities containing naphthalene and the like are separated and then sink to the bottom of the condensate tank under the action of gravity, water with light density floats on the upper portion, namely the upper portion of the liquid level on the left side of the partition plate II 4 is water, and the water is discharged from the left side of the partition plate II 4 through a water outlet 6 and enters a tar-ammonia water separation tank;
2) the condensate which is separated to remove impurities and water enters the right side of the first partition plate 3 in a full flow mode through the first partition plate 3, is stirred by light tar supplemented from a light tar inlet pipe 10 to be mixed into uniform spraying liquid, is discharged from a spraying liquid outlet 8, and enters the lower section of the primary cooler to be sprayed circularly to remove naphthalene;
3) the surplus spraying liquid higher than the full flow port is discharged through the spraying liquid full flow port 9 and enters the upper section condensate tank;
4) condensate containing impurities such as naphthalene is discharged from a condensate outlet 7 containing naphthalene.
Claims (2)
1. A condensate tank capable of removing impurities and separating water comprises a cylinder body, two end sockets, a first partition plate, a second partition plate, a condensate inlet pipe, a water outlet, a naphthalene-containing condensate outlet, a spray liquid full-flow port and a light tar inlet pipe, and is characterized in that the two end sockets are respectively and fixedly connected with the two ends of the cylinder body to form the condensate tank; the first partition plate is arranged at the left position of the center in the cylinder body, and the other three end parts are fixedly connected with the cylinder body except for the upper end part and the inner wall of the cylinder body which are provided with gaps; the second partition plate is arranged on the left side of the first partition plate in the barrel, and the other two end parts are fixedly connected with the barrel except that gaps are reserved between the upper end part and the lower end part of the second partition plate and the inner wall of the barrel; the condensate inlet pipe is arranged on the left side of the partition plate II and extends into the lower part of the condensate tank from the upper part of the cylinder, the outlet end of the condensate inlet pipe is L-shaped and horizontal, and the outlet of the condensate inlet pipe is arranged leftwards; the light tar inlet pipe is arranged on the right side of the first partition plate and extends into the lower part of the condensate tank from the upper part of the cylinder body; the naphthalene-containing condensate outlet is horizontally arranged on the left end socket and is lower than the outlet end of the condensate inlet pipe; the water outlet is horizontally arranged on the left end socket, and the position of the water outlet is lower than the upper end part of the second partition plate and higher than the upper end part of the first partition plate; the spraying liquid full flow port is horizontally arranged on the right side sealing head, and the position of the spraying liquid full flow port is lower than the upper end part of the second partition plate and higher than the upper end part of the first partition plate; the spraying liquid outlet is horizontally arranged on the right sealing head and is lower than the outlet end of the light tar inlet pipe.
2. The condensate tank of claim 1, wherein the lower end notch of the second partition plate is lower than the upper end notch of the first partition plate, and the upper end notch of the second partition plate is higher than the upper end notch of the first partition plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922176360.8U CN211420081U (en) | 2019-12-06 | 2019-12-06 | Condensate tank capable of removing impurities and separating water |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922176360.8U CN211420081U (en) | 2019-12-06 | 2019-12-06 | Condensate tank capable of removing impurities and separating water |
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| Publication Number | Publication Date |
|---|---|
| CN211420081U true CN211420081U (en) | 2020-09-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201922176360.8U Active CN211420081U (en) | 2019-12-06 | 2019-12-06 | Condensate tank capable of removing impurities and separating water |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110846088A (en) * | 2019-12-06 | 2020-02-28 | 中冶焦耐(大连)工程技术有限公司 | Condensate tank capable of removing impurities and separating water |
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- 2019-12-06 CN CN201922176360.8U patent/CN211420081U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110846088A (en) * | 2019-12-06 | 2020-02-28 | 中冶焦耐(大连)工程技术有限公司 | Condensate tank capable of removing impurities and separating water |
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