CN201322554Y - Triglycol glycol emptying pipe - Google Patents
Triglycol glycol emptying pipe Download PDFInfo
- Publication number
- CN201322554Y CN201322554Y CNU2008201702567U CN200820170256U CN201322554Y CN 201322554 Y CN201322554 Y CN 201322554Y CN U2008201702567 U CNU2008201702567 U CN U2008201702567U CN 200820170256 U CN200820170256 U CN 200820170256U CN 201322554 Y CN201322554 Y CN 201322554Y
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- CN
- China
- Prior art keywords
- pipe
- triethylene glycol
- triglycol
- cooling press
- glycol
- 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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a triglycol glycol emptying pipe, in particular to a triglycol glycol emptying pipe on a triglycol glycol furnace for melting polymers on a spinneret plate. The triglycol glycol furnace is communicated with condensation tanks which have three, the condensation tanks are communicated with each other and are in step type distribution, wherein top ends of two condensation tanks are equipped with emptying pipes, pipelines of the lower portions of the condensation tanks are all equipped with valves, bottoms of the pipelines of the condensation tanks are equipped with recovery pipes, the triglycol glycol furnace is further communicated and equipped with a cooling pressing pipe, wherein the emptying pipes at the top ends of the two condensation tanks are elongated and communicated to the recovery pipe, the other end of the recovery pipe is equipped with a sewage draining pipe, and the bottom end of the sewage draining pipe is equipped with a sewage draining opening. The utility model elongates the emptying pipes and additionally cools air containing water vapor inside the emptying pipes, wherein cooled liquid is discharged from the sewage draining opening. Further, the utility model elongates the cooling pressing pipe and additionally arranges a muffler on the same. Besides, a cooling pressing draining opening is in tower shape and is frequently expanded outwardly.
Description
Technical field
The utility model is a kind of triethylene glycol evacuated tube, and is particularly a kind of to the triethylene glycol evacuated tube on the triethylene glycol stove of the fusion of the polymers on the spinneret.
Background technology
In the prior art, the evacuated tube that is connected with drainer, be arranged on the upper end of drainer, pipeline is very short, the also not cooling fully of gas that so just causes the evacuated tube outlet to be discharged, the gas that causes discharging contains the triethylene glycol of trace and the polymer that burnt, smell pungent around the evacuated tube is very heavy, influence the pollution of environment, the cooling press blank pipe is because the empty floss hole pipe of compressed-air actuated pressure and cooling press is short, the empty manufacturing of cooling press noise is too big when causing cooling off the triethylene glycol stove at every turn, near the normal rest of the residential block that has a strong impact on.
Summary of the invention
The utility model mainly is to solve the deficiencies in the prior art, providing a kind of prolongs evacuated tube, increase the cooling of the gas that contains steam in the evacuated tube, cooled liquid is discharged by sewage draining exit, prolong the cooling press blank pipe, increase muffler on the cooling press blank pipe, the empty floss hole of cooling press is the tower shape, the outside flaring of floss hole.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals:
A kind of triethylene glycol evacuated tube, comprise the triethylene glycol stove, what be connected with the triethylene glycol stove is drainer, drainer is provided with three altogether, drainer is connected with each other logical, drainer is staged and distributes, wherein the top of two drainers is provided with evacuated tube, all is provided with valve on the pipeline of drainer bottom, and drainer pipeline bottom also is provided with recovery tube, also be communicated with on the triethylene glycol stove and be provided with the cooling press blank pipe, the not end of cooling press blank pipe is provided with the empty floss hole of cooling press, is communicated with the empty import of cooling press on the triethylene glycol stove, and the evacuated tube prolongation on described wherein two drainer tops is communicated in the recovery tube, the other end at recovery tube is provided with blow-off pipe, is provided with sewage draining exit in the bottom of blow-off pipe.Prolonging evacuated tube is to contain steam gas flow distance in order to increase, and increases the time of cooling, makes to contain steam gas and become liquid, is back in the recovery tube, is discharged by sewage draining exit.
As preferably, described evacuated tube upwards is provided with one 90 ° knuckle.
As preferably, described cooling press blank pipe pipeline prolongs, and is provided with muffler on pipeline prolongs, and the empty floss hole of described cooling press is the tower shape, the outside flaring of floss hole.Prolong the cooling press blank pipe, in cooling press blank pipe line, increase muffler, the noise of making when reducing the cooling press sky, the empty floss hole of cooling press is provided with the tower shape, and the outside flaring of floss hole can be reduced to noise minimum noise with wider diffusion.
Therefore, triethylene glycol evacuated tube of the present utility model, providing a kind of prolongs evacuated tube, increase the cooling of the gas that contains steam in the evacuated tube, cooled liquid is discharged by sewage draining exit, prolongs the cooling press blank pipe, increases muffler on the cooling press blank pipe, the empty floss hole of cooling press is the tower shape, the outside flaring of floss hole.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: as shown in Figure 1, a kind of triethylene glycol evacuated tube, comprise triethylene glycol stove 4, what be connected with triethylene glycol stove 4 is drainer 3, drainer 3 is provided with three altogether, drainer 3 is connected with each other logical, drainer 3 is staged and distributes, wherein the top of two drainers 3 is provided with evacuated tube 1, and wherein evacuated tube 1 prolongation on two drainer 3 tops is communicated in the recovery tube 9, and evacuated tube 1 upwards is provided with one 90 ° knuckle, the other end at recovery tube 9 is provided with blow-off pipe, be provided with sewage draining exit 10 in the bottom of blow-off pipe, all be provided with valve 2 on the pipeline of drainer 3 bottoms, drainer 3 pipelines bottom also is provided with recovery tube 9, also be communicated with on the triethylene glycol stove 4 and be provided with cooling press blank pipe 5, the not end of cooling press blank pipe 5 is provided with the empty floss hole 7 of cooling press, and cooling press blank pipe 5 pipelines prolong, and is provided with muffler 6 on pipeline prolongs, the empty floss hole 7 of described cooling press is the tower shape, the outside flaring of floss hole is communicated with the empty import 8 of cooling press on the triethylene glycol stove 4
Operation principle: triethylene glycol is joined in the triethylene glycol stove, when electric heater is heated to 275 ℃ to triethylene glycol, alcoholysis and dissolution can be arranged to the high polymer molten on the spinneret.The triethylene glycol that seethes with excitement during heating, high polymer molten analyte along with heat in the triethylene glycol evacuated tube is discharged stove.After cleaning process finishes, input cooling press sky cools off, the prolongation of evacuated tube winding displacement has increased the time of emptying greatly, make and contain steam gas and obtain cooling, cooled liquid discharges through floss hole, presses the noise that produces in the null process in order to reduce, on the cooling press blank pipe, be provided with muffler, again the empty floss hole of cooling press is designed to the tower shape, the outside flaring of floss hole makes noise reach lower.
Claims (3)
1, a kind of triethylene glycol evacuated tube, comprise triethylene glycol stove (4), what be connected with triethylene glycol stove (4) is drainer (3), drainer (3) is provided with three altogether, drainer (3) is connected with each other logical, drainer (3) is staged and distributes, wherein the top of two drainers (3) is provided with evacuated tube (1), all be provided with valve (2) on the pipeline of drainer (3) bottom, drainer (3) pipeline bottom also is provided with recovery tube (9), also be communicated with on the triethylene glycol stove (4) and be provided with cooling press blank pipe (5), the not end of cooling press blank pipe (5) is provided with the empty floss hole (7) of cooling press, be communicated with the empty import (8) of cooling press on the triethylene glycol stove (4), it is characterized in that: evacuated tube (1) prolongation on described wherein two drainers (3) top is communicated in the recovery tube (9), the other end at recovery tube (9) is provided with blow-off pipe, is provided with sewage draining exit (10) in the bottom of blow-off pipe.
2, triethylene glycol evacuated tube according to claim 1 is characterized in that: described evacuated tube (1) upwards is provided with one 90 ° knuckle.
3, triethylene glycol evacuated tube according to claim 1 and 2, it is characterized in that: described cooling press blank pipe (5) pipeline prolongs, be provided with muffler (6) on pipeline prolongs, the empty floss hole of described cooling press (7) is the tower shape, and the empty floss hole of cooling press (7) is flaring outwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201702567U CN201322554Y (en) | 2008-12-17 | 2008-12-17 | Triglycol glycol emptying pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201702567U CN201322554Y (en) | 2008-12-17 | 2008-12-17 | Triglycol glycol emptying pipe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201322554Y true CN201322554Y (en) | 2009-10-07 |
Family
ID=41159934
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201702567U Expired - Fee Related CN201322554Y (en) | 2008-12-17 | 2008-12-17 | Triglycol glycol emptying pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201322554Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102389885A (en) * | 2011-09-27 | 2012-03-28 | 新疆蓝山屯河聚酯有限公司 | Cleaning technology for spare flux pipeline in polyester production device |
-
2008
- 2008-12-17 CN CNU2008201702567U patent/CN201322554Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102389885A (en) * | 2011-09-27 | 2012-03-28 | 新疆蓝山屯河聚酯有限公司 | Cleaning technology for spare flux pipeline in polyester production device |
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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: 20091007 Termination date: 20161217 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |