CN207680527U - A kind of preparation facilities of spinning oil - Google Patents
A kind of preparation facilities of spinning oil Download PDFInfo
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- CN207680527U CN207680527U CN201721441195.9U CN201721441195U CN207680527U CN 207680527 U CN207680527 U CN 207680527U CN 201721441195 U CN201721441195 U CN 201721441195U CN 207680527 U CN207680527 U CN 207680527U
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Abstract
The utility model discloses a kind of preparation facilities of spinning oil, including heating crude oil deployment device and finish emulsion conveying and storing apparatus, the heating crude oil deployment device includes crude oil bucket, thermocirculator, measuring tank and surge-tank successively；Coil pipe is provided in the surge-tank, the measuring tank outlet is connect with surge-tank inner coil pipe；The finish emulsion conveying and storing apparatus includes head tank, oil storage tank, exhaust pipe and finish circulating pump, the head tank is connect by pipeline with surge-tank oil outlet, head tank outlet is equipped with basket filter, the oil storage tank outlet is equipped with Y-filter, filter is connect with upper oil pipeline, upper hydraulic fluid port is provided on the upper oil pipeline, upper oil pipeline is connect with finish pump inlet, and the upper oil pipeline tail portion is equipped with exhaust pipe.The utility model solves the problems, such as that finish allotment is uneven, and ensure that emulsion intercalation method and product quality.
Description
Technical field
The utility model is related to long filament production equipments, and in particular to a kind of finish preparation facilities for long filament production belongs to
In field of textiles.
Background technology
In the spinning process of polyester filament and during post-processing, require that fiber has certain surface characteristic, such as
Antistatic property, flatness and coherent etc..The purpose to oil is that the surface characteristic for improving fiber, can be with after oiling
The cohesive force between tow is set to increase, to improve winding, unwinding and the other processing performances of fiber；Due to special in finish
Ingredient changes the property of fiber surface, and the flatness of fiber can be made to be improved；After oiling to tow, finish and moisture meeting one
The surface for being evenly dispersed in monofilament is acted, the antistatic property accumulated on tow is made to be improved.The terylene of conventional variety is to oil
The formulation requirements of agent are relatively low, as long as by crude blends at lotion, and most of PET production producers are all developing at present
The high-end products such as super fine denier, shaped filaments or functional fiber, large specific surface area or total fiber number are less than normal, are not easy the unevenness that oils or oil
Deng, the saturability of tow is poor, in production process be easy broken end, appearance lousiness is more, intensity, elongation and strip dry CV value it is bigger than normal and dyeing
It is unequal, seriously affect the quality of product.
Utility model content
In order to overcome the shortage of prior art, the technical problems to be solved in the utility model provides a kind of spinning oil preparation dress
It sets, raising oils effect, ensures that lotion uniformity is good, and good emulsion stability, not stratified.
To achieve the above object, the utility model adopts the following technical solution：
A kind of preparation facilities of spinning oil includes mainly heating crude oil deployment device and finish emulsion conveying storage dress
It sets, the heating crude oil deployment device includes crude oil bucket, thermocirculator, measuring tank and surge-tank successively, is led between each equipment
Piping connects；It is provided with coil pipe in the surge-tank, several apertures, the measuring tank outlet and surge-tank are provided on coil pipe
Inner coil pipe connects；The finish emulsion conveying and storing apparatus includes head tank, oil storage tank, exhaust pipe and finish circulating pump, described
Head tank is connect by pipeline with surge-tank oil outlet, and head tank outlet is equipped with basket filter, is connected by pipeline and oil storage tank
It connects, the oil storage tank outlet is equipped with Y-filter, and filter connect with upper oil pipeline, is provided with and oils on the upper oil pipeline
Mouthful, upper oil pipeline is connect with finish pump inlet, and finish circulating-pump outlet is connected by pipeline with oil storage tank, the upper oil pipe
Line tail portion is equipped with exhaust pipe.
Further, the thermocirculator includes shell and inside tank, and it is empty that a closing is formed between shell and oil groove
Between, it is internally provided with liquid, is heated by heating source.
Further, the liquid is water, is heated by steam.
Further, the coil pipe is Stainless Steel Coil.
Further, small hole number is 10-20 on the coil pipe.
Further, orifice size is 4mm on the coil pipe.
Further, it is equipped with blender in the surge-tank and head tank.
Further, the oil storage trench bottom is equipped with telescoping shoring column.
Further, blender is equipped in the oil storage tank, mixing speed is 5-8 revs/min, and inside is additionally provided with anti-splashing
Ball-cock assembly is adjusted in liquid level.
Further, the upper oil pipeline tail portion is equipped with the exhaust pipe that transparent liquid level is shown.
The beneficial effects of the utility model：
The utility model finish preparation facilities solves the problems, such as that finish allotment is uneven, and ensure that emulsion intercalation method,
The effect that oils of superfine denier fiber, shaped filaments or functional fibre is improved, broken end is reduced in process of production, and lousiness is few, and intensity is stretched
Long and Unevenness CV % values are small, ensure that product quality.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model.
Fig. 2 is the utility model coil arrangement schematic diagram.
Figure label：1, crude oil bucket, 2, thermocirculator, 3, measuring tank, 4, surge-tank, 5, coil pipe, 6, head tank, 7, storage
Oil groove, 8, holder, 9, filter, 10, upper hydraulic fluid port, 11, drain tap, 12, exhaust pipe, 13, finish circulating pump, 14, oil outlet.
Specific implementation mode
The utility model is described further with reference to process route and embodiment.
As shown in Figure 1, a kind of preparation facilities of spinning oil of the utility model, includes mainly heating crude oil deployment device
With finish emulsion conveying and storing apparatus, the heating crude oil deployment device includes thermocirculator 2, circulating pump, measuring tank 3 and adjusts
Slot allocation 4, the finish emulsion conveying and storing apparatus include head tank 6, delivery pump, oil storage tank, exhaust pipe 12, finish circulating pump
13。
2 import of thermocirculator is connected by pipeline and crude oil bucket 1, and oil outlet is connected by pipeline with 3 import of measuring tank,
3 oil outlet of measuring tank is connected by pipeline and 4 inner coil pipe 5 of surge-tank, and 4 oil outlet of surge-tank is by pipeline, delivery pump with high-order
Slot 6 connects, and the outlet of head tank 6 is equipped with basket filter, is connected with oil storage tank between spinning 7 by pipeline, delivery pump, oil storage tank 7
Outlet is equipped with Y-filter 9, and filter 9 is same as above oil pipeline connection, and upper oil pipeline tail portion is equipped with exhaust pipe 12, upper hydraulic fluid port pipeline
It is connected with 13 import of finish circulating pump, the outlet of finish circulating pump 13 is connected by pipeline and oil storage tank 7.
As shown in Fig. 2, being equipped with coil pipe in surge-tank 4, coil pipe oil inlet passes through pipeline and valve with 3 bottom oil outlet of measuring tank
Door is connected, and 18 oil outlets, bore dia 4mm are uniformly distributed on coil pipe.
Specific work process：
（1）Crude oil prepares：Before the barreled finish being placed in 40 DEG C or so greenhouses is transported to crude oil circulating pump, pass through pipe
Road is connected with crude oil circulating pump, and interior cycle is beaten in crude oil bucket 1, tentatively that churning up the raw oil is uniform, prevents crude oil some components point
Layer is attached to a barrel bottom, and the time is 10 minutes or so.
（2）Crude oil thermal cycle：After crude oil cycle is accomplished fluently in crude oil bucket 1, it is pumped in thermocirculator 2 by cycle,
By pipeline thermal cycle 30 minutes in thermocirculator 2, an enclosure space is formed between thermocirculator shell and oil groove, it is internal
It equipped with water, can be heated by steam, ensure that crude oil temperature control is additionally provided with interior wall bracket between 35-38 DEG C, inside slot.It is former
Oil is futher stirred uniformly by thermal cycle, and effective solution causes tow to be not easy because of inhomogeneities when finish is allocated
Oil and oil uneven difficult point.
（3）Lotion is allocated：Crude oil after being recycled in thermocirculator 2 is pumped to by crude oil cycle in measuring tank 3, is passed through
3 outlet at bottom of measuring tank is sent by pipeline into surge-tank 4 in coil pipe 5, and 18 holes are uniformly distributed on coil pipe, and bore dia 4mm is former
Oil in hole on coil pipe 5 in a manner of thread from being injected in the fast pure water of mixing speed, because the oil water contact time is shorter, formation is coagulated
Poly- complex compound particle is smaller, and the finish allotment uniformity is more preferable, after crude oil note has closed, after continuing stirring 30 minutes or so, through conveying
Pump is delivered in head tank 6.
（4）Finish emulsion conveys：Finish from 6 outlet at bottom of head tank after basket filter filters, by finish delivery pump
It is delivered between spinning in finish oil storage tank 7 through conveyance conduit, each storage tank can adjust total conveyance conduit to storing up according to finish consumption
The valve opening of slot, extra finish flow back into head tank 6, continue cycling through use.
（5）Finish emulsion storage and use between spinning：Finish in finish oil storage tank 7 is from trench bottom exit through Y shape mistake
After filter 9 filters, after pipeline to spinning threadling, then it is connected on finishing oil pump through upper hydraulic fluid port 10 and hose and oils for silk thread.
Finish is recycled by finish circulating pump 13 in finish and oil storage tank 7 in pipeline, while blender is equipped in finish oil storage tank 7, is stirred
It is 5-8 revs/min to mix speed, so that lotion is constantly in dynamic, it is ensured that emulsion intercalation method prevents from being layered.Inside is also
Ball-cock assembly is adjusted equipped with anti-splashing liquid level, controls liquid level in finish oil storage tank.Upper oil pipeline tail portion is equipped with a transparent liquid
Position shows that exhaust pipe 12, upper opening, bottom are equipped with valve 11, and valve 11 remains opening state, pipeline during normal production
Interior bubble can smoothly be discharged.Finish oil storage tank bottom bracket 8 uses telescoping shoring column, in spinning superfine denier, shaped filaments or functionality
When fiber, because silk thread boundling point position is higher, when finish liquid level needs to improve in storage tank, in the case where not increasing finish amount,
By adjusting holder, you can finish oil storage tank liquid level is made to meet technological requirement.
Claims (10)
1. a kind of preparation facilities of spinning oil, it is characterised in that：Include mainly that heating crude oil deployment device and finish emulsion are defeated
It includes successively crude oil bucket, thermocirculator, measuring tank and surge-tank to send storage device, the heating crude oil deployment device, is respectively set
It is connected by pipeline between standby；It is provided with coil pipe in the surge-tank, several apertures, the measuring tank outlet are provided on coil pipe
It is connect with surge-tank inner coil pipe；The finish emulsion conveying and storing apparatus includes head tank, oil storage tank, exhaust pipe and finish cycle
Pump, the head tank are connect by pipeline with surge-tank oil outlet, and head tank outlet is equipped with basket filter, passes through pipeline and storage
Oil groove connects, and the oil storage tank outlet is equipped with Y-filter, and filter connect with upper oil pipeline, is arranged on the upper oil pipeline
There are upper hydraulic fluid port, upper oil pipeline to be connect with finish pump inlet, finish circulating-pump outlet is connected by pipeline with oil storage tank, described
Upper oil pipeline tail portion is equipped with exhaust pipe.
2. device as described in claim 1, it is characterised in that：The thermocirculator includes shell and inside tank, shell
An enclosure space is formed between oil groove, is internally provided with liquid, is heated by heating source.
3. device as claimed in claim 2, it is characterised in that：The liquid is water, is heated by steam.
4. device as described in claim 1, it is characterised in that：The coil pipe is Stainless Steel Coil.
5. device as described in claim 1 or 4, it is characterised in that：Small hole number is 10-20 on the coil pipe.
6. device as claimed in claim 5, it is characterised in that：Orifice size is 4mm on the coil pipe.
7. device as described in claim 1, it is characterised in that：It is equipped with blender in the surge-tank and head tank.
8. device as described in claim 1, it is characterised in that：The oil storage trench bottom is equipped with telescoping shoring column.
9. device as described in claim 1, it is characterised in that：Blender, mixing speed 5-8 are equipped in the oil storage tank
Rev/min, inside is additionally provided with anti-splashing liquid level and ball-cock assembly is adjusted.
10. device as described in claim 1, it is characterised in that：The upper oil pipeline tail portion is equipped with the row that transparent liquid level is shown
Tracheae.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721441195.9U CN207680527U (en) | 2017-11-02 | 2017-11-02 | A kind of preparation facilities of spinning oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721441195.9U CN207680527U (en) | 2017-11-02 | 2017-11-02 | A kind of preparation facilities of spinning oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207680527U true CN207680527U (en) | 2018-08-03 |
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ID=62988567
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721441195.9U Active CN207680527U (en) | 2017-11-02 | 2017-11-02 | A kind of preparation facilities of spinning oil |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110373732A (en) * | 2019-07-09 | 2019-10-25 | 长乐佳纶纺织实业有限公司 | A kind of production technology of coloured flame-retardant dacron thread |
| CN110961017A (en) * | 2019-11-26 | 2020-04-07 | 浙江嘉华特种尼龙有限公司 | Full-automatic spinning emulsified oil supply system |
-
2017
- 2017-11-02 CN CN201721441195.9U patent/CN207680527U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110373732A (en) * | 2019-07-09 | 2019-10-25 | 长乐佳纶纺织实业有限公司 | A kind of production technology of coloured flame-retardant dacron thread |
| CN110961017A (en) * | 2019-11-26 | 2020-04-07 | 浙江嘉华特种尼龙有限公司 | Full-automatic spinning emulsified oil supply system |
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