CN206587760U - A kind of composite fibre preparation system - Google Patents
A kind of composite fibre preparation system Download PDFInfo
- Publication number
- CN206587760U CN206587760U CN201720332436.XU CN201720332436U CN206587760U CN 206587760 U CN206587760 U CN 206587760U CN 201720332436 U CN201720332436 U CN 201720332436U CN 206587760 U CN206587760 U CN 206587760U
- Authority
- CN
- China
- Prior art keywords
- composite fibre
- reaction tank
- valve
- abstraction pool
- drying box
- 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
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 44
- 239000002131 composite material Substances 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 25
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 23
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 230000008676 import Effects 0.000 claims abstract description 12
- 235000011121 sodium hydroxide Nutrition 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 238000000605 extraction Methods 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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- Reinforced Plastic Materials (AREA)
Abstract
The utility model discloses a kind of composite fibre preparation system, including reaction tank, abstraction pool and drying box, multiple NaOH solution tank NaOHs are connected with the top of the reaction tank, the reaction tank side is connected with breather pipe, agitator is provided with the reaction tank, the reaction tank bottom is provided with heater and discharge gate, connected between the abstraction pool and discharge gate by drainage conduit, extract import is provided with the top of the abstraction pool, the abstraction pool bottom is provided with discharge channel and leakage fluid dram, the leakage fluid dram is connected with discharging tube, the drying box is connected with discharge channel by separating pipe, the drying box bottom is provided with zone of heating.The utility model is by the way that a variety of preparing raw materials are fully reacted in reaction tank, again by the high pressure in breather pipe other by reaction tank liquid send into abstraction pool, add and extracted after extract and enter drying box, dry and can obtain composite fibre, composite fibre prepared by which can continuously produce composite fibre, simple to operate.
Description
Technical field
The utility model belongs to technical field of fiber preparation, and in particular to a kind of composite fibre preparation system.
Background technology
At present, there are various ways to prepare and meet fiber, patent CN205313722U discloses a kind of for preparing compound fibre
The device of dimension, including for by the injection device of solution injection moulding fiber, for causing injection molding fiber solidifying coagulate
It is fixedly mounted with and puts, the stretching device stretched for the fiber in coagulation system, and the fiber after stretching can be carried out automatically
Automatically the collection device collected.This prepares the device of composite fibre, and the fiber in coagulation system is drawn by stretching device
Processing is stretched, to lift the mechanical strength of fiber；And the fiber after stretching is collected automatically using collection device, it is multiple to improve
Operating efficiency prepared by condensating fiber.But, in addition to preparing composite fibre using injection system, in addition to other modes are prepared again
Condensating fiber, the mode for for example extracting drying prepares composite fibre.
The content of the invention
The purpose of this utility model is：The problem of composite fibre mode is not unique, the utility model are prepared for above-mentioned
Offer is a kind of to prepare composite fiber systems using extraction drying mode.
The technical solution adopted in the utility model is as follows：
It is connected with the top of a kind of composite fibre preparation system, including reaction tank, abstraction pool and drying box, the reaction tank many
Individual NaOH solution tank NaOH, the reaction tank side, which is connected with breather pipe, the reaction tank, is provided with agitator, and the reaction tank bottom is provided with
Heater and discharge gate, are connected between the abstraction pool and discharge gate by drainage conduit, and extract is provided with the top of the abstraction pool
Import, the abstraction pool bottom is provided with discharge channel and leakage fluid dram, and the leakage fluid dram is connected with discharging tube, the drying box with
Discharge channel is connected by separating pipe, and the drying box bottom is provided with zone of heating.
Further, the discharge gate, discharge channel, be respectively equipped with valve a, valve b and valve c on leakage fluid dram.
It is preferred that, the valve a, valve b and valve c are check valve.
Further, the breather pipe is connected with nitrogen cylinder.
Further, the extract import is connected with extract inlet pipe, and the extract inlet pipe extends to abstraction pool bottom
Portion.
Further, the drying box side is provided with ventilating opening, and the ventilating opening is connected with vacuum draw-off pump.
In summary, by adopting the above-described technical solution, the beneficial effects of the utility model are：
1st, the utility model is by the way that a variety of preparing raw materials are fully reacted in reaction tank, then passes through the high pressure in breather pipe
Liquid in reaction tank is sent into abstraction pool by other, is added and is extracted after extract and enter drying box, and drying can be combined
Fiber, composite fibre prepared by which can continuously produce composite fibre, simple to operate.
2nd, the utility model discharge gate, discharge channel, be respectively equipped with valve a, valve b and valve c on leakage fluid dram, pass through
Open valve and valve is closed, reach and be independent of each other between each composite fibre preparatory phase, and preparation process is not interrupted, and is being entered
Enter after extraction stages, reaction tank can carry out the reaction of next round immediately, in drying stage, abstraction pool can carry out next immediately
The extraction of wheel, improves production efficiency.
3rd, the utility model is connected with extract inlet pipe in extract import, and the extract inlet pipe extends to abstraction pool bottom
Portion, can cause extract fully to be contacted with material to be extracted, the maximized purpose for reaching extraction.
4th, drying box of the present utility model is connected with vacuum draw-off pump, and the composite fibre prepared is dried under vacuum conditions,
Dry speed can be improved, while the influence for preventing temperature too high to composite fibre.
Brief description of the drawings
Fig. 1 is structure chart of the present utility model；
Marked in figure：1- reaction tanks, 2- breather pipes, 3- heaters, 4- agitators, 5- valve a, 6- discharge gate, 7- are dried
Case, 8- discharge channels, 9- zones of heating, 10- ventilating openings, 11- valve b, 12- leakage fluid dram, 13- valve c, 14- abstraction pool, 15-
Extract import, 16- drainage conduits, 17- NaOH solution tank NaOHs.
Embodiment
The present invention is elaborated with reference to Fig. 1.
As shown in figure 1, a kind of composite fibre preparation system, including reaction tank 1, abstraction pool 14 and drying box 7, the reaction
The top of pond 1 is connected with multiple NaOH solution tank NaOHs 17, and the side of reaction tank 1 is connected with breather pipe 2, the reaction tank 1 provided with stirring
Device 4, the bottom of reaction tank 1 is provided with heater 3 and discharge gate 6, and drainage conduit 16 is passed through between the abstraction pool 14 and discharge gate 6
Connection, the top of abstraction pool 14 is provided with extract import 15, and the bottom of abstraction pool 14 is provided with discharge channel 8 and leakage fluid dram
12, the leakage fluid dram 12 is connected with discharging tube, and the drying box 7 is connected with discharge channel 8 by separating pipe, the drying box
7 bottoms are provided with zone of heating 9.
In the present embodiment, before composite fibre is prepared, the oxygen in the discharge whole system of breather pipe 2 is opened, during ventilation
Between in more than 30min, after all oxygen discharge systems, close breather pipe 2, open NaOH solution tank NaOH 17 will need react solution
Reaction tank 1 is imported, agitator 4 is opened and solution is stirred, heater 3 is opened and solution is heated, accelerate the speed of reaction.Treat fully
After reaction, breather pipe 2 is opened, reacted solution is pressed into abstraction pool 14 using air pressure.Import and extract from extract import 15
Liquid, extract is contacted with reacted solution, and the oligomer in solution enters in extract, will be extracted by discharge channel 8
Liquid imports drying box 7, and remaining liquid is discharged by leakage fluid dram 12.After being heated into the heated layer 9 of extract in drying box 7,
Composite fibre is made.
Further, the drainage conduit 16, separating pipe, be respectively equipped with valve a5, valve b11 and valve c13 on discharging tube,
By Open valve and valve is closed, reach and be independent of each other between each composite fibre preparatory phase, and preparation process is not interrupted,
After extraction stages are entered, reaction tank 1 can carry out the reaction of next round immediately, and in drying stage, abstraction pool 14 can be immediately
The extraction of next round is carried out, production efficiency is improved.
It is preferred that, the valve a5, valve b11 and valve c13 are check valve, prevent liquid from flowing backwards, to preparation process
Impact.
Further, the breather pipe 2 is connected with nitrogen cylinder, and by the oxygen in inert gas discharge system, protection is multiple
Condensating fiber is not influenceed by oxygen at high temperature.
Further, the extract import 15 is connected with extract inlet pipe, and the extract inlet pipe extends to abstraction pool
14 bottoms, can be without stirring for just can be so that extract and solution be fully contacted, the maximized purpose for reaching extraction.
The side of drying box 7 is provided with ventilating opening 10, and the ventilating opening 10 is connected with vacuum draw-off pump, under vacuum conditions
The composite fibre prepared is dried, dry speed can be improved, while the influence for preventing temperature too high to composite fibre.
It is embodiment of the present utility model as described above.The utility model is not limited to above-mentioned embodiment, anyone
The structure change made under enlightenment of the present utility model should be learnt, it is every that there is same or like skill with the utility model
Art scheme, each falls within protection domain of the present utility model.
Claims (6)
1. a kind of composite fibre preparation system, it is characterised in that including reaction tank (1), abstraction pool (14) and drying box (7), institute
State and be connected with multiple NaOH solution tank NaOHs (17) at the top of reaction tank (1), reaction tank (1) side is connected with breather pipe (2), the reaction
Agitator (4) is provided with pond (1), reaction tank (1) bottom is provided with heater (3) and discharge gate (6), the abstraction pool (14)
It is connected between discharge gate (6) by drainage conduit (16), extract import (15), the extraction is provided with the top of the abstraction pool (14)
Pond (14) bottom is taken to be provided with discharge channel (8) and leakage fluid dram (12), the leakage fluid dram (12) is connected with discharging tube, the drying
Case (7) is connected with discharge channel (8) by separating pipe, and drying box (7) bottom is provided with zone of heating (9).
2. a kind of composite fibre preparation system according to claim 1, it is characterised in that the drainage conduit (16), separation
Valve a (5), valve b (11) and valve c (13) are respectively equipped with pipe, discharging tube.
3. a kind of composite fibre preparation system according to claim 2, it is characterised in that the valve a (5), valve b
And valve c (13) is check valve (11).
4. a kind of composite fibre preparation system according to claim 1, it is characterised in that the breather pipe (2) is connected with
Nitrogen cylinder.
5. a kind of composite fibre preparation system according to claim 1, it is characterised in that the extract import (15) is even
Extract inlet pipe is connected to, the extract inlet pipe extends to abstraction pool (14) bottom.
6. a kind of composite fibre preparation system according to claim 1, it is characterised in that drying box (7) side is set
There is ventilating opening (10), the ventilating opening (10) is connected with vacuum draw-off pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720332436.XU CN206587760U (en) | 2017-03-31 | 2017-03-31 | A kind of composite fibre preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720332436.XU CN206587760U (en) | 2017-03-31 | 2017-03-31 | A kind of composite fibre preparation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206587760U true CN206587760U (en) | 2017-10-27 |
Family
ID=60122782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720332436.XU Expired - Fee Related CN206587760U (en) | 2017-03-31 | 2017-03-31 | A kind of composite fibre preparation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206587760U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112604317A (en) * | 2020-12-16 | 2021-04-06 | 鼎泰（湖北）生化科技设备制造有限公司 | Efficient multichannel extraction device |
-
2017
- 2017-03-31 CN CN201720332436.XU patent/CN206587760U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112604317A (en) * | 2020-12-16 | 2021-04-06 | 鼎泰（湖北）生化科技设备制造有限公司 | Efficient multichannel extraction device |
| CN112604317B (en) * | 2020-12-16 | 2022-06-10 | 鼎泰（湖北）生化科技设备制造有限公司 | Efficient multichannel extraction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 645350 Yibin City Pingshan County of Sichuan province stone plate Industrial Park Patentee after: Yibin Pingshan Pfizer Technology Co.,Ltd. Address before: 645350 Yibin City Pingshan County of Sichuan province stone plate Industrial Park Patentee before: YIBIN PINGSHAN HUIRUI GREASE Co.,Ltd. |
|
| 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: 20171027 |