CN206538509U - A kind of polymer raw hybrid system of novel nylon 6 - Google Patents
A kind of polymer raw hybrid system of novel nylon 6 Download PDFInfo
- Publication number
- CN206538509U CN206538509U CN201720123229.3U CN201720123229U CN206538509U CN 206538509 U CN206538509 U CN 206538509U CN 201720123229 U CN201720123229 U CN 201720123229U CN 206538509 U CN206538509 U CN 206538509U
- Authority
- CN
- China
- Prior art keywords
- valve
- auxiliary material
- pipe
- way diverter
- discharge nozzle
- 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
Abstract
The utility model provides a kind of polymer raw hybrid system of novel nylon 6, including a motor, one dynamic mixer, one polymerization tower, one major ingredient adds pipe, one first auxiliary material adds pipe, one second auxiliary material adds pipe, one feeding pipe and one first discharge nozzle, also include a front end static mixer, one first auxiliary material static mixer, one second auxiliary material static mixer, one end Integrated Static blender, one first three-way diverter valve, one second three-way diverter valve, one the 3rd three-way diverter valve, one second discharge nozzle, one the 3rd discharge nozzle, one the 4th discharge nozzle, one the 5th discharge nozzle, one first connecting tube, one second connecting tube, one the 3rd connecting tube, one first valve, one first check-valve, one second valve, one second check-valve and one the 3rd valve.The utility model reduces energy consumption, efficiently ensure that the quality of polymerization product (slices of caprone).
Description
Technical field
The utility model is related to spining technology field, more particularly to a kind of polymer raw hybrid system of novel nylon 6.
Background technology
In spining technology field, the various raw materials for production of Pa-6 Polymerization factory need to be mixed, and are re-fed into polymerization tower
In.Added as shown in figure 1, traditional raw material mixing system includes a motor 1, a dynamic mixer 2, a polymerization tower 3, a major ingredient
Pipe 4 (caprolactam adds pipe), one first auxiliary material add pipe 5 (acid additives add pipe), one second auxiliary material and add pipe 6 (two
Titanium oxide adds pipe), a feeding pipe 7 and one first discharge nozzle 8, the dynamic mixer 2 respectively with the motor 1, described
One discharge nozzle 8 and the feeding pipe 7 are connected, and the feeding pipe 7 adds pipe 4, first auxiliary material with the major ingredient and added respectively
Pipe 5 and second auxiliary material add pipe 6 and connected, and first discharge nozzle 8 is connected with the polymerization tower 3.
Traditional raw material mixing system be usually by main material (caprolactam) and various auxiliary materials (acid additives and
Titanium dioxide) add that pipe 4, first auxiliary material add pipe 5 and second auxiliary material adds pipe 6 and entered by the major ingredient respectively
The feeding pipe 7, then enter the dynamic mixer 2 via the feeding pipe 7, it is then directly mixed with motor 1 with one
After clutch (dynamic mixer 2) is stirred, then sent into the polymerization tower 3 by first discharge nozzle 8.It has the disadvantage：
1. there was only mixed once, have and mix uneven or not thorough problem generation；2. delustering agent (titanium dioxide) prematurely adds with acidity
Plus agent mixing, it may occur that particle agglomeration phenomena, this has had a strong impact on the quality of product (slices of caprone)；3. when dynamic mixer stops
Only run or hinder parking maintenance for some reason, just can not carry out material again is mixed with, and production line must stop production, and so not only influence
The continuity of production, also seriously reduces the quality of product (slices of caprone).
The content of the invention
The technical problems to be solved in the utility model, is to provide a kind of polymer raw hybrid system of novel nylon 6, reduction
Energy consumption, efficiently ensure that the quality of polymerization product (slices of caprone).
What the utility model was realized in：
A kind of polymer raw hybrid system of novel nylon 6, including a motor, a dynamic mixer, a polymerization tower, a major ingredient
Add pipe, one first auxiliary material and add pipe, one second auxiliary material and add pipe, a feeding pipe and one first discharge nozzle, in addition to a front end
Static mixer, one first auxiliary material static mixer, one second auxiliary material static mixer, an end Integrated Static blender, one
First three-way diverter valve, one second three-way diverter valve, one the 3rd three-way diverter valve, one second discharge nozzle, one the 3rd discharge nozzle, one
4th discharge nozzle, one the 5th discharge nozzle, one first connecting tube, one second connecting tube, one the 3rd connecting tube, one first valve, one
First check-valve, one second valve, a second check-valve and one the 3rd valve；
The motor, the dynamic mixer, first discharge nozzle, the front end static mixer, described second go out
Expects pipe, the first auxiliary material static mixer, the 3rd discharge nozzle, the second auxiliary material static mixer, the described 4th go out
Expects pipe, the end Integrated Static blender, the 5th discharge nozzle and the polymerization tower are sequentially connected；The dynamic mixer
Also add that pipe, first auxiliary material add pipe and second auxiliary material adds Guan Lian with the major ingredient respectively by the feeding pipe
It is logical；
The B chambers of the A chambers of first three-way diverter valve and first three-way diverter valve are placed in first auxiliary material and thrown
Plus on pipe, the C chambers of first three-way diverter valve are connected by first connecting tube with the first auxiliary material static mixer；
The B chambers of the A chambers of second three-way diverter valve and second three-way diverter valve are placed in second auxiliary material and added on pipe, institute
The C chambers for stating the second three-way diverter valve are connected by second connecting tube with the second auxiliary material static mixer；Described 3rd
The B chambers of the A chambers of three-way diverter valve and the 3rd three-way diverter valve are placed on the feeding pipe, the 3rd three-way diverter valve
C chambers connected by the 3rd connecting tube with the front end static mixer；
First valve and the first check-valve are all positioned in first connecting tube, second valve and institute
State second check-valve to be all positioned in second connecting tube, the 3rd valve is placed on first discharge nozzle.
Further, first valve is disposed adjacent with the first check-valve, and the first check-valve is located at institute
State between the first three-way diverter valve and first valve；Second valve is disposed adjacent with the second check-valve, and institute
Second check-valve is stated to be located between second three-way diverter valve and second valve.
The utility model has the advantage of：
1st, in process of production, with without motor-driven static mixer motor-driven dynamic can have been replaced to mix
Device, can also make two kinds of blenders while using by operating three-way diverter valve；
2nd, raw materials for production can be subjected to substep mixing, finally comprehensive mixing, can avoid that only mixed once brings is mixed
Close uneven phenomenon；And the time that titanium dioxide is contacted with acid additives is greatly reduce both, it effectively prevent two
Titan oxide particles occur coalescence and influence product quality；
3rd, static mixer drives without motor, can save electric energy, reduce energy consumption；
4th, flexible and convenient operation, can change hybrid mode at any time, and selectivity is strong, and when dynamic mixer parking maintenance,
Raw material, which can proceed with, is mixed and fed into polymerization tower, does not influence production line normally to produce, and production line is without stopping, so efficiently
It ensure that the quality of polymerization product (slices of caprone).
Brief description of the drawings
The utility model is further described in conjunction with the embodiments with reference to the accompanying drawings.
Fig. 1 is the structural representation of traditional raw material mixing system.
Fig. 2 is a kind of structural representation of the polymer raw hybrid system of novel nylon 6 of the utility model.
Label declaration in figure：
1- motors, 2- dynamic mixers, 3- polymerization towers, 4- major ingredients add pipe, the auxiliary materials of 5- first and add pipe, the auxiliary materials of 6- second
Add pipe, 7- feeding pipes, the discharge nozzles of 8- first, 9- front ends static mixer, the first auxiliary materials of 10- static mixer, 11- second auxiliary
Expect static mixer, 12- ends Integrated Static blender, the three-way diverter valves of 13- first, the three-way diverter valves of 14- second, 15- the
Three three-way diverter valves, the discharge nozzles of 16- second, the discharge nozzles of 17- the 3rd, the discharge nozzles of 18- the 4th, the discharge nozzles of 19- the 5th, 20- first
Connecting tube, the connecting tubes of 21- second, the connecting tubes of 22- the 3rd, the valves of 23- first, 24- first check-valves, the valves of 25- second, 26-
Second check-valve, the valves of 27- the 3rd.
Embodiment
The utility model is made with reference to specific embodiment and further being described in detail, but structure of the present utility model
It is not limited in following examples.
One preferred embodiment is：
Refer to shown in Fig. 2, a kind of polymer raw hybrid system of novel nylon 6 of the present utility model, including a motor 1,
One dynamic mixer 2, a polymerization tower 3, a major ingredient, which add pipe 4, one first auxiliary material and add pipe 5, one second auxiliary material, adds pipe 6, one
Feeding pipe 7, one first discharge nozzle 8, a front end static mixer 9, one first auxiliary material static mixer 10, one second auxiliary material are static
Blender 11, an end Integrated Static blender 12, one first three-way diverter valve 13, one second three-way diverter valve 14, one the 3rd
Three-way diverter valve 15, the discharge nozzle 19,1 of the 4th discharge nozzle 18,1 of the 3rd discharge nozzle 17,1 of one second discharge nozzle 16,1 the 5th
One connecting tube 20, one second connecting tube 21, one the 3rd connecting tube 22, one first valve 23, a first check-valve 24, one second valve
The second check-valve 26 of door 25 and one；The major ingredient adds pipe 4 and adds pipe for caprolactam, for by major ingredient (caprolactam CPL)
Pipe 4 is added through the major ingredient to be conveyed, first auxiliary material adds pipe 5 and adds pipe for acid additives, for acidity to be added
Plus agent MOD adds pipe 5 through first auxiliary material and conveyed, second auxiliary material adds pipe 6 and adds pipe for titanium dioxide, is used for
By titanium dioxide TiO2Pipe 6 is added through second auxiliary material to be conveyed；The first auxiliary material static mixer 10 adds to be acid
Agent blender, the second auxiliary material static mixer 11 is titanium dioxide TiO2(delustering agent) blender, second auxiliary material is static
Blender 11 must be arranged on behind the first auxiliary material static mixer 10, to reduce the time that it is contacted with acid material,
Prevent titanium dioxide from occurring agglomeration phenomena and influenceing product quality；
The motor 1, the dynamic mixer 2, first discharge nozzle 8, the front end static mixer 9, described
Two discharge nozzles 16, the first auxiliary material static mixer 10, the 3rd discharge nozzle 17, the second auxiliary material static mixer
11st, the 4th discharge nozzle 18, the end Integrated Static blender 12, the 5th discharge nozzle 19 and the polymerization tower 3 according to
Secondary connection；
The dynamic mixer 2 also adds pipe 4, first auxiliary material by the feeding pipe 7 with the major ingredient and thrown respectively
Plus pipe 5 and second auxiliary material add pipe 6 and connected；
It is auxiliary that the B chambers of the A chambers of first three-way diverter valve 13 and first three-way diverter valve 13 are placed in described first
Material is added on pipe 5, and the C chambers of first three-way diverter valve 13 are mixed by first connecting tube 20 and first auxiliary material static state
Clutch 10 is connected；The B chambers of the A chambers of second three-way diverter valve 14 and second three-way diverter valve 14 are placed in described second
Auxiliary material is added on pipe 6, and the C chambers of second three-way diverter valve 14 are static by second connecting tube 21 and second auxiliary material
Blender 11 is connected；The A chambers of 3rd three-way diverter valve 15 and the B chambers of the 3rd three-way diverter valve 15 enter described in being placed in
In expects pipe 7, the C chambers of the 3rd three-way diverter valve 15 are connected by the 3rd connecting tube 22 and the front end static mixer 9
It is logical.
First valve 23 and the first check-valve 24 are all positioned in first connecting tube 20, first valve
Door 23 is disposed adjacent with the first check-valve 24, that is, the position for stating first check-valve 24 should be close proximity to first valve
23, and the first check-valve 24 is located between first three-way diverter valve 13 and first valve 23；Second valve
Door 25 and the second check-valve 26 are all positioned in second connecting tube 21, second valve 25 and second non-return
Valve 26 is disposed adjacent, i.e., the position of described second check-valve 26 should be close proximity to second valve 25, and second non-return
Valve 26 is located between second three-way diverter valve 14 and second valve 25；Because the dynamic mixer 2 and it is described before
The material pressure on the feeding pipe 7 (main pipeline) where end static mixer 9 is likely to be greater than the first check-valve 24
With the pressure in first connecting tube 20 and second connecting tube 21 (auxiliary material pipeline) where the second check-valve 26,
So auxiliary material is possible to plus does not enter blender and suffer, and has the first check-valve 24 and the second check-valve 26 to be prevented from
Material can not enter main pipeline because of pressure unfavourable balance, in addition when the infeed failure of pump of auxiliary material stopped, prevented also from main pipeline
Material flow into auxiliary material pipeline in and formed block；And first valve 23 and second valve 24 are easy for parking of driving
Pan feeding is operated；
3rd valve 27 is placed on first discharge nozzle 8, the effect of the 3rd valve 27：If taken apart
It is necessary to close the 3rd three-way diverter valve 15 and the 3rd valve 27 when overhauling the dynamic mixer 2, not so material is just
It can spill.
Operation principle of the present utility model is as follows：
When two kinds of blenders are used simultaneously：
(the intrinsic situation of scheme one：Synchronized mixes)：First three-way diverter valve 13, second threeway is adjusted to change
To valve 14 and the 3rd three-way diverter valve 15, major ingredient caprolactam CPL is added into pipe 4 via the major ingredient and sends into the pan feeding
In pipe 7, auxiliary material acid additives MOD via first auxiliary material add pipe 5 send into the feeding pipe 7, auxiliary material titanium dioxide
TiO2Pipe 6 is added via second auxiliary material to send into the feeding pipe 7, then unifies to enter the dynamic by the feeding pipe 7
Blender 2 is once stirred mixing, then sequentially enters the front end static mixer 9, the first auxiliary material static mixing
Device 10, the second auxiliary material static mixer 11 and the end Integrated Static blender 12 are carried out after repeatedly stirring mixing, are sent
Enter in the polymerization tower 3.
Scheme two (substep is mixed)：Adjust first three-way diverter valve 13, second three-way diverter valve 14 and described
3rd three-way diverter valve 15, adds pipe 4 via the major ingredient successively by major ingredient caprolactam CPL and the feeding pipe 7 enters institute
State dynamic mixer 2 and once stirred mixing, enter back into the front end static mixer 9；Auxiliary material acid additives MOD via
First connecting tube 20 is stirred mixing into the first auxiliary material static mixer 10；Auxiliary material titanium dioxide TiO2Via
Second connecting tube 21 is stirred mixing into the second auxiliary material static mixer 11；It is most quiet through end synthesis afterwards
State blender 12 integrate after stirring mixing, is sent into the polymerization tower 3.
When only using static mixer：
Scheme one (synchronized mixes)：Adjust first three-way diverter valve 13, second three-way diverter valve 14 and described
3rd three-way diverter valve 15, by major ingredient caprolactam CPL via the major ingredient add pipe 4 send into the feeding pipe 7, auxiliary material acid
Property additive MOD via first auxiliary material add pipe 5 send into the feeding pipe 7, auxiliary material titanium dioxide TiO2Via described
Two auxiliary materials add pipe 6 and sent into the feeding pipe 7, then unify into the front end static mixer 9 to be entered by the feeding pipe 7
Row once stirring mixing, then sequentially enters the first auxiliary material static mixer 10, the second auxiliary material static mixer 11
And the end Integrated Static blender 12 is carried out after repeatedly stirring mixing, is sent into the polymerization tower 3.
Scheme two (substep is mixed)：
First three-way diverter valve 13, second three-way diverter valve 14 and the 3rd three-way diverter valve 15 are adjusted,
Major ingredient caprolactam CPL is added into pipe 4 via the major ingredient successively and the feeding pipe 7 enters the front end static mixer 9
Carry out once stirring mixing；It is mixed that auxiliary material acid additives MOD enters first auxiliary material static state via first connecting tube 20
Clutch 10 is stirred mixing；Auxiliary material titanium dioxide TiO2Enter second auxiliary material static state via second connecting tube 21 mixed
Clutch 11 is stirred mixing；Most carried out afterwards through the end Integrated Static blender 12 after integrating stirring mixing, feeding is described
In polymerization tower 3.
Advantage of the present utility model is as follows：
1st, in process of production, with without motor-driven static mixer motor-driven dynamic can have been replaced to mix
Device, can also make two kinds of blenders while using by operating three-way diverter valve；
2nd, raw materials for production can be subjected to substep mixing, finally comprehensive mixing, can avoid that only mixed once brings is mixed
Close uneven phenomenon；And the time that titanium dioxide is contacted with acid additives is greatly reduce both, it effectively prevent two
Titan oxide particles occur coalescence and influence product quality；
3rd, static mixer drives without motor, can save electric energy, reduce energy consumption；
4th, flexible and convenient operation, can change hybrid mode at any time, and selectivity is strong, and when dynamic mixer parking maintenance,
Raw material, which can proceed with, is mixed and fed into polymerization tower, does not influence production line normally to produce, and production line is without stopping, so efficiently
It ensure that the quality of polymerization product (slices of caprone).
Although the foregoing describing embodiment of the present utility model, those familiar with the art should
Work as understanding, the specific embodiment described by us is merely exemplary, rather than for the limit to scope of the present utility model
Fixed, those skilled in the art should in the equivalent modification and change made according to spirit of the present utility model
Cover in scope of the claimed protection of the present utility model.
Claims (2)
1. a kind of polymer raw hybrid system of novel nylon 6, including a motor, a dynamic mixer, a polymerization tower, a major ingredient are thrown
Plus pipe, one first auxiliary material add pipe, one second auxiliary material and add pipe, a feeding pipe and one first discharge nozzle, it is characterised in that：Also wrap
A front end static mixer, one first auxiliary material static mixer, one second auxiliary material static mixer, an end Integrated Static is included to mix
Clutch, one first three-way diverter valve, one second three-way diverter valve, one the 3rd three-way diverter valve, one second discharge nozzle, one the 3rd go out
Expects pipe, one the 4th discharge nozzle, one the 5th discharge nozzle, one first connecting tube, one second connecting tube, one the 3rd connecting tube, one first
Valve, a first check-valve, one second valve, a second check-valve and one the 3rd valve；
The motor, the dynamic mixer, first discharge nozzle, the front end static mixer, second discharge nozzle,
The first auxiliary material static mixer, the 3rd discharge nozzle, the second auxiliary material static mixer, the 4th discharge nozzle,
The end Integrated Static blender, the 5th discharge nozzle and the polymerization tower are sequentially connected；The dynamic mixer also leads to
Cross the feeding pipe and add that pipe, first auxiliary material add pipe and second auxiliary material adds pipe and connected with the major ingredient respectively；
The B chambers of the A chambers of first three-way diverter valve and first three-way diverter valve are placed in first auxiliary material and add pipe
On, the C chambers of first three-way diverter valve are connected by first connecting tube with the first auxiliary material static mixer；It is described
The B chambers of the A chambers of second three-way diverter valve and second three-way diverter valve are placed in second auxiliary material and added on pipe, and described
The C chambers of two three-way diverter valves are connected by second connecting tube with the second auxiliary material static mixer；3rd threeway
The B chambers of the A chambers of reversal valve and the 3rd three-way diverter valve are placed on the feeding pipe, the C of the 3rd three-way diverter valve
Chamber is connected by the 3rd connecting tube with the front end static mixer；
First valve and the first check-valve are all positioned in first connecting tube, second valve and described
Two check-valves are all positioned in second connecting tube, and the 3rd valve is placed on first discharge nozzle.
2. a kind of polymer raw hybrid system of novel nylon 6 as claimed in claim 1, it is characterised in that：First valve
It is disposed adjacent with the first check-valve, and the first check-valve is located at first three-way diverter valve and first valve
Between；Second valve is disposed adjacent with the second check-valve, and the second check-valve is changed located at second threeway
To between valve and second valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720123229.3U CN206538509U (en) | 2017-02-10 | 2017-02-10 | A kind of polymer raw hybrid system of novel nylon 6 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720123229.3U CN206538509U (en) | 2017-02-10 | 2017-02-10 | A kind of polymer raw hybrid system of novel nylon 6 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206538509U true CN206538509U (en) | 2017-10-03 |
Family
ID=59946263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720123229.3U Expired - Fee Related CN206538509U (en) | 2017-02-10 | 2017-02-10 | A kind of polymer raw hybrid system of novel nylon 6 |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206538509U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113148268A (en) * | 2021-04-19 | 2021-07-23 | 河南芝元堂智能设备有限公司 | Full-automatic powder packaging equipment |
-
2017
- 2017-02-10 CN CN201720123229.3U patent/CN206538509U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113148268A (en) * | 2021-04-19 | 2021-07-23 | 河南芝元堂智能设备有限公司 | Full-automatic powder packaging equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205924767U (en) | Formula proportioning device is gone into to mechanical pump | |
| CN206538509U (en) | A kind of polymer raw hybrid system of novel nylon 6 | |
| CN202343133U (en) | Coating homogenization system | |
| CN104589503A (en) | Concrete circulating-stirring continuous-pumping machine | |
| CN104196514B (en) | A kind of acidizing and fracturing fluid is i.e. joined and is i.e. used device | |
| CN211988268U (en) | Compound female jar that circulates of water-reducing agent | |
| CN218535236U (en) | White carbon black and rubber mixing device | |
| CN201643994U (en) | High efficient liquid-powder homogenization and emulsification device for vacuum emulsifying mixer | |
| CN214809983U (en) | Stainless steel vortex type gas-liquid mixing water pump | |
| CN213680453U (en) | Emulsification pharmacy system that start automatic cycle and sweep | |
| CN109821454A (en) | A kind of Agitation Tank that can guarantee with liquid quality and have automatic detection function | |
| CN210434441U (en) | Solid powder mixing system | |
| CN105713119B (en) | A kind of neodymium series rare earth polybutadiene rubber polyplant and its feed system | |
| CN211837475U (en) | Combined liquid product blending device | |
| CN209138430U (en) | One kind using Efficient Agitator based on tetramethylammonium hydroxide production | |
| CN207562725U (en) | Medical liquid mixer | |
| CN206854226U (en) | A kind of automatic clear system of powdery paints | |
| CN207805417U (en) | A kind of integral type delivery pump for mixture homogenizing | |
| CN220940454U (en) | Homogenizer | |
| CN202428611U (en) | High-pressure reaction injection molding device | |
| CN206215096U (en) | A kind of cosmetics make blender | |
| CN220802965U (en) | Homogenizer washes subassembly and homogenizer | |
| CN215693389U (en) | Novel combined dosing system | |
| CN211917355U (en) | PVC automobile insulation is plasticizer compounding device for material | |
| CN210449021U (en) | Electronic blending system for automobile cleaning agent |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171003 Termination date: 20210210 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |