CN204224749U - The toner sprinkling of singe screw squash type toner spinning system, conveying, mixing arrangement - Google Patents
The toner sprinkling of singe screw squash type toner spinning system, conveying, mixing arrangement Download PDFInfo
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- CN204224749U CN204224749U CN201420640830.6U CN201420640830U CN204224749U CN 204224749 U CN204224749 U CN 204224749U CN 201420640830 U CN201420640830 U CN 201420640830U CN 204224749 U CN204224749 U CN 204224749U
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Abstract
The toner sprinkling of singe screw squash type toner spinning system, conveying, mixing arrangement, comprise toner metered injection mechanism, the dry slices synthesis method pipeline of PLA, spinning screw extruder, melt pipe; Described spinning screw extruder is horizontally disposed with, and PLA dry slices synthesis method pipeline lower end is connected with the feed end of spinning screw extruder, and the outlet of spinning screw extruder is connected with the import of melt pipe, is provided with static blender in melt pipe.The utility model is reasonable in design, structure is simple, directly toner and PLA are done section to mix, eliminate toner and make this procedure of Masterbatch, and directly some groups of batch mixing unit are set in melt pipe, reach the object of melt even batch mixing when flowing through conveyance conduit, eliminating, on conveyance conduit, mixing system being installed, greatly save cost, improve production efficiency.
Description
Technical field
The utility model belongs to chemical fibre spinning technical field, is specifically related to a kind of toner sprinkling of singe screw squash type toner spinning system, conveying, mixing arrangement.
Background technology
Chemical fibre spinning comprises the preparation of spinning melt or solution, fibre forming and winding and last handling process.Last handling process then has the stretching of as-spun fibre, heat setting to series of processes such as finished product packings.
Existing spinning process has melt spinning and solution-polymerized SBR two class.Usually the fibre-forming polymer not occurring in the molten state significantly to decompose adopts melt spinning, such as polyester fiber, polyamide fiber etc.Melt spinning process is simple, and spinning speed is high.The fibre-forming polymer that solution spinning will decompose when being applicable to melting, dissolves the spinning solution of obtained thickness in a solvent, then carries out spinning by fibre-forming polymer.By the solidification mode of the spinning solution thread extruded from capillary spinneret orifice, solution-polymerized SBR is divided into again wet spinning and dry spinning two kinds.It is lower that solution-polymerized SBR spins speed, especially wet spinning.For improving spinning capability, the spinning head that hole count is a lot of need be adopted.Spinning of dry spinning is fast higher than wet spinning, but far below melt spinning.
At present, could do section with PLA after dry powder color needs granulation to become Masterbatch and together enter spinning screw extruder, operation is quite loaded down with trivial details, and production efficiency is low, and production cost is high.
Utility model content
The utility model is in order to solve weak point of the prior art, and the toner mixing the singe screw squash type toner spinning system carrying out spinning operation of cutting into slices sprays, carries, mixing arrangement to provide a kind of toner directly to do with PLA.
For solving the problems of the technologies described above, the utility model adopts following technical scheme: the toner sprinkling of singe screw squash type toner spinning system, conveying, mixing arrangement, comprise toner metered injection mechanism, the dry slices synthesis method pipeline of PLA, spinning screw extruder, melt pipe;
Described toner metered injection mechanism comprises the cylinder of open top, cylinder top is removably connected with gland by bolt, rotate between gland and the center of cylinder and be provided with rotating shaft, rotating shaft lower end is coaxial is provided with metering rotating disk, rotating shaft upper end is connected with the actuating unit be positioned at above gland, be respectively equipped with rear side the baffle plate that a piece is fixedly connected on cylinder inside on front side of rotating shaft, baffle plate be provided with respectively with rotating shaft and the sealing strip measuring disc surfaces and contact, cylinder interior separation is feed cavity and discharging chamber by rotating shaft and two pieces of baffle plates, gland is provided with the toner import being positioned at feed cavity side, gland is provided with the first dry compressed air inlet being positioned at side, discharging chamber, metering rotating disk is evenly provided with a circle storage hole along the centre of gyration, cylinder bottom side is provided with the toner outlet being positioned at side, discharging chamber, toner outlet is corresponding up and down with storage hole, toner outlet is connected with tremie pipe, the outlet of tremie pipe is connected with stuff-spraying pipe, one end of stuff-spraying pipe is provided with shower nozzle, the other end of stuff-spraying pipe is the second dry compressed air inlet, in the blanking direction of tremie pipe and stuff-spraying pipe compressed-air actuated spray between angle be acute angle,
The dry slices synthesis method pipeline of described PLA is vertically arranged, shower nozzle on stuff-spraying pipe extend in the dry slices synthesis method pipeline of PLA, the dry section of PLA is carried from top to bottom in the dry slices synthesis method pipeline of PLA, the direction of sprinkler toner down and surrounding, has between shower nozzle outer edge and PLA dry slices synthesis method pipeline inwall and does section for PLA and pass through circular passage;
Described spinning screw extruder is horizontally disposed with, and PLA dry slices synthesis method pipeline lower end is connected with the feed end of spinning screw extruder, and the outlet of spinning screw extruder is connected with the import of melt pipe, is provided with static blender in melt pipe.
Described static blender comprises melt pipe body, is provided with batch mixing unit in melt pipe body; Batch mixing unit comprises the first helical baffle and the second helical baffle, melt pipe body is separated into the first semi-circular tube helical duct and the second semi-circular tube helical duct by the first helical baffle, melt pipe body is separated into the 3rd semi-circular tube helical duct and the 4th semi-circular tube helical duct by the second helical baffle, all the arranging along melt pipe body radial direction with one side of the second helical baffle and mutual to be vertically connected of the first helical baffle.
The both sides of described first helical baffle all to be arranged and mutually vertical along melt pipe body radial direction, and the both sides of the second helical baffle all to be arranged and mutually vertical along melt pipe body radial direction.
The quantity of described batch mixing unit is more than or equal to two groups, being connected with the helical baffle of adjacent one group of batch mixing unit is mutually vertical on one side of the helical baffle of one group of batch mixing unit.
Adopt technique scheme, singe screw squash type toner spinning system also comprises toner feed bin, measuring pump, filament spinning component and spinnerets.
The outlet of described toner feed bin is connected by discharge nozzle with between toner import, and discharge nozzle is provided with electromagnetic valve.
The outlet of described spinning screw extruder is connected with the import of measuring pump by melt pipe, and metering delivery side of pump is connected with the import of filament spinning component, and the outlet of filament spinning component is connected with the import of spinnerets.
The specific works process of singe screw squash type toner spinning system is as follows: dry powder color is stored in toner feed bin, the rotating speed of actuating unit is regulated to control rotary speed by frequency converter, the so just discharge quantity of adjustable toner, toner enters in feed cavity by toner import, and be filled in the storage hole of metering rotating disk, actuating unit drives axis of rotation, toner entrained in feed cavity is transferred in discharging chamber, simultaneously, empty storage hole forwards in feed cavity and carries out storing, when storage hole and the toner of the full toner of storage export up and down to time corresponding at himself gravity and from the first dry compressed air inlet passes into compressed-air actuated effect, toner is blown in tremie pipe, second dry compressed air inlet passes into pressure-air to stuff-spraying pipe, negative pressure is produced in tremie pipe, toner enters in stuff-spraying pipe, under compressed-air actuated effect, sprayed by shower nozzle.PLA is done section and is done section output channel according to certain ratio and flow velocity by PLA, the toner of shower nozzle ejection is sprayed onto in the dry section of PLA equably, with toner polylactic acid slice by deadweight and under the effect of dry air air-flow, enter spinning screw extruder, cut into slices through the melting of spinning screw extruder, mixing enter spinning pump by the static blender in melt pipe and melt pipe, after metering, make look silk by filament spinning component, spinnerets.
Because toner and polylactic acid slice mix not too even in the dry slices synthesis method pipeline of PLA, therefore static blender is set again in melt pipe.The mixing principle of static blender is as follows: assuming that A melt and B melt are when mixing, A melt enters the first semi-circular tube helical duct, B melt enters the second semi-circular tube helical duct, when A melt and B melt enter into the second helical baffle by the first helical baffle, due to the first helical baffle while all arrange along melt pipe body radial direction with one side of the second helical baffle and mutual to be vertically connected, a part for a part for A melt and B melt is so just made to enter in the 3rd semi-circular tube helical duct, another part of A melt and another part of B melt enter in the 4th semi-circular tube helical duct.After the mixing of first group of batch mixing unit, then enter into second group of batch mixing unit, after some groups of batch mixing unit, A melt and B melt mixed evenly after directly enter into next process.
Singe screw squash type toner spinning system is reasonable in design, structure is simple, directly toner and PLA are done section to mix, eliminate toner and make this procedure of Masterbatch, and directly some groups of batch mixing unit are set in melt pipe, reach the object of melt even batch mixing when flowing through conveyance conduit, eliminating, on conveyance conduit, mixing system being installed, greatly save cost, improve production efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the static blender in Fig. 1 with one group of batch mixing unit;
Fig. 3 is the explosive view of Fig. 2.
Detailed description of the invention
As shown in Figure 1, Figure 2 and Figure 3, singe screw squash type toner spinning system, comprises toner feed bin 8, toner metered injection mechanism, the dry slices synthesis method pipeline 9 of PLA, spinning screw extruder 10, melt pipe 11, measuring pump 12, filament spinning component 13 and spinnerets 14.
Toner metered injection mechanism comprises the cylinder 15 of open top, cylinder 15 top is removably connected with gland 17 by bolt 16, rotate between the center of gland 17 and cylinder 15 and be provided with rotating shaft 18, rotating shaft 18 lower end is coaxial is provided with metering rotating disk 19, rotating shaft 18 upper end is connected with the actuating unit be positioned at above gland 17, be respectively equipped with rear side the baffle plate 20 that a piece is fixedly connected on cylinder 15 inside on front side of rotating shaft 18, baffle plate 20 be provided with respectively with rotating shaft 18 and the sealing strip 21 measuring rotating disk 19 surface contact, cylinder 15 interior separation is feed cavity 22 and discharging chamber 23 by rotating shaft 18 and two pieces of baffle plates 20, gland 17 is provided with the toner import 24 being positioned at feed cavity 22 side, gland 17 is provided with the first dry compressed air inlet 25 being positioned at side, discharging chamber 23, metering rotating disk 19 is evenly provided with a circle storage hole 26 along the centre of gyration, bottom cylinder 15, side is provided with the toner outlet 27 being positioned at side, discharging chamber 23, toner outlet 27 is corresponding with storage hole about 26, toner outlet 27 is connected with tremie pipe 28, the outlet of tremie pipe 28 is connected with stuff-spraying pipe 29, one end of stuff-spraying pipe 29 is provided with shower nozzle 30, the other end of stuff-spraying pipe 29 is the second dry compressed air inlet 31, in the blanking direction of tremie pipe 28 and stuff-spraying pipe 29 compressed-air actuated spray between angle N be acute angle.
The outlet of toner feed bin 8 is connected by discharge nozzle 32 with between toner import 24, and discharge nozzle 32 is provided with electromagnetic valve 33.
The dry slices synthesis method pipeline 9 of PLA is vertically arranged, shower nozzle 30 on stuff-spraying pipe 29 extend in the dry slices synthesis method pipeline 9 of PLA, the dry section of PLA is carried from top to bottom in the dry slices synthesis method pipeline 9 of PLA, the direction that shower nozzle 30 sprays toner down and surrounding, has between shower nozzle 30 outer edge and PLA dry slices synthesis method pipeline 9 inwall and does section for PLA and pass through circular passage.
Spinning screw extruder 10 is horizontally disposed with, PLA dry slices synthesis method pipeline 9 lower end is connected with the feed end of spinning screw extruder 10, the outlet of spinning screw extruder 10 is connected by the import of melt pipe 11 with measuring pump 12, static blender 34 is provided with in melt pipe 11, the outlet of measuring pump 12 is connected with the import of filament spinning component 13, and the outlet of filament spinning component 13 is connected with the import of spinnerets 14.
Static blender 34 comprises melt pipe body 1, is provided with batch mixing unit in melt pipe body 1; Batch mixing unit comprises the first helical baffle 2 and the second helical baffle 3, melt pipe body 1 is separated into the first semi-circular tube helical duct 4 and the second semi-circular tube helical duct 5 by the first helical baffle 2, what melt pipe body 1 was separated into the 3rd semi-circular tube helical duct 6 and the 4th semi-circular tube helical duct 7, first helical baffle 2 by the second helical baffle 3 all arranges along melt pipe body 1 radial direction with one side of the second helical baffle 3 and mutual to be vertically connected.
The both sides of the first helical baffle 2 all to be arranged and mutually vertical along melt pipe body 1 radial direction, and the both sides of the second helical baffle 3 all to be arranged and mutually vertical along melt pipe body 1 radial direction.
In order to improve the uniformity of mixing, the quantity that can arrange batch mixing unit is more than or equal to two groups, being connected with the helical baffle of adjacent one group of batch mixing unit is mutually vertical on one side of the helical baffle of one group of batch mixing unit.
Spinning screw extruder 10, measuring pump 12, filament spinning component 13 and spinnerets 14 in singe screw squash type toner spinning system are existing mature technology, and concrete structure repeats no more.
The specific works process of singe screw squash type toner spinning system is as follows: dry powder color is stored in toner feed bin 8, the rotating speed of actuating unit is regulated to control rotary speed by frequency converter, the so just discharge quantity of adjustable toner, toner enters in feed cavity 22 by toner import 24, and be filled in the storage hole 26 of metering rotating disk 19, actuating unit drives rotating shaft 18 to rotate, toner entrained in feed cavity 22 is transferred in discharging chamber 23, simultaneously, empty storage hole 26 forwards in feed cavity 22 and carries out storing, when storage hole 26 and the toner of the full toner of storage export about 27 to time corresponding at himself gravity and from the first dry compressed air inlet 25 passes into compressed-air actuated effect, toner is blown in tremie pipe 28, second dry compressed air inlet 31 passes into pressure-air to stuff-spraying pipe 29, negative pressure is produced in tremie pipe 28, toner enters in stuff-spraying pipe 29, under compressed-air actuated effect, sprayed by shower nozzle 30.PLA is done section and is done section output channel according to certain ratio and flow velocity by PLA, the toner that shower nozzle 30 sprays is sprayed onto in the dry section of PLA equably, with toner polylactic acid slice by deadweight and under the effect of dry air air-flow, enter spinning screw extruder 10, cut into slices through spinning screw extruder 10 melting, mixing enter spinning pump 12 by the static blender 34 in melt pipe 11 and melt pipe 11, after metering, make look silk by filament spinning component 13, spinnerets 14.
Because toner and polylactic acid slice mix not too even in the dry slices synthesis method pipeline 9 of PLA, therefore static blender 34 is set in melt pipe 11 again.The mixing principle of static blender 34 is as follows: assuming that A melt and B melt are when mixing, A melt enters the first semi-circular tube helical duct 4, B melt enters the second semi-circular tube helical duct 5, when A melt and B melt enter into the second helical baffle 3 by the first helical baffle 2, due to the first helical baffle 2 while all arrange along melt pipe body 1 radial direction with one side of the second helical baffle 3 and mutual to be vertically connected, a part for a part for A melt and B melt is so just made to enter in the 3rd semi-circular tube helical duct 6, another part of A melt and another part of B melt enter in the 4th semi-circular tube helical duct 7.After the mixing of first group of batch mixing unit, then enter into second group of batch mixing unit, after some groups of batch mixing unit, A melt and B melt mixed evenly after directly enter into next process.
Above embodiment is the unrestricted the technical solution of the utility model in order to explanation only, although be described in detail the utility model with reference to above-described embodiment, those of ordinary skill in the art is to be understood that: still can modify to the utility model or equivalent replacement, and not departing from any modification or partial replacement of spirit and scope of the present utility model, it all should be encompassed in the middle of right of the present utility model.
Claims (4)
1. singe screw squash type toner spinning system toner spray, conveying, mixing arrangement, it is characterized in that: comprise toner metered injection mechanism, the dry slices synthesis method pipeline of PLA, spinning screw extruder, melt pipe;
Described toner metered injection mechanism comprises the cylinder of open top, cylinder top is removably connected with gland by bolt, rotate between gland and the center of cylinder and be provided with rotating shaft, rotating shaft lower end is coaxial is provided with metering rotating disk, rotating shaft upper end is connected with the actuating unit be positioned at above gland, be respectively equipped with rear side the baffle plate that a piece is fixedly connected on cylinder inside on front side of rotating shaft, baffle plate be provided with respectively with rotating shaft and the sealing strip measuring disc surfaces and contact, cylinder interior separation is feed cavity and discharging chamber by rotating shaft and two pieces of baffle plates, gland is provided with the toner import being positioned at feed cavity side, gland is provided with the first dry compressed air inlet being positioned at side, discharging chamber, metering rotating disk is evenly provided with a circle storage hole along the centre of gyration, cylinder bottom side is provided with the toner outlet being positioned at side, discharging chamber, toner outlet is corresponding up and down with storage hole, toner outlet is connected with tremie pipe, the outlet of tremie pipe is connected with stuff-spraying pipe, one end of stuff-spraying pipe is provided with shower nozzle, the other end of stuff-spraying pipe is the second dry compressed air inlet, in the blanking direction of tremie pipe and stuff-spraying pipe compressed-air actuated spray between angle be acute angle,
The dry slices synthesis method pipeline of described PLA is vertically arranged, shower nozzle on stuff-spraying pipe extend in the dry slices synthesis method pipeline of PLA, the dry section of PLA is carried from top to bottom in the dry slices synthesis method pipeline of PLA, the direction of sprinkler toner down and surrounding, has between shower nozzle outer edge and PLA dry slices synthesis method pipeline inwall and does section for PLA and pass through circular passage;
Described spinning screw extruder is horizontally disposed with, and PLA dry slices synthesis method pipeline lower end is connected with the feed end of spinning screw extruder, and the outlet of spinning screw extruder is connected with the import of melt pipe, is provided with static blender in melt pipe.
2. singe screw squash type toner spinning system according to claim 1 toner spray, conveying, mixing arrangement, it is characterized in that: described static blender comprises melt pipe body, is provided with batch mixing unit in melt pipe body; Batch mixing unit comprises the first helical baffle and the second helical baffle, melt pipe body is separated into the first semi-circular tube helical duct and the second semi-circular tube helical duct by the first helical baffle, melt pipe body is separated into the 3rd semi-circular tube helical duct and the 4th semi-circular tube helical duct by the second helical baffle, all the arranging along melt pipe body radial direction with one side of the second helical baffle and mutual to be vertically connected of the first helical baffle.
3. singe screw squash type toner spinning system according to claim 2 toner spray, conveying, mixing arrangement, it is characterized in that: the both sides of described first helical baffle all to be arranged and mutually vertical along melt pipe body radial direction, the both sides of the second helical baffle all to be arranged and mutually vertical along melt pipe body radial direction.
4. singe screw squash type toner spinning system according to claim 3 toner spray, conveying, mixing arrangement, it is characterized in that: the quantity of described batch mixing unit is more than or equal to two groups, being connected with the helical baffle of adjacent one group of batch mixing unit is mutually vertical on one side of the helical baffle of one group of batch mixing unit.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110801748A (en) * | 2019-11-21 | 2020-02-18 | 道真自治县泓禾生态农业开发有限责任公司 | Peach tree planting device |
| CN114933362A (en) * | 2021-11-30 | 2022-08-23 | 中国水利水电科学研究院 | Device and method for supplementing constructed wetland solid carbon source |
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2014
- 2014-10-31 CN CN201420640830.6U patent/CN204224749U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110801748A (en) * | 2019-11-21 | 2020-02-18 | 道真自治县泓禾生态农业开发有限责任公司 | Peach tree planting device |
| CN114933362A (en) * | 2021-11-30 | 2022-08-23 | 中国水利水电科学研究院 | Device and method for supplementing constructed wetland solid carbon source |
| CN114933362B (en) * | 2021-11-30 | 2023-02-28 | 中国水利水电科学研究院 | Device and method for supplementing constructed wetland solid carbon source |
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