CN208038605U - A kind of spinning-drawing machine producing 56 fiber of biomass polyamide - Google Patents
A kind of spinning-drawing machine producing 56 fiber of biomass polyamide Download PDFInfo
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- CN208038605U CN208038605U CN201721873828.3U CN201721873828U CN208038605U CN 208038605 U CN208038605 U CN 208038605U CN 201721873828 U CN201721873828 U CN 201721873828U CN 208038605 U CN208038605 U CN 208038605U
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Abstract
The utility model embodiment discloses a kind of spinning-drawing machine producing 56 fiber of biomass polyamide, which includes：N number of spinning subsystem, it is successively set in the rack of spinning-drawing machine, in each spinning subsystem screw extruder is disposed with according to the direction of travel of tow, melt pipe system, M manifold, annealer component, cross air blasting cooling-part, path component, opposite oil tanker, godet roller, P weaving position is provided in each manifold, there are one components of weaving for setting on each weaving position, there are one annealer components for setting below the spinneret of each weaving component, there are one cross air blasting cooling-parts for lower section setting, each cross air blasting cooling-part lower part connects a path component, there are one godet rollers for setting below each opposite oil tanker, every M godet roller setting, there are one draw-off godets；The feeding machine of the draw-off godet side of the least significant end for several draw-off godets being arranged in order, the silk cylinder reciprocating apparatus at the corresponding position of feeding machine.
Description
Technical field
The utility model is related to textile technology field more particularly to a kind of spinning producing 56 fiber of biomass polyamide
Machine.
Background technology
In the prior art, polyamide is largely produced using petrochemistry method, but with energy increasingly depleted, oil
It holds at high price, causes production cost higher and higher, in order to reduce production cost, more and more people turn one's attention to
Biochemical field, the requirement of sustainable production can be met to produce polyamide by substituting petroleum law using bioanalysis.It is existing
The spinning-drawing machine of 56 fiber of production biomass polyamide mostly uses greatly the short fine spinning-drawing machine of other types and restructures, and can cause to give birth in this way
The 56 fibre spinning product quality and performances of biomass polyamide of output are unstable.
Utility model content
The utility model embodiment provides a kind of spinning-drawing machine producing 56 fiber of biomass polyamide, to solve existing skill
The unstable technical problem of the 56 fibre spinning product quality and performances of biomass polyamide produced in art.
The utility model provides a kind of 56 fiber spinning machine of production biomass polyamide, including：
N number of spinning subsystem, is successively set in the rack of the spinning-drawing machine, according to silk in each spinning subsystem
The direction of travel of beam is disposed with screw extruder, melt pipe system, M manifold, annealer component, side-blown air cooling
Component, path component, opposite oil tanker, godet roller, the screw extruder are connect with the melt pipe system, the melt pipe
Road system is connect with the M manifold, and P weaving position is provided in each manifold, is provided on each position of weaving
One weaving component, each weaving component are connect with a metering pump system, and each metering pump system includes two
Metering pump, there are one the annealer component, each annealer portions for the spinneret lower section setting of each weaving component
There are one the cross air blasting cooling-parts, each cross air blasting cooling-part lower part to connect a path for setting below part
Component, there are one the opposite oil tankers for each path component lower part setting, and each there are one institutes for setting below opposite oil tanker
State godet roller, wherein N is the integer more than 0, and M is the integer more than 0, and P is the integer more than 0；
Several draw-off godets, several described godet rollers in N number of spinning subsystem are arranged in order, and are led every M
There are one the draw-off godets for the setting of silk wheel, wherein M is the integer more than 0；
Feeding machine is arranged in the side of the draw-off godet of the least significant end for several draw-off godets being arranged in order；
Silk cylinder reciprocating apparatus, is arranged at the corresponding position of the feeding machine.
Optionally, the spinning-drawing machine further includes：
Measurement head, the screw extruder being arranged in each spinning subsystem and the melt pipe system it
Between, temperature sensor and pressure sensor are provided in the measurement head, the measurement head is internally provided with filter ring, for pair
Material more than presetting granularity is filtered.
Optionally, the spinning-drawing machine further includes：
Monomer suction component is arranged below the spinneret of each filament spinning component in each spinning subsystem, institute
It states monomer suction component and monomer is aspirated by high-pressure water jet, electric boiling plate is provided at the monomer suction component suction inlet.
Optionally, the spinning-drawing machine further includes：
Dragger, be arranged in all draw-off godets being arranged in order draw-off godet and the feeding machine positioned at end it
Between, the dragger includes that 8 top-bottom cross arrange carry-over pinch rolls.
Optionally, the screw extruder is horizontal screw extruder.
Optionally, the melt pipe system in each spinning subsystem includes the connection M manifold
Pipeline, the pipeline is interior to be arranged static mixer element, and the pipeline is jacket type structure.
Optionally, the manifold is double-layer structure, is combined using detachable melt pipeline modular, in the manifold
It is additionally provided with melt pressure measuring point, to measure the pressure of filament spinning component in the manifold, each spinning station in the manifold
Pipeline is equipped with melt freezing valve, and insulation cover of the heat-insulating material as charges is provided with outside the manifold.
Optionally, transmission shaft is telescopic in the metering pump, and the transmission shaft is equipped with universal coupling and safety pin
Protective device.
Optionally, the spinning-drawing machine further includes：
Silk cylinder is contained, the silk cylinder reciprocating apparatus is placed in the Sheng silk cylinder.
Said one in the embodiment of the present application or multiple technical solutions at least have following one or more technology effects
Fruit：
Due to the weaving loom in the embodiment of the present application, it is provided with N number of spinning subsystem, is successively set on the rack of spinning-drawing machine
On, in each spinning subsystem screw extruder, melt pipe system, M spinning are disposed with according to the direction of travel of tow
Silk case, annealer component, cross air blasting cooling-part, path component, opposite oil tanker, godet roller, screw extruder and melt pipe
System connects, and melt pipe system is connect with M manifold, and P weaving position is provided in each manifold, each to weave on position
There are one component of weaving, each components of weaving to be connect with a metering pump system for setting, and each metering pump system includes two meters
Amount pump, there are one annealer component, each annealer component lower section is provided with one for the spinneret lower section setting for component of each weaving
A cross air blasting cooling-part, each cross air blasting cooling-part lower part connect a path component, the setting of each path component lower part
There are one opposite oil tanker, there are one godet rollers for setting below each opposite oil tanker, and every M godet roller setting, there are one seal wires
Disk, in the side feeding machine of the draw-off godet of the least significant end for several draw-off godets being arranged in order, the setting of silk cylinder reciprocating apparatus is being fed
Enter at the corresponding position of machine.In this way, biomass polyamide 56 slice after screw extruder melt extruded at after melt through melt
Pipe-line system is by being mixed into manifold, subsequently into metering pump system, metering pump system by melt supply to
Tow is sprayed by spinneret after filament spinning component, tow enters cross air blasting cooling-part after annealer component and cools down, after cooling
Tow after the component of path, the dewing that oils is carried out to tow by opposite oil tanker, the tow after oiling pass through multiple seal wires
It is sent into feeding machine after integrating a branch of crin after wheel, feeding machine feeds crin to silk cylinder reciprocating apparatus, and crin is reciprocal by silk cylinder
Device, which is positioned over, contains silk cylinder, in this way, the stabilization and quality of the performance for 56 fiber of polyamide produced can be effectively ensured.
Description of the drawings
Fig. 1 is the structural schematic diagram of the spinning-drawing machine of 56 fiber of production biomass polyamide provided by the embodiments of the present application；
Fig. 2 is the partial enlarged view of the spinning subsystem in Fig. 1.
Specific implementation mode
In technical solution provided by the embodiments of the present application, by providing a kind of biomass polyamide 56 fiber of producing
Spinning-drawing machine, it is unstable to solve 56 fibre spinning product quality and performances of the biomass polyamide produced in the prior art
Technical problem.The weaving loom includes：N number of spinning subsystem, is successively set in the rack of the spinning-drawing machine, each spinning
In subsystem screw extruder, melt pipe system, M manifold, annealer are disposed with according to the direction of travel of tow
Component, cross air blasting cooling-part, path component, opposite oil tanker, godet roller, the screw extruder and the melt pipe system
Connection, the melt pipe system are connect with the M manifold, P weaving position are provided in each manifold, each
There are one components of weaving, each weaving component to be connect with a metering pump system for setting on weaving position, each metering
Pumping system includes two metering pumps, and there are one the annealer components for setting below the spinneret of each weaving component, often
There are one the cross air blasting cooling-parts, each cross air blasting cooling-part lower part to connect for setting below a annealer component
A path component is connect, there are one the opposite oil tankers for each path component lower part setting, each under opposite oil tanker
There are one the godet rollers for side's setting, wherein N is the integer more than 0, and M is the integer more than 0, and P is the integer more than 0；It is several
A draw-off godet, several described godet rollers in N number of spinning subsystem are arranged in order, and M godet roller is provided with one
A draw-off godet, wherein M is the integer more than 0；The least significant end in several draw-off godets being arranged in order is arranged in feeding machine
Draw-off godet side；Silk cylinder reciprocating apparatus, is arranged at the corresponding position of the feeding machine.
In order to better understand the above technical scheme, in conjunction with appended figures and specific embodiments to upper
It states technical solution to be described in detail, it should be understood that the specific features in the utility model embodiment and embodiment are to this reality
With the detailed description of new technique scheme, rather than to the restriction of technical solutions of the utility model, in the absence of conflict,
Technical characteristic in the utility model embodiment and embodiment can be combined with each other.
Embodiment
The embodiment of the present application provides a kind of spinning-drawing machine producing 56 fiber of biomass polyamide, which includes N number of spinning
Silk subsystem, is successively set in the rack of spinning-drawing machine, is set gradually according to the direction of travel of tow in each spinning subsystem
There is screw extruder 1, the melt pipe system 3 being connect with screw extruder 1, melt pipe system 3 is connected with M manifold 4,
Be provided with P weaving position in each manifold 4, on each position of weaving setting there are one component 6 of weaving, it is each weave component 6 and
One metering pump system 5 connects, and each metering pump system includes two metering pumps, is set below the spinneret of each component 6 of weaving
It sets there are one annealer component 7, there are one cross air blasting cooling-parts 9 for the lower section setting of 7 component of each annealer, each side-blown air-cooled
But 9 lower part of component connects a path component 10, and there are one opposite oil tankers 11 for each 10 lower part of path component setting, each opposite
There are one godet rollers 12 for 11 lower section setting of oil tanker, wherein N is the integer more than 0, and M is the integer more than 0, and P is whole more than 0
Number；
Draw-off godet 13, several godet rollers 12 in N number of spinning subsystem are arranged in order, are provided with every M godet roller
One draw-off godet 13, wherein M is the integer more than 0；
Feeding machine 17 is arranged in the side of the draw-off godet 13 of the least significant end for several draw-off godets 13 being arranged in order；
Silk cylinder reciprocating apparatus, is arranged at the corresponding position of feeding machine.
Specifically, Fig. 1 is the structural schematic diagram of the weaving loom in the present embodiment, Fig. 2 is the office of the spinning subsystem in Fig. 1
Portion's enlarged drawing, the weaving loom in Fig. 1 include 6 spinning subsystems, and each spinning subsystem includes 4 weaving positions, amounts to 24.
Each spinning subsystem is provided with 2 manifolds 4,2 spinning stations is provided in each manifold 4, each spinning station is provided with
One metering pump system 5, metering pump system 5 include two metering pumps, and a metering pump is used to the melt of manifold being pumped into and spin
Silk component 6, a metering pump are used to extrude the melt of filament spinning component 6, and there are one filament spinning components for each spinning station setting, each
Spinning station is correspondingly arranged there are one annealer component 7, annealer component 7 be arranged spinneret in filament spinning component 6 with it is side-blown air-cooled
But between component 9,9 lower part of cross air blasting cooling-part connects path component 10, and opposite oil tanker 11 is arranged in component 10 lower part in path,
Every 10 lower part of path component is additionally provided with godet roller 12.6 lower section of filament spinning component of i.e. each spinning station is disposed with slow cooling
Device component 7, monomer suction component 8, cross air blasting cooling-part 9, path component 10, godet roller 12.
It is arranged in order in Fig. 1 and is provided with 24 godet rollers 12, there are one draw-off godets 13 every 2 settings of godet roller 12, altogether
Meter 12 draw-off godets 13 of setting.13 side of draw-off godet of right end is provided with feeding machine 17, at 17 corresponding position of feeding machine
It is provided with and contains silk cylinder 19, silk cylinder reciprocating apparatus 20, which is placed on, to be contained in silk cylinder 19.In specific implementation process, the spinning of weaving loom
Position number can be set according to actual conditions, here, the application is not limited.
Specifically, in ability embodiment, screw extruder 1 is horizontal screw extruder, and screw extruder includes exchange
Motor, retarder, screw rod, sleeve, heating and temperature control system, dragging speed-adjusting and control system, dragging speed-adjusting and control system use
Pressure closed loop speed-regulating control device.Screw rod can be selected according to spinning denier, digit and head number, due to spinning biomass polyamide
56, therefore the screw rod of the big L/D ratio of extrusion capacity increase by 20% is used, 105mm-170mm, length can be selected in the specification of screw diameter
With diameter ratio L/D=30.
The slice of biomass polyamide 56 enters from screw feed mouth in screw extruder 1, in each area's heating of screw rod and screw rod
Under rotary squeezing, the slice of solid, which is melted, is squeezed into melt, and establishes certain pressure in head and injected for 5 fair current of metering pump
With.Screw extruder 1 uses horizontal type structure, AC induction motor frequency control retarder to be dragged by V belt, through retarder
Drive screw turns after two-stage gear reduction.Screw rod is additionally provided with multiple heating zones, and each Heating Zone Temperature is 240 DEG C -280
DEG C, cooling zone is equipped with to ensure that slices synthesis method is unimpeded in feed inlet, prevents slice from bonding.Heating temperature-control system is set with temperature
Fixed, control and display function.It drags speed-adjusting and control system and uses pressure closed loop speed-regulating control device, be equipped with pressure bound report
Alert, parking, the parking of screw speed hypervelocity is (such as：The 15% of super setting speed) and super temperature upper limit stop heating etc. functions.It is raw
The slice of substance polyamide 56 is through 1 melt extruded of screw extruder at melt.
In turn, melt flows into the measurement head 2 that is arranged between screw extruder 12 and melt pipe system 3, in measurement head 2
Temperature sensor and pressure sensor are provided with, the online pressure and temperature parameter of 56 melt of biomass polyamide can be measured,
In turn, the heating and temperature control system of screw extruder 1 can carry out parameter regulation according to the parameter of measurement, be set inside measurement head 2
It is equipped with filter ring, for being filtered to the material for being more than presetting granularity in melt.
In turn, melt enters melt pipe system 3 after the filtering of measurement head 2, and melt pipe system 3 includes connection manifold
Pipeline, static mixer element is set in pipeline, and pipeline is jacket type structure.The pipeline that melt passes through melt pipe system 3
It distributes to manifold 4.Also, since static mixer element is arranged in pipe, melt can be made fully to be homogenized mixing, be stopped with equal
It stays time and pressure drop to be transported to the spinning pump intake of each spinning station in manifold 4, makes the spinning pump intake of each spinning station
The consistent precision to ensure metering of pressure and good fiber number.Further, pipeline is jacket type structure, is protected by heating medium for heating
Temperature, it is 270 DEG C to be maintained at temperature, and melt must be to the distribution of the residence time of each spinning station, temperature, shearing and pressure
Even consistent, inner wall of the pipe is bright and clean, and junction prevents material stock from degrading without dead angle, eliminates stagnation point and dead point.
In turn, melt is distributed by pipe-line system 3 to manifold 4, and the weaving loom in the present embodiment in Fig. 1 is 24 weavings
A manifold 4 (2/case) is arranged every two in machine, and spinning station is away from being set as 1150mm, pitch 1150mm.Manifold 4
It for double-layer structure, is combined using detachable melt pipeline modular, cancels melt pipe fitting, all using detachable melt pipeline
Modular combines, that is, improves rheological characteristic, reduces the residence time, improves fuel factor, and can regular dismounting calcining.Upper dress formula high pressure is certainly
Envelope rectangular module, manifold are kept the temperature by heating medium for heating, temperature-controlled precision ± 1 DEG C.Melt pressure survey is additionally provided in every manifold 4
Point, to measure the pressure of filament spinning component 6 in manifold 4, the pipeline of each spinning station is equipped with melt freezing valve in manifold 4,
Achieve the purpose that prevent the interior melt flows of pipe using compressed air cooling to replace metering pump.It is provided with outside manifold 4 absolutely
Hot material is kept the temperature as the insulation cover of charges.
In turn, since each spinning station is furnished with metering pump system 5, the melt in manifold 4 can be utilized high pressure continuously
It is accurately-supplied filament spinning component 6.The discharge capacity of metering pump system 5 is 2x15cc/rev, power of motor 1.5kw.Requirement that meter
Amount pumping system 5 has high-accuracy metering accuracy, and pumping and moving transmission shaft is driven by permanent magnet synchronous motor direct connection cycloidal pin teeth retarder
Dynamic, frequency control, each pump are independently driven.Transmission shaft can stretch, and transmission shaft is equipped with universal coupling and safety pin is protected
Protection unit.
Further, melt is supplied by metering pump system 5 to filament spinning component 6, is sprayed by the spinneret in filament spinning component 6
Go out tow.6 structure design of filament spinning component is that binary channels distributes rectangular configuration, and the polyamide 56 of melting is by left and right feed inlet,
It is even to enter spinneret, keep the tow sprayed from spinneret uniform, the spinnability of tow and the uniformity of tow are improved with this.Spinning
Component 6 may be sized to 500mm × 160mm, and spinneret is 1000 holes.
Textile machines in the present embodiment are in the spinning short fibre of 56 fiber of biomass polyamide, since the structure of as-spun fibre is wanted
Inside and outside unification, while the unexpected cooling of 56 melt of polyamide in order to prevent are asked, entwining for macromolecular key is caused, influences finished silk
Intensity is correspondingly arranged on annealer component 7,56 melt of polyamide can be made temporary so setting postpones but cold-zone under spinneret
When in 240 DEG C~280 DEG C of hot-air retain a period of time, be unlikely to rapid cooling.
The tow that spinneret sprays is through annealer component 7, it is also necessary to enter monomer suction component 8, biomass polyamide 56
Contain a certain amount of monomer and oligomer in slice, these monomers and oligomer are at high temperature in gaseous form with melt from spinneret
It is escaped in hole, by the cooling effect of cross air blasting and environment temperature, can crystallize and be adhered to spinneret and cross air blasting cooling-part 9
On web plate, spinning condition is caused to deteriorate, broken end increases.So being provided with monomer suction component 8 below spinneret, monomer is taken out
It inhales component 8 and monomer is aspirated by high-pressure water jet, electric boiling plate is provided at 8 suction inlet of monomer suction component, to ensure monomer not
It can crystallisation by cooling blocking pump orifice.
Further, tow needs to be cooled down through cross air blasting cooling-part 9 after monomer suction component 8 aspirates monomer, by
More in 56 fiber spinneret hole count of biomass polyamide, filament number and total fiber number are big, it is desirable that through cross air blasting cooling-part 9 into
Blowing area can be used in row cooling, cross air blasting cooling-part 9：The cross air blasting of wide by 1030 × long 1700mm, main air duct pressure are
500~800pa, wind-warm syndrome are normally controlled in 20 DEG C~25 DEG C.Wind speed irregularity≤± 9%, relative humidity 75 ± 5%, wind speed 0.4
~0.8m/s.
Cross air blasting cooling-part 9 is mounted on 4 lower part of manifold, is provided surely from air-conditioning system to cross air blasting cooling-part 9
Fixed, clean cooling wind.Tow, which goes out after spinneret, to be become to mould the monofilament of shape its structure hair in a short period of time by melt stream
Changing.This variation is influenced very big by speed, the uniformity of the air stream on cross air blasting top.Transverse direction of the wind speed in side-blowing air chamber
Upper holding stable and consistent, it is in the right direction, and VELOCITY DISTRIBUTION is reasonable in cross air blasting short transverse, ensure that tow is uniform solid
It is melted into shape.It is equipped with volume damper in 9 air inlet of cross air blasting cooling-part, cooling wind is filtered through horizontal drawer formula filter,
The horizontal blowout after vertical porous plate, cellular board, multiple layer metal net rectification again, it is rectilinear to can be taken off clearly with drawer type filter
It washes.
In turn, tow sequentially enters path component 10 after the cooling of cross air blasting cooling-part 9, and tow is in path component 10
It is interior, the interference of ambient temperature and wind direction is can avoid, the swing of 56 fiber of biomass polyamide is reduced.Tow passes through path portion
After part 10, the dewing that oils is carried out by the opposite oil tanker 11 being arranged face-to-face, increases the cohesive force of fiber, improves the anti-quiet of fiber
Electrical property reduces the break-in power between fiber and equipment, fiber and fiber, improves the aft-loaded airfoil performance of fiber.
Tow after oiling enters reel system, and reel system uses guide-roller type boundling, i.e.,：Reel system includes every river in Zhejiang Province
The godet roller 12 of road lower part setting, godet roller 12 are disposed side by side on successively under every path, and the size of godet roller can select Φ
70×96mm.In turn, the tow in first article of path bypasses the 2nd godet roller 12 of the 1st 12 rear steering of godet roller.Article 2 path
Tow of the tow in the 2nd godet roller 12 and first article of path accumulate it is a branch of, and so on, the tow in a plurality of path is whole
It is collected to the last one godet roller 12, accumulates one crin.
Further, when weaving loom in the present embodiment uses 24, away from 1150mm, the path of wire is longer for position, winding
System carries out wire feed using draw-off godet 13, and a draw-off godet 13 is arranged between each two godet roller 12, and draw-off godet 13 is passed using active
It is dynamic individually to be dragged, and frequency control is used, the synchronization of 13 wire feed rate of each draw-off godet can be reached, it is ensured that tow uniformly reaches
To dragger 15.The size of draw-off godet 13 can select 160 × 150mm of Φ.
By reel system by the corresponding tow in multiple paths after the last one godet roller 12 accumulates one crin,
Finish is required supplementation with, increases the component 14 that always oils and oils to crin, the crin after oiling enters dragger 15.Dragger 15
It is arranged between the draw-off godet 13 and feeding machine 17 of the end for all draw-off godets 13 being arranged in order, dragger 15 includes on 8
Lower cross arrangement carry-over pinch rolls, carry-over pinch rolls size can select 400 × 245mm of Φ.Dragger 15 enters feeding for controlling tow
The tension of machine 17.Since as-spun fibre intensity is relatively low, elongation is larger, and hauling speed is very high, and carry-over pinch rolls smooth running is without shaking
It is dynamic.Curling round the roll in order to prevent, traction roller surface is smooth, is accompanied by dress wrap detection device, once curling round the roll sends out signal immediately, so as to
Timely processing.
In turn, crin is sent into feeding machine 17 by dragger 15, and feeding directive wheel is provided between dragger 15 and feeding machine 17
16, crin is after by dragger 15, and by feeding 16 deflecting of directive wheel to feeding machine 17, feeding machine 17 is engagement type structure.
Engagement type feeding machine is the equal gear of a pair of of modulus, is fed for silk cylinder reciprocating apparatus by the engagement of two gear to hold crin
20。
It is additionally provided with automatic repairing component 18 in feeding machine 17 and silk cylinder reciprocating apparatus 20, crin is carried out on further
Oil, to reduce friction.Silk cylinder reciprocating apparatus 20, which is placed on, to be contained in silk cylinder 19, and silk cylinder reciprocating apparatus 20 includes empty cylinder conveyer, past
It answers a pager's call, tow-stapling machine, yarn swaying machine, completely cylinder slideway and control system.The silk longitudinally reciprocal velocity interval of cylinder is 3~10 ms/min, silk
Cylinder transverse reciprocating speed is 0.5~2.5 m/min, and output speed is 8 ms/min.It can be spinned using the weaving loom in the present embodiment
Fiber dimensious is 56 staple fiber of biomass polyamide of 1.5d~5.0d.
Although the preferred embodiment of the utility model has been described, once a person skilled in the art knows basic
Creative concept, then additional changes and modifications may be made to these embodiments.It is wrapped so the following claims are intended to be interpreted as
It includes preferred embodiment and falls into all change and modification of the scope of the utility model.
Obviously, those skilled in the art can carry out the utility model various modification and variations without departing from this practicality
Novel spirit and scope.If in this way, these modifications and variations of the present invention belong to the utility model claims and
Within the scope of its equivalent technologies, then the utility model is also intended to include these modifications and variations.
Claims (9)
1. a kind of spinning-drawing machine producing 56 fiber of biomass polyamide, which is characterized in that including：
N number of spinning subsystem, is successively set in the rack of the spinning-drawing machine, according to tow in each spinning subsystem
Direction of travel is disposed with screw extruder, melt pipe system, M manifold, annealer component, cross air blasting cooling end
Part, path component, opposite oil tanker, godet roller, the screw extruder are connect with the melt pipe system, the melt pipe
System is connect with the M manifold, and P weaving position is provided in each manifold, one is provided on each position of weaving
A weaving component, each weaving component are connect with a metering pump system, and each metering pump system includes two meters
Amount pump, there are one the annealer component, each annealer components for the spinneret lower section setting of each weaving component
There are one the cross air blasting cooling-part, each cross air blasting cooling-part lower parts to connect a path portion for lower section setting
Part, each there are one the opposite oil tankers for the setting of path component lower part, and there are one described for each opposite oil tanker lower section setting
Godet roller, wherein N is the integer more than 0, and M is the integer more than 0, and P is the integer more than 0；
Several draw-off godets, several described godet rollers in N number of spinning subsystem are arranged in order, every M godet roller
There are one the draw-off godets for setting, wherein M is the integer more than 0；
Feeding machine is arranged in the side of the draw-off godet of the least significant end for several draw-off godets being arranged in order；
Silk cylinder reciprocating apparatus, is arranged at the corresponding position of the feeding machine.
2. spinning-drawing machine as described in claim 1, which is characterized in that the spinning-drawing machine further includes：
Measurement head, is arranged the screw extruder in each spinning subsystem and between the melt pipe system,
Temperature sensor and pressure sensor are provided in the measurement head, the measurement head is internally provided with filter ring, for big
It is filtered in the material of presetting granularity.
3. spinning-drawing machine as described in claim 1, which is characterized in that the spinning-drawing machine further includes：
Monomer suction component is arranged below the spinneret of each filament spinning component in each spinning subsystem, the list
Body pumping part aspirates monomer by high-pressure water jet, and electric boiling plate is provided at the monomer suction component suction inlet.
4. spinning-drawing machine as described in claim 1, which is characterized in that the spinning-drawing machine further includes：
Dragger is arranged in all draw-off godets being arranged in order between the draw-off godet and the feeding machine of end,
The dragger includes that 8 top-bottom cross arrange carry-over pinch rolls.
5. spinning-drawing machine as described in claim 1, which is characterized in that the screw extruder is horizontal screw extruder.
6. spinning-drawing machine as described in claim 1, which is characterized in that the melt pipe system in each spinning subsystem
System includes the pipeline for connecting the M manifold, and static mixer element is arranged in the pipeline, and the pipeline is jacket type knot
Structure.
7. spinning-drawing machine as described in claim 1, which is characterized in that the manifold is double-layer structure, using detachable melt
Ducting module formula combines, and melt pressure measuring point is additionally provided in the manifold, to measure the pressure of filament spinning component in the manifold
Power, the pipeline of each spinning station is equipped with melt freezing valve in the manifold, and heat-insulating material is provided with outside the manifold
Insulation cover as charges.
8. spinning-drawing machine as described in claim 1, which is characterized in that transmission shaft is telescopic, the biography in the metering pump
Moving axis is equipped with universal coupling and safety pin protective device.
9. spinning-drawing machine as described in claim 1, which is characterized in that the spinning-drawing machine further includes：
Silk cylinder is contained, the silk cylinder reciprocating apparatus is placed in the Sheng silk cylinder.
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| CN201721873828.3U CN208038605U (en) | 2017-12-27 | 2017-12-27 | A kind of spinning-drawing machine producing 56 fiber of biomass polyamide |
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| CN201721873828.3U CN208038605U (en) | 2017-12-27 | 2017-12-27 | A kind of spinning-drawing machine producing 56 fiber of biomass polyamide |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107904685A (en) * | 2017-12-27 | 2018-04-13 | 北京中丽制机工程技术有限公司 | A kind of spinning-drawing machine and method for producing 56 fiber of biomass polyamide |
| CN109629021A (en) * | 2019-02-18 | 2019-04-16 | 苏州软石智能装备有限公司 | The path automatic seaming device of spinning machine |
-
2017
- 2017-12-27 CN CN201721873828.3U patent/CN208038605U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107904685A (en) * | 2017-12-27 | 2018-04-13 | 北京中丽制机工程技术有限公司 | A kind of spinning-drawing machine and method for producing 56 fiber of biomass polyamide |
| CN109629021A (en) * | 2019-02-18 | 2019-04-16 | 苏州软石智能装备有限公司 | The path automatic seaming device of spinning machine |
| CN109629021B (en) * | 2019-02-18 | 2023-12-19 | 苏州软石智能装备有限公司 | Automatic channel closing-up device of spinning machine |
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