CN107904683B - It is used to prepare the spinneret and equipment of the parallel composite fiber with wet guiding function - Google Patents

It is used to prepare the spinneret and equipment of the parallel composite fiber with wet guiding function Download PDF

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Publication number
CN107904683B
CN107904683B CN201711102398.XA CN201711102398A CN107904683B CN 107904683 B CN107904683 B CN 107904683B CN 201711102398 A CN201711102398 A CN 201711102398A CN 107904683 B CN107904683 B CN 107904683B
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spinneret
trail
channel
bonding
section
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CN107904683A (en
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沈坤良
张春华
冯爱华
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Nantong Huasheng Polymer Technology Co Ltd
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Nantong Huasheng Polymer Technology Co Ltd
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • D01D5/32Side-by-side structure; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/253Formation of filaments, threads, or the like with a non-circular cross section; Spinnerette packs therefor

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

The invention discloses a kind of spinneret for being used to prepare the parallel composite fiber with wet guiding function and equipment, including spinneret, spinneret includes two extruding cavities, at least one spinneret orifice and two spinneret channels;Spinneret channel connects extruding cavity and spinneret orifice, two spinneret channels collectively form " ┥ ┝ " shape channel cross-section, multiple bonding trails are connected between two spinneret channels, bonding trail two sides are connect with spinneret channel, spinneret channel and bonding trail are accessed in spinneret orifice, spinneret channel and bonding trail collectively form " Lv " shape channel, and spinneret orifice is in " Lv " shape.Utilize multiple bonding trails between two spinneret channels, make the binding part that intersecting is generated in the middle part of fiber filament, the fiber adhesion strength on composite fibre interface is greatly strengthened, peeling is avoided to generate, so that the high polymer for being heat-shrinked difference can be used as the material of parallel composite fiber;It is in " Lv " shape by the fiber filament that spinneret orifice sprays, it is more obvious to the guide functions of liquid, there is good wet guilding.

Description

It is used to prepare the spinneret and equipment of the parallel composite fiber with wet guiding function
Technical field
The invention belongs to field of new material preparation, and in particular to it is a kind of prepare the compound wet fiber spinneret of parallel type and Spinneret equipment.
Background technique
Parallel composite fiber is along fiber longitudinal direction, and two kinds of component polymers are respectively in the composite fibre of fiber two sides.Benefit It is poor that contraction is generated in pre- cold events with two different polymer fibers, so that composite fibre is in volume surface elastic threadiness.
At present in the preparation process of parallel composite fiber, often there is adhesion strength deficiency in interface, and fiber occurs The phenomenon that being removed from interface.
Therefore in parallel composite fiber, it is difficult to the excessive material of difference, which is heat-shrinked, by two kinds bonds, once bonding. One of fiber volume contraction is excessive, due to adhesion strength deficiency, will lead to two kinds of fiber spin-offs.
Summary of the invention
The object of the present invention is to provide a kind of compound wet fiber spinnerets of parallel type, using between two spinneret channels Multiple bonding trails make the binding part for generating intersecting in the middle part of fiber filament, greatly strengthen on composite fibre interface Fiber adhesion strength avoids peeling from generating, so that the high polymer for being heat-shrinked difference can be used as the material of parallel composite fiber Material;It is in " Lv " shape by the fiber filament that spinneret orifice sprays, there is groove and biggish surface area, more to the guide functions of liquid Obviously, there is good wet guilding.
In order to achieve the above-mentioned object of the invention, the invention adopts the following technical scheme:
A kind of spinneret being used to prepare the parallel composite fiber with wet guiding function, including at least one thread spraying structure, The thread spraying structure includes two extruding cavities, a spinneret orifice and two spinneret channels;Spinneret channel connection extruding cavity and Spinneret orifice, two spinneret channels are divided into cross sectional shape in the first spinneret channel and cross sectional shape of " ┥ " shape in " ┝ " The second capable spinneret channel;Multiple bonding trails are connected between first spinneret channel and the middle part in the second spinneret channel, it is described The length direction for bonding trail is consistent with the extrusion spinneret direction in spinneret channel;In the cross-direction, each bonding trail both ends It is respectively communicated with Middle face in the connection in the first, second spinneret channel, parallel up and down, first spinneret between adjacent bonding trail Channel and the second spinneret channel and bonding trail collectively form " Lv " shape channel, and spinneret orifice is in " Lv " shape;" Lv " shape of adhesive section " Lv " shape spinneret orifice is accessed in channel.
Preferably, the spinneret channel includes the diversion section adjacent to each other for two kinds of polymer and is used for two kinds of polymer The adhesive section of bonding, the angle between the diversion section axial line and spinneret orifice axial line are greater than adhesive section axial line and spinneret orifice Angle between axial line, the bonding trail are located in adhesive section.
Preferably, the diversion section, which is equipped with, is filled up completely for hot-melt polymer and carries out mobile lead into bonding trail Trail is flowed, water conservancy diversion trail is located between two spinneret channels, and the area of section in the water conservancy diversion trail is greater than bonding trail section face Product, water conservancy diversion trail side are connected to the side in the ipsilateral spinneret channel in diversion section, and the section in the water conservancy diversion trail is along crowded Direction is staggered between the water conservancy diversion trail on described two spinneret channels gradually to the section transitions in bonding trail out.
Preferably, the side in the water conservancy diversion trail of spinneret channel side is along extrusion direction gradually to other side spinneret channel Extension.
Preferably, water conservancy diversion trail section is round or oval.
Preferably, the section in the spinneret channel is semicircle.
In order to achieve the above-mentioned object of the invention, present invention employs another technical solutions: one kind, which is used to prepare to have, leads wet function The spinneret equipment of the parallel composite fiber of energy, including two feeding-distribution devices and above-mentioned spinneret, spinneret are equipped with multiple spinnerets Mechanism, the feeding-distribution device include the feed inlet being sequentially communicated, filter chamber, dispensing orifice and multiple feeding passages;
Feed inlet enters filter chamber for hot-melt polymer;
Filter chamber was filled with filter sand in the filter chamber for being filtered to hot-melt polymer;
Dispensing orifice flows into each feeding passage for being collected to the polymer in filter chamber and uniformly conveying, Dispensing orifice is located at below filter chamber, and dispensing orifice connects filter chamber and each feeding passage;
Feeding passage, for further conveying to spinneret to hot-melt polymer, the connection of feeding passage output end is squeezed Chamber out.
Preferably, equipped with multiple partitions for changing hot-melt polymer fluid flow direction, the partition in the filter chamber Filter chamber is separated to form multiple flow cavities, the flow cavity includes inner cavity, the chamber that raises up, exhaust port and dirty chamber;It is interior Chamber is located at below feed inlet, and inner cavity connects raise up chamber and feed inlet;Raise up chamber, and moving up for hot-melt polymer makes inside Fluid and bubble are to mobile at exhaust port;Exhaust port, for raising up to highest point and start in the fluid to flow downward Bubble discharge, exhaust port is located at the height highest point that raises up between chamber and dirty chamber;Flow down chamber, is used for flows downward And forming opposite direction with bubble movement makes air entrapment indwelling at exhaust port.
Filter chamber is separated by aforementioned barriers, forms the chamber of different flow directions, so that after fluid first raises up It flows downward, so that the bubble discharge that inside includes, avoids bubble from bringing into spinneret.
Preferably, the partition circumference setting, exhaust port is annular opening.
Preferably, the feed inlet is equipped with T-type aluminum sealing ring.
Preferably, the inlet of the filter chamber is equipped with upper filter plate, and the exit of filter chamber is equipped with lower filter plate, lower mistake Filter plate is located at dispensing orifice upper surface.
Compared with prior art, it is filled using the compound wet fiber spinneret of the parallel type of above-mentioned technical proposal and spinneret It sets, has the following beneficial effects:
One, using the compound wet fiber spinneret of parallel type of the invention, by multiple viscous between two spinneret channels Trail is tied, different filametntary binding parts are bonded, staggered layered laminate bonding is generated in its interface, greatly reinforces Fiber adhesion strength on composite fibre interface, avoids peeling from generating, and the high polymer for being heat-shrinked difference is made Material selection range for the material of parallel composite fiber, parallel composite fiber can be bigger.
Two, spinneret channel and bonding trail come out fiber filament in the middle part of binding part be still layered laminate, after by " Lv " shape spinneret orifice presses the binding part at middle part again, so that further compressing after the binding part pressing on composite fibre, heat It is fusible to became one, improve adhesion strength.
Three, two spinneret channels collectively form " ┥ ┝ " shape channel cross-section, so that is finally come out out of spinneret orifice is compound Fiber is in " Lv " shape structure, has stronger guiding role for liquid fluid, so that liquid is flowed in composite fiber surface It is more faster, assign the composite fibre higher wet guilding.
In the present invention, the section of spinneret orifice is " Lv " shape, can also be " * * " shape, " rice rice " shape etc., is only merely fiber The change of the quantity of silk division.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the compound wet fiber spinneret embodiment 1 of parallel type of the present invention;
Fig. 2 is the partial enlarged view in Fig. 1 at B;
Fig. 3 is the cross-sectional view in Fig. 2 at A1-A1;
Fig. 4 is the cross-sectional view in Fig. 2 at A2-A2;
Fig. 5 is the cross-sectional view in Fig. 2 at A3-A3;
Fig. 6 is the cross-sectional view in Fig. 2 at A4-A4;
Fig. 7 is two kinds of filametntary bonding schematic diagrames when entering spinneret orifice by adhesive section.
Fig. 8 is the cross-sectional view in Fig. 2 at A5-A5.
Fig. 9 is the structural schematic diagram of the compound wet fiber spinning appts embodiment 1 of parallel type of the present invention;
Figure 10 is the structural schematic diagram of flow cavity in the present embodiment 1;
Figure 11 is spinning appts structural schematic diagram in embodiment 2.
Appended drawing reference: 1, extruding cavity;2, spinneret channel;21, diversion section;210, water conservancy diversion trail;22, adhesive section;220, it glues Tie trail;23, spinneret orifice;5, feed inlet;50, T-type aluminum sealing ring;6, filter chamber;60, upper filter plate;61, first partition; 62, second partition;63, lower filter plate;70, dispensing orifice;71, assignment channel;8, spinneret;90, inner cavity;91, raise up chamber;92, Air exit;93, flow down chamber.
Specific embodiment
The present invention is described further with reference to the accompanying drawing.
Embodiment 1:
The compound wet fiber spinning appts of parallel type as shown in Figure 9, including two feeding-distribution devices and spinneret 8, spinneret Plate 8 is equipped with multiple thread spraying structures, and feeding-distribution device includes the feed inlet 5 being sequentially communicated, filter chamber 6, dispensing orifice 70 and multiple points With channel 71;Filter plate 60, lower filter plate 63 are provided at 6 entrance and exit of filter chamber, to disengaging filter chamber material into Row refined filtration.
Hot-melt polymer enters filter chamber 6 by feed inlet 5;Pass through upper 60 refined filtration of filter plate one time when into filter chamber 6;It crosses It was filled with filter sand in filter chamber 6, the impurity in hot-melt polymer can further be screened out;When being flowed out out of filter chamber 6, Again passing by 63 refined filtration of filter plate avoids filtering sand ribbon from going out.
Uniformly in distribution to multiple and different assignment channel 71,71 pairs of hot melts of assignment channel polymerize in material the allocated hole 70 Object is further conveyed to spinneret 8, so that the material that filtering finishes enters in the extruding cavity 1 on spinneret 8.
Multiple first partitions 61 for changing hot-melt polymer fluid flow direction, second partition 62 are equipped in filter chamber 6, the One partition 61, second partition 62 are separated filter chamber 6 to form multiple flow cavities, flow cavity include inner cavity 90, the chamber 91 that raises up, Exhaust port 92 and dirty chamber 93;
As shown in Figure 10, inner cavity 90 is located at 5 lower section of feed inlet, connects raise up chamber 91 and feed inlet 5.Material enters later Raise up chamber 91, makes internal flow and bubble to movement at exhaust port 92;Exhaust port 92 is located at raise up chamber 91 and dirty chamber 93 Between height highest point, the flow direction of fluid becomes flowing downward from flowing up, but the mobile side of internal bubble To remaining unchanged upward, bubble is allowed to be detained or be discharged at exhaust port 92;Flow down chamber 93 in flows downward and with Bubble movement forms opposite direction, flows downward, and bubble is back at exhaust port 92;Bubble is carried out by above structure It excludes, when avoiding subsequent spinneret, generates dead zone in spinneret channel.
First partition 61, the setting of 62 circumference of second partition, exhaust port 92 are annular opening, maximize 92 face of exhaust port Product, so that the bubbles volume of discharge maximizes.
The spinneret for being used to prepare the parallel composite fiber with wet guiding function as shown in Figures 1 to 6, it includes two sprays Silk mechanism, the thread spraying structure include two extruding cavities, 1, spinneret orifice 23 and two spinneret channels 2.The spinneret channel 2 Connect extruding cavity 1 and spinneret orifice 23.
According to direction is squeezed out, is come out from extruding cavity 1 and enter spinneret channel 2, spinneret channel 2 is divided into cross sectional shape and is in The first spinneret channel of " ┥ " shape and cross sectional shape are in the second spinneret channel of " ┝ " row.First spinneret channel and the second spinneret Multiple bonding trails 220, the length direction in above-mentioned bonding trail 220 and squeezing for spinneret channel 2 are connected between the middle part in channel Spinneret direction is consistent out.In the cross-direction, each bonding 220 both ends of trail are respectively communicated with the company in the first, second spinneret channel 2 Connect interior Middle face, it is parallel up and down between adjacent bonding trail 220, it first spinneret channel and the second spinneret channel and bonds small Road 220 collectively forms " Lv " shape channel, and spinneret orifice 23 is in " Lv " shape;" Lv " shape spinneret orifice is accessed in " Lv " the shape channel of adhesive section 22 23。
As shown in fig. 6, bonding trail 220 in adhesive section 22 is located at two spinneret channels, 2 inside, by bonding trail 2 Hot-melt polymer in two spinneret channels 2 is bonded in advance, is had between the parallel composite fiber made relatively strong Adhesion strength, effectively interface is avoided to remove.
As shown in Figures 3 to 5,2 side wall of spinneret channel in diversion section 21 is equipped with water conservancy diversion trail 210, water conservancy diversion trail 210 Side along squeeze out direction gradually to other side spinneret channel 2 extend.Purpose is so that the hot melt in water conservancy diversion trail 210 polymerize Object can slowly flow and be filled up completely water conservancy diversion trail 210, and allow hot-melt polymer gradually to opposite spinneret Channel 2 is close, and 210 section of water conservancy diversion trail is more slowly, to generate when can avoid close dead with the deformation velocity for squeezing out direction Area.
Secondly, 210 section of water conservancy diversion trail is round or oval, the hot melt entered in the water conservancy diversion trail 210 can be made Polymer flow rate maximizes, and can be sufficient filling with water conservancy diversion trail 210 and bonding trail 220, avoid dead zone.
As shown in Figure 4 and Figure 5, it is staggered between the water conservancy diversion trail 210 on two spinneret channels 2, passes through water conservancy diversion trail Hot-melt polymer in 210 pairs of respective spinneret channels 2 is dredged, so that two finally flowed out from spinneret orifice 23 polymer Fiber filament 3 is rendered as the structure in Fig. 7, and the binding part 30 between fiber filament 3 passes through the guidance of water conservancy diversion trail 210 to bonding trail 220 form, and the filametntary binding part 30 of two kinds of polymer is intersecting state, in addition to left and right is the same as the bonding of filament Outside, there are also the face contact between the binding part 30 under laminated arrangement, adhesion strength is greatly improved, interface is avoided to remove.
Since water conservancy diversion trail 210 mainly guides the flow direction of hot-melt polymer, and bond trail 220 and spray Wire hole 23 is to need to bond the binding part 30 in fiber filament, therefore the axis between diversion section 21 and two spinneret channels 2 The angle of heart line is greater than the angle between adhesive section 22 and axial line, since the section in water conservancy diversion trail 210 in diversion section 21 is bigger, Therefore it is bigger to can permit the inclination of diversion section 21;But it is adhered state since the binding part 30 of fiber filament 3 in adhesive section 22 is in, It needs for binding part 30 at two to be slowly pressed against, therefore bonding trail 220 in adhesive section 22 and spinneret channel 2 are slowly to lean on Close, the inclined degree opposite flow section 21 of adhesive section 22 is smaller.
The initial cross-section area in water conservancy diversion trail 210 is greater than bonding 220 area of section of trail, the polymerization in water conservancy diversion trail 210 Logistics speed can be higher, and the polymer of receiving is also just more, so that a large amount of hot-melt polymer is entered by water conservancy diversion trail 210 It bonds in trail 220, guarantees that in bonding trail 220 be not in dead zone, gap is avoided to generate.
Along section conversion of the direction gradually to bonding trail 220 is squeezed out, water conservancy diversion trail 210 is flowed in the section in water conservancy diversion trail 210 The flow velocity for entering to bond the polymer in trail 220 is slowly varying process, and unexpected change in ladder shape is not present, and avoids flow velocity prominent Raw gap or bubble are sold of one's property, dead zone is avoided the formation of.
If Fig. 3 is into Fig. 5, when moving in water conservancy diversion trail 210, the filametntary binding part 30 in side is gradually to other side fibre Silk movement is tieed up, and forms the shape of intersecting in moving process.
When binding part 30 enters bonding trail 220 by water conservancy diversion trail 210, the filametntary binding part 30 in side start with Fiber filament connection in the other side bonds, and still there are certain gaps between binding part 30 adjacent at this time.
Binding part 30 is pressed by spinneret orifice 23 to middle part after as shown in figure 8, completes the bonding of middle part binding part 30.
The section of spinneret orifice is " Lv " shape in this implementation, and the composite fibre finally come out is in " Lv " shape structure, for liquid Body fluid has stronger guiding role, so that liquid is more faster in composite fiber surface flowing, assigns the compound fibre Tie up higher wet guilding.
Embodiment 2:
As shown in figure 9, since the flow cavity in the filter chamber 6 in the spinning appts in embodiment 1 needs to carry out bubble It excludes, therefore its placement angle is very limited, it is necessary to vertical display, therefore spinning appts bottom needs a large amount of space For being collected to composite fibre silk.
Therefore for expansion space, as shown in figure 11, spinneret 8 is turned down 90 degree in the present embodiment, so that spinneret 8 Outlet is towards level, and the location of filter chamber 6 is constant.
Therefore fiber filament comes out direction towards side, can utilize to horizontal space, greatly expands needed for operation Space.
The above is a preferred embodiment of the present invention, does not depart from this hair for those of ordinary skill in the art Under the premise of bright principle, several variations and modifications can also be made, these also should be regarded as protection scope of the present invention.

Claims (9)

1. a kind of spinneret for being used to prepare the parallel composite fiber with wet guiding function, including at least one thread spraying structure, institute Stating thread spraying structure includes two extruding cavities (1), a spinneret orifice (23) and two spinneret channels (2);The spinneret channel (2) is even Connect extruding cavity (1) and spinneret orifice (23), it is characterised in that: two spinneret channels are divided into cross sectional shape in the of " ┥ " shape One spinneret channel and cross sectional shape are in the second spinneret channel of " ┝ " shape;The middle part in the first spinneret channel and the second spinneret channel Between be connected with multiple bonding trails (220), the length direction of bonding trail (220) and the extrusion spray of spinneret channel (2) Silk direction is consistent;In the cross-direction, each bonding trail (220) both ends are respectively communicated with the company in the first, second spinneret channel (2) Connect interior Middle face, parallel up and down between adjacent bonding trail (220), first spinneret channel and the second spinneret channel and bonding Trail (220) collectively forms " Lv " shape channel, and spinneret orifice (23) is in " Lv " shape;" Lv " is accessed in " Lv " the shape channel of adhesive section (22) Shape spinneret orifice (23).
2. the spinneret according to claim 1 for being used to prepare the parallel composite fiber with wet guiding function, feature exist In: the spinneret channel (2) includes the diversion section adjacent to each other for two kinds of polymer (21) and bonds for two kinds of polymer Adhesive section (22), angle between diversion section (21) axial line and spinneret orifice (23) axial line is greater than adhesive section (22) axis Angle between heart line and spinneret orifice (23) axial line, the bonding trail (220) are located in adhesive section (22).
3. the spinneret according to claim 2 for being used to prepare the parallel composite fiber with wet guiding function, feature exist In: equipped with being used for, hot-melt polymer is filled up completely the diversion section (21) and trail (220) are interior to carry out mobile water conservancy diversion to bonding Trail (210), water conservancy diversion trail (210) are located between two spinneret channels (2), and the area of section of the water conservancy diversion trail (210) is big Ipsilateral spinneret channel (2) in bonding trail (220) area of section, water conservancy diversion trail (210) side and diversion section (21) Side connection, the section of the water conservancy diversion trail (210) is along squeezing out direction gradually to the section transitions of bonding trail (220), institute It states and is staggered between the water conservancy diversion trail (210) on two spinneret channels (2).
4. the spinneret according to claim 3 for being used to prepare the parallel composite fiber with wet guiding function, feature exist In: the side in the water conservancy diversion trail (210) of spinneret channel (2) side is along extrusion direction gradually to other side spinneret channel (2) Extension.
5. the spinneret according to claim 3 or 4 for being used to prepare the parallel composite fiber with wet guiding function, feature Be: water conservancy diversion trail (210) section is round or oval.
6. a kind of spinneret equipment for being used to prepare the parallel composite fiber with wet guiding function, it is characterised in that: including two use Enter described in feeding-distribution device and the claim 1-5 any one of spinneret (8) in carrying out sub-material two kinds of hot-melt polymers Spinneret (8), spinneret (8) are equipped with multiple thread spraying structures, and the feeding-distribution device includes the feed inlet (5) being sequentially communicated, mistake Filter chamber (6), dispensing orifice (70) and multiple assignment channels (71);
Feed inlet (5) enters filter chamber (6) for hot-melt polymer;
Filter chamber (6) was filled with filter sand in the filter chamber (6) for being filtered to hot-melt polymer;
Dispensing orifice (70) flows into each assignment channel for being collected to the polymer in filter chamber (6) and uniformly conveying (71) in, dispensing orifice (70) is located at below filter chamber (6), and dispensing orifice (70) connects filter chamber (6) and each assignment channel (71);
Assignment channel (71), for further being conveyed to spinneret (8) to hot-melt polymer, assignment channel (71) output End connection extruding cavity (1).
7. a kind of spinneret equipment for being used to prepare the parallel composite fiber with wet guiding function according to claim 6, It is characterized in that: described equipped with multiple partitions (61,62) for changing hot-melt polymer fluid flow direction in the filter chamber (6) Partition (61,62) is separated filter chamber (6) to form multiple flow cavities, and the flow cavity includes inner cavity (90), raise up chamber (91), exhaust port (92) and dirty chamber (93);
Inner cavity (90) is located at below feed inlet (5), and inner cavity (90) connection raises up chamber (91) and feed inlet (5);
Raise up chamber (91), and moving up for hot-melt polymer makes internal flow and bubble to movement at exhaust port (92);
Exhaust port (92), for raising up to highest point and start the intracorporal bubble of the stream to flow downward and be discharged, exhaust port (92) it is located at the height highest point to raise up between chamber (91) and dirty chamber (93);
It flows down chamber (93), for flows downward and forming opposite direction with bubble movement opens air entrapment indwelling in exhaust At mouth (92).
8. a kind of spinneret equipment for being used to prepare the parallel composite fiber with wet guiding function according to claim 7, Be characterized in that: partition (61,62) the circumference setting, exhaust port (92) are annular opening.
9. a kind of spinneret equipment for being used to prepare the parallel composite fiber with wet guiding function according to claim 7, Be characterized in that: the feed inlet (5) is equipped with T-type aluminum sealing ring (50);The inlet of the filter chamber (6) is equipped with upper filter plate (60), the exit of filter chamber (6) is equipped with lower filter plate (61), and lower filter plate (61) is located at dispensing orifice (70) upper surface.
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