CN203159767U - One-step method fiber-combining spinning box device - Google Patents
One-step method fiber-combining spinning box device Download PDFInfo
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- CN203159767U CN203159767U CN 201320124701 CN201320124701U CN203159767U CN 203159767 U CN203159767 U CN 203159767U CN 201320124701 CN201320124701 CN 201320124701 CN 201320124701 U CN201320124701 U CN 201320124701U CN 203159767 U CN203159767 U CN 203159767U
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Abstract
The utility model discloses a one-step method fiber-combining spinning box device, and belongs to the technical field of chemical fiber machine manufacturing. The types of the spinning box device include two types. In the first type, the spinning box device comprises melt pipes, an air-sealed box body, a heat-medium inlet and a heat-medium outlet, wherein the heat-medium inlet and the heat-medium outlet are formed in the box body, and the number of the melt pipes is at least two. In the second type, the spinning box device comprises melt pipes and air-sealed box bodies, wherein the number of the box bodies is at least two, each box body is provided with a heat-medium inlet, a heat-medium outlet and one melt pipe, and each melt pipe is provided with at least one metering pump. Each metering pump is provided with at least one spinning assembly. Each spinning assembly is provided with at least one melt inlet and a spinning nozzle provided with at least one set of spinneret orifices. According to the one-step method fiber-combining spinning box device, fiber-combined composite filaments made of multiple raw materials can be spun, temperatures of different melts can be independently controlled, and increase of the number of spinning positions is benefited.
Description
Technical field
The utility model relates to chemical fibre equipment manufacturing technology field, is specifically related to one-step method and mixes fine manifold device.
Background technology
The fiber composite of mixing fine bicomponent filament yarn and be by two kinds of different materials, different fiber number, different hole count, different elongation, the contraction of different boiling water, different cross section shape, different orientation degree (preorientation, drawing-off entirely) forms, the fabric that is spun into is after the later process arrangement, because the how different characteristic of two kinds of silks, make fabric have simulate wool, emulation silk and superpower characteristic such as dangle, possess easily simultaneously wash, characteristics such as non-ironing, quick-drying, be clothing with comparatively ideal novel synthesising fibre material in the chemical fibre.
In the prior art, all be to adopt a manifold in the equipment of spinning filament yarn, the melt pipe of manifold has only one, and the one end is communicated with the melt inlet of a plurality of measuring pumps, and each measuring pump is communicated with a plurality of filament spinning components.The spinning that mixes fine bicomponent filament yarn is to spin out different long filament (as: terylene fully drawn long filament, terylene pre-tropism continuous yarn, polyamide fibre fully drafting, polyamide fibre pre-tropism continuous yarn) respectively by different equipment (as: terylene fully drawn filament drawing coiler device, terylene pre-tropism continuous yarn drawing-off coiler device, polyamide fibre fully drafting drawing-off coiler device, polyamide fibre pre-tropism continuous yarn drawing-off coiler device) earlier, select two or more long filaments to make up according to the demand of product then, after doubling is handled, form and mix fine bicomponent filament yarn.Obviously, the mixed fine bicomponent filament yarn of spinning can't be finished in a step like this, needs just can finish through a plurality of steps, and production efficiency is low, the production cost height.
In order a step to finish the spinning that mixes fine bicomponent filament yarn, the applicant has invented a kind of " how different mixed fine bicomponent filament yarn drawing-off coiler device ", and on September 7th, 2011 to this innovation and creation application Chinese utility model patent, this application was authorized by bulletin on May 9th, 2012, and notification number is CN202214509U.It has a full drafting system, preorientation device, doubling parts and a coiler device, it is that the tow that will come out from a manifold is divided into two parts tow, part tow spins out fully drafting by full drafting system, simultaneously, another part tow spins out pre-tropism continuous yarn by the preorientation device, form after the fully drafting that spins out and the man-to-man doubling of pre-tropism continuous yarn process doubling parts and mix fine bicomponent filament yarn, mixed fine bicomponent filament yarn forms spinning cake by the coiling processing of coiler device.The mixed fine bicomponent filament yarn of spinning can be finished in a step like this, and production efficiency improves greatly, and production cost reduces greatly.But, because each spinning station of how different mixed fine bicomponent filament yarn drawing-off coiler device only disposes an original horizontal manifold, this manifold has only a melt pipe, a heating agent entrance and a heating agent outlet, so only be applicable to the mixed fine bicomponent filament yarn of the single raw material of spinning, the kind of mixing fine bicomponent filament yarn is very limited, and can't carry out temperature control respectively to two parts tow in the manifold, also be difficult to two parts tow in the manifold is carried out temperature control respectively even the outlet of a plurality of heating agent entrances and a plurality of heating agent is set respectively on a casing, be difficult to spin out high-quality mixed fine bicomponent filament yarn.Owing to adopt original manifold spinning to mix fine bicomponent filament yarn, the number that its specific lobe spins common long filament reduces half, can't give full play to the production capacity of how different mixed fine bicomponent filament yarn drawing-off coiler device, causes the waste of device resource and the energy again.
For this reason, the applicant improves manifold, manifold after the improvement remains a horizontal manifold, and still have a melt pipe, a heating agent entrance and a heating agent outlet, its difference is, the length of manifold casing has increased nearly one times than originally, correspondingly, measuring pump and filament spinning component in the casing also double respectively.Such improvement can be given full play to the production capacity of how different mixed fine bicomponent filament yarn drawing-off coiler device.But, still there is the mixed fine bicomponent filament yarn that only can spin single raw material, be unfavorable for the exploitation of many kinds; Can't carry out temperature control respectively to the melt in the manifold, be difficult to spin out the problem of high-quality mixed fine bicomponent filament yarn; Simultaneously, because the length of horizontal manifold casing nearly doubles, so when the manifold cross direction profiles of a plurality of spinning station correspondences, the distance of positions of spinning station increases greatly, the number of spinning station is greatly limited, and influences the raising of spinning output.
The utility model content
The technical problems to be solved in the utility model provides one-step method and mixes fine manifold device, it can spin out in a step many raw materials mixed fine bicomponent filament yarn, be conducive to the exploitation of many kinds.
For solving the problems of the technologies described above, the utility model provides one-step method to mix fine manifold device, comprise: the casing of melt pipe, a hermetic seal and the heating agent import and the heating agent that are positioned on the casing export, described melt pipe has two at least, the one end penetrates described casing, and each described melt pipe disposes at least one measuring pump; Each described measuring pump all has a melt inlet and the outlet of a plurality of melt; The melt inlet of described measuring pump is communicated with an end of described melt pipe by the melt arm respectively; Each described measuring pump disposes at least one filament spinning component; Each described filament spinning component all has at least one melt inlet and a spinning head that contains at least one group of spinneret orifice; Each melt inlet of described filament spinning component is communicated with the melt outlet of described measuring pump by the melt distributing pipe respectively; With the described filament spinning component that each described melt pipe is communicated with, it is all identical that the group of the spinneret orifice that it is contained is counted sum; The spinning head of described filament spinning component penetrates described casing.
The technical program is owing to adopted the technological means that at least two melt pipes are set at the casing of a hermetic seal, so one-step method of the present utility model is mixed fine manifold device and can be communicated with a plurality of independently different material supply systems respectively by a plurality of melt pipes.The melt of different material is transported to corresponding melt pipe in the manifold by a plurality of independently different material supply systems respectively, melt in each melt pipe, its raw material is all different, be transported to the measuring pump that is communicated with melt pipe respectively by the melt arm, each measuring pump with the melt sent into by in the filament spinning component that the melt distributing pipe is dispensed into equably with it is communicated with, be dispensed into the spinneret orifice that melt passes through in the spinning head in the filament spinning component and spray multifilament, multifilament of each group spinneret orifice ejection forms a rhizoid bar.This shows have several melt pipes just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.
Described casing is horizontal cuboid; The rear side of the close described box top of described melt pipe is the lateral symmetry distribution with respect to the center of described box top, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is lateral symmetry with respect to described melt pipe and distributes; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is lateral symmetry with respect to described measuring pump and distributes; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrates the bottom surface of casing.
The technical program so it is minimum that interior each the corresponding pipeline length difference of casing is approached, reaches unanimity the melt dispensing of each filament spinning component owing to adopted the technological means of symmetrical structure, makes the strand that spins out more even.
Described melt pipe has two; Each described melt pipe all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; Described heating agent import is positioned at a basifacial side behind the described casing, and described heating agent outlet is positioned at basifacial opposite side behind the described casing.
The technical program is owing to adopted each melt pipe all to be furnished with two described measuring pumps; Each measuring pump all is furnished with 5 or 6 filament spinning components; Each filament spinning component is the technological means of circular down-mounting type dual chamber assembly, so can spin out 20 or different mixed fine bicomponent filament yarn more than 24.
Described casing is the vertical cuboid of putting; Described melt pipe has even number, is equally divided into two row and is lateral symmetry near the longitudinal midline of described box top with respect to the center of described box top and vertically is symmetrically distributed, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described melt pipe; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described measuring pump; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; The filament spinning component that is communicated with the described melt pipe of row is arranged on a side of described casing, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing; Be listed as the opposite side that filament spinning component that described melt pipe is communicated with is arranged on described casing with another, its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing.
The technical program is owing to adopted casing to be the vertical cuboid of putting, each parts is equally divided into two row and vertically distributes, so, can be under the situation that filament spinning component doubles, the casing lateral dimension still can reduce, the distance of positions that is conducive to spinning station reduces, and the figure place that is conducive to spinning station increases, and is conducive to the raising of spinning output.Owing to adopted the technological means of symmetrical structure, so it is minimum that interior each the corresponding pipeline length difference of casing is approached, the melt dispensing of each filament spinning component is reached unanimity again, make the strand that spins out more even.
Described melt pipe has two; Each described melt pipe all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; Described heating agent import is positioned at a basifacial side behind the described casing, and described heating agent outlet is positioned at basifacial opposite side behind the described casing.
The technical program is owing to adopted each melt pipe all to be furnished with two described measuring pumps; Each measuring pump all is furnished with 5 or 6 filament spinning components; Each filament spinning component is the technological means of circular down-mounting type dual chamber assembly, so can spin out 20 or different mixed fine bicomponent filament yarn more than 24.
The technical problem that the utility model further will solve provides one-step method and mixes fine manifold device, it not only can one the step spin out many raw materials mixed fine bicomponent filament yarn, be conducive to the exploitation of many kinds, but also can carry out temperature control respectively to the melt in the manifold, be conducive to spin out high-quality mixed fine bicomponent filament yarn.
For solving the problems of the technologies described above, one-step method of the present utility model is mixed fine manifold device, comprise: the casing of melt pipe, hermetic seal, described casing have two at least, and each described casing all has a heating agent import and a heating agent outlet and a described melt pipe; Described melt pipe one end penetrates described casing; Described melt pipe disposes at least one measuring pump; Each described measuring pump all has a melt inlet and the outlet of a plurality of melt; The melt inlet of described measuring pump is communicated with an end of described melt pipe by the melt arm respectively; Each described measuring pump disposes at least one filament spinning component; Each described filament spinning component all has at least one melt inlet and a spinning head that contains at least one group of spinneret orifice; Each melt inlet of described filament spinning component is communicated with the melt outlet of described measuring pump by described melt distributing pipe respectively; With the filament spinning component that melt pipe in each described casing is communicated with, it is all identical that the group of the spinneret orifice that it is contained is counted sum; The spinning head of described filament spinning component penetrates described casing.
The technical program is owing to adopted the casing of at least two hermetic seals, each casing all has the technological means of a described melt pipe, so one-step method of the present utility model is mixed fine manifold device and can be communicated with a plurality of independently different material supply systems respectively by the melt pipe in a plurality of casings equally.The melt of different material is transported to corresponding melt pipe in the manifold by a plurality of independently different material supply systems respectively, melt in the melt pipe of each casing, its raw material is all different, be transported to the measuring pump that is communicated with melt pipe respectively by the melt arm, each measuring pump with the melt sent into by in the filament spinning component that the melt distributing pipe is dispensed into equably with it is communicated with, the melt that is dispensed in the filament spinning component sprays multifilament by the spinneret orifice in the spinning head, and multifilament of each group spinneret orifice ejection forms a rhizoid bar.This shows have several casings that several melt pipes are just arranged, and then just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.Again owing to adopted each casing all to have the technological means of a heating agent import and a heating agent outlet, each casing respectively with the heating agent system connectivity that can independently control, so, can control the temperature in each casing respectively, and then realize the melt temperature in melt pipe, measuring pump and the filament spinning component of each casing is controlled, be conducive to spin out high-quality mixed fine bicomponent filament yarn.
Described casing is the horizontal cuboid of delegation; For each described casing, described melt pipe is positioned at the middle part of described box top rear side, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is lateral symmetry with respect to described melt pipe and distributes; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is lateral symmetry with respect to described measuring pump and distributes; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrates the bottom surface of casing.
The technical program so it is minimum that interior each the corresponding pipeline length difference of casing is approached, reaches unanimity the melt dispensing of each filament spinning component owing to adopted the technological means of symmetrical structure, makes the strand that spins out more even.
Described casing has two; Melt pipe in each described casing all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; The heating agent import of each described casing is positioned at a basifacial side behind the described casing, and the heating agent outlet of each described casing is positioned at basifacial opposite side behind the described casing.
The technical program is owing to adopted each melt pipe all to be furnished with two described measuring pumps; Each measuring pump all is furnished with 5 or 6 filament spinning components; Each filament spinning component is the technological means of circular down-mounting type dual chamber assembly, so can spin out 20 or different mixed fine bicomponent filament yarn more than 24.
Described casing has even number, is the vertical cuboid of putting, and is equally divided into two row and puts side by side; For each described casing, described melt pipe is positioned at the middle part of described box top inboard, and the one end penetrates described casing from described box top; The measuring pump of described melt pipe configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described melt pipe, and described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described measuring pump; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the outside of described casing inner bottom surface, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing.
The technical program is owing to adopted casing that even number is arranged, be the vertical cuboid of putting, being equally divided into two row puts side by side, each parts in each casing vertically distribute, so, can be under the situation that filament spinning component doubles, the casing lateral dimension still can reduce, the distance of positions that is conducive to spinning station reduces, and the figure place that is conducive to spinning station increases, and is conducive to the raising of spinning output.Owing to adopted the technological means of symmetrical structure, so it is minimum that interior each the corresponding pipeline length difference of casing is approached, the melt dispensing of each filament spinning component is reached unanimity again, make the strand that spins out more even.
Described casing has two; Melt pipe in each described casing all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; The heating agent import of each described casing is positioned at a basifacial side behind the described casing, and the heating agent outlet of each described casing is positioned at basifacial opposite side behind the described casing.
The technical program is owing to adopted each melt pipe all to be furnished with two described measuring pumps; Each measuring pump all is furnished with 5 or 6 filament spinning components; Each filament spinning component is the technological means of circular down-mounting type dual chamber assembly, so can spin out 20 or different mixed fine bicomponent filament yarn more than 24.
Description of drawings
Fig. 1 is the plan structure schematic diagram that one-step method of the present utility model is mixed fine first embodiment of manifold device.
Fig. 2 is A-A line stagewise cutaway view structural representation among Fig. 1.
Fig. 3 is the plan structure schematic diagram that one-step method of the present utility model is mixed second embodiment of fine manifold device.
Fig. 4 is B-B line stagewise cutaway view structural representation among Fig. 3.
Fig. 5 is the plan structure schematic diagram that one-step method of the present utility model is mixed the 3rd embodiment of fine manifold device.
Fig. 6 is C-C line stagewise cutaway view structural representation among Fig. 5.
Fig. 7 is the plan structure schematic diagram that one-step method of the present utility model is mixed the 4th embodiment of fine manifold device.
Fig. 8 is D-D line stagewise cutaway view structural representation among Fig. 7.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is described in further detail.
Embodiment one:
Fig. 1 and Fig. 2 show the one-step method of a horizontal casing 11 and mix fine manifold device.This casing 11 is casings that are cuboid (can be the casing of other shape also, as cylindrical shape) of a hermetic seal.The outside of casing 11 is coated with heat-insulation layer 19.Basifacial left side, casing 11 backs is provided with heating agent outlet 18, basifacial right sides, casing 11 back are provided with heating agent import 17(heating agent import 17 and heating agent outlet 18 can transposition, also can be arranged on other face of casing according to actual conditions), more convenient like this employee's operation.Casing 11 is by heating agent import 17 and heating agent outlet 18 and heating agent system connectivity, and the heating agent system controls the melt temperature in the melt pipe 12 in the casing, measuring pump 14 and the filament spinning component 16.
As can be seen from Figure 1, each melt pipe 12 all disposes two measuring pump 14(and also can dispose one or more measuring pumps).Two measuring pumps 14 of each melt pipe 12 are lateral symmetry with respect to this melt pipe 12 and distribute; Described measuring pump 14 is arranged on the end face in the described casing 11, and the end face of casing 11 is passed on its top; Each described measuring pump 14 all has a melt inlet and 12 melt outlets; Two measuring pumps 14 of each melt pipe 12, its melt inlet are symmetrical connection by an end of melt arm 13 and this melt pipe 12 respectively.
As can be seen from Figure 1, each measuring pump 14 all disposes 6 filament spinning component 16(and also can dispose one or more filament spinning components); Described filament spinning component 16 is circular down-mounting type dual chamber assembly (double end filament spinning component), and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices; Each melt inlet of described filament spinning component 16 is communicated with the melt outlet of described measuring pump 14 by melt distributing pipe 15 respectively.The described filament spinning component 16 that is communicated with each described melt pipe 12 all has 12, and the group of the spinneret orifice that it is contained is counted sum and is 24 groups; The described filament spinning component 16 that is communicated with two described melt pipes 12 has 24, and these 24 filament spinning components 16 are arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrates the bottom surface of casing.
In the present embodiment owing to adopted the technological means that two melt pipes are set at the casing of a hermetic seal, so, one-step method of the present utility model mix fine manifold device can by two melt pipes respectively with two independently the different material supply system be communicated with.The melt of two kinds of different materials can be respectively by two independently the different material supply system be transported to corresponding melt pipe in the manifold.The strand that melt in each melt pipe can spin out a kind of raw material by the measuring pump that is communicated with this melt pipe and filament spinning component.Because each melt pipe is furnished with two measuring pumps, each measuring pump all has 12 melt outlets, and each measuring pump all disposes 6 filament spinning components; Described filament spinning component is circular down-mounting type dual chamber assembly, and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices, and one group of spinneret orifice can spray a captacula bar, comprises multifilament in the captacula bar; With the described filament spinning component that a described melt pipe is communicated with, it is 24 groups that the group of the spinneret orifice that it is contained is counted sum.Therefore, melt in corresponding each melt pipe can spray 24 captacula bars, how different mixed each 24 captacula bar that different melt in two melt pipes is sprayed carry out drawing-off and the processing of doubling one to one respectively by how different mixed fine bicomponent filament yarn drawing-off coiler device, can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.This shows have several melt pipes just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.Because adopted the technological means of symmetrical structure, so, can make the approaching minimum of each corresponding pipeline length difference in the casing, the melt dispensing of each filament spinning component is reached unanimity, make the strand that spins out more even.Obviously, in the present embodiment, export when each measuring pump has 10 melts, and all be furnished with 5 circular down-mounting type dual chamber assemblies (double end filament spinning component), can spin out 20 how different mixed fine bicomponent filament yarns that comprise two kinds of raw materials.Certainly, the measuring pump that each melt pipe disposes, its quantity can not wait yet, the filament spinning component that each measuring pump disposes, its quantity can not wait yet, as: two measuring pumps of a melt pipe configuration, each measuring pump configuration 6 circular down-mounting type dual chamber assembly (double end filament spinning component), 4 measuring pumps of another melt pipe configuration, how different mixed each measuring pump configuration 6 circular down-mounting type list cavity assembly (single unit spinning assembly) so also can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.
Embodiment two:
Fig. 3 and Fig. 4 show a vertical one-step method of putting casing 21 and mix fine manifold device.This casing 21 is casings that are cuboid of a hermetic seal.The outside of casing 21 is coated with heat-insulation layer 29.Basifacial left side, casing 21 backs is provided with heating agent outlet 28, basifacial right sides, casing 21 back are provided with heating agent import 27(heating agent import 27 and heating agent outlet 28 can transposition, also can be arranged on other face of casing according to actual conditions), more convenient like this employee's operation.Casing 21 is by heating agent import 27 and heating agent outlet 28 and heating agent system connectivity, and the heating agent system controls the melt temperature in the melt pipe 22 in the casing, measuring pump 24 and the filament spinning component 26.
As can be seen from Figure 3, each melt pipe 22 all disposes two measuring pump 24(and also can dispose one or more measuring pumps).Two measuring pumps 24 of each melt pipe 22 are vertical symmetrical distribution with respect to this melt pipe 22; Described measuring pump 24 is arranged on the end face in the described casing 21, and the end face of casing 21 is passed on its top; Each described measuring pump 24 all has a melt inlet and 12 melt outlets; Two measuring pumps 24 of each melt pipe 22, its melt inlet are symmetrical connection by an end of melt arm 23 and this melt pipe 22 respectively.
As can be seen from Figure 3, each measuring pump 24 all disposes 6 filament spinning component 26(and also can dispose one or more filament spinning components); Described filament spinning component 26 is circular down-mounting type dual chamber assembly (double end filament spinning component), and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices; Each melt inlet of described filament spinning component 26 is communicated with the melt outlet of described measuring pump 24 by melt distributing pipe 25 respectively.As can be seen from Figure 3, the filament spinning component 26 that is communicated with a described melt pipe 22 on the left side has 12, and these 12 filament spinning components 26 are arranged on the left side of described casing 21, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing 21; The filament spinning component 26 that is communicated with a described melt pipe 22 on the right has 12, and these 12 filament spinning components 26 are arranged on the right side of described casing 21, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing.
In the present embodiment owing to adopted the technological means that two melt pipes are set at the casing of a hermetic seal, so, one-step method of the present utility model mix fine manifold device can by two melt pipes respectively with two independently the different material supply system be communicated with.The melt of two kinds of different materials can be respectively by two independently the different material supply system be transported to corresponding melt pipe in the manifold.The strand that melt in each melt pipe can spin out a kind of raw material by the measuring pump that is communicated with this melt pipe and filament spinning component.Because each melt pipe is furnished with two measuring pumps, each measuring pump all has 12 melt outlets, and each measuring pump all disposes 6 filament spinning components; Described filament spinning component is circular down-mounting type dual chamber assembly, and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices, and one group of spinneret orifice can spray a captacula bar, comprises multifilament in the captacula bar; With the described filament spinning component that a described melt pipe is communicated with, it is 24 groups that the group of the spinneret orifice that it is contained is counted sum.Therefore, melt in corresponding each melt pipe can spray 24 captacula bars, how different mixed each 24 captacula bar that different melt in two melt pipes is sprayed carry out drawing-off and the processing of doubling one to one respectively by how different mixed fine bicomponent filament yarn drawing-off coiler device, can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.This shows have several melt pipes just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.Because adopted the technological means of symmetrical structure, so, can make the approaching minimum of each corresponding pipeline length difference in the casing, the melt dispensing of each filament spinning component is reached unanimity, make the strand that spins out more even.Obviously, in the present embodiment, export when each measuring pump has 10 melts, and all be furnished with 5 circular down-mounting type dual chamber assemblies, can spin out 20 how different mixed fine bicomponent filament yarns that comprise two kinds of raw materials.Certainly, the measuring pump that each melt pipe disposes, its quantity can not wait yet, the filament spinning component that each measuring pump disposes, its quantity can not wait yet, as: two measuring pumps of a melt pipe configuration, each measuring pump configuration 6 circular down-mounting type dual chamber assembly (double end filament spinning component), 4 measuring pumps of another melt pipe configuration, how different mixed each measuring pump configuration 6 circular down-mounting type list cavity assembly (single unit spinning assembly) so also can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.In the present embodiment, owing to adopted casing to be the vertical cuboid of putting, each parts (melt pipe, measuring pump, filament spinning component) are equally divided into two row and vertically distribute, so, can be under the situation that filament spinning component doubles, the casing lateral dimension still can reduce, and the distance of positions that is conducive to spinning station reduces, the figure place that is conducive to spinning station increases, and is conducive to the raising of spinning output.Because filament spinning component vertically is distributed in the both sides of casing, so, be convenient to employee's spinning operation.
Embodiment three:
Fig. 5 and Fig. 6 show the one-step method of two horizontal casings 31 and mix fine manifold device.These two casings 31 are cuboid for the casing of hermetic seal, and (also can be the casing that is in line more than three and three) be in line.The outside of two casings 31 is coated with heat-insulation layer 39, and is connected as a single entity by heat-insulation layer 39.Each basifacial left side, casing 31 backs is provided with heating agent outlet 38, basifacial right sides, each casing 31 backs are provided with heating agent import 37(heating agent import 37 and heating agent outlet 38 can transposition, also can be arranged on other face of casing according to actual conditions), more convenient like this employee's operation.Each casing 31 by heating agent import 37 and heating agent outlet 38 respectively with heating agent system connectivity independently, each independently the heating agent system all the melt temperature in the melt pipe 32 in the casing, measuring pump 34 and the filament spinning component 36 is carried out independent control.
Each casing 31 all has a melt pipe 32, and this melt pipe 32 is positioned at the middle part (referring to Fig. 5) of described casing 31 end face rear sides, and the one end penetrates this casing 31 from described casing 31 end faces; Like this, be conducive to dispose measuring pump 34 and filament spinning component 36.In each casing 31 other end of melt pipe 32 respectively with one independently the different material supply system be communicated with.The melt of two kinds of different materials can be transported to corresponding melt pipe 32 in the manifold by these two independently raw material supply systems respectively, and the melt in the melt pipe 32 of each casing 31 has nothing in common with each other.
As can be seen from Figure 5, the melt pipe 32 in each casing 31 all disposes two measuring pump 34(and also can dispose one or more measuring pumps).Two measuring pumps 34 of each melt pipe 32 are lateral symmetry with respect to this melt pipe 32 and distribute; Described measuring pump 34 is arranged on the end face in the described casing 31, and the end face of casing 31 is passed on its top; Each described measuring pump 34 all has a melt inlet and 12 melt outlets; Two measuring pumps 34 of each melt pipe 32, its melt inlet are symmetrical connection by an end of melt arm 33 and this melt pipe 32 respectively.
As can be seen from Figure 5, each measuring pump 34 all disposes 6 filament spinning component 36(and also can dispose one or more filament spinning components); Described filament spinning component 36 is circular down-mounting type dual chamber assembly (double end filament spinning component), and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices; Each melt inlet of described filament spinning component 36 is respectively by the melt outlet symmetrical connection of melt distributing pipe 35 with described measuring pump 34.The described filament spinning component 36 that is communicated with melt pipe 32 described in each casing 31 all has 12, and the group of the spinneret orifice that it is contained is counted sum and is 24 groups; These 12 filament spinning components 36 are arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrate the bottom surface of casing.
In the present embodiment, owing to adopted the casing of two hermetic seals, each casing all has the technological means of a described melt pipe, so, one-step method of the present utility model mix fine manifold device can by the melt pipe in each casing respectively with one independently the different material supply system be communicated with.The melt of two kinds of different materials can be respectively by two independently the different material supply system be transported to corresponding melt pipe in the manifold.The strand that melt in the melt pipe of each casing can spin out a kind of raw material by the measuring pump that is communicated with this melt pipe and filament spinning component.Because each melt pipe is furnished with two measuring pumps, each measuring pump all has 12 melt outlets, and each measuring pump all disposes 6 filament spinning components; Described filament spinning component is circular down-mounting type dual chamber assembly, and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices, and one group of spinneret orifice can spray a captacula bar, comprises multifilament in the captacula bar; With the described filament spinning component that a described melt pipe is communicated with, it is 24 groups that the group of the spinneret orifice that it is contained is counted sum.Therefore, melt in the melt pipe of corresponding each casing can spray 24 captacula bars, how different mixed each 24 captacula bar that different melt in two melt pipes is sprayed carry out drawing-off and the processing of doubling one to one respectively by how different mixed fine bicomponent filament yarn drawing-off coiler device, can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.This shows have several melt pipes just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.Again owing to adopted each casing all to have the technological means of a heating agent import and a heating agent outlet, each casing respectively with the heating agent system connectivity that can independently control, so, one-step method of the present utility model is mixed fine manifold device and can be controlled the temperature in each casing respectively, and then realize the melt temperature in melt pipe, measuring pump and the filament spinning component of each casing is controlled, be conducive to spin out high-quality mixed fine bicomponent filament yarn.Because adopted the technological means of symmetrical structure, so, can make the approaching minimum of each corresponding pipeline length difference in the casing, the melt dispensing of each filament spinning component is reached unanimity, make the strand that spins out more even.Obviously, in the present embodiment, export when each measuring pump has 10 melts, and all be furnished with 5 circular down-mounting type dual chamber assemblies, can spin out 20 how different mixed fine bicomponent filament yarns that comprise two kinds of raw materials.Certainly, the measuring pump that melt pipe in each casing disposes, its quantity can not wait yet, the filament spinning component that each measuring pump disposes, its quantity can not wait yet, as: two measuring pumps of melt pipe configuration in casing, each measuring pump configuration 6 circular down-mounting type dual chamber assembly (double end filament spinning component), 4 measuring pumps of melt pipe configuration in another casing, how different mixed each measuring pump configuration 6 circular down-mounting type list cavity assembly (single unit spinning assembly) so also can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.
Embodiment four:
Fig. 7 and Fig. 8 show two vertical one-step method of putting casing 41 and mix fine manifold device.These two casings 41 are put (described casing also can have even number, is the vertical cuboid of putting, and is equally divided into two row and puts side by side) side by side.The outside of casing 41 is coated with heat-insulation layer 49, and is connected as a single entity by heat-insulation layer 49.Each basifacial left side, casing 41 backs is provided with heating agent outlet 48, basifacial right sides, casing 41 back are provided with heating agent import 47(heating agent import 47 and heating agent outlet 48 can transposition, also can be arranged on other face of casing according to actual conditions), more convenient like this employee's operation.Each casing 41 by heating agent import 47 and heating agent outlet 48 respectively with heating agent system connectivity independently, each independently the heating agent system all the melt temperature in the melt pipe 42 in the casing, measuring pump 44 and the filament spinning component 46 is carried out independent control.
Each casing 41 all has a melt pipe 42, and this melt pipe 42 is positioned at the middle part (referring to Fig. 7) of described casing 41 inside top surface, and the one end penetrates this casing 41 from described casing 41 end faces; Like this, be conducive to dispose measuring pump 44 and filament spinning component 46.In each casing 41 other end of melt pipe 42 respectively with one independently the different material supply system be communicated with.The melt of two kinds of different materials can be transported to corresponding melt pipe 42 in the manifold by these two independently raw material supply systems respectively, and the melt in the melt pipe 42 of each casing 41 has nothing in common with each other.
As can be seen from Figure 7, the melt pipe 42 in each casing 41 all disposes two measuring pump 44(and also can dispose one or more measuring pumps).Two measuring pumps 44 of each melt pipe 42 are vertical symmetrical distribution with respect to this melt pipe 42; Described measuring pump 44 is arranged on the end face in the described casing 41, and the end face of casing 41 is passed on its top; Each described measuring pump 44 all has a melt inlet and 12 melt outlets; Two measuring pumps 44 of each melt pipe 42, its melt inlet are symmetrical connection by an end of melt arm 43 and this melt pipe 42 respectively.
As can be seen from Figure 7, each measuring pump 44 all disposes 6 filament spinning component 46(and also can dispose one or more filament spinning components); Described filament spinning component 46 is circular down-mounting type dual chamber assembly (double end filament spinning component), and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices; Each melt inlet of described filament spinning component 46 is communicated with the melt outlet of described measuring pump 44 by melt distributing pipe 45 respectively.The described filament spinning component 26 that is communicated with melt pipe 42 described in each casing 41 all has 12, and the group of the spinneret orifice that it is contained is counted sum and is 24 groups; These 12 filament spinning components 46 are arranged on the outside (referring to Fig. 7) of casing inner bottom surface, and its spinning head vertically is distributed on same the straight line equably, and penetrate the bottom surface of casing.
In the present embodiment, owing to adopted the casing of two hermetic seals, each casing all has the technological means of a described melt pipe, so, one-step method of the present utility model mix fine manifold device can by the melt pipe in each casing respectively with one independently the different material supply system be communicated with.The melt of two kinds of different materials can be respectively by two independently the different material supply system be transported to corresponding melt pipe in the manifold.The strand that melt in the melt pipe of each casing can spin out a kind of raw material by the measuring pump that is communicated with this melt pipe and filament spinning component.Because each melt pipe is furnished with two measuring pumps, each measuring pump all has 12 melt outlets, and each measuring pump all disposes 6 filament spinning components; Described filament spinning component is circular down-mounting type dual chamber assembly, and this circle down-mounting type dual chamber assembly has 2 melt inlets and a spinning head that contains 2 groups of spinneret orifices, and one group of spinneret orifice can spray a captacula bar, comprises multifilament in the captacula bar; With the described filament spinning component that a described melt pipe is communicated with, it is 24 groups that the group of the spinneret orifice that it is contained is counted sum.Therefore, melt in the melt pipe of corresponding each casing can spray 24 captacula bars, how different mixed each 24 captacula bar that different melt in two melt pipes is sprayed carry out drawing-off and the processing of doubling one to one respectively by how different mixed fine bicomponent filament yarn drawing-off coiler device, can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.This shows have several melt pipes just can spin out the strand of several different materials.And the strand of single raw material just can spin out the mixed fine bicomponent filament yarn of multiple various combination in the prior art by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions.Can predict, the strand of plurality of raw materials just can make up by the processing of how different mixed fine bicomponent filament yarn drawing-off coiler device under different technology conditions with doubling and spin out more how different mixed fine bicomponent filament yarn, has increased the potentiality of many variety developments greatly.Again owing to adopted each casing all to have the technological means of a heating agent import and a heating agent outlet, each casing respectively with the heating agent system connectivity that can independently control, so, one-step method of the present utility model is mixed fine manifold device and can be controlled the temperature in each casing respectively, and then realize the melt temperature in melt pipe, measuring pump and the filament spinning component of each casing is controlled, be conducive to spin out high-quality mixed fine bicomponent filament yarn.Because adopted the technological means of symmetrical structure, so, can make the approaching minimum of each corresponding pipeline length difference in the casing, the melt dispensing of each filament spinning component is reached unanimity, make the strand that spins out more even.Obviously, in the present embodiment, export when each measuring pump has 10 melts, and all be furnished with 5 circular down-mounting type dual chamber assemblies, can spin out 20 how different mixed fine bicomponent filament yarns that comprise two kinds of raw materials.Certainly, the measuring pump that melt pipe in each casing disposes, its quantity can not wait yet, the filament spinning component that each measuring pump disposes, its quantity can not wait yet, as: two measuring pumps of melt pipe configuration in casing, each measuring pump configuration 6 circular down-mounting type dual chamber assembly (double end filament spinning component), 4 measuring pumps of melt pipe configuration in another casing, how different mixed each measuring pump configuration 6 circular down-mounting type list cavity assembly (single unit spinning assembly) so also can spin out 24 fine bicomponent filament yarns that comprise two kinds of raw materials.In the present embodiment, because the means that adopted two vertical casings of putting to be set up in parallel, parts in each casing (melt pipe, measuring pump, filament spinning component) are vertical distribution respectively, so, can be under the situation that filament spinning component doubles, the casing lateral dimension still can reduce, and the distance of positions that is conducive to spinning station reduces, the figure place that is conducive to spinning station increases, and is conducive to the raising of spinning output.Because filament spinning component vertically is distributed in the outside of casing, so, be convenient to employee's spinning operation.
The above only is preferred embodiment of the present utility model, and in order to limit the utility model, the common variation that those skilled in the art carries out in the technical solutions of the utility model scope and replacement all should not be included in the protection domain of the present utility model.
Claims (10)
1. one-step method is mixed fine manifold device, comprise: the casing of melt pipe, a hermetic seal and the heating agent import and the heating agent that are positioned on the casing export, it is characterized in that: described melt pipe has two at least, and the one end penetrates described casing, and each described melt pipe disposes at least one measuring pump; Each described measuring pump all has a melt inlet and the outlet of a plurality of melt; The melt inlet of described measuring pump is communicated with an end of described melt pipe by the melt arm respectively; Each described measuring pump disposes at least one filament spinning component; Each described filament spinning component all has at least one melt inlet and a spinning head that contains at least one group of spinneret orifice; Each melt inlet of described filament spinning component is communicated with the melt outlet of described measuring pump by the melt distributing pipe respectively; With the described filament spinning component that each described melt pipe is communicated with, it is all identical that the group of the spinneret orifice that it is contained is counted sum; The spinning head of described filament spinning component penetrates described casing.
2. one-step method according to claim 1 is mixed fine manifold device, and it is characterized in that: described casing is horizontal cuboid; The rear side of the close described box top of described melt pipe is the lateral symmetry distribution with respect to the center of described box top, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is lateral symmetry with respect to described melt pipe and distributes; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is lateral symmetry with respect to this measuring pump and distributes; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrates the bottom surface of casing.
3. one-step method according to claim 2 is mixed fine manifold device, and it is characterized in that: described melt pipe has two; Each described melt pipe all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; Described heating agent import is positioned at a basifacial side behind the described casing, and described heating agent outlet is positioned at basifacial opposite side behind the described casing.
4. one-step method according to claim 1 is mixed fine manifold device, it is characterized in that: described casing is the vertical cuboid of putting; Described melt pipe has even number, is equally divided into two row and is lateral symmetry near the longitudinal midline of described box top with respect to the center of described box top and vertically is symmetrically distributed, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described melt pipe; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described measuring pump; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; The filament spinning component that is communicated with the described melt pipe of row is arranged on a side of described casing, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing; Be listed as the opposite side that filament spinning component that described melt pipe is communicated with is arranged on described casing with another, its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing.
5. one-step method according to claim 4 is mixed fine manifold device, and it is characterized in that: described melt pipe has two; Each described melt pipe all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; Described heating agent import is positioned at a basifacial side behind the described casing, and described heating agent outlet is positioned at basifacial opposite side behind the described casing.
6. one-step method is mixed fine manifold device, and comprising: the casing of melt pipe, hermetic seal is characterized in that: described casing has two at least, and each described casing all has a heating agent import and a heating agent outlet and a described melt pipe; Described melt pipe one end penetrates described casing; Described melt pipe disposes at least one measuring pump; Each described measuring pump all has a melt inlet and the outlet of a plurality of melt; The melt inlet of described measuring pump is communicated with an end of described melt pipe by the melt arm respectively; Each described measuring pump disposes at least one filament spinning component; Each described filament spinning component all has at least one melt inlet and a spinning head that contains at least one group of spinneret orifice; Each melt inlet of described filament spinning component is communicated with the melt outlet of described measuring pump by the melt distributing pipe respectively; With the filament spinning component that melt pipe in each described casing is communicated with, it is all identical that the group of the spinneret orifice that it is contained is counted sum; The spinning head of described filament spinning component penetrates described casing.
7. one-step method according to claim 6 is mixed fine manifold device, and it is characterized in that: described casing is the horizontal cuboid of delegation; For each described casing, described melt pipe is positioned at the middle part of described box top rear side, and the one end penetrates described casing from described box top; The measuring pump of described each melt pipe configuration, its quantity is all identical, is lateral symmetry with respect to described melt pipe and distributes; Described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is lateral symmetry with respect to described measuring pump and distributes; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the front side of casing inner bottom surface, and its spinning head laterally is distributed on same the straight line equably, and penetrates the bottom surface of casing.
8. one-step method according to claim 7 is mixed fine manifold device, and it is characterized in that: described casing has two; Melt pipe in each described casing all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; The heating agent import of each described casing is positioned at a basifacial side behind the described casing, and the heating agent outlet of each described casing is positioned at basifacial opposite side behind the described casing.
9. one-step method according to claim 6 is mixed fine manifold device, and it is characterized in that: described casing has even number, is the vertical cuboid of putting, and is equally divided into two row and puts side by side; For each described casing, described melt pipe is positioned at the middle part of described box top inboard, and the one end penetrates described casing from described box top; The measuring pump of described melt pipe configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described melt pipe, and described measuring pump is arranged on the end face in the described casing, and the end face of casing is passed on its top; One end of the melt inlet of described measuring pump and described melt pipe is symmetrical connection; The filament spinning component of described each measuring pump configuration, its quantity is all identical, is vertical symmetrical distribution with respect to described measuring pump; The melt inlet of described filament spinning component and the outlet of the melt of described measuring pump are symmetrical connection; Described filament spinning component is arranged on the outside of described casing inner bottom surface, and its spinning head vertically is distributed on same the straight line equably, and penetrates the bottom surface of casing.
10. one-step method according to claim 9 is mixed fine manifold device, and it is characterized in that: described casing has two; Melt pipe in each described casing all is furnished with two described measuring pumps; Each described measuring pump all has 10 or 12 melt outlets; Correspondingly, each described measuring pump all is furnished with 5 or 6 described filament spinning components; Each described filament spinning component is circular down-mounting type dual chamber assembly, and two melt inlets and a spinning head that contains two groups of spinneret orifices are all arranged; The heating agent import of each described casing is positioned at a basifacial side behind the described casing, and the heating agent outlet of each described casing is positioned at basifacial opposite side behind the described casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320124701 CN203159767U (en) | 2013-03-19 | 2013-03-19 | One-step method fiber-combining spinning box device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201320124701 CN203159767U (en) | 2013-03-19 | 2013-03-19 | One-step method fiber-combining spinning box device |
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| CN203159767U true CN203159767U (en) | 2013-08-28 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103741227A (en) * | 2013-12-29 | 2014-04-23 | 大连华阳化纤科技有限公司 | Adjustable breadth spinning manifold |
| CN104195651A (en) * | 2014-05-06 | 2014-12-10 | 北京德厚朴化工技术股份有限公司 | Double-temperature spinning box for producing blend fibers in industrialization one-step method |
| CN105088363A (en) * | 2015-08-26 | 2015-11-25 | 北京中丽制机工程技术有限公司 | Spinning box structure |
| CN105200544A (en) * | 2015-09-16 | 2015-12-30 | 北京中丽制机工程技术有限公司 | Spinning device |
| CN105714387A (en) * | 2016-03-24 | 2016-06-29 | 北京中丽制机工程技术有限公司 | Spinning pack |
| CN106381528A (en) * | 2016-11-30 | 2017-02-08 | 南京瘦懒猴信息科技有限公司 | Long spinning box |
| CN106757409A (en) * | 2015-11-19 | 2017-05-31 | 张家港市宏盛贸易有限公司 | Manifold |
| CN106757411A (en) * | 2015-11-19 | 2017-05-31 | 张家港市宏盛贸易有限公司 | Manifold |
| CN108950705A (en) * | 2018-09-14 | 2018-12-07 | 安徽丰原生物材料股份有限公司 | A kind of polylactic acid manifold |
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2013
- 2013-03-19 CN CN 201320124701 patent/CN203159767U/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103741227A (en) * | 2013-12-29 | 2014-04-23 | 大连华阳化纤科技有限公司 | Adjustable breadth spinning manifold |
| CN104195651A (en) * | 2014-05-06 | 2014-12-10 | 北京德厚朴化工技术股份有限公司 | Double-temperature spinning box for producing blend fibers in industrialization one-step method |
| CN105088363A (en) * | 2015-08-26 | 2015-11-25 | 北京中丽制机工程技术有限公司 | Spinning box structure |
| CN105088363B (en) * | 2015-08-26 | 2017-08-01 | 北京中丽制机工程技术有限公司 | A kind of spinning box structure |
| CN105200544A (en) * | 2015-09-16 | 2015-12-30 | 北京中丽制机工程技术有限公司 | Spinning device |
| CN105200544B (en) * | 2015-09-16 | 2018-03-27 | 北京中丽制机工程技术有限公司 | Device for spinning |
| CN106757409A (en) * | 2015-11-19 | 2017-05-31 | 张家港市宏盛贸易有限公司 | Manifold |
| CN106757411A (en) * | 2015-11-19 | 2017-05-31 | 张家港市宏盛贸易有限公司 | Manifold |
| CN105714387A (en) * | 2016-03-24 | 2016-06-29 | 北京中丽制机工程技术有限公司 | Spinning pack |
| CN105714387B (en) * | 2016-03-24 | 2019-08-02 | 北京中丽制机工程技术有限公司 | A kind of filament spinning component |
| CN106381528A (en) * | 2016-11-30 | 2017-02-08 | 南京瘦懒猴信息科技有限公司 | Long spinning box |
| CN108950705A (en) * | 2018-09-14 | 2018-12-07 | 安徽丰原生物材料股份有限公司 | A kind of polylactic acid manifold |
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