Novel spinneret plate
Technical field
The present invention relates to chemical fiber machinery field, particularly relate to a kind of spinnerets.
Background technology
Spinnerets is as the indispensable precise part of spinning machine, and its function is that the spinning melt that Spinning pumps (i.e. measuring pump) exact dose is crossed is extruded the fibre bundle having certain thickness He be of close texture by the micropore jet on spinnerets.Its shape and characteristic size are the essential condition ensureing fibrous finished product quality.
Summary of the invention
The technical problem that the present invention mainly solves is to provide a kind of Novel spinneret plate.
For solving the problems of the technologies described above, the technical scheme that the present invention adopts is:
A kind of Novel spinneret plate is provided, comprise some spinneret orifices, described spinneret orifice comprises feed zone, flow region, fluffing zone, refinement district and discharge zone from top to bottom successively, described feed zone is wide at the top and narrow at the bottom trapezoidal on longitudinal section, described flow region is isometrical cylinder, described fluffing zone is cydariform, and described refinement district is trapezoidal on longitudinal section, and the length in described refinement district is greater than the total length of described feed zone, described flow region, described fluffing zone.
In a preferred embodiment of the present invention, the cross sectional shape of the discharge zone of described spinneret orifice is circle, cross or abnormity.
In a preferred embodiment of the present invention, the opening diameter of described feed zone is 0.5 ~ 3mm.
In a preferred embodiment of the present invention, the lenth ratio in described feed zone, described flow region, described fluffing zone and described refinement district is: 1:1 ~ 2:0.5 ~ 1:4 ~ 8:1 ~ 2.
The invention has the beneficial effects as follows: Novel spinneret plate of the present invention, comprise some spinneret orifices, described spinneret orifice comprises feed zone, flow region, fluffing zone, refinement district and discharge zone from top to bottom successively, this spinneret pore structure is reasonable in design, design according to fluid mechanics principle, make spinning solution flowing wherein stable, produce the fibre single thread steady quality obtained.
Accompanying drawing explanation
Fig. 1 is the vertical section structure schematic diagram of spinneret orifice in a preferred embodiment of the present invention;
In accompanying drawing, the mark of each parts is as follows: 1, feed zone, and 2, flow region, 3, fluffing zone, 4, refinement district, 5, discharge zone.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present invention is described in detail, can be easier to make advantages and features of the invention be readily appreciated by one skilled in the art, thus more explicit defining is made to protection scope of the present invention.
A kind of Novel spinneret plate, comprise some spinneret orifices, described spinneret orifice comprises feed zone 1, flow region 2, fluffing zone 3, refinement district 4 and discharge zone 5 from top to bottom successively, described feed zone 1 is wide at the top and narrow at the bottom trapezoidal on longitudinal section, described flow region 2 is isometrical cylinder, described fluffing zone 3 is cydariform, and described refinement district 4 is trapezoidal on longitudinal section, and the length in described refinement district 4 is greater than the total length of described feed zone 1, described flow region 2, described fluffing zone 3.
Wherein, the cross sectional shape of the discharge zone 5 of described spinneret orifice can be circle, cross or abnormity, if the cross sectional shape of described discharge zone 5 is non-circular, then still gradually changes from refinement district 4 contact portion; The opening diameter of described feed zone 1 is 0.5 ~ 3mm, and the lenth ratio in described feed zone 1, described flow region 2, described fluffing zone 3 and described refinement district 4 is: 1:1 ~ 2:0.5 ~ 1:4 ~ 8:1 ~ 2.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present invention.