Fiber structure and method for producing same
A manufacturing method and structure technology, applied in the field of fiber structures, can solve the problems of increased pressure loss, reduced collection efficiency, and high dust collection ability, and achieve the effect of suppressing fluff and excellent handling
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Embodiment 1
[0252] (1) Production of ultrafine fiber layer
[0253] For 100 parts by mass of polypropylene (MFR [230°C, 21.18N load] = 700g / 10min), the spinning temperature is 215°C, the air temperature is 215°C, and the air flow rate is 10Nm using a common melt blown equipment. 3 / min, single hole ejection amount 0.036g / hole·min, capture distance 11cm, hole diameter 0.3mm, hole interval 0.75mm to carry out melt-blown spinning, obtained ultrafine fiber sheet (number average fiber diameter of single fiber 1.2μm , unit area weight 10.0g / m 2 , thickness 0.10mm, apparent density 0.10g / cm 3 ).
[0254] (2) Production of non-fine fiber layer
[0255] For 100 parts by mass of polypropylene (MFR [230°C, 21.18N load] = 30g / 10min), the spinning temperature is 260°C, the air temperature is 260°C, and the air flow rate is 13Nm using a common melt blown equipment. 3 / min, single-hole ejection amount 0.3g / hole·min, hole diameter 0.4mm, hole interval 1.5mm, sprays from the nozzle hole, and collects ...
Embodiment 2
[0264] For the ultrafine fiber sheet obtained in Example 1 (1) and the non-ultrafine fiber sheet obtained in Example 1 (2), the ultrafine fiber sheet was superimposed on one of the non-extrafine fiber sheets having convex portions. side, placed on the porous support used in Example 1, and continuously transported along the length direction of the laminate at a speed of 5.0 m / min, and at the same time, using Two nozzles with a hole diameter of 0.10mm (the distance between adjacent nozzles is 20.0cm), the water pressure of the high-pressure water jetted from the nozzles in the first row is set to 3.0MPa, and the water jetted from the nozzles in the second row The water pressure of the high-pressure water flow was set to 5.0 MPa, and the high-pressure water flow was sprayed from the non-ultrafine fiber layer side to carry out the coagulation treatment. Next, charging treatment was performed in the same manner as in Example 1 to obtain a fiber structure in which ultrafine fibers a...
Embodiment 3
[0266] For the ultrafine fiber sheet obtained in Example 1 (1) and the non-ultrafine fiber sheet obtained in Example 1 (2), the ultrafine fiber sheet was superimposed on one of the non-extrafine fiber sheets having convex portions. side, placed on the porous support used in Example 1, and transported continuously along the length direction of the laminate at a speed of 5.0 m / min, and at the same time, using Three nozzles with a hole diameter of 0.10mm (the distance between adjacent nozzles is 20.0cm), the water pressure of the high-pressure water jetted from the nozzles in the first row is set to 3.0MPa, and the water jetted from the nozzles in the second row The water pressure of the high-pressure water stream was set at 5.0 MPa, and the water pressure of the high-pressure water stream sprayed from the third row of nozzles was set at 7.0 MPa, and the high-pressure water stream was sprayed from the non-microfiber layer side to carry out the coagulation treatment. Next, chargin...
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