High stretch soft cotton and manufacturing method thereof
A technology of soft cotton and high elasticity, applied in textiles, papermaking, non-woven fabrics, etc., can solve problems such as poor elasticity, high price, and not washable
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Embodiment 1
[0014] Production 260g / m 2 Specification high elastic soft cotton. The ratio of raw materials is: 10% of polyester fiber with specification of 1.5De′×51mm; 20% of polyester fiber with specification of 1.8De′×64mm; 20% of polyester staple fiber with specification of 2.5De′×64mm; 27% of hollow fiber with specification of 3.33De′×64mm; 4De'×51mm specification low melting point fiber 13%. After the fibers are mixed, they are loosened and sent to the cotton box. After carding and laying, the upper and lower sides are sprayed with vinyl acetate copolymer emulsion accounting for 10% of the total, and sent to the dryer for drying. The temperature of the dryer is controlled at 150°C-175°C. Between, depending on the speed and temperature adjustment, the melting of low-melting-point fibers in the product and the drying of surface-adhesive latex shall prevail. The dried product is naturally cooled, then compressed and packaged.
Embodiment 2
[0016] Production 180g / m 2 Specification high elastic soft cotton. Raw material ratio: 1.5De′×51mm specification polyester fiber 15%; 1.8De′×64mm specification polyester fiber 20%; 2.5De′×64mm specification polyester fiber 17%; 3.33 De′×64mm specification hollow fiber 25%; 4De '×51mm specification low melting point fiber 14%. Spray vinyl acetate copolymer emulsion accounting for 9% of the total. The temperature of the dryer is controlled between 140-170°C. Its production process flow is identical with embodiment 1.
Embodiment 3
[0018] Production 80g / m 2 Specification high elastic soft cotton. Raw material ratio: 1.5De′×51mm polyester fiber 20%; 1.8De′×64mm polyester fiber 22%; 2.5De′×64mm polyester fiber 10%; 3.33De′×64mm hollow fiber 23%; 2De '×51mm specification low melting point fiber 17%. Spray the vinyl acetate copolymerization solution accounting for 8% of the total amount, and control the temperature of the dryer between 130-165°C. Its production process flow is identical with embodiment 1.
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Abstract
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