US2012231273A1PendingUtilityA1
Raw yarn for air bag and method for producing the raw yarn
Est. expiryMar 10, 2028(~1.7 yrs left)· nominal 20-yr term from priority
D10B 2505/124D10B 2331/02D02G 3/446Y10T428/2976Y10T428/298
44
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Claims
Abstract
A yarn for air bags including polyamide multifilament with a total fineness of 200 to 700 dtex, a single fiber fineness of 1 to 2 dtex, strength of 7 to 10 cN/dtex, and elongation of 20 to 30%.
Claims
exact text as granted — not AI-modified1 . A yarn for air bags comprising polyamide multifilament with a total fineness of 200 to 700 dtex, a single fiber fineness of 1 to 2 dtex, strength of 7 to 10 cN/dtex, and elongation of 20 to 30%.
2 . The yarn as claimed in claim 1 , wherein the polyamide is polyhexamethylene adipamide with a sulfuric acid relative viscosity of 3 to 4.
3 . The yarn as claimed in claim 1 , wherein fineness unevenness is 0.5 to 1.5%.
4 . A method for producing the yarn as claimed in claim 1 , wherein polyamide is melt-spun, cooled with circular cooling equipment, and then stretched.
5 . The method as claimed in claim 4 , wherein fiber extruded from a spinning orifice after being melt-spun is supplied with steam and then passed through a slow cooling cylinder.
6 . The method as claimed in claim 5 , wherein the slow cooling cylinder has a length of 30 to 150 mm and the circular cooling equipment has a cooling air blowout length of 600 to 1,200 mm.
7 . The method of claim 4 , wherein the difference between internal pressure in the cooling cylinder of the circular cooling equipment and atmospheric pressure is 500 to 1200 Pa.
8 . The method of claim 4 , wherein air speed cooling air is nonuniform along a length direction of the circular cooling equipment, upper side air speed V U being smaller than lower side air speed V L , and values of V L/ V U , V U , and V L being 2 to 3, 10 to 30 m/min, and 40 to 80 m/min, respectively.
9 . The method of claim 5 , wherein steam blowout pressure is 100 to 600 Pa.Cited by (0)
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