Process for the welding of two polyamide parts

Abstract

A process for the welding of two polyamide parts, both made of a polyamide composition comprising a polyamide and optionally additives, the polyamide of one part (part L) having a lower softening temperature than the polyamide of the other part (part H) and wherein the polyamide composition of part L comprises one or more viscosity increasing additives increasing the melt shear viscosity of the polyamide composition at least by 30% compared to melt shear viscosity of the polyamide (measured according to ISO 11443 (A1) standard at a shear rate of 100 s −1 in a capillary rheometer with l/d=30 mm/1 mm). A good weld strength is obtained and parts with different properties can be combined. Polyamide welded objects such as corrugated tubes, bellows, containers, fuel inlet systems, air inlet manifolds and airducts, may be obtained.

1 . Process for the manufacture of polyamide welded object comprising welding by laser welding, vibration welding or hot plate welding two polyamide parts made of a polyamide composition comprising a polyamide and optionally additives, the polyamide of one part (part L) having a lower softening temperature than the polyamide of the other part (part H), wherein the polyamide composition of part L comprises a high molecular weight polyamide and/or viscosity increasing additives and the polyamide composition of part L has a melt shear viscosity of at least 200 Pa.s at 100 s −1 . 
     
     
         2 . Process according to  claim 1 , wherein the polyamide composition of part L has a melt shear viscosity of at least 300 Pa.s at 100 s −1 . 
     
     
         3 . Process according to  claim 1 , wherein the polyamide composition in part L comprises polyamide having a relative solution viscosity between 2.0 and 4 and viscosity increasing additives, the relative solution viscosity being determined from a solution of 1 gram/100 ml in 90% formic acid at 25° C. 
     
     
         4 . Process according to  claim 3 , wherein the polyamide composition in part L comprises polyamide having a relative solution viscosity between 2.4 and 4 
     
     
         5 . Process according to  claim 3 , wherein the polyamide of part H has a softening temperature above 280° C. and the polyamide of part L has a softening temperature below 270° C. 
     
     
         6 . Process according to  claim 5 , wherein the polyamide of part H is at least one selected from the group consisting of polyamide-4,6 and semi-aromatic(co-)polyamides 
     
     
         7 . Process according to  claim 6 , wherein the polyamide of part H is at least one selected from the group consisting of polyamide (6,6/6,T/6,I) and polyamide (6,T/4,T). 
     
     
         8 . Process according to  claim 4 , wherein the polyamide of pad H is polyamide-4,6 and the polyamide of part L is polyamide-6. 
     
     
         9 . Process according to  claim 4 , wherein the polyamide composition of part L comprises one or more viscosity increasing additive chosen from the group of fibers, chain extenders, branching agents and nano-filters. 
     
     
         10 . Process according to  claim 9 , wherein the polyamide composition of part L comprises, as a viscosity increasing additive, at least 10 wt. % fibers. 
     
     
         11 . Process according to  claim 9 , wherein the polyamide composition of part L comprises at least 20 wt. % fibers. 
     
     
         12 . Process according to  claim 9 , wherein the composition of part L comprises at least 30 wt. % fibers. 
     
     
         13 . Process according to  claim 9 , wherein the composition of part L comprises at least 40 wt. % fibers. 
     
     
         14 . Process according to  claim 10 , wherein the fibers are glass fibers. 
     
     
         15 . Process according to  claim 10 , wherein the fibers have an aspect ratio L/d of at least 20. 
     
     
         16 . Process according to  claim 4 , wherein the polyamide composition of part L comprises, as a viscosity increasing additive, a branching agent that reacts with the polyamide giving the polyamide composition a non-Newtonian melt flow behaviour. 
     
     
         17 . Process according to  claim 16 , wherein the branching agent is an anhydride containing copolymer. 
     
     
         18 . Process according to  claim 17 , wherein the branching agent is a copolymer of maleic anhydride and styrene. 
     
     
         19 . Process according to  claim 16 , wherein the branching agent comprises a) a copolymer of at least an unsaturated dicarboxylic acid or a derivative thereof and a vinylaromatic monomer and b) a copolymer of acrylonitril and a vinylaromatic monomer, and wherein (a) and (b) are miscible and the ratio (a)/(b) is between 1/3 to 3/1. 
     
     
         20 . Process according to  claim 19 , wherein the branching agent comprises a) a styrene maleic anhydride copolymer (SMA), and b) a styrene-acrylonitril copolymer (SMA) 
     
     
         21 . Process according to  claim 4 , wherein the polyamide composition of part L comprises, as a viscosity increasing additive, a chain extender. 
     
     
         22 . Process according to  claim 16 , wherein the chain extender is carbonylbislactamate.