POLYAMIDE POWDER FOR SELECTIVE SINTERING METHODS

1 . A polyamide powder, wherein the polyamide has a solution viscosity measured according to ISO 307 of 1.55 to 1.75 and an increase in the solution viscosity of 10% to 40% when measured in a nitrogen atmosphere at a temperature of 10° C. below a melting temperature of the polyamide for 24 h.

2 . The polyamide powder according to claim 1 , wherein the polyamide comprises excessive amine end groups as compared to carboxylic acid end groups.

3 . The polyamide powder according to claim 2 , wherein the excessive amine end groups are achieved through monoamines.

4 . The polyamide powder according to claim 2 , wherein an excess of the amine end groups over the carboxylic acid end groups is 20 to 60 mmol/kg, based on a total mass of the polyamide powder.

5 . The polyamide powder according to claim 1 , wherein the polyamide comprises excessive carboxylic acid end groups as compared to amine end groups.

6 . The polyamide powder according to claim 5 , wherein the excessive carboxylic acid end groups are achieved through monocarboxylic acids.

7 . The polyamide powder according to claim 5 , wherein an excess of the carboxylic acid end groups over the amine end groups over is 20 to 60 mmol/kg, based on a total mass of the polyamide powder.

8 . The polyamide powder according to claim 1 , wherein the polyamide powder has a BET surface area measured according to DIN ISO 9277 of at least 1 m 2 /g.

9 . The polyamide powder according to claim 1 , wherein the polyamide powder has a weight-average particle diameter d 50 measured by laser diffraction of not more than 100 μm.

10 . The polyamide powder according to claim 1 , wherein the polyamide powder has a bulk density measured according to DIN 53466 of 300 g/l to 600 g/l.

11 . The polyamide powder according to claim 1 , wherein the polyamide powder has a surface energy of not more than 35 mN/m, and the surface energy is determined via a contact angle measurement by capillary rise height method using Washburn equation and an evaluation method according to Owens, Wendt, Rabel and Kaelble.

12 . The polyamide powder according to claim 1 , obtained by a precipitation process.

13 . The polyamide powder according to claim 1 , wherein the polyamide is at least one selected from the group consisting of polyamide 6, polyamide 11, polyamide 12, polyamide 1013, polyamide 1012, polyamide 66, polyamide 46, polyamide 613, polyamide 106, and polyamide 12/1012.

14 . A process for preparing the polyamide powder according to claim 1 , the process comprising

a) preparing the polyamide via a polymerization and/or polycondensation of monomers, and

b) preparing the powder by grinding or reprecipitation,

wherein, in a), either monoamines to achieve excessive amine end groups or monocarboxylic acids to achieve excessive carboxylic acid end groups are added as chain transfer agents.

15 . The process according to claim 14 , wherein

at least one AB type polyamide, produced by polymerization of at least one lactam comprising a monomer unit of 4 to 14 carbon atoms or by polycondensation of at least one corresponding ω-aminocarboxylic acid comprising a monomer unit of 4 to 14 carbon atoms, and at least one AABB type polyamide, produced by polycondensation of at least one diamine and at least one dicarboxylic acid, each having a monomer unit of 4 to 14 carbon atoms, are obtained in a), and

the powder is obtained in b) by coprecipitation of the at least one AB type polyamide and the at least one AABB type polyamide.

16 . A powder bed fusion method for producing a shaped body, the method comprising:

preparing the shaped body from the polyamide powder according to claim 1 .

17 . A shaped body, obtained at least partly from the polyamide powder according to claim 1 .