Polyamide powder for selective sintering methods
A polyamide powder for selective absorbing sintering, SAS, or selective inhibition sintering, SIS. The polyamide powder has a solution viscosity to ISO 307 of 1.8 to 2 and a rise in the solution viscosity of 0% to 25% when it is subjected to a temperature 20° C. below its melting temperature under air for 20 hours.
1. A polyamide powder for selective absorbing sintering, SAS, or selective inhibition sintering, SIS, wherein the polyamide has a solution viscosity to ISO 307 of 1.8 to 2 and a rise in the solution viscosity of 5% to 25%, when subjected to a temperature 20° C. below its melting temperature under air for 20 hours,
an excess of carboxylic acid end groups over amine end groups of 20 to 60 mmol/kg,
a surface energy of the polyamide, determined by a contact angle measurement by a capillary rise height method by use of the Washburn equation and the evaluation method according to Owens, Wendt, Rabel and Kaelble, is not more than 35 mN/m,
the polyamide powder absorbs liquid in a volume of 1,000 pl/g to 30,000 pl/g, wherein the polyamide powder contains only a single type of polyamide, and
wherein the single type of polyamide is an AB type or AABB type polyamide.
2. The polyamide powder according to claim 1 , wherein the polyamide has a rise in solution viscosity of 5 to 15% when subjected to a temperature 20° C. below its melting temperature under air for 20 hours.
3. A polyamide powder for selective absorbing sintering, SAS, or selective inhibition sintering, SIS,
wherein the polyamide has a solution viscosity to ISO 307 of 1.8 to 2 and a rise in the solution viscosity of 5% to 25%, when subjected to a temperature 20° C. below its melting temperature under air for 20 hours,
an excess of carboxylic acid end groups over amine end groups of 20 to 60 mmol/kg,
a surface energy of the polyamide, determined by a contact angle measurement by a capillary rise height method by use of the Washburn equation and the evaluation method according to Owens, Wendt, Rabel and Kaelble, is not more than 35 mN/m,
wherein the polyamide powder absorbs liquid in a volume of 1.000 pl/g to 30,000 pl/g, wherein the polyamide powder contains only a single type of polyamide, and
wherein the powder has open mesopores and the cumulative pore volume distribution of the mesopores, measured to DIN 66134, is at least 0.01 cm 3 /g.
4. The polyamide powder according to claim 1 , wherein a weight-average particle diameter d 50 of the polyamide powder, measured by laser diffraction, is not more than 100 μm.
5. The polyamide powder according to claim 1 , wherein a weight-average particle diameter d 50 of the polyamide powder, measured by laser diffraction, is from 10 μm to 80 μm.
6. A polyamide powder for selective absorbing sintering, SAS, or selective inhibition sintering SIS,
wherein the polyamide has a solution viscosity to ISO 307 of 1.8 to 2 and a rise in the solution viscosity of 5% to 25%, when subjected to a temperature 20° C. below its melting temperature under air for 20 hours,
an excess of carboxylic acid end groups over amine end groups of 20 to 60 mmol/kg,
a surface energy of the polyamide, determined by a contact angle measurement by a capillary rise height method by use of the Washburn equation and the evaluation method according to Owens, Wendt, Rabel and Kaelble, is not more than 35 mN/m,
wherein the polyamide powder absorbs liquid in a volume of 1,000 pl/g to 30,000 pl/g, wherein the polyamide powder contains only a single type of polyamide, and
wherein a bulk density of the polyamide powder, measured to DIN 53466, is between 300 g/l and 600 g/l.
7. The polyamide powder according to claim 1 , wherein a surface energy of the polyamide, determined by a contact angle measurement by a capillary rise height method by use of the Washburn equation and the evaluation method according to Owens, Wendt, Rabel and Kaelble, is from 25 mN/m to 32 mN/m.
8. The polyamide powder according to claim 1 , wherein the polyamide powder is obtained by a precipitation process.
9. A process for producing the polyamide powder according to claim 1 , comprising:
(a) polymerizing and/or polycondensing monomers to give a polyamide; and
(b) producing a powder by grinding or precipitation,
wherein dicarboxylic acids are added as a chain transfer agent in (a) to achieve a carboxylic acid end group excess.
10. The process according to claim 9 , wherein the dicarboxylic acids are added in such a ratio as to achieve an excess of 20 to 60 mmol/kg, based on a mass of the polyamide powder.
11. Shaped bodies which are obtained at least partly from the polyamide powder according to claim 1 .
12. A process for producing shaped bodies, comprising using the polyamide powder according to claim 1 in a SAS method or a SIS method.
13. The polyamide powder according to claim 8 , wherein a suspension obtained by precipitation is left at a temperature of 2-4 K above the precipitation temperature for 10 to 180 min, after precipitation.
14. The polyamide powder according to claim 1 , wherein a BET surface area of the polyamide powder, measured to DIN ISO 9277, is from 10 m 2 /g to 30 m 2 /g.
15. The polyamide powder according to claim 1 , wherein the single type of polyamide is nylon-12.
16. The polyamide powder according to claim 1 , wherein the single type of polyamide is an AB type polyamide.
17. The polyamide powder according to claim 1 , wherein the single type of polyamide is an AABB type polyamide.
18. The polyamide powder according to claim 1 , wherein the polyamide powder consists essentially of the single type of polyamide.
19. The polyamide powder according to claim 15 , wherein the polyamide powder consists essentially of nylon-12.
20. The polyamide powder according to claim 15 , wherein the polyamide of the polyamide polymer consists of nylon-12.