Large scale process for polymerization of DAPBI-containing polyaramid
A method for obtaining an aromatic polyamide crumb from an aromatic diamine and an aromatic diacid chloride, which aromatic polyamide comprises 5(6)-amino-2-(p-aminophenyl)benzimidazole terephthalamide units and has a relative viscosity η rel of at least 3, by: (1) adding at least monomers (i)-(iii) in N-methyl pyrrolidone as solvent wherein (i) is 0-30 mole % para-phenylenediamine (PPD), (ii) is 20-50 mole % 5(6)-amino-2-(p-aminophenyl)benzimidazole (DABPI), (iii) is 49.05-50.05 mole % terephthaloyl dichloride (TDC), and optionally calcium chloride to obtain a CaCl 2 /aromatic diamine molar ratio less than 0.5, and an aromatic diamine/aromatic diacid chloride ratio between 0.99 and 1.01; (2) mixing the monomers and the optional calcium chloride to a homogenous mixture having a monomer concentration of 5 to 12 wt %; followed by (3) adding calcium chloride to the homogeneous mixture to obtain a CaC1 2 /aromatic diamine molar ratio 0.6-1.0; and (4) polymerizing the mixture.
1. A method for obtaining an aromatic polyamide crumb from an aromatic diamine and an aromatic diacid chloride, which aromatic polyamide comprises 5(6)-amino-2-(p-aminophenyl)benzimidazole terephthalamide units and has a relative viscosity η rel of at least 3, comprising:
adding at least monomers (i)-(iii) in N-methyl pyrrolidone as solvent wherein:
i) is 0-30 mole % para-phenylenediamine (PPD);
ii) is 20-50 mole % 5(6)-amino-2-(p-aminophenyl)benzimidazole (DABPI);
iii) is 49.05-50.05 mole % terephthaloyl dichloride (TDC); and optionally calcium chloride to obtain a CaCl 2 /aromatic diamine molar ratio less than 0.5, and an aromatic diamine/aromatic diacid chloride ratio between 0.99 and 1.01;
mixing the monomers and the optional calcium chloride to a homogeneous mixture having a monomer concentration of 5 to 12 wt %, followed by
adding calcium chloride to the homogeneous mixture to obtain a CaCl 2 /aromatic diamine molar ratio of 0.6-1.0; and
polymerizing the mixture in a reactor having a measure capacity of at least 160 L, wherein mole % relates to the molar percentage of the monomers with regard to the total of aromatic diamine and aromatic diacid chloride monomers.
2. The method according to claim 1 wherein the CaCl 2 /aromatic diamine molar ratio in the homogeneous mixture is 0.65-0.85.
3. The method according to claim 2 wherein the CaCl 2 /aromatic diamine molar ratio in the homogeneous mixture is 0.70-0.80.
4. The method according to claim 1 wherein first the aromatic diamines are mixed for 1 to 180 min in N-methyl pyrrolidone wherein the CaCl 2 /aromatic diamine molar ratio is 0, after which the aromatic diacid chlorides are added and mixed for another 1 to 180 min followed by adding calcium chloride to obtain a CaCl 2 /aromatic diamine molar ratio 0.6-1.0.
5. The method according to claim 1 wherein calcium chloride is added as an NMP/CaCl 2 mixture.
6. The method according to claim 1 which is performed in a cylindrical reactor having a measure capacity of at least 160 L, which is equipped with a single mixing gear for use as stirrer and granulator.
7. The method according to claim 1 , wherein first the aromatic diamines are mixed for 3-30 min in N-methyl pyrrolidone wherein the CaC 1 2 /aromatic diamine molar ratio is 0, after which the aromatic diacid chlorides are added and mixed for another 3-30 min, followed by adding calcium chloride to obtain a CaCl 2 /aromatic diamine molar ratio of 0.6-1.0.