Method for producing polyimide resin powder, and thermoplastic polyimide resin powder

Patent metadata

Field	Value
Publication number	US-2016159984-A1
Application number	US-201414905637-A
Country	US
Kind code	A1
Filing date	Aug 4, 2014
Priority date	Aug 6, 2013
Publication date	Jun 9, 2016
Grant date	—

Abstract

The present invention provides a method for producing a polyimide resin powder, including the step of reacting (A) a tetracarboxylic acid component containing a tetracarboxylic dianhydride with (B) a diamine component containing an aliphatic diamine in the presence of (C) a solvent containing an alkylene glycol-based solvent represented by the formula (1):

wherein Ra 1 represents a hydrogen atom or an alkyl group having from 1 to 4 carbon atoms, Ra 2 represents a linear alkylene group having from 2 to 6 carbon atoms, and n represents an integer of 1-3.

First claim

1 . A production method for a polyimide resin powder, comprising the step of reacting (A) a tetracarboxylic acid component comprising a tetracarboxylic dianhydride with (B) a diamine component comprising an aliphatic diamine in the presence of (C) a solvent comprising an alkylene glycol-based solvent represented by the formula (1):

wherein Ra 1 represents a hydrogen atom or an alkyl group having from 1 to 4 carbon atoms, Ra 2 represents a linear alkylene group having from 2 to 6 carbon atoms, and n represents an integer of 1-3.

2 . The production method according to claim 1 , wherein the alkylene glycol-based solvent has a boiling point of 140° C. or higher.

3 . The production method according to claim 1 , wherein Ra 1 is an alkyl group having from 1 to 4 carbon atoms.

4 . The production method according to claim 1 , wherein n is 2 or 3.

5 . (canceled)

6 . The production method according to claim 1 , wherein the alkylene glyco-based solvent is 2-(2-methoxyethoxy)ethanol or 2-(2-ethoxyethoxy)ethanol.

7 . The production method according to claim 1 , wherein the content of the alkylene glycol-based solvent in the solvent (C) is 75 mass % or more.

8 . The production method according to claim 1 , wherein the step of reacting (A) the tetracarboxylic acid component with (B) the diamine component comprises: step (i) of adding (b) a solution comprising the diamine component (B) to (a) a solution comprising the tetracarboxylic acid component (A) to prepare (c) a solution comprising a polyamic acid; and step (ii) imidizing the polyamic acid by heating the solution (c) to obtain a polyimide resin, wherein in the step (i), the solution (b) is added to the solution (a) such that the amount of the diamine component (B) added per unit time with respect to 1 mol of the tetracarboxylic acid component (A) is 0.1 mol/min or lower.

9 . The production method according to claim 8 , wherein in the step (i), the solution (b) is added to the solution (a) such that the amount of the diamine component (B) added per unit time with respect to 1 mol of the tetracarboxylic acid component (A) is 0.005 mol/min or higher.

10 . The production method according to claim 1 , wherein the diamine component (B) comprises (B1) a diamine represented by the formula (B1-1) and (B2) a diamine represented by the formula (B2-1) as the aliphatic diamine:
H 2 N—R 1 —NH 2   (B1-1)
H 2 N—R 2 —NH 2   (B2-1)

wherein R 1 represents a divalent group having from 6 to 22 carbon atoms containing at least one alicyclic hydrocarbon structure, and R 2 represents a divalent chain aliphatic group having from 5 to 20 carbon atoms.

11 . The production method according to claim 10 , wherein the diamine (B1) is represented by the formula (B1-2):

wherein m 11 and m 12 each independently represent an integer of 0-2.

12 . The production method according to claim 10 , wherein the amount of the diamine (B1) with respect to the total amount of the diamine (B1) and the diamine (B2) is from 40 to 70 mol %.

13 . The production method according to claim 10 , wherein the diamine component (B) further comprises (B3) a diamine represented by the formula (B3-1) in addition to the aliphatic diamine, wherein the amount of the diamine (B3) with respect to the total amount of the diamine (B1) and the diamine (B2) is 25 mol %. or less:
H 2 N—R 3 —NH 2   (B3-1)

wherein R 3 represents a divalent group having from 6 to 22 carbon atoms containing at least one aromatic ring.

14 . The production method according to claim 1 , wherein the tetracarboxylic dianhydride is represented by the formula (A-1):

wherein X represents a tetravalent group having from 6 to 22 carbon atoms containing at least one aromatic ring.

15 . (canceled)

16 . The production method according to claim 1 , wherein the polyimide resin to be produced is a thermoplastic polyimide resin comprising a repeating unit represented by the following formula (I) and a repeating unit represented by the following formula (II), wherein the content ratio of the repeating unit of the formula (I) with respect to the total of the repeating unit of the formula (I) and the repeating unit of the formula (II) is from 40 to 70 mol %.:

wherein R 1 represents a divalent group having from 6 to 22 carbon atoms containing at least one alicyclic hydrocarbon structure, R 2 represents a divalent chain aliphatic group having from 5 to 20 carbon atoms, and X 1 and X 2 each independently represent a tetravalent group having from 6 to 22 carbon atoms containing at least one aromatic ring.

17 . (canceled)

18 . The production method according to claim 8 , wherein the area ratio of a peak whose peak top is present at a molecular weight of 1000 or smaller is 2 area % or less when the obtained product is measured by gel permeation chromatography.

19 . A thermoplastic polyimide resin powder which is a powder of a thermoplastic polyimide resin comprising a repeating unit represented by the following formula (I) and a repeating unit represented by the following formula (II), wherein the content ratio of the repeating unit of the formula (I) with respect to the total of the repeating unit of the formula (I) and the repeating unit of the formula (II) is 40 to 70 mol %, and the ratio of particles passing through a sieve with a mesh opening of 500 μm is 90 mass % or more:

wherein R 1 represents a divalent group having from 6 to 22 carbon atoms containing at least one alicyclic hydrocarbon structure, R 2 represents a divalent chain aliphatic group having from 5 to 20 carbon atoms, and X 1 and X 2 each independently represent a tetravalent group having from 6 to 22 carbon atoms containing at least one aromatic ring.

20 . The thermoplastic polyimide resin powder according to claim 19 , wherein the ratio of particles passing through a sieve with a mesh opening of 250 μm is 90 mass % or more.

21 . The thermoplastic polyimide resin powder according to claim 19 , wherein R 1 is a divalent group represented by the following formula (R1-1) or (R1-2):

wherein m 11 and m 12 each independently represent an integer of 0-2, and m 13 to m 15 each independently represent an integer of 0-2.

22 . (canceled)

23 . The thermoplastic polyimide resin powder according to claim 19 , wherein R 2 is an alkylene group having from 5 to 20 carbon atoms.

24 .- 25 . (canceled)

26 . The thermoplastic polyimide resin powder according to claim 19 , wherein X 1 and X 2 are each independently a tetravalent group represented by any of the following formulas (X-1) to (X-4):

wherein R 11 to R 18 each independently represent an alkyl group having from 1 to 4 carbon atoms, p 11 to p 13 each inde

Assignees

• Mitsubishi Gas Chemical Co

Inventors

• Sato Yuuki
• Mitadera Jun

Classifications

• C08G73/1082

  wholly aromatic in the tetracarboxylic moiety · CPC title

• C08G73/1032 Primary

  characterised by the solvent(s) used · CPC title

• C09J179/08

  Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors · CPC title

• C08G73/1028

  characterised by the process itself, e.g. steps, continuous · CPC title

• C08G73/105

  with oxygen only in the diamino moiety · CPC title