IP Library Granted Patent US 9,624,329
Granted Patent B2
US 9,624,329 · App. 14/099,477 · Granted Apr 18, 2017

Process for producing fluorinated copolymer

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,624,329
App. No.
14/099,477
Granted
Apr 18, 2017
Kind
B2
Abstract

A process for producing a fluorinated copolymer includes polymerizing a fluorinated monomer having a carboxylic acid functional group or a sulfonic acid functional group and a fluorinated olefin by a solution polymerization method in a polymerization medium to obtain a mixture containing a fluorinated copolymer, an unreacted monomer and the polymerization medium. The mixture is continuously or intermittently transferred to an evaporation vessel provided with a stirrer and heating the mixture with stirring in the evaporation vessel to evaporate and recover the unreacted monomer and the polymerization medium.

Claims (24)

1. A process for producing a fluorinated copolymer, the process comprising:

(I) polymerizing a fluorinated monomer having a carboxylic acid functional group or a sulfonic acid functional group and a fluorinated olefin by a solution polymerization method in a polymerization medium to obtain slurry containing a fluorinated copolymer, an unreacted monomer and the polymerization medium;

(II) continuously or intermittently transferring the slurry to an evaporation vessel provided with a stirrer and heating the slurry with stirring in the evaporation vessel under a pressure below atmospheric pressure to evaporate and recover the unreacted monomer and the polymerization medium, while keeping the fluorinated copolymer in the evaporation vessel; and

(III) taking out the fluorinated copolymer from the evaporation vessel after finishing the recovery of the unreacted monomer and the polymerization medium,

wherein a stirring blade in the evaporation vessel is a scraping blade which rubs against a wall surface of the evaporation vessel when rotating.

2. The process for producing a fluorinated copolymer according to claim 1 , wherein the fluorinated monomer having a sulfonic acid functional group is a compound represented by the following formula (2) or (3):

CF 2 ═CF—O—R f2 -A 2   (2)

CF 2 ═CF—R f2 -A 2   (3)

wherein R f2 is a C 1-20 perfluoroalkylene group, which may contain an etheric oxygen atom, and which may be linear or branched, and A 2 is a sulfonic acid functional group.

3. The process for producing a fluorinated copolymer according to claim 1 , wherein a stirring blade in the evaporation vessel is a helical ribbon blade.

4. The process for producing a fluorinated copolymer according to claim 1 , wherein in the step (II), the slurry is transferred to the evaporation vessel so that the overall coefficient of heat transfer becomes at least 80 kJ/m 2 ·h·° C.

5. The process for producing a fluorinated copolymer according to claim 1 , wherein the amount of the unreacted monomer remaining is at most 1.0 mass % per 100 mass % of the fluorinated copolymer.

6. A process for producing a fluorinated copolymer, the process comprising:

(I′) polymerizing a fluorinated monomer having a carboxylic acid functional group or a sulfonic acid functional group and a fluorinated olefin by a bulk polymerization method to obtain slurry containing a fluorinated copolymer and an unreacted monomer;

(II′) after the polymerizing of the fluorinated monomer and the fluorinated olefin is completed, continuously or intermittently transferring the slurry to an evaporation vessel provided with a stirrer and heating the slurry with stirring in the evaporation vessel under a pressure below atmospheric pressure to evaporate and recover the unreacted monomer, while keeping the fluorinated copolymer in the evaporation vessel; and

(III′) taking out the fluorinated copolymer from the evaporation vessel after finishing the recovery of the unreacted monomer,

wherein a stirring blade in the evaporation vessel is a scraping blade which rubs against a wall surface of the evaporation vessel when rotating.

7. The process for producing a fluorinated copolymer according to claim 6 , wherein the fluorinated monomer having a sulfonic acid functional group is a compound represented by the following formula (2) or (3):

CF 2 ═CF—O—R f2 -A 2   (2)

CF 2 ═CF—R f2 -A 2   (3)

wherein R f2 is a C 1-20 perfluoroalkylene group, which may contain an etheric oxygen atom, and which may be linear or branched, and A 2 is a sulfonic acid functional group.

8. The process for producing a fluorinated copolymer according to claim 6 , wherein a stirring blade in the evaporation vessel is a helical ribbon blade.

9. The process for producing a fluorinated copolymer according to claim 6 , wherein in the step (II′), the slurry is transferred to the evaporation vessel so that the overall coefficient of heat transfer becomes at least 80 kJ/m 2 ·h·° C.

10. The process for producing a fluorinated copolymer according to claim 6 , wherein the amount of the unreacted monomer remaining is at most 1.0 mass % per 100 mass % of the fluorinated copolymer.

Assignments (2)
CHANGE OF NAME Recorded Aug 7, 2018
From: ASAHI GLASS COMPANY, LIMITED
To: AGC INC.
Reel/Frame 046730/0786 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 20, 2013
From: AIDA, SHIGERU; TOMITA, TOSHINORI; ETO, TOSHINORI; UMEMURA, KAZUO; TSUJI, ATSUSHI
To: ASAHI GLASS COMPANY, LIMITED
Reel/Frame 031827/0532 →