IP Library Granted Patent US 7,521,524
Granted Patent B2
US 7,521,524 · App. 11/071,326 · Granted Apr 21, 2009

Polymerization method and polymerization apparatus

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Quick Facts
Patent No.
US 7,521,524
App. No.
11/071,326
Granted
Apr 21, 2009
Kind
B2
Abstract

A polymerization method comprises, prior to polymerization of a monomer of the cyclic dimer of alpha-hydroxycarboxylic acid, a first mixture of a polymerization catalyst by bypassing a part of the monomer of the cyclic dimer is prepared. Then, the first mixture is mixed with a dominant amount of the monomer introduced into a polymerization reactor. The monomer of the cyclic dimer in the polymerization reactor is conducted in the presence of a polymerization initiator.

Claims (26)

1. A polymerization method comprising:

prior to polymerization of a monomer of the cyclic dimer of alpha-hydroxycarboxylic acid,

preparing a first mixture of a polymerization catalyst by bypassing a part of the monomer of the cyclic dimer of the alpha-hydroxycarboxylic acid,

mixing the first mixture with a dominant amount of the monomer of the cyclic dimer of the alpha-hydroxycarboxylic acid introduced into a polymerization reactor, and

polymerizing the monomer of the cyclic dimer of alpha-hydroxycarboxylic acid in the polymerization reactor in the presence of a polymerization initiator.

2. The polymerization method according to claim 1 , wherein a part of the monomer of the cyclic dimer of the alpha-hydroxycarboxylic acid is further bypassed to prepare a second mixture of the monomer of the cyclic dimer of the alpha-hydroxycarboxylic acid and the polymerization initiator, and wherein the mixture is introduced into the polymerization reactor to effect the polymerization of the monomer of the cyclic dimer in the polymerization reactor.

3. The polymerization method according to claim 2 ,

wherein the second mixture is introduced into the polymerization reactor after the first mixture is introduced into in the polymerization reactor.

4. The polymerization method according to claim 1 , wherein the dominant amount of the monomer of the cyclic dimer of alpha-hydroxycarboxylic acid is kept at a temperature lower than a polymerization initiation temperature before it is introduced into the polymerization reactor.

5. The polymerization method according to claim 1 , wherein a time period between the preparation of the first mixture and the polymerization initiation where the dominant amount of the monomer of the cyclic dimer of alpha-hydroxycarboxylic acid is introduced into the polymerization reactor is less than 5 hours.

6. The polymerization method according to claim 1 , wherein the dominant amount of the monomer of the cyclic dimer of alpha-hydroxycarboxylic acid is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

7. The polymerization method according to claim 1 , wherein the first mixture is kept at a temperature lower than a polymerization temperature before it is introduced into the polymerization reactor.

8. The polymerization method according to claim 7 , wherein the first mixture is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

9. The polymerization method according to claim 2 , wherein the first mixture is kept at a temperature lower than a polymerization temperature before it is introduced into the polymerization reactor.

10. The polymerization method according to claim 9 , wherein the first mixture is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

11. The polymerization method according to claim 4 , wherein the first mixture is kept at a temperature lower than a polymerization temperature before it is introduced into the polymerization reactor.

12. The polymerization method according to claim 11 , wherein the first mixture is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

13. The polymerization method according to claim 5 , wherein the first mixture is kept at a temperature lower than a polymerization temperature before it is introduced into the polymerization reactor.

14. The polymerization method according to claim 13 , wherein the first mixture is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

15. The polymerization method according to claim 6 , wherein the first mixture is kept at a temperature lower than a polymerization temperature before it is introduced into the polymerization reactor.

16. The polymerization method according to claim 15 , wherein the first mixture is kept at a temperature higher than 80° C. before it is introduced into the polymerization reactor.

17. The polymerization method according to claim 1 , wherein the first mixture does not contain the polymerization initiator.

18. The polymerization method according to claim 2 , wherein the first mixture does not contain the polymerization initiator, and the second mixture does not contain the polymerization catalyst.

19. The polymerization method according to claim 4 , wherein the first mixture does not contain the polymerization initiator.

20. The polymerization method according to claim 5 , wherein the first mixture does not contain the polymerization initiator.

21. The polymerization method according to claim 6 , wherein the first mixture does not contain the polymerization initiator.

Assignments (3)
MERGER Recorded Mar 4, 2014
From: HITACHI PLANT TECHNOLOGIES, LTD.
To: HITACHI, LTD.
Reel/Frame 032384/0877 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 5, 2009
From: HITACHI, LTD.
To: HITACHI PLANT TECHNOLOGIES, LTD.
Reel/Frame 023319/0953 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 26, 2005
From: MIZUMOTO, MAMORU; MATSUO, TOSHIAKI; MATSUMOTO, TAKAYUKI; OKAMOTO, NARUYASU; KAJIYA, RYUUJI
To: HITACHI, LTD.
Reel/Frame 016615/0778 →