Continuous polymerization device, method for producing polymer composition, and injection valve

Patent metadata

Field	Value
Publication number	US-9403922-B2
Application number	US-201414764890-A
Country	US
Kind code	B2
Filing date	Jan 15, 2014
Priority date	Jan 31, 2013
Publication date	Aug 2, 2016
Grant date	Aug 2, 2016

Abstract

A continuous polymerization apparatus uses at least a first reactor and a second reactor ( 10, 20 ). Each of the reactors ( 10, 20 ) comprises a supply port ( 11 a , 21 a ) and an effluent port ( 11 b , 21 b ). The supply port ( 11 a ) of the first reactor ( 10 ) is connected to supply sources ( 1, 3 ) of a raw material monomer and a polymerization initiator, and the effluent port ( 11 b ) thereof is connected to the supply port ( 21 a ) of the second reactor ( 20 ) by a connection line ( 15 a ). The connection line ( 15 a ) is combined with a replenishing line ( 15 b ) through an injection valve ( 50 ) at a combining part. The injection valve ( 50 ) comprises, in a full closure state thereof, a clearance that may cause a fluid comprising at least the raw material monomer to flow from the replenishing line ( 15 b ) to the connection line ( 15 a ).

First claim

The invention claimed is:

1. A continuous polymerization apparatus at least comprising
a first reactor and a second reactor, wherein
each of the reactors comprises a supply port and an effluent port, wherein
the supply port of the first reactor is connected to supply sources of a raw material monomer and a polymerization initiator, wherein
the effluent port of the first reactor is connected to the supply port of the second reactor by a connection line, wherein
the connection line is combined with a replenishing line through an injection valve at a combining part located between the effluent port of the first reactor and the supply port of the second reactor, and wherein
the injection valve in a full closure state thereof comprises a clearance capable of causing a fluid comprising at least the raw material monomer to flow from the replenishing line to the connection line.

2. The continuous polymerization apparatus of claim 1 , wherein the injection valve comprises:
a plug;
a body comprising a space that accommodates the plug; and
a shaft that supports and operates the plug in the space, and wherein
in the full closure state, the clearance is formed between an inner wall face of the body and a surface of the plug.

3. The continuous polymerization apparatus of claim 1 , wherein an inner volume of the body of the injection valve in the full closure state thereof is 1 to 30% of an inner volume of the body in a full open state of the injection valve.

4. The continuous polymerization apparatus of claim 1 , wherein
the replenishing line is connected to a supply source of a raw material monomer and a polymerization initiator and a supply source of a raw material monomer and a polymerization inhibitor, switchably therebetween.

5. The continuous polymerization apparatus of claim 1 , wherein
each of the first reactor and the second reactor is a tank type reactor, and wherein
the effluent port of each of the reactors is located at a top of the reactor.

6. The continuous polymerization apparatus of claim 1 , wherein
each of the first reactor and the second reactor is a complete mixing type reactor.

7. The continuous polymerization apparatus of claim 1 , wherein
each of the first reactor and the second reactor further comprises a temperature detecting means that detects a temperature in the reactor.

8. The continuous polymerization apparatus of claim 1 , wherein
the connection line comprises a cooling means.

9. The continuous polymerization apparatus of claim 1 , wherein
the connection line comprises a mixing means.

10. The continuous polymerization apparatus of claim 1 , wherein
another supply port provided on the second reactor is connected to a supply source of a new polymerization initiator.

11. A production method of a polymer composition using the continuous polymerization apparatus of claim 1 , the production method comprising:
a first polymerization step of continuously supplying the raw material monomer and the polymerization initiator from the supply sources of the raw material monomer and the polymerization initiator, to the first reactor, through the supply port of the first reactor to subject the raw material monomer and the polymerization initiator to a continuous polymerization in the first reactor, and continuously taking out an intermediate composition obtained thereby from an effluent port of the first reactor;
a raw material monomer supply step of supplying a fluid comprising at least a raw material monomer from the replenishing line to the intermediate composition through the injection valve in a course of transfer of the intermediate composition from the effluent port of the first reactor to the supply port of the second reactor through the connection line; and
a second polymerization step of continuously supplying a mixture of the intermediate composition taken out from the effluent port of the first reactor and the fluid supplied from the replenishing line through the injection valve, to the second reactor, through the supply port of the second reactor to further subject the mixture to a continuous polymerization in the second reactor, and continuously taking out a polymer composition obtained thereby from an effluent port of the second reactor.

12. The production method of a polymer composition of claim 11 , wherein
the fluid comprising at least the raw material monomer further comprises a polymerization initiator.

13. The production method of a polymer composition of claim 11 , further comprising:
an intermediate cooling step of continuously cooling at least the intermediate composition using a cooling means of the connection line in a course of transfer of the intermediate composition from the effluent port of the first reactor to the supply port of the second reactor through the connection line.

14. The production method of a polymer composition of claim 11 , wherein
a temperature of the mixture at the supply port of the second reactor is lower by 5 to 80° C. than a temperature of the intermediate composition at the effluent port of the first reactor.

15. A production method of a polymer composition using the continuous polymerization apparatus of claim 1 , the production method comprising:
a polymerization step of continuously supplying the raw material monomer and the polymerization initiator from the supply sources of the raw material monomer and the polymerization initiator, to the first reactor, through a supply port of the first reactor to subject the raw material monomer and the polymerization initiator to a continuous polymerization in the first reactor, and continuously taking out an intermediate composition obtained thereby from the effluent port of the first reactor;
a raw material monomer supply step of supplying a fluid comprising at least a raw material monomer from the replenishing line to the intermediate composition through the injection valve in a course of transfer of the intermediate composition from the effluent port of the first reactor to the supply port of the second reactor through the connection line; and
a passage step of continuously supplying a mixture of the intermediate composition taken out from the effluent port of the first reactor and the fluid supplied from the replenishing line through the injection valve, to the second reactor, through a supply port of the second reactor for the mixture to pass through the second reactor, and continuously taking out the mixture as a polymer composition from an effluent port of the second reactor.

16. The production method of a polymer composition of claim 15 , wherein
at the raw material monomer supply step, the injection valve is used in the full closure state thereof.

17. The production method of a polymer composition of claim 15 , wherein
the fluid comprising at least the raw material monomer further comprises a polymerization inhibitor.

18. The production method of a polymer composition of claim 11 , wherein
a temperature in the first reactor detected by a temperature detecting means of the first reactor and a temperature in the second reactor detected by a temperature detecting means of the second reactor are within a range from 120 to 180° C., respectively.

19. An injection valve comprising:
a plug;
a body comprising a space to accommodate the plug; and
a shaft that supports and operates the plug in the space, wherein
a clearance is formed between an inner wall face of the body and a surface of the plug in a full closure state of the injection valve.

20. A polymerization a

Assignees

• Sumitomo Chemical Co

Inventors

• Sumida Masakazu
• Yamazaki Kazuhiro
• Nishitani Akira

Classifications

• C08F2/01 Primary

  characterised by special features of the polymerisation apparatus used · CPC title

• C08F20/10 Primary

  Esters · CPC title

• B01J2219/00103

  in a heat exchanger separate from the reactor · CPC title

• B01J2219/24

  Stationary reactors without moving elements inside · CPC title

• B01J2219/00058

  Temperature measurement · CPC title