System and process for the production of functionalized olefinic-based polymer

Patent metadata

Field	Value
Publication number	US-10947375-B2
Application number	US-201615774302-A
Country	US
Kind code	B2
Filing date	Dec 9, 2016
Priority date	Jan 29, 2016
Publication date	Mar 16, 2021
Grant date	Mar 16, 2021

Abstract

A system for producing a functionalized olefinic-based polymer, the system comprising a polymerization zone for producing an olefinic-based polymer comprising a mixing section, a deliquifying section, and a quenching section, wherein at least one section of the polymerization zone has a defined cross-sectional area that continually decreases from a first end to a second end of said section; a devolatilization zone comprising a kneader or extruder, wherein said devolatilization zone is downstream of said polymerization zone and in fluid communication with said polymerization zone; and a functionalization zone downstream of said devolatilization zone and in fluid communication with said devolatilization zone.

First claim

The invention claimed is:

1. A synthesis system for producing a functionalized olefinic-based polymer comprising:
(i) a polymerization zone for producing an olefinic-based polymer, said polymerization zone comprising a mixing section, a deliquifying section, and a quenching section, wherein at least one section of the polymerization zone has a defined cross-sectional area that continually decreases from a first end to a second end of said section;
(ii) a devolatilization zone comprising a kneader or extruder, wherein said devolatilization zone is downstream of said polymerization zone and in fluid communication with said polymerization zone; and
(iii) a functionalization zone downstream of said devolatilization zone and in fluid communication with said devolatilization zone.

2. The system of claim 1 , wherein said functionalization zone comprises:
a. a first extruder;
b. a first functionalization kneader downstream of said first extruder and in fluid communication with said first extruder;
c. a second extruder downstream of said first functionalization kneader and in fluid communication with said first functionalization kneader;
d. a second functionalization kneader downstream of said second extruder and in fluid communication with said second extruder; and
e. a third extruder downstream of said second functionalization kneader and in fluid communication with said second functionalization kneader.

3. The system of claim 2 ,
wherein said first extruder is a screw extruder adapted to compact and heat the olefinic-based polymer,
and wherein said first functionalization kneader is a sealed vessel that is adapted to maintain gaseous reactants that are introduced into said first functionalization kneader.

4. The system of claim 2 , wherein said second extruder is a single screw extruder adapted to regulate the volume of material within said first functionalization kneader and provide a flow rate of material into said second kneader.

5. The system of claim 2 , wherein said first functionalization kneader and said second functionalization kneader include an intermeshing array of hooks and rotating paddles.

6. The system of claim 1 , wherein said mixing section has a cylindrical housing, an inlet proximate to a first end and an outlet proximate to an opposed second end, where said mixing section includes a rotatable shaft positioned axially within said housing and including at least two shearing paddles extending radially outward from said rotatable shaft.

7. The system of claim 1 , wherein said mixing section has a cylindrical housing, an inlet proximate to a first end and an outlet proximate to an opposed second end, where said mixing section includes a rotatable shaft positioned axially within said housing, said housing including at least two kneading hooks fixed to said housing and extending inwardly toward said rotatable shaft.

8. The system of claim 1 , wherein said deliquifying section and said quenching section are housed within a deliquifying-quench extruder having an inlet proximate to a first end and an outlet proximate to an opposed second end, said extruder including a shaft assembly positioned axially within said extruder and including multiple helical flight configurations, said extruder including multiple processing sections defined by the multiple flight configurations, said processing sections including a deliquifying-compaction section having the continually decreasing cross-sectional area, a sealing section downstream of the deliquifying-compaction section, a devolatilization section downstream of the sealing section, a quenching section downstream of the devolatilization section, and a conveying section downstream of the quenching section.

9. The system of claim 1 , wherein said deliquifying section is housed within a polymerization reactor, wherein said deliquifying section has the continually decreasing cross-sectional area in the form of a frustoconical housing having a first end larger than a second end, said first end constituting an inlet to said deliquifying section, and an outlet at said second end, where said deliquifying section includes a rotatable shaft positioned axially within said frustoconical housing and including at least one helical flight extending radially from the rotatable shaft.

10. The system of claim 1 , wherein said polymerization zone further comprises a compaction section for compacting the olefinic-based polymer.

11. A process for the production of a functionalized olefinic-based polymer using the synthesis system of claim 1 , wherein the process comprises:
polymerizing a monomer mixture comprising either (i) two or more C 4 to C 7 monoolefin monomers or (ii) at least one C 4 to C 7 olefin monomer and at least one non-conjugated aliphatic diene, non-isoprene conjugated aliphatic diene, aromatic diene, or aryl monomer, wherein the monomer mixture is polymerized in the presence of a catalyst or catalyst components within a polymerization reactor to form a polymerization mixture comprising an olefinic-based polymer,
optionally deliquifying and/or quenching the polymerization mixture, and
functionalizing the olefinic-based polymer, wherein functionalizing comprises reacting the olefinic-based polymer substantially in the bulk phase with a functionalizing agent within a first kneader reactor to produce a functionalized polymer and by-products of the functionalization reaction.

12. The process of claim 11 , wherein the olefinic-based polymer exits the polymerization reactor in a granulated state.

13. The process of claim 11 , wherein the functionalization comprises halogenation.

14. The process of claim 11 , wherein the functionalization comprises maleation.

15. The process of claim 11 , wherein said step of reacting the olefinic-based polymer with the functionalizing agent takes place when the olefinic-based polymer is at a temperature of from about 20 to about 200° C. and a pressure of from about 0.5 to about 10 atmospheres.

16. The process of claim 11 , wherein the olefinic-based polymer has (i) a crossover angular frequency (ω c ) of greater than or equal to 1 rad/s or (ii) a ω c of less than 1 rad/s and a plateau modulus (G N ) of less than 1.2×10 5 Pa.

17. The process of claim 11 , further comprising separating the functionalized polymer from at least a portion of the by-products of the functionalization reaction within a second kneader reactor.

18. The process of claim 17 , wherein said step of separating takes place at a temperature of from about 20 to about 200° C. and a pressure of from about 0.02 to about 2 atmospheres.

19. The process of claim 11 , wherein the polymerization takes place in at least one of a solution and a slurry system.

20. The process of claim 19 , wherein the monomer mixture, catalyst, polymer, and a diluent are subjected to kneading and/or granulating to thereby form the polymerization mixture within the polymerization reactor.

21. The process of claim 19 , wherein the polymerization mixture is subjected to deliquifying, quenching, and devolatilization prior to said functionalization.

22. The process of claim 21 , wherein said deliquifying, said quenching, and said devolatilization comprises processing the polymerization mixture within a deliquifying-quench extruder by subjecting the polymerization mixture, or a portion thereof, to a sequential series of steps including (a) compacting the polymerization mixture to force diluent entrained within the polymer to separate from the polymer while permittin

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Wang Yu Feng
• Hembree Richard D
• Mcdonald Jr Michael F
• Maier Joseph A
• Yeh Richard C M
• Gu Leming
• Shaffer Timothy D
• Wright Pamela J

Classifications

• C08F8/00

  Chemical modification by after-treatment (graft polymers, block polymers, crosslinking with unsaturated monomers or with polymers C08F251/00 - C08F299/00; of conjugated diene rubbers C08C) · CPC title

• B01J19/00 Primary

  Chemical, physical or physico-chemical processes in general; Their relevant apparatus · CPC title

• B01J2219/0004

  Processes in series · CPC title

• B01J19/1862

  placed in series · CPC title

• B01J19/20

  in the form of helices, e.g. screw reactors · CPC title