Wire-wetting fall polymonization process for the production of polycarbonates

• US 5,589,564 A
• Filed: 02/01/1996
• Issued: 12/31/1996
• Est. Priority Date: 07/23/1993
• Status: Expired due to Term

• Current Assignee: Asahi Kasei Chemicals Corporation (Asahi Kasei Corporation)
• Original Assignee: Asahi Kasei Kogyo Kabushiki Kaisha (Asahi Kasei Corporation)
• Inventors: Kawakami, Yoshifumi, Okamoto, Hiroshige, Komiya, Kyosuke
• Primary Examiner(s): BOYKIN, TERRESSA M
• Application Number:
  US08/595,081
• Time in Patent Office: 334 Days
• Field of Search: 528/196, 528/198, 526/62, 526/64, 526/65, 526/67
• US Class Current: 528/196
• CPC Class Codes: B01J 19/245 placed in series
• CPC Class Codes: B01J 2219/00085 Plates; Jackets; Cylinders
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: C08G 64/205 characterised by the apparatus used
• CPC Class Codes: C08G 64/307 and phenols

Abstract

A method for producing an aromatic polycarbonate comprises feeding to a feeding zone (having a foraminous plate) at least one polymerizing material selected from the group consisting of a) a molten monomer mixture of an aromatic dihydroxy compound and a diaryl carbonate, and b) a molten prepolymer obtained by a process comprising reacting an aromatic dihydroxy compound with a diaryl carbonate, and allowing the polymerizing material to pass downwardly through the foraminous plate and fall along and in contact with a wire through a wire-wetting fall polymerization reaction zone, thereby effecting polymerization of the polymerizing material during the wire-wetting fall thereof. Colorless and high quality aromatic polycarbonates are thus stably produced at a high polymerization rate for a prolonged period of time, using an apparatus which has excellent sealing properties under high vacuum and maintenance of which is easy.

Claims

1. A method for producing an aromatic polycarbonate, which comprises:

feeding, to a feeding zone having a foraminous plate, at least one polymerizing material selected from the group consisting of;

a molten monomer mixture of an aromatic dihydroxy compound and a diaryl carbonate, and

a molten prepolymer obtained by a process comprising reacting an aromatic dihydroxy compound with a diaryl carbonate,

said foraminous plate having at least one hole, said feeding zone communicating, through said at least one hole, with a polymerization zone comprising a wire-wetting fall polymerization reaction zone, said wire-wetting fall polymerization reaction zone having at least one wire in correspondence with said at least one hole, said at least one wire being securely held at one end thereof in an upper end portion of said wire-wetting fall polymerization reaction zone and extending downwardly through said wire-wetting fall polymerization reaction zone, so that said polymerizing material fed to the feeding zone is enabled to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire toward the other end of said at least one wire, and

allowing said polymerizing material to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through a wire-wetting fall polymerization reaction zone, to effect a wire-wetting fall polymerization of said polymerizing material,

thereby obtaining a polymer at a bottom of said polymerization zone comprising said wire-wetting fall polymerization reaction zone.

2. A method according to claim 1, which further comprises recirculating, to said feeding zone having the foraminous plate, a part or all of said polymer obtained at the bottom of said polymerization zone, and allowing the recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby increasing the degree of polymerization of said recirculated polymer to a predetermined level.

3. A method according to claim 1, wherein the feeding of the polymerizing material to said feeding zone having the foraminous plate is continuously conducted, and which method further comprises continuously conducting a sequence of steps of recirculating, to said feeding zone having the foraminous plate, a part of said polymer obtained at the bottom of said polymerization zone, and allowing an admixture of the continuously fed polymerizing material and the recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby continuously effecting a wire-wetting fall polymerization of said admixture, while continuously withdrawing the remainder of said polymer obtained at the bottom of said polymerization zone.

4. A method according to claim 1, wherein said polymerizing material is the molten prepolymer.

5. A method according to claim 4, wherein said molten prepolymer is a molten second prepolymer which has been obtained by a process selected from the group consisting of:

(a) a free-fall polymerization process comprising introducing, to an introduction zone having a perforated plate, at least one starting material selected from the group consisting of;

a monomer mixture of an aromatic dihydroxy compound and a diaryl carbonate, and

a first prepolymer obtained by reacting an aromatic dihydroxy compound with a diaryl carbonate, and

allowing said starting material to pass downwardly through said perforated plate and fall freely through a free-fall polymerization reaction zone, thereby effecting a free-fall polymerization of said starting material during the free-fall thereof,

(b) an agitation polymerization process comprising agitating at least one starting material in a molten state in an agitation type polymerizer vessel, wherein said starting material is as defined above, thereby effecting an agitation polymerization of said starting material, and

(c) a thin film-state polymerization process comprising subjecting at least one starting material in a molten state to a thin film-forming treatment to form a thin film of said starting material, wherein said starting material is as defined above, thereby effecting a thin film-state polymerization of said starting material while allowing said thin film to maintain a thin film-state thereof, and

wherein said molten second prepolymer as the polymerizing material is subjected to said wire-wetting fall polymerization to obtain said polymer at the bottom of said polymerization zone.

6. A method according to claim 5, which further comprises recirculating to said feeding zone a part or all of said polymer obtained at the bottom of said polymerization zone, and allowing said recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby increasing the degree of polymerization of said recirculated polymer to a predetermined level.

7. A method according to claim 5, wherein, in said wire-wetting fall polymerization of said second prepolymer, the feeding of the second prepolymer to said feeding zone having the foraminous plate is continuously conducted, and which method further comprises continuously conducting a sequence of steps of recirculating to said feeding zone a part of the polymer obtained at the bottom of said polymerization zone, and allowing an admixture of the continuously fed second prepolymer in the molten state and the recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby continuously effecting a wire-wetting fall polymerization of said admixture, while continuously withdrawing the remainder of said polymer obtained at the bottom of said polymerization zone.

8. A method according to claim 4, wherein said molten prepolymer is a molten third prepolymer which has been obtained by a process selected from the group consisting of:

(d) an agitation and free-fall polymerization process comprising;

agitating a starting material in a molten state in an agitation type polymerizer vessel, said starting material being at least one member selected from the group consisting of;

a monomer mixture of an aromatic dihydroxy compound and a diaryl carbonate, and

a first prepolymer obtained by reacting an aromatic dihydroxy compound with a diaryl carbonate,

thereby effecting an agitation polymerization of said starting material to obtain a second prepolymer; and

introducing said second prepolymer in a molten state to an introduction zone having a perforated plate, and allowing said second prepolymer to pass downwardly through said perforated plate and fall freely through a free-fall polymerization reaction zone, thereby effecting a free-fall polymerization of said second prepolymer during the free-fall thereof, and

(e) an agitation and thin film-state polymerization process comprising;

agitating a starting material in a molten state in an agitation type polymerizer vessel, wherein said starting material is as defined above, thereby effecting an agitation polymerization of said starting material to obtain a second prepolymer; and

subjecting said second prepolymer in a molten state to a thin film-forming treatment to form a thin film of said starting material, wherein said starting material is as defined above, thereby effecting a thin film-state polymerization of said second prepolymer while allowing said thin film to maintain a thin film state thereof, and

wherein said molten third prepolymer as the polymerizing material is subjected to said wire-wetting fall polymerization to obtain said polymer at the bottom of said polymerization zone.

9. A method according to claim 8, which further comprises recirculating to said feeding zone a part or all of said polymer obtained at the bottom of said polymerization zone, and allowing said recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby increasing the degree of polymerization of said recirculated polymer to a predetermined level.

10. A method according to claim 8, wherein, in said wire-wetting fall polymerization of said third prepolymer, the feeding of the third prepolymer to said feeding zone having the foraminous plate is continuously conducted, and which method further comprises continuously conducting a sequence of steps of recirculating to said feeding zone a part of the polymer obtained at the bottom of said polymerization zone, and allowing an admixture of the continuously fed third prepolymer in the molten state and the recirculated polymer to pass downwardly through said foraminous plate and fall along and in contact with said at least one wire through said wire-wetting fall polymerization reaction zone, thereby continuously effecting a wire-wetting fall polymerization of said admixture, while continuously withdrawing the remainder of said polymer obtained at the bottom of said polymerization zone.

11. A method according to claim 5, wherein said agitation polymerization of said starting material is effected using at least one member selected from the group consisting of a vertical agitation type polymerizer vessel having agitating elements rotating on a vertically extending axis and a horizontal agitation type polymerizer vessel having agitating elements rotating on a horizontally extending axis.

12. A method according to claim 11, wherein said agitation polymerization of said starting material is effected using both of said vertical agitation type polymerizer vessel and said horizontal agitation type polymerizer vessel in this order.

13. A method according to claim 1, wherein said wire-wetting fall is conducted through a distance of 0.3 m or more.

14. A method according to claim 1, wherein said polymerizing material is allowed to pass downwardly through said foraminous plate at a flow rate in the range of from 10^-2 to 10² liters/hr per hole.

15. A method according to claim 13, wherein said polymerizing material is allowed to pass downwardly through said foraminous plate at a flow rate in the range of from 10^-2 to 10² liters/hr per hole.

16. A method according to claim 1, wherein said polymerization zone comprising said wire-wetting fall polymerization reaction zone further comprises a free-fall polymerization reaction zone on at least one side selected from an upstream side and a downstream side relative to said wire-wetting fall polymerization reaction zone in contiguous relationship.