IP Library Granted Patent US 10,584,208
Granted Patent B2
US 10,584,208 · App. 16/149,867 · Granted Mar 10, 2020

Flow reactor synthesis of polymers

Inventors: Patrick John Kinlen (Fenton, MO); Andrew M. Zweig (Ellisville, MO)
Assignee: THE BOEING COMPANY
C08G73/0266B01J19/0093B01J19/242B01J19/243B01J19/2415B01J19/2425C09D179/02B01J2219/0086B01J2219/00087B01J2219/00164B01J2219/00795B01J2219/00822B01J2219/00831B01J2219/00833B01J2219/00837B01J2219/00867B01J2219/00869B01J2219/00873B01J2219/00889B01J2219/00963B01J2219/24
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Quick Facts
Patent No.
US 10,584,208
App. No.
16/149,867
Granted
Mar 10, 2020
Kind
B2
Abstract

A flow reactor system and methods having tubing useful as polymerization chamber. The flow reactor has at least one inlet and at least one mixing chamber, and an outlet. The method includes providing two phases, an aqueous phase and a non-aqueous phase and forming an emulsion for introduction into the flow reactor.

Claims (33)

1. A system for polymerizing one or more monomers for producing a polymer salt, comprising:

an amount of tubing having:

at least one inlet port configured for receiving an emulsified reactant composition comprising an aqueous monomer solution and a non-aqueous solution; and

at least one outlet port configured for discharging a polymer salt;

a temperature controller sized to receive at least a portion of the amount of tubing;

a mixing chamber, the mixing chamber having an inlet and an outlet, the outlet fluidically coupled to the inlet port of the tubing, the mixing chamber configured to emulsify a reactant composition; and

at least one fluid flow control device fluidically coupled to the inlet of the mixing chamber.

2. The system of claim 1 ; wherein the at least one fluid flow control device comprises an aqueous monomer fluid flow control device and a non-aqueous fluid flow control device.

3. The system of claim 1 , further comprising a second mixing chamber fluidically coupled to the inlet of the tubing.

4. The system of claim 3 , further comprising a catalyst fluid flow control device fluidically coupled to the second mixing chamber or to the amount of tubing, the catalyst fluid flow control device configured to introduce a catalyst to the reactant composition.

5. The system of claim 1 , further configured to introduce organic solvent to the amount of tubing for recovering the polymer salt.

6. A system for continuous flow synthesis of polyaniline (PANI) salt, comprising:

an amount of tubing of an inner diameter, the amount of tubing having:

at least one inlet port configured for receiving an emulsified reactant composition comprising an aqueous aniline solution and a non-aqueous acid solution; and

at least one outlet port configured for discharging a polyaniline (PANI) salt;

a temperature controller sized to receive at least a portion of the tubing;

a mixing chamber, the mixing chamber having an outlet fluidically coupled to the inlet port of the tubing, and an inlet, the mixing chamber configured to emulsify a reactant composition; and

at least one fluid flow control device fluidically coupled to the inlet of the mixing chamber.

7. The system of claim 6 ; wherein the at least one fluid flow control device comprises an aqueous aniline fluid flow control device and a non-aqueous acid fluid flow control device.

8. The system of claim 6 , further comprising a second mixing chamber fluidically coupled to the inlet of the tubing.

9. The system of claim 8 , further comprising a catalyst fluid flow control device fluidically coupled to the second mixing chamber or to the amount of tubing, the catalyst fluid flow control device configured to introduce a catalyst to the reactant composition.

10. The system of claim 6 , further configured to introduce organic solvent to the amount of tubing for recovering the polyaniline (PANI) salt.

11. A system for diffusion limited synthesis of a conductive polymer salt, comprising:

an amount of tubing of an inner diameter providing diffusion limiting polymerization conditions, the amount of tubing having:

at least one inlet port configured for receiving an emulsified reactant composition comprising an aqueous monomer solution and a non-aqueous acid solution; and

at least one outlet port configured for discharging a diffusion limited polymerized conductive polymer salt;

a temperature controller sized to receive at least a portion of the tubing;

a mixing chamber, the mixing chamber having an inlet and an outlet, the outlet fluidically coupled to the inlet port of the amount of tubing, the mixing chamber configured to emulsify a reactant composition; and

at least one fluid flow control device fluidically coupled to the inlet of the mixing chamber.

12. The system of claim 11 ; wherein the at least one fluid flow control device comprises an aqueous monomer fluid flow control device and a non-aqueous acid fluid flow control device.

13. The system of claim 11 , further comprising a second mixing chamber fluidically coupled to the inlet of the tubing.

14. The system of claim 13 , further comprising a catalyst fluid flow control device fluidically coupled to the second mixing chamber or to the tubing, the catalyst fluid flow control device configured to introduce a catalyst to the reactant composition.

15. The system of claim 11 , further configured to introduce organic solvent to the amount of tubing for recovering the diffusion limited polymerized conductive polymer salt.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 2, 2018
From: KINLEN, PATRICK JOHN; ZWEIG, ANDREW M.
To: THE BOEING COMPANY
Reel/Frame 047041/0092 →
Continuity (4)
Division 15662503 · Jul 28, 2017
Continuation 15261441 · Sep 9, 2016
Continuation 14882073 · Oct 13, 2015
Related Publication 20190062502A1 · Feb 28, 2019