Continuous inverse emulsion polymerization process for uniform polymer size distribution
A continuous inverse emulsion polymerization process may involve combining an aqueous monomer composition with an oil composition in a premix vessel and allowing the aqueous monomer composition to interact with the oil composition in the premix vessel for a period of time effective to form a stable pre-emulsion. The stable pre-emulsion may then be homogenized to form a homogenized emulsion that is then polymerized to form a water-in-oil inverse emulsion polymer. By forming a stable pre-emulsion that is then homogenized, the resulting water-in-oil inverse emulsion polymer may have uniform and consistent polymer size distribution.
1. A continuous or semi-continuous inverse emulsion polymerization process, comprising:
combining an aqueous monomer composition with an oil composition in a premix vessel and allowing the aqueous monomer composition to interact with the oil composition in the premix vessel for a period of time effective to form a stable pre-emulsion;
conveying the stable pre-emulsion from the premix vessel to a homogenizer and homogenizing the stable pre-emulsion to form a homogenized emulsion; and
polymerizing the homogenized emulsion in a reactor to form a water-in-oil inverse emulsion polymer,
wherein homogenizing the stable pre-emulsion comprises homogenizing the stable pre-emulsion to provide the homogenized emulsion with a mean emulsion particle size ranging from about 0.1 to 5 microns and an emulsion particle size standard deviation less than 1 micron.
2. The process of claim 1 , wherein the mean emulsion particle size ranges from about 0.1 to 2 microns and the emulsion particle size standard deviation less than 0.5 microns.
3. The process of claim 1 , wherein the period of time ranges from about 5 seconds to 30 seconds.
4. The process of claim 1 , wherein the premix vessel has a monomer inlet through which the aqueous monomer composition is introduced into the premix vessel and an oil inlet through which the oil composition is introduced into the premix vessel, and at least one of the monomer inlet and the oil inlet defines a nozzle.
5. The process of claim 1 , wherein combining the aqueous monomer composition with the oil composition in the premix vessel comprises:
pressurizing the aqueous monomer composition and injecting the aqueous monomer composition under pressure into the premix vessel, and
pressurizing the oil composition and injecting the oil composition under pressure into the premix vessel,
wherein allowing the aqueous monomer composition to interact with the oil composition in the premix vessel comprises causing the aqueous monomer composition injected under pressure into the premix vessel to intermix with the oil composition injected under pressure into the premix vessel without agitating the aqueous monomer composition and the oil composition in the premix vessel using a driven agitator.
6. The process of claim 1 , wherein the homogenizer is a multi-stage homogenizer.
7. The process of claim 1 , wherein conveying the stable pre-emulsion from the premix vessel to the homogenizer comprises passing the stable pre-emulsion through a static mixer.
8. The process of claim 1 , wherein the reactor is a continuous stirred tank reactor.
9. The process of claim 1 , wherein the oil composition is selected from the group consisting of a petroleum oil, a natural oil, a synthetically derived oil, a mineral oil, a silicone oil, and combinations thereof.
10. The process of claim 1 , wherein the aqueous monomer composition includes a monomer selected from the group consisting of vinyl esters, alkyl acrylates, alkyl methacrylates, vinyl ethers, acrylonitrile, styrene, N-vinyl carbazole, vinyl halides, and combinations thereof.
11. The process of claim 1 , wherein at least one of the aqueous monomer composition and oil composition comprises a polymeric surfactant.
12. A system comprising:
a source of an aqueous monomer composition;
a source of an oil composition;
a premix vessel in fluid communication with the source of the aqueous monomer composition and the source of the oil composition, the premix vessel being configured to receive the aqueous monomer composition and receive the oil composition and allow the aqueous monomer composition to interact with the oil composition for a period of time effective to form a stable pre-emulsion;
a homogenizer in fluid communication with the premix vessel, the homogenizer being configured to receive the stable pre-emulsion from the premix vessel and homogenize the stable pre-emulsion to form a homogenized emulsion; and
a reactor in fluid communication with the homogenizer, the reactor being configured to receive the homogenized emulsion from the homogenizer and react the homogenized emulsion to form a water-in-oil inverse emulsion polymer,
wherein the homogenizer is configured to homogenize the stable pre-emulsion to provide the homogenized emulsion with a mean emulsion particle size ranging from 0.1 to 5 microns and an emulsion particle size standard deviation less than 1 micron.
13. The system of claim 12 , wherein the period of time ranges from about 5 second to 30 seconds.
14. The system of claim 12 , wherein the premix vessel has a monomer inlet through which the aqueous monomer composition is introduced into the premix vessel and an oil inlet through which the oil composition is introduced into the premix vessel, and at least one of the monomer inlet and the oil inlet defines a nozzle.
15. The system of claim 12 , further comprising:
a monomer pump configured to pressurize the aqueous monomer composition from the aqueous monomer composition source and inject the aqueous monomer composition under pressure into the premix vessel, and
an oil pump configured to pressurize the oil composition from the oil composition source and inject the oil composition under pressure into the premix vessel,
wherein the premix vessel is configured to allow the aqueous monomer composition to interact with the oil composition by causing the aqueous monomer composition injected under pressure into the premix vessel to intermix with the oil composition injected under pressure into the premix vessel without agitating the aqueous monomer composition and the oil composition in the premix vessel using a driven agitator.
16. The system of claim 12 , wherein the homogenizer is a multi-stage homogenizer.
17. The system of claim 12 , further comprising a static mixer positioned between the premix vessel and the homogenizer, wherein the stable pre-emulsion passes through the static mixer flowing from the premix vessel to the homogenizer.
18. The system of claim 12 , wherein:
the aqueous monomer composition is selected from the group consisting of vinyl esters, alkyl acrylates, alkyl methacrylates, vinyl ethers, acrylonitrile, styrene, N-vinyl carbazole, vinyl halides, and combinations thereof, and
the oil composition is selected from the group consisting of a petroleum oil, a natural oil, a synthetically derived oil, a mineral oil, a silicone oil, and combinations thereof.
19. A system comprising:
a source of an aqueous monomer composition;
a source of an oil composition;
a premix vessel in fluid communication with the source of the aqueous monomer composition and the source of the oil composition, the premix vessel being configured to receive the aqueous monomer composition and receive the oil composition and allow the aqueous monomer composition to interact with the oil composition for a period of time effective to form a stable pre-emulsion;
a homogenizer in fluid communication with the premix vessel, the homogenizer being configured to receive the stable pre-emulsion from the premix vessel and homogenize the stable pre-emulsion to form a homogenized emulsion; and
a reactor in fluid communication with the homogenizer, the reactor being configured to receive the homogenized emulsion from the homogenizer and react the homogenized emulsion to form a water-in-oil inverse emulsion polymer, wherein the reactor is a continuous stirred tank reactor.