Addition of organic initiators during the pressure drop in vinyl chloride monomer polymerization reactions
View Patent ↗The invention pertains to a process to polymerize one or more monomers wherein one or more initiators and optionally one or more surfactants are added to a polymerization mixture when the pressure in the polymerization reactor is dropping. This process allows a shorter polymerization time due to a higher pressure drop rate at the end of the polymerization reaction. Moreover, the cooling capacity of the polymerization reactor is used more efficiently.
1. Process wherein two or more initiators are used to polymerize a mixture containing one or more monomers of which one is vinyl chloride monomer,
wherein the one or more monomers are polymerized at a polymerization temperature using an initiator with a half-life of more than 1 hour at the polymerization temperature,
and one or more additional initiators are added to the polymerization mixture at the same polymerization temperature when the pressure in the polymerization reactor is dropping due to the depletion of gas phase vinyl chloride monomer,
and said additional initiators have a half-life of less than 1 hour at polymerization temperature,
wherein addition of said one or more additional initiator is not before the pressure has become less than the pressure that was observed earlier at the same polymerization temperature,
with the proviso that the polymer formed is not subject to radio frequency dielectric heating in the presence of additional organic initiator.
2. A process according to claim 1 wherein the initiator added after the start of the pressure drop and/or during the pressure drop has a half-life of from 0.0001 hour to 1 hour at the polymerization temperature.
3. A process according to claim 2 wherein the additional organic initiator added after and/or during the pressure drop has a half-life of from 0.0001 hour to 0.05 hour at the polymerization temperature.
4. A process according to claim 1 wherein at least part of the initiators is added intermittently and/or continuously after the start of the pressure drop and/or during the pressure drop.
5. A process according to claim 1 wherein a surfactant is also added when the pressure in the polymerization reactor is dropping due to the depletion of the vinyl chloride monomer to reduce the formation of foam.
6. A process according to claim 2 wherein at least part of the initiators is added intermittently and/or continuously after the start of the pressure drop and/or during the pressure drop.
7. A process according to claim 3 wherein at least part of the initiators is added intermittently and/or continuously after the start of the pressure drop and/or during the pressure drop.
8. A process according to claim 2 wherein a surfactant is also added when the pressure in the polymerization reactor is dropping due to the depletion of the vinyl chloride monomer to reduce the formation of foam.
9. A process according to claim 3 wherein a surfactant is also added when the pressure in the polymerization reactor is dropping due to the depletion of the vinyl chloride monomer to reduce the formation of foam.
10. A process according to claim 4 wherein a surfactant is also added when the pressure in the polymerization reactor is dropping due to the depletion of the vinyl chloride monomer to reduce the formation of foam.
11. A process according to claim 1 wherein at least one initiator of said conventional initiating system is different from at least one initiator of said one or more additional initiators.
12. A process according to claim 1 wherein a half-life of said conventional initiating system is different from a half-life of said one or more additional initiators.
13. A process according to claim 1 wherein a half-life of said conventional initiating system is longer than a half-life of said one or more additional initiators.
14. A process according to claim 1 wherein a half-life of said conventional initiating system is more than one hour and a half-life of said one or more additional initiators is less than one hour.
15. A process according to claim 1 wherein a half-life of said conventional initiating system is more than one hour and a half-life of said one or more additional initiators is less than 0.05 hour.
16. A process according to claim 1 , wherein the polymerization temperature is at a pre-set temperature.
17. A process according to claim 1 , wherein the polymerization mixture in the first part of the polymerization reaction is a constant pressure and polymerization temperature.
18. A process according to claim 1 , wherein the pressure drop is observed towards the end of the polymerization process.