Process for efficient polymer particle purging
A process comprising polymerizing olefin monomers and optionally comonomers in a first reactor vessel, thereby forming a raw product stream comprising polymerized solids, unreacted monomer and optionally comonomer, the polymerized solids comprising olefin polymer, volatile organic compounds (VOC) and catalyst system. Then the polymerized solids are contacted with a catalyst poison selected from carbon monoxide, carbon dioxide, oxygen, water, alcohols, amines, or mixtures thereof, thereby forming a passivated stream. The passivated stream is maintained in an agitated state within a second reactor. The passivated stream within the second reactor is then contacted with a circulating gas comprising unreacted monomer for a residence time, thereby reducing the concentration of VOC in the polymerized solids by at least 10 wt % compared to the level before entering the second reactor, thereby forming a purified olefin polymer solids stream.
1. A process comprising:
a. polymerizing olefin monomers and optionally comonomers in a two reactor system comprising a first reactor and a second reactor, where a polymerization product of the first reactor is routed to a second reactor where it is mixed with a polymerization product of the second reactor, thereby forming a raw product stream comprising polymerized solids, unreacted monomer and optionally comonomer, the polymerized solids comprising olefin polymer, VOC and a catalyst system;
b. routing the raw product stream to a storage silo, thereby forming a stored polymerized solids stream;
c. discontinuing polymerization in the second reactor;
d. routing the stored polymerized solids to the second reactor;
e. contacting the stored polymerized solids stream with a catalyst poison selected from carbon monoxide, carbon dioxide, oxygen, water, alcohols, amines, or mixtures thereof, thereby forming a passivated stream wherein the catalyst system is deactivated;
f. maintaining the passivated stream in an agitated state within a second reactor; and
g. contacting the passivated stream in the second reactor with a circulating gas comprising unreacted monomer present in an amount from 50.0 to 99.5 wt % based on the total weight of the circulating gas for a residence time, thereby reducing the concentration of VOC in the polymerized solids by at least 10 wt % compared to the level before entering the second reactor, thereby forming a purified olefin polymer solids stream, wherein the first and second reactor vessels are fluidized bed gas phase reactors.
2. The process of claim 1 wherein the passivated stream is maintained in the agitated state within the second reactor with the circulating gas.
3. The process of claim 1 wherein the passivated stream is maintained in the agitated state within the second reactor with mechanical agitation or stirring.
4. The process of claim 1 wherein the catalyst poison is contacted with the stored polymerized solids stream after leaving the storage silo but before it enters the second reactor.
5. The process of claim 1 wherein the catalyst poison is contacted with the stored polymerized solids stream after it has entered the second reactor.
6. A process comprising:
a. polymerizing olefin monomers and optionally comonomers in a first reactor vessel, thereby forming a raw product stream comprising polymerized solids, unreacted monomer and optionally comonomer, the polymerized solids comprising olefin polymer, VOC and a catalyst system;
b. contacting the polymerized solids with a catalyst poison selected from carbon monoxide, carbon dioxide, oxygen, water, alcohols, amines, or mixtures thereof, thereby forming a passivated stream, wherein the catalyst system is deactivated;
c. maintaining the passivated stream in an agitated state within a fluidized bed gas phase second reactor with a circulating gas comprising unreacted monomer present in an amount from 50.0 to 99.5 wt % based on the total weight of the circulating gas for a residence time, thereby reducing the concentration of VOC in the polymerized solids by at least 10 wt % compared to the level before entering the second reactor, thereby forming a purified olefin polymer solids stream, wherein the first reactor vessel is a fluidized bed gas phase reactor.