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A system and method for polymerizing olefin in a gas phase reactor into a polyolefin in presence of catalyst, measuring static charge in the reactor system; determining an indication of polyolefin fines in the reactor system, and adjusting operation of the reactor system in response to the indicatio

A system and method for polymerizing olefin in a gas phase reactor into a polyolefin in presence of catalyst, measuring static charge in the reactor system; determining an indication of polyolefin fines in the reactor system, and adjusting operation of the reactor system in response to the indication.

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1. A polyolefin reactor system comprising: a gas phase reactor configured to polymerize olefin into a polyolefin in presence of a catalyst;a static charge probe configured to measure static electricity in the gas phase reactor; anda control system configured to determine polyolefin fines accumulatio

1. A polyolefin reactor system comprising: a gas phase reactor configured to polymerize olefin into a polyolefin in presence of a catalyst;a static charge probe configured to measure static electricity in the gas phase reactor; anda control system configured to determine polyolefin fines accumulation in the gas phase reactor based on the measured static electricity and anticipated polyolefin fines accumulation in the gas phase reactor based on a transition to a different catalyst, and the control system configured to adjust an addition rate of antistat to the gas phase reactor in response to the determination. 2. The polyolefin reactor system of claim 1, wherein the static charge probe is disposed at a disengagement section of the gas phase reactor. 3. The polyolefin reactor system of claim 1, wherein the static charge probe is disposed at a reaction zone of the gas phase reactor. 4. The polyolefin reactor system of claim 1, wherein the static charge probe is configured to measure static electricity at a point in a top twelve inches of a fluidized bed in the gas phase reactor. 5. The polyolefin reactor system of claim 1, wherein the static charge probe is disposed on overhead piping from the gas phase reactor. 6. The polyolefin reactor system of claim 1, wherein the determination of polyolefin fines accumulation comprises a disturbance of the static electricity indicated by the static charge probe. 7. The polyolefin reactor system of claim 1, wherein the determination of polyolefin fines accumulation comprises a change in amount of polyolefin fines. 8. The polyolefin reactor system of claim 1, wherein the determination of polyolefin fines accumulation comprises an anticipated onset of an operating problem related to polyolefin fines. 9. The polyolefin reactor system of claim 1, wherein the control system is configured to adjust fluidization velocity through a fluidized bed in the gas phase reactor, and wherein the fluidized bed comprises the polyolefin and the catalyst. 10. The polyolefin reactor system of claim 1, comprising: a first lock hopper disposed at a first location along a reaction zone of the gas phase reactor for a first product withdrawal of the polyolefin from the gas phase reactor; anda second lock hopper disposed at a second location along a reaction zone for a second product withdrawal of the polyolefin from the gas phase reactor, wherein the control system is configured to adjust a ratio of a first rate of the first product withdrawal to a second rate of the second product withdrawal in response to the indication of polyolefin fines accumulation. 11. The polyolefin reactor system of claim 1, comprising a catalyst feed system configured to feed the catalyst to the gas phase reactor and to transition to feeding a different catalyst to the gas phase reactor without interrupting the polymerizing of the olefin to a polyolefin in the gas phase reactor. 12. The polyolefin reactor system of claim 1, comprising: a primary feed vessel configured to feed the catalyst to the gas phase reactor; andan intermediate feed vessel configured to feed a different catalyst to the gas phase reactor while the primary feed vessel is being prepared to feed the different catalyst to the gas phase reactor. 13. A reactor system comprising: a gas phase reactor configured to polymerize olefin into a polyolefin in presence of a catalyst;an overhead system configured to receive overhead gas from the gas phase reactor, the overhead gas having entrained polyolefin fines from the gas phase reactor;a plurality of static charge probes configured to measure static charge at different locations in the reactor system; anda control system configured to detect polyolefin fines accumulation in the reactor system based on the measured static charge and anticipated polyolefin fines accumulation in the reactor system based on a transition to a different catalyst, and the control system configured to adjust an addition rate of antistat to the reactor system in response to the detecting polyolefin fines accumulation. 14. The reactor system of claim 13, wherein detecting polyolefin fines accumulation comprises receiving an indication of a static electricity disturbance in the reactor system from one or more of the static charge probes. 15. A polyolefin reactor system comprising: a gas phase reactor configured to polymerize olefin into a polyolefin in presence of a catalyst;a catalyst feed system configured to feed the catalyst to the gas phase reactor and to transition to feeding a different catalyst to the gas phase reactor without interrupting the polymerizing of the olefin to a polyolefin in the gas phase reactor;a static charge probe configured to measure static electricity in the gas phase reactor; anda control system configured to determine polyolefin fines accumulation in the gas phase reactor based on the measured static electricity and to adjust an addition rate of antistat to the gas phase reactor in response to the determination. 16. The polyolefin reactor system of claim 15, wherein the determination of polyolefin fines accumulation comprises a disturbance of the static electricity indicated by the static charge probe. 17. The polyolefin reactor system of claim 15, wherein the determination of polyolefin fines accumulation comprises a change in amount of polyolefin fines. 18. The polyolefin reactor system of claim 15, wherein the determination of polyolefin fines accumulation comprises an anticipated onset of an operating problem related to polyolefin fines. 19. The polyolefin reactor system of claim 15, wherein the control system is configured to adjust fluidization velocity through a fluidized bed in the gas phase reactor, and wherein the fluidized bed comprises the polyolefin and the catalyst.