초록 ▼

The present invention relates generally to polyolefin production and to reducing volatile organic content (VOC) associated with the polyolefin. Techniques include the construction and implementation of a purge column model to calculate or estimate the VOC content in the polyolefin exiting the purge

The present invention relates generally to polyolefin production and to reducing volatile organic content (VOC) associated with the polyolefin. Techniques include the construction and implementation of a purge column model to calculate or estimate the VOC content in the polyolefin exiting the purge column. The techniques facilitate the design and operation of the polyolefin manufacturing process.

대표청구항 ▼

1. A method for operating a polyolefin manufacturing process, comprising: purging a recovered polyolefin stream comprising polyolefin particles and residual hydrocarbon in a purge column with a purge gas to remove a first portion of the residual hydrocarbon from the recovered polyolefin stream;disch

1. A method for operating a polyolefin manufacturing process, comprising: purging a recovered polyolefin stream comprising polyolefin particles and residual hydrocarbon in a purge column with a purge gas to remove a first portion of the residual hydrocarbon from the recovered polyolefin stream;discharging a polyolefin product stream from the purge column, the polyolefin product stream having a second portion of the residual hydrocarbon, wherein the second portion comprises a volatile organic content (VOC) of the polyolefin product stream; andcalculating an estimated value representing the VOC of the polyolefin product stream based on a flow rate of the polyolefin particles flowing through the purge column and a flow rate of the purge gas flowing through the purge column. 2. The method as recited in claim 1, comprising adjusting a residence time of the polyolefin particles in the purge column based on the estimated value representing the VOC. 3. The method as recited in claim 1, comprising adjusting a flow rate of the purge gas entering the purge column based on the estimated value representing the VOC. 4. The method as recited in claim 1, comprising adjusting a temperature of the polyolefin particles in the purge column based on the estimated value representing the VOC. 5. The method as recited in claim 4, wherein adjusting a temperature of the polyolefin particles in the purge column comprises adjusting an operating temperature of an upstream flash vessel that separates flashed hydrocarbon from a slurry discharging from a polyolefin reactor. 6. The method as recited in claim 4, wherein adjusting a temperature of the polyolefin particles in the purge column comprises adjusting an operating temperature of an upstream flash line heater that flashes hydrocarbon from a slurry discharging from a polyolefin reactor. 7. The method as recited in claim 1, comprising changing, based on the estimated value representing the VOC, a type of catalyst employed in a polymerization reactor that produces the polyolefin particles. 8. The method as recited in claim 1, wherein calculating an estimated value representing the VOC comprises iteratively driving a difference in flow values for material flow to and from the purge column to zero for all components of the purge column. 9. The method as recited in claim 8, wherein calculating an estimated value representing the VOC comprises: estimating an initial value of a specified product stream from the purge column; andvarying the initial value iteratively until the difference in flow values for material flow to and from the purge column is approximately equal to zero for all components of the purge column. 10. A method for operating a polyolefin manufacturing process, comprising: purging a recovered polyolefin stream comprising polyolefin particles and residual hydrocarbon in a purge column with a purge gas to generate a discharge stream comprising a first portion of the residual hydrocarbon and the purge gas and a polyolefin product stream comprising the polyolefin particles and a second portion of the residual hydrocarbon, wherein the second portion comprises a volatile organic content (VOC) of the polyolefin product stream;discharging the polyolefin product stream from the purge column;calculating an estimated value representing the VOC of the polyolefin product stream based on a flow rate of the polyolefin particles flowing through the purge column and a flow rate of the purge gas flowing through the purge column; andadjusting an operating condition of the purge column based on the estimated value representing the VOC. 11. The method of claim 10, comprising processing the polyolefin particles to form a polyolefin product. 12. The method of claim 10, wherein adjusting an operating condition of the purge column comprises adjusting a residence time of the purge column, a temperature of the purge column, or the flow rate of the purge gas stream, or a combination thereof. 13. The method as recited in claim 10, wherein calculating an estimated value representing the VOC comprises iteratively driving a difference in flow values for material flow to and from the purge column to zero for all components of the purge column. 14. The method of claim 10, wherein calculating an estimated value representing the VOC comprises: determining an initial value for a component mass flow rate of a purge gas stream entering a bottom stage of the purge column; andvarying the initial value iteratively until a difference in material flow to and from the purge column is approximately equal to zero for all components of the purge column. 15. The method of claim 10, wherein calculating an estimated value representing the VOC comprises: determining an initial value for a component mass flow rate of the polyolefin product stream discharging from the purge column; andvarying the initial value iteratively until a difference in material flow to and from the purge column is approximately equal to zero for all components of the purge column.