[특허]Catalyst slurry feeding assembly for a polymerization reactor

IPC분류정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	C08F-004/42
출원번호	US-0662264 (2003-09-15)
발명자 / 주소	Burns, David H. Verser, Donald W.
출원인 / 주소	Chevron Phillips Chemical Company, LP
인용정보	피인용 횟수 : 33 인용 특허 : 2

초록 ▼

A catalyst slurry for a polymerization reactor can be prepared in a mixing tank and the catalyst slurry fed to one or more storage tanks. The storage tanks can include agitators so that the catalyst slurry is maintained at an essentially homogeneous solids-to-liquid ratio. From the storage tank(s),

A catalyst slurry for a polymerization reactor can be prepared in a mixing tank and the catalyst slurry fed to one or more storage tanks. The storage tanks can include agitators so that the catalyst slurry is maintained at an essentially homogeneous solids-to-liquid ratio. From the storage tank(s), the catalyst slurry can be pumped to the polymerization reactor along a fluid passage having a flow meter. The flow of the catalyst slurry can be continuous and/or adjusted based on a measured parameter. The catalyst slurry may be continuously and reliability fed to the polymerization reactor.

대표청구항 ▼

1. A process for preparing a catalyst slurry and providing the catalyst slurry to a polymerization reaction zone, wherein the process comprises:forming a catalyst slurry from a solid catalyst and a liquid medium; maintaining the catalyst slurry at a substantially homogeneous solids-to-liquid ratio;

1. A process for preparing a catalyst slurry and providing the catalyst slurry to a polymerization reaction zone, wherein the process comprises:forming a catalyst slurry from a solid catalyst and a liquid medium; maintaining the catalyst slurry at a substantially homogeneous solids-to-liquid ratio; pumping the catalyst slurry into the polymerization reaction zone; measuring the flow of the catalyst slurry pumped into the polymerization reaction zone; determining the amount of the solid catalyst fed to the polymerization reaction zone in the catalyst slurry over a selected period; and altering the flow of the catalyst slurry pumped into the polymerization reaction zone at least partially in response to the measured flow of catalyst slurry and to the determined amount of solid catalyst fed over the selected period. 2. A process according to claim 1, comprising substantially continuously agitating the catalyst slurry to maintain the catalyst slurry at a substantially homogeneous solid-to-liquid ratio prior to pumping the catalyst slurry into the polymerization reaction zone.3. A process for preparing a catalyst slurry and providing the catalyst slurry to a polymerization reaction zone, wherein the process comprises:forming a catalyst slurry from a dry catalyst and a liquid medium; maintaining the catalyst slurry at a substantially homogeneous solids-to-liquid ratio; pumping the catalyst slurry into the polymerization reaction zone; measuring the flow of the catalyst slurry pumped into the polymerization reaction zone; altering the flow of the catalyst slurry pumped into the polymerization reaction zone at least partially in response to the measured flow; and pumping a liquid diluent in place of the catalyst slurry into the polymerization reaction zone. 4. A process according to claim 3, comprising resuming pumping catalyst slurry into the polymerization reaction zone.5. A process according to claim 1, further comprising operating the polymerization reaction zone to produce solid polymer particles.6. A process for preparing a catalyst slurry and providing the catalyst slurry to a polymerization reaction zone, wherein the process comprises:transporting a dry catalyst into a mixing zone by pneumatic transport; forming a catalyst slurry from the dry catalyst and a liquid medium in the mixing zone; maintaining the catalyst slurry at a substantially homogeneous solids-to-liquid ratio; pumping the catalyst slurry into the polymerization reaction zone; measuring the flow of the catalyst slurry pumped into the polymerization reaction zone; and altering the flow of the catalyst slurry pumped into the polymerization reaction zone at least partially in response to the measured flow. 7. A process for providing a catalyst slurry generally continuously to a polymerization reaction zone, wherein the process comprises:introducing a dry catalyst and a liquid medium into a mixing tank to form a catalyst slurry; agitating the catalyst slurry with one or more impellers in the mixing tank to maintain the catalyst slurry at a substantially homogeneous solid-to-liquid ratio; feeding the catalyst slurry to a storage tank; agitating the catalyst slurry in the storage tank so as to maintain the catalyst slurry at a substantially homogeneous solid-to-liquid ratio; and pumping the catalyst slurry substantially continuously into the polymerization reaction zone. 8. The process of claim 7, wherein the polymerization reaction zone has a plurality of catalyst feeds points spaced to facilitate generally even distribution of the catalyst slurry in the reaction zone.9. The process according to claim 7, comprising monitoring the amount of the catalyst slurry pumped into the polymerization reaction zone, and altering the flow rate of the catalyst slurry pumped into the polymerization reaction zone in response to the monitored amount.10. A process according to claim 7, comprising operating the polymerization reaction zone to produce solid polymer particles.11. A process according to claim 7, comprising transporting the dry catalyst into the mixing tank by pneumatic transport.12. A process for feeding catalyst slurry generally continuously to a polymerization reaction zone, wherein the process comprises:preparing a catalyst slurry of solid catalyst and a liquid medium; maintaining the catalyst slurry in a plurality of tanks at a substantially homogeneous solid-to-liquid ratio, wherein the plurality of tanks are maintained at a lower pressure than the polymerization reaction zone; and pumping the catalyst slurry from at least one of the tanks into the polymerization reaction zone. 13. A process for feeding catalyst slurry generally continuously to a polymerization reaction zone, wherein the process comprises:preparing a catalyst slurry of solid catalyst and a liquid medium; maintaining the catalyst slurry in a plurality of tanks at a substantially homogeneous solids-to-liquid ratio; pumping the catalyst slurry from a first one of the tanks into the polymerization reaction zone; detecting the amount of catalyst slurry in the first one of the tanks; and automatically switching to a second one of the tanks when the amount in the first one of the tanks is at a predetermined level. 14. A process for feeding catalyst slurry generally continuously to a polymerization reaction zone, wherein the process comprises:preparing a catalyst slurry of solid catalyst and a liquid medium; maintaining the catalyst slurry in a plurality of tanks at a substantially homogeneous solids-to-liquid ratio; pumping the catalyst slurry from at least one of the tanks into a plurality of locations along the polymerization reaction zone. 15. A process for feeding catalyst slurry generally continuously to a polymerization reaction zone, wherein the process comprises:preparing a catalyst slurry of two types of solid catalyst and a liquid medium; maintaining the catalyst slurry in a plurality of tanks at a substantially homogeneous solids-to-liquid ratio; and pumping the catalyst slurry from at least one of the tanks into the polymerization reaction zone. 16. A process according to claim 12, further comprising operating the polymerization reaction zone to produce solid polymer particles.17. The process of claim 12, wherein the reaction zone has a plurality of catalyst feeds spaced to facilitate even distribution of the catalyst slurry.18. A process according to claim 12, comprising transporting the solid catalyst into a mixing zone by pneumatic transport.

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이 특허에 인용된 특허 (2) 인용/피인용 타임라인 분석

Hottovy John D. ; Burns David H. ; Kufeld Scott E. ; Roetman Timothy ; Vaidyanathan Ragavan, Diluent slip stream to give catalyst wetting agent.
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이 특허를 인용한 특허 (33) 인용/피인용 타임라인 분석

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McElvain, Robert R.; Hottovy, John D.; Romig, Ralph W.; Verser, Donald W.; Burns, David H.; Tait, John H.; Peacock, Richard; Hein, James E.; Kufeld, Scott E.; Fenderson, Carl W.; Gupta, Anurag; Zellers, Dale A., Energy efficient polyolefin process.
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McElvain, Robert R.; Hottovy, John D.; Romig, Ralph W.; Verser, Donald W.; Burns, David H.; Tait, John H.; Peacock, Richard; Hein, James E.; Kufeld, Scott E.; Fenderson, Carl W.; Gupta, Anurag; Zellers, Dale A.; Zellers, legal representative, Penny A., Energy efficient polyolefin process.
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McElvain, Robert R.; Hottovy, John D.; Romig, Ralph W.; Verser, Donald W.; Burns, David H.; Tait, John H.; Peacock, Richard; Hein, James E.; Kufeld, Scott E.; Fenderson, Carl W.; Gupta, Anurag; Zellers, Dale A.; Zellers, legal representative, Penny A., Energy efficient polyolefin process.
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