Raw material composition for preparing oxygen carrier particles, oxygen carrier particles prepared by using same, and method for preparing oxygen carrier particles
US-2019170346-A1 · Jun 6, 2019 · US
US9050573B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9050573-B2 |
| Application number | US-201013514096-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2010 |
| Priority date | Dec 18, 2009 |
| Publication date | Jun 9, 2015 |
| Grant date | Jun 9, 2015 |
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The present invention relates to a method for monitoring the level of an ethylene polymerization catalyst slurry in a mud pot ( 2 ), whereby said catalyst slurry is prepared by introducing a solid catalyst and a liquid diluent in said mud pot ( 2 ), and whereby through sedimentation an interface ( 35 ) is formed between said diluent and the obtained catalyst slurry, characterized in that said interface ( 35 ) is monitored with Time Domain Reflectometry.
Opening claim text (preview).
The invention claimed is: 1. A method comprising: preparing a catalyst slurry by introducing a solid catalyst and a liquid diluent in a mud pot, whereby through sedimentation an interface is formed between said liquid diluent and the obtained catalyst slurry, and wherein the catalyst slurry is an ethylene polymerization catalyst slurry; and monitoring the level of the catalyst slurry in the mud pot by monitoring the level of said interface in the mud pot with Reflectometry using a reflectometer. 2. The method according to claim 1 , whereby said Reflectometry is also used for monitoring level of the liquid diluent in said mud pot. 3. The method according to claim 1 , whereby electromagnetic pulses are guided into said mud pot by at least two rigid or flexible conductors. 4. The method according to claim 1 , whereby said catalyst slurry is transferred to a mixing vessel for diluting said catalyst slurry to a concentration suitable for use in an ethylene polymerization reactor. 5. The method according to claim 1 , whereby said solid catalyst is a free-flowing catalyst. 6. The method according to claim 1 , whereby said liquid diluent is a hydrocarbon diluent. 7. The method according to claim 1 , whereby a pressure of between 4 barg and 16 barg is obtained in said mud pot by blanketing of said catalyst slurry with nitrogen. 8. A method comprising: introducing a solid catalyst and a liquid diluent into a mud pot and allowing sedimentation of solid catalyst particles to form a catalyst slurry, wherein a solid-liquid boundary is formed between the catalyst slurry and the liquid diluent; and measuring a level of the solid-liquid boundary in the mud pot with Domain Reflectometry using a reflectometer. 9. The method of claim 8 , wherein the Domain Reflectometry is Time Domain Reflectometry or Frequency Domain Reflectometry. 10. The method of claim 8 , wherein the Domain Reflectometry is Radar based Time Domain Reflectometry. 11. The method of claim 8 , wherein the Domain Reflectometry is Time Domain Reflectometry, wherein the Time Domain Reflectometry comprises measuring electromagnetic energy reflected from the solid-liquid boundary, and wherein the electromagnetic energy has a power of at most 2 Watt. 12. The method of claim 8 , further comprising measuring a level of the liquid diluent in the mud pot using Domain Reflectometry. 13. The method of claim 8 , wherein the solid catalyst has an angle of repose that is smaller than 38 degrees.
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