Patent DE685181C successfully refreshed from Google Patents.
Patent US4613484A successfully refreshed from Google Patents.
US4613484A
Expired / Lapsed
US
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Loop reactor settling leg system for separation of solid polymers and liquid diluent
Assignee: Phillips Petroleum Co
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Filing: 1984-11-30
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Granted: 1986-09-23
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Expires: 2004-11-30
Abstract
Abstract Method and apparatus for the separation of solid particulate polymer from liquid diluent comprising the use of one or more accumulator legs to which diluent is supplied, and separated diluent is recycled to the polymerization process.
Inventors
- 👤 C. A. Ayres
- 👤 John N. Scott, Jr.
- 👤 Fred T. Sherk
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 08:36
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/18; B01J19/1812; B01J19/1837; B01J8/00; B01J8/005; B01J8/007
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
222 words
An apparatus comprising: a loop reactor defining a fluid flowpath and comprising a series of interconnected alternating vertical and horizontal segments defining a flowpath adapted for a particulate solids-diluent slurry, and a solids-concentrating device for concentrating said particulate solids from said particulate solids-diluent slurry, comprising in operable sequence, a first elongated tube disposed at an angle α of about up to 45° from the vertical relative to said horizontal segments of said loop reactor comprising a first end having an opening defined therein and defining a passage therethrough, a second end having an opening defined therein, said ends disposed at opposite ends of said first elongated tube, said first elongated tube having a length:diameter ratio greater than 1, at least one inlet in said tube adapted for diluent feed thereinto, at least one outlet in said first elongated tube adapted for diluent removal, said outlet positioned a first distance from said first end along said first elongated tube, said inlet positioned a second distance along said first elongated tube, wherein said second distance is greater than said first distance; said second end further connected by fluid-open passage to a first end of a converging member and defining a passage therethrough, and a second elongated the adapted for fluid passage from said outlet to said loop and closably controllably connected to said loop.
Claim 2
Independent Claim
222 words
An apparatus comprising: a loop reactor defining a fluid flowpath and comprising a series of interconnected alternating vertical and horizontal segments defining a flowpath adapted for a particulate solids-diluent slurry, and a solids-concentrating device for concentrating said particulate solids from said particulate solids-diluent slurry, comprising in operable sequence, a first elongated tube disposed at an angle α of about up to 45° from the vertical relative to said horizontal segments of said loop reactor comprising a first end having an opening defined therein and defining a passage therethrough, a second end having an opening defined therein, said ends disposed at opposite ends of said first elongated tube, said first elongated tube having a length:diameter ratio greater than 1, at least one inlet in said tube adapted for diluent feed thereinto, at least one outlet in said first elongated tube adapted for diluent removal, said outlet positioned a first distance from said first end along said first elongated tube, said inlet positioned a second distance along said first elongated tube, wherein said second distance is greater than said first distance; said second end further connected by fluid-open passage to a first end of a converging member and defining a passage therethrough, and a second elongated the adapted for fluid passage from said outlet to said loop and closably controllably connected to said loop.
Claim 3
Dependent Claim
20 words
The apparatus of claim 1 wherein said first elongated tube has a length:inside diameter ratio of about 9:1 to 16:1.
Claim 4
Dependent Claim
20 words
The apparatus of claim 2 wherein said first elongated tube has a length:inside diameter ratio of about 12:1 to 14:1.
Claim 5
Dependent Claim
31 words
The apparatus of claim 5 wherein said first elongated tube is disposed at an angle α of about 22.5° from the vertical relative to said horizontal segments of said loop reactor.
Claim 6
Independent Claim
175 words
An apparatus comprising: a loop reactor comprising a series of interconnected alternating vertical and horizontal segments defining a fluid flowpath, and a solids-concentrating device adapted for concentrating particulate solids from a particulate solids-diluent slurry contained in said flowpath, comprising in operable sequence, a first elongated tube disposed at an angle α of about up to 45° from the vertical relative to said horizontal segments of said loop reactor comprising a first end having an opening defined therein, and a second end having an opening defined therein, said ends disposed at opposite ends of said elongated tube, said elongated tube defining a passage therebetween and having a length:diameter ratio greater than 1, an outlet in said tube adapted for liquid removal, said outlet positioned a first distance from said first end along said first elongated tube, said second end controllably connected to a first end of a converging member and defining a passage therethrough, and a second elongated tube adapted for fluid passage from said outlet to said loop and closably controllably connected to said loop.
Claim 7
Independent Claim
175 words
An apparatus comprising: a loop reactor comprising a series of interconnected alternating vertical and horizontal segments defining a fluid flowpath, and a solids-concentrating device adapted for concentrating particulate solids from a particulate solids-diluent slurry contained in said flowpath, comprising in operable sequence, a first elongated tube disposed at an angle α of about up to 45° from the vertical relative to said horizontal segments of said loop reactor comprising a first end having an opening defined therein, and a second end having an opening defined therein, said ends disposed at opposite ends of said elongated tube, said elongated tube defining a passage therebetween and having a length:diameter ratio greater than 1, an outlet in said tube adapted for liquid removal, said outlet positioned a first distance from said first end along said first elongated tube, said second end controllably connected to a first end of a converging member and defining a passage therethrough, and a second elongated tube adapted for fluid passage from said outlet to said loop and closably controllably connected to said loop.
Claim 8
Dependent Claim
20 words
The apparatus of claim 5 wherein said first elongated tube has a length:inside diameter ratio of about 9:1 to 16:1.
Claim 9
Dependent Claim
20 words
The apparatus of claim 6 wherein said first elongated tube has a length:inside diameter ratio of about 12:1 to 14:1.
Claim 10
Dependent Claim
31 words
The apparatus of claim 7 wherein said first elongated tube is disposed at an angle α of about 22.5° from the vertical relative to said horizontal segments of said loop reactor.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-09-22 | 1990-03-24 | 1990-09-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-09-22 | 1994-03-24 | 1994-09-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-09-22 | 1998-03-24 | 1998-09-23 | $7700.00 | Window Closed / Lapsed |