Patent US3384305A successfully refreshed from Google Patents.
US4686279A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Device and process for recovering polymer from a solution
Assignee: DSM IP Assets BV
•
Filing: 1986-03-10
•
Granted: 1987-08-11
•
Expires: 2006-03-10
Abstract
Abstract The invention relates to a device and a process for recovering polymer from a melt or solution containing volatile components. The device consists of an evaporating zone passing, via a metering device, which can function also as a pressure-reducing device, into a devolatilizing extruder. The metering and pressure-reducing device makes it possible also to process highly viscous melts of high-molecular polymers and to fill the extruder screws incompletely so that substantial devolatilization is realized in the extruder.
Inventors
- 👤 Nicolaas P. Nagtzaam
- 👤 Cornelis Bronke
- 👤 Albert J. H. Brasz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 19:49
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/06; C08F6/12; B; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/50; B29C48/76; B29C48/022; B29C48/03; B29C48/04; B29C48/285; B29C48/29; B29C48/295
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
215 words
A process for recovering polymer from a solution containing volatile solvents, high molecular weight polymers having a melt index lower than 2 and unreacted monomers comprising the combination of: preparing the polymer solution containing solvents in a reactor; feeding the polymer solution from the reactor to at least one separate evaporating zone through a first valve means positioned upstream of the evaporating zone to control upstream pressure and evaporating sufficient solvent to produce a concentrated polymer solution having 80-99 percent weight polymer; maintaining pressure in the evaporating zone while feeding the concentrated polymer solution from the evaporating zone to a second valve means positioned downstream from the evaporating zone; feeding the concentrated polymer solution from the second valve means to the feed section of a devolatizing extruder under reduced pressure from the pressure in the evaporating zone and maintaining a pressure difference between the evaporating zone and the feed section of the extruder so that the pressure difference is used as the driving force to feed the concentrated polymer solution via the second valve means while simultaneously isolating the feed section from upstream evaporating zone pressures; and adjusting the operating speed of the extruder so that the feeding of the concentrated polymer solution will incompletely fill the extruder at the feed section of the extruder.
Claim 2
Dependent Claim
215 words
A process for recovering polymer from a solution containing volatile solvents, high molecular weight polymers having a melt index lower than 2 and unreacted monomers comprising the combination of: preparing the polymer solution containing solvents in a reactor; feeding the polymer solution from the reactor to at least one separate evaporating zone through a first valve means positioned upstream of the evaporating zone to control upstream pressure and evaporating sufficient solvent to produce a concentrated polymer solution having 80-99 percent weight polymer; maintaining pressure in the evaporating zone while feeding the concentrated polymer solution from the evaporating zone to a second valve means positioned downstream from the evaporating zone; feeding the concentrated polymer solution from the second valve means to the feed section of a devolatizing extruder under reduced pressure from the pressure in the evaporating zone and maintaining a pressure difference between the evaporating zone and the feed section of the extruder so that the pressure difference is used as the driving force to feed the concentrated polymer solution via the second valve means while simultaneously isolating the feed section from upstream evaporating zone pressures; and adjusting the operating speed of the extruder so that the feeding of the concentrated polymer solution will incompletely fill the extruder at the feed section of the extruder.
Claim 3
Dependent Claim
20 words
A process as in claim 1, wherein the reduced pressure in the feed section of the extruder is substantially atmospheric.
Claim 4
Dependent Claim
24 words
A process as in claim 1, including the further step of venting volatile solvent and monomer components from the feed section of said extruder.
Claim 5
Dependent Claim
31 words
A process as in claim 1, wherein the volume of the extruder will be filled from a minimum of about 25% to a maximum of about 65% of the extruder volume.
Claim 6
Dependent Claim
21 words
A process as in claim 4, wherein from about 30% to about 50% of the volume of the extruder is filled.
Claim 7
Dependent Claim
17 words
A process as in claim 1, wherein the recovered polymer has a density less than about 0.935.
Claim 8
Dependent Claim
23 words
A process as in claim 1, wherein the pressure maintained n the evaporating zone will vary from about 1.5 to about 6 BAR.
Claim 9
Dependent Claim
19 words
A process as in claim 1, wherein the pressure maintained in the evaporating zone is at least 1.5 BAR.
References Cited (Backward Citations)
US3506640A
Cited
US3963558A
Cited
US4093795A
Cited
US4169929A
Cited
EP0027700A2
Cited
EP0068561A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-08-10 | 1991-02-09 | 1991-08-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-08-10 | 1995-02-09 | 1995-08-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-08-10 | 1999-02-09 | 1999-08-11 | $7700.00 | Window Closed / Lapsed |