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Patent US4332748A successfully refreshed from Google Patents.
US4332748A
Expired / Lapsed
US
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Polyethylene recovery from broke
Assignee: Champion International Corp
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Filing: 1980-06-02
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Granted: 1982-06-01
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Expires: 2000-06-02
Abstract
Abstract A process of making polyethylene pellets from polyethylene broke comprising forming a polyethylene solvent-free aqueous slurry of said broke and defibering said slurry to produce a polyethylene slurry having a fiber to solid polyethylene ratio of no more 1:20, dehydrating said polyethylene slurry to less than about 15% water, and pelletizing the polyethylene.
Inventors
- 👤 Henry A. Fremont
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:07
CPC Classifications
B; B29; B29B; B29B17/00; B29B17/02; C; C08; C08J; C08J11/00; C08J11/04; C08J11/06; B29B2017/0213; B29B2017/0217; B29B2017/0251; B29K; B29K2023/00; B29K2023/04; B29K2023/06; B29K2711/00; B29K2711/12; B29L; B29L2009/00; B29L2009/005; C08J2323/00; C08J2323/02; C08J2323/04; C08J2323/06; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/62
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
102 words
A process for the recovery of polyethylene from a mixture comprising water, polyethylene fragments and cellulosic pulp fibers, said process comprising: defibering said mixture in a first hydropulper to remove a first quantity of said cellulosic pulp fibers; thermally drying the defibered mixture in a thermal tumbler dryer to dehydrate said defibered mixture to less than about 15% water, said thermal tumbler dryer having a stream of drying air flowing therein which serves to carry away a second quantity of cellulosic pulp fibers from said defibered mixture during said drying process; and pelletizing the polyethylene fragments remaining in said dehydrated defibered mixture.
Claim 2
Dependent Claim
102 words
A process for the recovery of polyethylene from a mixture comprising water, polyethylene fragments and cellulosic pulp fibers, said process comprising: defibering said mixture in a first hydropulper to remove a first quantity of said cellulosic pulp fibers; thermally drying the defibered mixture in a thermal tumbler dryer to dehydrate said defibered mixture to less than about 15% water, said thermal tumbler dryer having a stream of drying air flowing therein which serves to carry away a second quantity of cellulosic pulp fibers from said defibered mixture during said drying process; and pelletizing the polyethylene fragments remaining in said dehydrated defibered mixture.
Claim 3
Dependent Claim
54 words
The process of claim 1 wherein prior to the thermal drying step, the defibered mixture is passed through a second hydropulper to remove an additional quantity of said cellulosic pulp fibers from said defibered mixture, thereby reducing the fiber to polyethylene content of said defibered mixture to a ratio of no more than 1:20.
Claim 4
Dependent Claim
69 words
The process of claim 1 or 2 wherein said pelletizing step comprises the steps of: shredding the polyethylene fragments in a heated vortex to produce a molten mass of polyethylene; blowing air over said molten mass to remove cellulosic pulp fibers which appear on its surface; injecting a measured amount of water into said mass to explode it into uniform pellets; and cooling said pellets so that they harden.
Claim 5
Dependent Claim
41 words
The process of claim 1 or 2 further comprising the step of partially dehydrating the defibered mixture prior to thermally drying it by passing it over a dewatering screen so as to remove water and suspended clumps of cellulosic fiber therefrom.
Claim 6
Dependent Claim
39 words
The process of claim 3 further comprising the step of partially dehydrating the defibered mixture prior to thermally drying it by passing it over a dewatering screen so as to remove water and suspended clumps of cellulosic fiber therefrom.
Claim 7
Dependent Claim
64 words
The process of claim 3 wherein said mixture of water, polyethylene fragments and cellulosic pulp fibers further comprises extraneous particulate matter, said extraneous particulate matter remaining in said mixture throughout said process and being comingled with said polyethylene pellets at the completion of said process, further comprising the step of selectively screening said polyethylene pellets to separate them from said comingled extraneous particulate matter.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-05-31 | 1985-11-30 | 1986-06-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-05-31 | 1989-11-30 | 1990-06-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-05-31 | 1993-11-30 | 1994-06-01 | $7700.00 | Window Closed / Lapsed |