US2006178069A1PendingUtilityA1

Compacted olefin fibers

56
Assignee: BTG INT LTDPriority: Oct 4, 1996Filed: Jan 6, 2006Published: Aug 10, 2006
Est. expiryOct 4, 2016(expired)· nominal 20-yr term from priority
B29C 43/006B29K 2023/06B29C 2035/0877B29K 2105/243B29K 2105/06B29C 2035/0827D04H 1/554Y10T428/24826Y10T428/24994Y10T428/249942B29B 13/08B29K 2023/12D04H 1/4291Y10T442/69B29K 2105/25B29C 2071/022B29C 2791/005D04H 1/54B29K 2223/06Y10T428/31855Y10T428/249947D04H 1/44B29C 2035/085
56
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Claims

Abstract

A polyolefin plaque is made by hot compaction of an assembly of fibres of the oriented polymer. It has been found to be beneficial to subject the fibres to a prior crosslinking process. Hot compaction is then less temperature-sensitive and produces plaques with excellent hot strength properties. Preferably the fibres have been subjected to prior stages of irradiation and annealing, both in a non-oxidising environment, for example acetylene.

Claims

exact text as granted — not AI-modified
1 . A process for the production of a monolithic article in which process an assembly of fibres of an polyolefin oriented polymer is subjected to a compaction stage wherein the assembly of fibres is maintained in intimate contact at an elevated temperature sufficient to melt a proportion of the polymer, and is compressed, characterised in that prior to the compaction stage the fibres have been subjected to a crosslinking process.  
     
     
         2 . A process as claimed in  claim 1 , wherein the compaction stage comprises two distinct steps, namely a step of maintaining the assembly of fibres in intimate contact at an elevated temperature sufficient to melt a proportion of the fibre at a first, contact, pressure, and a subsequent compression step wherein the assembly is subjected to a second, compaction, pressure, higher than the contact pressure.  
     
     
         3 . A process as claimed in  claim 1 , wherein the compaction stage comprises a single step of maintaining the assembly of fibres in intimate contact at a given pressure and at an elevated temperature sufficient to melt a proportion of the fibres.  
     
     
         4 . A process as claimed in  claim 1 , wherein the crosslinking process is an irradiation crosslinking process involving an ionising step which comprises irradiating the fibres with an ionising radiation, and then an annealing step comprising annealing the irradiated polymer at an elevated temperature.  
     
     
         5 . A process as claimed in  claim 4 , wherein the irradiation step is carried out in an environment which is substantially free of oxygen gas and which comprises a monomeric compound selected from alkynes, and from alkenes having at least two double bonds.  
     
     
         6 . A process as claimed in  claim 5 , wherein said environment comprises acetylene.  
     
     
         7 . A process as claimed in  claim 4 , wherein the annealing step which follows irradiation is carried out in an environment which is substantially free of oxygen gas and which comprises a monomeric compound selected from alkynes, and from alkenes having at least two double bonds.  
     
     
         8 . A process as claimed in  claim 7 , wherein said environment comprises acetylene.  
     
     
         9 . A process as claimed in  claim 1 , wherein the fibres used in the process as formed from molten polymer.  
     
     
         10 . A process as claimed in  claim 1 , wherein the fibres have a weight average molecular weight in the range 10,000 to 400,000.  
     
     
         11 . A process as claimed in  claim 10 , wherein the fibres have a weight average molecular weight in the range 50,000 to 200,000.  
     
     
         12 . A process as claimed in  claim 1 , wherein the polyolefin polymer is selected from the group comprising polypropylene homopolymer, a copolymer containing a major proportion of polypropylene, polyethylene homopolymer and a copolymer containing a major proportion of polyethylene.  
     
     
         13 . A process as claimed in  claim 4 , wherein the irradiation step is effected at a temperature not exceeding 100° C.  
     
     
         14 . A process as claimed in  claim 13 , wherein the irradiation step is effected at a temperature in the range 0-50° C.  
     
     
         15 . A process as claimed in  claim 4 , wherein the ionizing radiation is selected from electron beam, ultraviolet and γ-radiation.  
     
     
         16 . A process as claimed in  claim 4 , wherein the radiation dose is in the range 0.5 to 100 MRads.  
     
     
         17 . A process as claimed in  claim 16 , wherein the radiation dose is in the range 2 to 20 MRads.  
     
     
         18 . A process as claimed in  claim 4 , wherein the polyolefin polymer is annealed at a temperature of at least 60° C.  
     
     
         19 . A process as claimed in  claim 4 , wherein the polyolefin polymer after the irradiation and annealing steps has a gel fraction of at least 0.4.  
     
     
         20 . A process as claimed in  claim 19 , wherein the polyolefin polymer after the irradiation and annealing steps has a gel fraction in the range 0.55 to 0.7.  
     
     
         21 . A process as claimed in  claim 2 , wherein the contact pressure is in the range 0.01 to 2 MPa, and the compaction pressure is in the range 0.1 to 50 MPa, but is higher than the contact pressure.  
     
     
         22 . A process as claimed in  claim 21 , wherein the contact pressure is in the range 0.3 to 0.7 MPa and the compaction pressure is in the range 0.6 to 7 Mpa, but is at least double the contact pressure.  
     
     
         23 . A process as claimed in  claim 3 , wherein the single pressure applied is in the range 0.1 to 10 MPa.  
     
     
         24 . A process as claimed in  claim 1 , wherein the proportion of the polymer which melts during the compaction stage is 10 to 50% by weight.  
     
     
         25 . A process as claimed in  claim 1 , which process employs an inorganic filler material, such that the filler is present in the compacted monolithic article in an amount up to 60 vol % of the article.  
     
     
         26 . A polyolefin polymer monolith prepared in accordance with the process of the invention, as claimed in  claim 1.

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