METHOD FOR RECYCLING GLASS FIBRE REINFORCED PLASTIC
The present invention relates to a process for recycling glass fiber-reinforced plastics, in particular plastics based on polyamide, polybutylene terephthalate or polyethylene terephthalate, to recover both the monomers of the polymer and the glass used for the glass fibers.
1 . A process for recycling glass fiber-reinforced plastics (GRP), comprising the steps of
a) depolymerizing up to 80% by weight of the polymer matrix of glass fiber-reinforced plastics, removing the cleavage products resulting from the polymer matrix and enriching the remaining residues in a mixture of glass-based component, residual matrix, monomer, cleavage products and constituents problematic for recycling and
b) utilizing the organic proportion remaining in the residue at the end of process step a) as an energy source by using its heat of combustion for heating and melting the glass-based component and simultaneously for removing the organic constituents by conversion into gaseous combustion products.
2 . The process as claimed in claim 1 , wherein at least 50% by weight of the polymer matrix, is depolymerized.
3 . The process as claimed in claim 1 , wherein the glass fiber-reinforced plastics be employed in process step a) are previously collected in type-similar, fashion and employed in process step a) in type-similar, fashion.
4 . The process as claimed in of claim 1 , wherein the glass fiber-reinforced plastics components to be employed in process step a) are shredded into small pieces before use in the depolymerization.
5 . The process as claimed in of claim 1 , whereinthe glass fiber-reinforced plastics to be employed in process step a) are subjected to a cleaning before the depolymerization.
6 . The process as claimed in of claim 1 , wherein the glass fiber-reinforced plastics to be employed in process step a) is heated and after addition of additives subjected to pyrolytic cleavage in the absence of air.
7 . The process as claimed in of claim 1 , wherein the glass fiber-reinforced plastics to be employed in process step a) is depolymerized in the presence of water or alcohols.
8 . The process as claimed in of claim 1 , wherein during or after process step a) the cleavage products and/or the added hydrolysis/solvolysis liquids are distilled off by pressure reduction.
9 . The process as claimed in of claim 1 , wherein in process step a) at least 20% by weight of the original polymer matrix remains in the organic residue.
10 . The process as claimed in of claim 1 , wherein the cleavage products of the glass fiber-reinforced plasticsGRP (matrix) polymer matrix generated in process step a) by cleavage of the polymer chains are supplied to a subsequent repolymerization to produce a recyclate plastic having virgin material character.
11 . The process as claimed in of claim 1 , wherein the cleavage product is ε-caprolactam and the recyclate plastic is polyamide 6.
12 . The process as claimed in one or more of claim 1 , wherein the cleavage products are terephthalic acid and 1,4-butanediol/the dehydration product thereof tetrahydrofuran and the recyclate plastic is polybutylene terephthalate.
13 . The process as claimed in of claim 1 , wherein the cleavage products of the glass fiber-reinforced plastics polymer matrix generated in process step a) by cleavage of the polymer chains are at least in part also employed as fuel for the combustion operation in process step b).
14 . The process as claimed in of claim 1 , wherein the remaining at least 20% by weight of organic material, impurities, additives and decomposition products remaining on the glass constituents are removed from the glass reinforcement/glass melt in the combustion process in process step b)
15 . The process as claimed in of claim 1 , wherein additional energy is supplied in process step b).
16 . The process as claimed in claim 2 , at least 50% by weight and at most 80% by weight of the polymer matrix is depolymerized.
17 . The process as claimed in claim 3 , wherein the glass fiber-reinforced plastics to be employed in process step a) are previously collected in type-identical fashion and employed in process step a) in type-identical fashion.
18 . The process as claimed in claim 1 , wherein the remaining at least 20% by weight of organic material, impurities, additives and decomposition products remaining on the glass constituents are converted to CO 2 by oxidation.
19 . The process as claimed in claim 15 , wherein additional energy is supplied in process step b) by means of a gas burner.