Abstract
This paper describes the process for
removing barrier layers and coatings (oxygen and carbon dioxide) from
polyethylene terephthalate (PET) substrates through a conventional
mechanical bottle recycling system. Varied wash chemistry and barrier
medium have been examined and the effect on residual multilayer material
or coating has been evaluated. Wash chemistry was found to be the
controlling factor in improving the external coating removal efficiency.
Delamination through mechanical working was found to be the controlling
mechanism for separating multilayer materials. The conclusion drawn from
our experiments is that the PPG Bairocade coatings were removed most
efficiently. Internal deposition techniques may contribute fewer residues
to the RPET, however substantiating this is difficult.
Introduction
PET resins are widely used in the food
packaging industry, in such products as bottles and films. PET bottles
have a large market share in the carbonated soft drink, fruit juice and
bottled water markets. These products have a shelf life of 8-12 weeks,
over this period the gas permeability properties of PET are sufficient.
However, alcoholic beverages are much more sensitive to oxygen and carbon
dioxide diffusion either into or out of the bottle.
When this sensitivity to migrating gases is
combined with the need for a longer shelf life, it is necessary to improve
on the gas permeability properties of PET. To overcome the excessive gas
ingress the bottle industry manufacturers have several options. The
bottles can be made from a polyester with lower gas permeability, such as
polyethylene naphthalate (PEN). In most cases these materials do not
reduce the gas permeability sufficiently.
A widely adopted technique is to utilise a
multilayer bottle construction. This method can be used to incorporate
thin layers of polymers that have low gas permeability, into a sandwich
structure where the barrier layer or layers are in the centre of the
bottle wall encapsulated by PET on either side. [1]
Other methods that have been employed are
to coat the external or internal walls of the bottle with materials that
lower the overall ingress of gas into the beverage. These techniques use
materials such as graphite carbon, silica and epoxy resins to achieve the
effect. [2]
This research was aimed at understanding
how the introduction of barrier coated or multilayer bottles into the
recycling stream will effect the final PET quality. This will help in
developing modifications to plant, processing conditions and wash
chemistry whilst processing these materials in order to minimise the
percentage of residual material in the RPET flake.
Materials and Methods
Materials
Bottles for these trials were supplied PPG
bairocade (functional coatings), Nylon & Oxygen scavenger multilayer,
nylon multilayer, Krones (surface SiOx deposition), Sidel ACTIS (internal
carbon deposition).
Trial Procedure
The multilayer and surface deposition
materials were all run with a constant wash chemistry of 2% NaOH and 0.02%
Oakite RC-7A detergent. The PPG Bairocade functional coated material was
processed with a modified wash chemistry of 2.5% NaOH, 1.5% Butyl Carbitol
and 0.1% Cetostearyl Alcohol (Teric).
Firstly, a hot caustic, whole bottle wash
was used, followed by wet granulation, flake wash and a centrifuge
separation prior to drying. Whole bottle wash NaOH concentration and
temperature was 1% and 70-80 o C respectively. Flake wash residence time
and temperature was 15min and 85-90 o C.
Barrier bottles were added into a pure PET
bottle stream at a 10-weight percent addition rate. This rate was chosen
to simulate 10% of the test bottles in the waste stream. The flake
produced was blended during processing and prior to testing to ensure even
dispersion of barrier material in the flake.
Laboratory testing of the processed flake
involved oven-aging 1.5 kg of flake at 230 o C for 1 hour and then visual
identifying and removing the barrier layer for quantitative parts per
million (ppm) determination.
Results and Discussion
For the Bairocade functional coatings, a
series of trials were conducted to optimise the wash chemistry composition.
This work improved the delamination and break-up from the PET substrate.
This allowed very effective separation through sink float techniques. The
high delamination and separation resulted in an approximate 99.96% removal
efficiency, the best result in this series of trials, as can be seen in
table 1.
Changes to the wash chemistry in the
laboratory made little difference with separating the multilayer nylon
materials shown in table 1. It was observed that the abrasion during
granulation, washing and centrifuge treatment were the main drivers for
delamination.
Furthermore the delamination of the
multilayer materials was higher than the removal rate. This was due to by
the density of the middle layer Nylon 1.02-1.15 being too high to float in
the sink float separation tank. It was found that an addition of a
hydrophobic frothing agent into the sink float tank could greatly improve
separation of such contaminants with densities higher than that of water.
The Krones barrier bottles were clear in
colour. It was not possible to identify the presence of coating using
standard contamination identification methods using oven aging, due to the
thermal stability of the SiOx layer. Since the SiOx barrier layer could
not be detected through conventional techniques, the processed flake was
subjected to Infrared (IR) spectroscopy. The samples did not display any
Si peaks in the IR spectrum. This could be due to the low levels of SiOx
initially present in the bottles.
The Sidel carbon coating was visible,
however removal was minimal. These coatings are very thin 0.1 micron or 3
milligrams to treat a 500ml bottle and do not contribute high levels of
contamination into the RPET. [3]
Conclusion
It was found that with PPG Bairocade
functional coatings the wash chemistry played a critical role in lifting
and separating the epoxy-amine coating from the substrate.
With multilayer barrier bottles mechanical
delamination was the variable controlling the removal efficiency. To
promote further removal efficiency with these bottle additional
centrifuges would need to be added. Otherwise the adhesion between the
layers could be reduced through material modification to promote
delamination during the recycling processing.
The Krones SiOx coated bottles exhibited no
visual or colour change during the standards testing. As the coating was
clear it is not possible to comment on its removal.
References
1. R. J. Judson, “Latest Economics of
High-Speed, In Line Barrier Coating of PET Bottles”, Nova-Pack Americas
– 98, Ohio, USA.
2. www.grm.org.miller3.html, 4/02/999.
3. Extract from Sidel, ACTIS Amorphous Carbon Treatment on Internal
Surface, Industrial Application presentation, 1999.
Key Word Index
PET Recycling, Barrier Coated Bottles,
Multilayer Bottles.
Table 1. Residual barrier
materials remaining in RPET flake after processing and removal
efficiencies.
| Material |
Wash
Treatment |
Residual
Barrier Layer (ppm) |
Removal
Efficiency (%) |
| PPG Bairocade Functional
Coating |
2.5% NaOH, 1.5% Butyl
Carbitol, 0.1% (Teric) |
4-8 |
99.96 |
| Multilayer Nylon &
Scavenger |
2% NaOH, 0.02% Oakite
RC-7A |
700 |
86 |
| Nylon |
2% NaOH, 0.02% Oakite
RC-7A |
546 |
94.54 |
| Krones SiOx Surface
Deposition |
2% NaOH, 0.02% Oakite
RC-7A |
None
detected |
Unknown |
| Sidel Internal Carbon
Deposition |
2% NaOH, 0.02% Oakite
RC-7A |
None
detected |
Unknown |

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