The bales consisting mostly of PET mostly of a single colour are delivered to plants where the bottles may be treated by a variety of processes to convert them into usable feedstocks. The preferred method for recycling this stream is mechanical recycle, a process in which the resin is remelted, filtered and extruded or molded into new PET articles, such as bottles, strapping or fibers.(Bottles or flakes may be exported from one country to another) If the PET feedstock is not pure enough for mechanical recycle, then chemical recycling back to monomers or oligomers is used.
Terephthalic acid (PTA) or
dimethyl terephthalate (DMT) and
ethylene glycol (EG), or
bis(2-hydroxyethyl) terephthalate (BHET) are popular reaction products. However, chemical recycling to other products is also done.
Physical recycling For physical recycling, especially for recycle to food contact applications, rigorous sorting and cleaning is required. In Switzerland, for example, the steps that the bottles follow are the following • metal separation (to protect the granulator) • granulation to "flake" • washing in hot water • flotation (which separates materials with density 6000 m/min, microfilaments, and micro-fibers are produced from virgin polyester only.
Simple re-pelletizing of bottle flakes This process consists of transforming bottle waste into flakes, by drying and crystallizing the flakes, by plasticizing and filtering, as well as by pelletizing. Product is an amorphous re-granulate of an intrinsic viscosity in the range of 0.55–0.7, depending on how complete pre-drying of PET flakes has been done. Special feature are: Acetaldehyde and oligomers are contained in the pellets at lower level; the viscosity is reduced somehow, the pellets are amorphous and have to be crystallized and dried before further processing. Processing to: • A-PET film for
thermoforming • Addition to PET virgin production •
BoPET packaging film • PET Bottle
resin by SSP • Carpet yarn •
Engineering plastic • Filaments •
Non-woven • Packaging stripes •
Staple fibre. Choosing the re-pelletizing way means having an additional conversion process that is, at the one side, energy-intensive and cost-consuming, and causes thermal destruction. At the other side, the pelletizing step is providing the following advantages: • Intensive melt filtration • Intermediate quality control • Modification by additives • Product selection and separation by quality • Processing flexibility increased • Quality uniformization.
Manufacture of PET-pellets or flakes for bottles (bottle to bottle) and A-PET This process is, in principle, similar to the one described above; however, the pellets produced are directly (continuously or discontinuously) crystallized and then subjected to a solid-state polycondensation (SSP) in a tumbling drier or a vertical tube reactor. During this processing step, the corresponding intrinsic viscosity of 0.80–0.085 dℓ/g is rebuilt again and, at the same time, the acetaldehyde content is reduced to 2 is necessary for full dull or semi dull yarn. In order to protect the spinnerets, an efficient filtration of the melt is, in any case is necessary. For the time-being, the amount of POY made of 100% recycling polyester is rather low because this process requires high purity of spinning melt. Most of the time, a blend of virgin and recycled pellets is used. Staple fibers are spun in an intrinsic viscosity range that lies rather somewhat lower and that should be between 0.58 and 0.62 dℓ/g. In this case, too, the required viscosity can be adjusted via drying or vacuum adjustment in case of vacuum extrusion. For adjusting the viscosity, however, an addition of chain length modifier like
ethylene glycol or
diethylene glycol can also be used. Spinning non-woven—in the fine titer field for textile applications as well as heavy spinning non-woven as basic materials, e.g. for roof covers or in road building—can be manufactured by spinning bottle flakes. The spinning viscosity is again within a range of 0.58–0.65 dℓ/g. One field of increasing interest where recycled materials are used is the manufacture of high-tenacity packaging stripes, and monofilaments. In both cases, the initial raw material is a mainly recycled material of higher intrinsic viscosity. High-tenacity packaging stripes as well as monofilament are then manufactured in the melt spinning process.
Drying PET polymer is very sensitive to hydrolytic degradation, resulting in severe reduction in its molecular weight, thereby adversely affecting its subsequent melt processability. Therefore, it is essential to dry the PET flakes or granules to a very low moisture level prior to melt extrusion. PET must be dried to <100 parts per million (ppm) moisture and maintained at this moisture level to minimize hydrolysis during melt processing. Dehumidifying Drying – These types of dryers circulate hot and de-humidified dry air onto the resin, suck the air back, dry it and then pump again in a closed loop operation. This process reduces moisture level in the PET down to 50ppm or lower. The efficiency of moisture removal depends on the air dew point. If the air dew point is not good, then some moisture remains in the chips and cause IV loss during processing. Infrared Drying polyester pellets and flakes – A new type of dryer has been introduced in recent years, using Infrared drying (IRD). Due to the high rate of energy transfer with IR heating in combination with the specific wavelength used, the energy costs involved with these systems can be greatly reduced, along with the size. Polyester can be dried and amorphous flake crystallized and dried within only about 15 minutes down to a moisture level of approx. 300ppm in one step, and down to <50 ppm using a buffer hopper to complete the drying in typically under 1 hour == Global statistics ==