4.2.2. Fluoropolymers (i.e. backbone containing C-F bonds)
4.2.2.1. Valuable Fluoropolymers with exceptional properties
This sub-section is devoted to polymers bearing C-F bonds within the backbone and it is divided into four parts. These unique specialty polymers are niche products (production: 330,000 tonnes/year
64 compared to >400 million tonnes/year of all polymers), known to be safe, bio-inert, persistent and not degradable under environmental conditions. These durable materials display outstanding properties,
56-64 prolong lifetimes, increase fire safety, reduce maintenance needs and keep good performances (even in extreme conditions or aggressive/corrosive media) where other materials fail. One example is the Challenger dramatic explosion in 1986, 73 seconds after liftoff, related to poly(thioether) seals which had too high Tg values. Since then, all shuttle packings and gaskets have been made of fluoroelastomers.
69Advantageously, they are the unique candidates displaying the best heat and oil resistance (e.g. aircraft fluids as Skydrol®)
68 (
Figure 5) and excellent flexibility. Essential for our daily life
63 and involved in many High-Tech areas, FPs are endowed with exceptional features,
56-64 their molar masses being able to reach several million g.mol
-1 (as PTFE). Because of the growing need for higher requirements and engineering materials which combine specific properties for high-tech applications, FPs are currently undergoing an increasing development.
70
One example is poly(vinylidene fluoride), PVDF, which satisfies stringent leachable limits and other national health regulations, ensuring that they are safe for use in water treatment. In addition, this FP is durable, withstanding high pressures while maintaining structural integrity.
Actually, these specialty polymers are also involved in specific UV and aging resistant coatings and have been involved in many other applications: i) wires and cables in wide domains such as aerospace (because of high limiting oxygen index value, PTFE coatings ensure fire retardancy to several hundred km-cables and connections in planes, insulation (insulation resistance ≥ 1500 MΩ.km), electrical and high frequency (5000 V) performance, coaxial cables for avionics and high temperature resistant cables for aero engine services.71 The resilience and inertness of crosslinked elastomers provide in exceptional performance to gaskets in shuttles72); ii) materials for Energy storage and conversion (as key-candidates for the energetic transition: cathode binders in Lithium ion batteries, proton exchange fuel cell membranes, backsheets of photovoltaic panels, electroactive (piezoelectric and electrothermal) devices,73 haptics, printed electronics, dielectrics, for virtual reality, actuators for artificial muscles, and are indispensable drivers of the European Green Deal], iii) chemical process industry (e.g., injection molded PVDF tower packing is used over and over in sulfuric acid and chlorine scrubber systems and does not lose its properties like other polymers when exposed to harsh chemistries and high temperature.), iv) transport (transmission fluids and specific seals and gaskets)57,74, telecommunications (optical fibers among more than 4 million km of undersea cables are carrying information via a huge network),75 food and water treatment, electronics,76 pharmaceutical and medical devices.77-82
FPs should only be involved in uses required for health, safety, or are critical for the functioning of society and no alternatives are available. 9,63,64,83-84 In addition, searching alternative materials would reduce the time required for toxicological analyses.
The most prevalent materials are PTFE,61 PVDF,73,85 poly(chlorotrifluoroethylene), PCTFE,86 and the copolymers based on tetrafluoroethylene, TFE, 87 and vinylidene fluoride, VDF,88 which can be either thermoplastics or elastomers.72 Usually, in their conditions of uses, FPs are safe, stable (thermally, chemically to UV and aging, and biologically), durable, non-toxic, non-bioaccumulative, insoluble in water and thus non-mobile, are hydrolytically stable, and are not subject to hydrolysis catalyzed or metabolized degradation. For these features, they are not considered as substances of very high concern (SVHC) and fulfil the 13 criteria (see section 4.2.2.3.).35,89-90 Furthermore, their relevant combinations of properties are not matched by any of the alternative hydrocarbon polymers, 9,63,83-84 hence making them so unique and valuable.
The regulatory agencies, such as Registration, Evaluation, Authorization and Restriction of Chemicals (REACH), 32 Toxic Substances Control Act (TSCA) and Japanese Existing New Chemical Substances Inventory (ENCSI) support initiatives aimed at regulating the substances of greatest concern. They will endeavor to contribute to the broad and complex scientific, technical but also economic forthcoming debate on those substances. Actually, FPs seem to be impacted by the upcoming restriction on PFASs under the EU REACH Regulation, published on February 2023.32
4.2.2.2. Improvement of FP production in more environmentally friendly processes
Because they are concerned about the negative aspects of fluorinated polymerization aids (FPAs or surfactants) currently used to replace PFOA, FP manufacturers have been overcoming the great challenge to produce FPs free from FPAs. They are currently searching solutions in both replacing such PFAs by non-FPAs and processing by reducing fluorinated effluents and gas emissions. Indeed, a few years ago, the Chemours and Dyneon companies developed and used Gen®ex and Adona®, respectively, though these FPAs have been found as traces in rivers and soils.
33 However, the regulatory agencies are currently pushed from various authorities in helping the industry to swiftly move towards sustainable technologies and many efforts from these FPs producers have been recently taken in two main strategies: i) absence of FPA, as well as matching the PLC criteria are more appropriate to specific syntheses (as FKM). Much progress has been observed in the last decade after several FP manufacturers modified their production using NFPAs (or surfactants) leading to major innovations by the whole industry (such as 3M,
91 AGC,
92 Arkema,
93 Chemours,
94-95 Daikin,
96 Gujarat Fluorochemicals
97-99, Solvay
100 and others in filing multiple patents claiming such a “NFPA Technology” for various products (
Table 1).
101
However, the use of NFPAs in a specific recipe (for example, in aqueous radical polymerization of M1 fluoromonomer, e.g., TFE), does not necessary lead to the same success for that of another M2 monomer; e.g., VDF or a mixture of various fluorinated comonomers). The legislation process should be focused on the use of FPAs and the emissions of fluorinated derivatives. In this regard, a regulatory decision tree was suggested
101 (
Figure 6), linked to the manufacturing FPs in presence or absence of such surfactants (with process abatement to get a PFAS concentration lower than 25 ppb
38), essential use criteria in terms of safety, performance, health, improvement of the process and alternatives.
Hence, FPs produced without any FPAs should be exempted for all uses across all industries including consumer applications as they raise no risk to Environment, to mammal and to the human health, in addition to the fact that FPs also match the PLC criteria.
ii) Manufacturing modification. The second action taken by many FP manufacturers aimed at changing their process to eliminate fluorinated side-products such as residual reactants, oligomers, low molar mass-derivatives and intermediates, aqueous residues and volatiles. Actually, improving the abatement processes and PFAS recovery in the manufacture of FPs have enabled the reduction of 99% of fluorosurfactant emissions since the 1990s 102 while recent studies have brought it as high as 99.99%.103 For example, though severe analyses were published in the last decade 104, the Arkema Company strongly reacted and announced that, since February 2023, this innovative solution made it possible to reduce C6F13-telomer sulfonates (6:2 FTS) emissions by more than 90% and that emissions of such a telomer now represents less than 1 kg per day 105 in the FP manufacture in Pierre-Bénite (France) without the use of any fluorosurfactants. Actually, by the end of 2024, a similar process will equip all its other production sites around the world.105
Other companies have also been modifying their process to significantly reduced their emissions, many of them having announced such strategies. 105-111 An abundant literature is available in relation to the control and treatment of emitted PFASs from industrial processes43-45 while many studies are still ongoing.39,113
4.2.2.3. Polymer of Low Concern criteria
More recently, the American Chemical Council led the Fluoropolymer industry Group (Fluoropolymergroup) to investigate a similar study on 14 additional fluorinated (co)polymers.90 FPs and the Stockholm Convention persistent organic pollutants (POP) criteria meet the persistence criterion only, but not the bioaccumulative, toxic, or mobile criteria.
According to OECD definition,1,35,114 the criteria of polymers of low concern (PLC) that result from the combined experience and knowledge of global regulatory authorities on predictive parameters of health and environmental hazards induced by polymers have been extensively reported in several reviews.114-116 Indeed, to be regarded as a PLC, a polymer must not have any known hazard classification while they also should commit to the following criteria:
i) a high average molar mass in number (Mn) and a minimum oligomer amount are the most important requirements for PLC assessment, as claimed by EU:115 “most potential health concern polymers have a low number average molecular weight, Mn, (< 1000 Da) and an oligomer content >1%.” The higher the amount of oligomers, the more the polymer eco-toxicological.114 Actually, by comparing the potential health concern of polymers with varying the oligomer percentage, “the distribution of potential health concern polymers showed an increased incidence of higher oligomer content that began at 5% for <1000 Da and 2% for <500 Da oligomeric content”.114
ii) Reactive functional groups (RFG) requirements.;
iii) solubility in solvents and in water lower than 10 mg.L-1;
iv) other criteria such as a low cationic density, not containing any CF2 or CF3 groups; being stable under the conditions in which it is used. The primary concern for such FPs is its degradation in the environment to release persistent, bioaccumulative or toxic products, not being a high molar mass water absorbing polymer (≥10,000 g.mol-1) and not having any known hazard classification.
Indeed, regarding the RFGs and RFG ratio to Mn,90,115-116 FPs fulfill the PLC criteria. PTFE most typically bears terminal –CF3 groups35 that is not considered as an RFG. Furthermore, Mn value is an important feature of biological effect because very large molecules (>1000–10 000 Da) are too big to cross the cellular membrane117-119 and thus cannot react with “target organs,” such as the reproductive system. Hence, as the Mn of a polymer increases, a reduced incidence of potential health concern effects might be expected,114 and, as a proof, expended PTFE (e-PTFE) materials are currently used for stents, cardiovascular prostheses, and many other medical items. 80-81
In contrast and as expected, a polymer is not suitable to the PLC criteria if it decomposes considerably, degrades or depolymerizes during use. In other words, it undergoes a deep modification into simpler, lower molar mass-chemicals as the result of oxidation, hydrolysis, heat, sunlight, attack by solvents or microbial action or any other reaction(s). Indeed, FPs are resistant to such reactions/decompositions.
59 Based on such relevant features and above PLC criteria, Henry et al.
35 supplied key-evidences on four main FPs (PTFE, FEP, PFA and ETFE) matching the 13 PLC criteria.
120 By gas chromatography/mass spectrometry (GC/MS) and liquid chromatography/mass spectrometry (LC/MS) analyses, these authors characterized the extractible fractions from these FPs and detected less than 2 ppm leachable from PTFE (
Table 2).
35 As expected, since the monomers are gases, they were not detected.
Advantageously, as most FPs, PTFE is insoluble in water and, therefore, is not mobile in the environment. Using the descriptive solubility table for the US Pharmacopeia,121 the water solubility of PTFE would be classified as insoluble (10–5 mg.L-1 or 0.01 mg.L-1) to very slightly soluble (10–4 mg.L-1 or 0.1 mg.L-1).
The polymer policies of 10 countries, including the EU REACH handling of polymers, were examined
114 and concluded that “Polymers with <1% of M
n <1000 Da and low water extractivity are not able to cause systemic effects which are toxicologically or ecotoxicologically relevant.” In the case of high molar mass-FPs, such characteristics are not observed (
Table 2).
Among all FPs, PTFE is not a substance currently registered under REACH regulations supplying the definition of a polymer substance: “a molecule that contains a sequence of at least 3 monomer units, which are covalently bound to at least one other monomer unit or other reactant”.122 But, because PTFE, as all FPs, is an identifiable organic substance, the suggested Universal Basic Asset (UBA) framework for assessment using the proposed PMT criteria (persistent, mobile and toxic) would be applicable. Moreover, PTFE is highly stable in the environment and is resistant to thermal degradation. Being stable for years at temperatures up to 260 °C; 35,123,124 it is stable to hydrolysis, oxidation, and light, as well as to anaerobic and aerobic degradations.125 Therefore, PTFE would fulfill the UBA’s proposed persistence criterion.
As stated by USEPA, regarding PFAS and PFCA, the regulatory agency suggests a clarification about the nature of the linkage, stating “How these materials are incorporated into the polymer is immaterial (they may be counter ions, terminal/end capping agents, or part of the polymer backbone).”126 Surprisingly, the key characteristic is the presence of a –CF3 group that is attached to, or forms part of, the polymer backbone and “this link (between the polymer backbone and the –CF3 group) is susceptible to degradation and cleavage.”126 Thus, in a USEPA’s report, the presence of –CF3 group is relevant since it is a structural alert to consider potential degradation products.127 This statement is quite surprising since a CF3 end-group prevents from depolymerization by unzipping.59
As listed in
Table 2, these FPs are not subject to degradation.
Another advantage of PTFE deals with its non-toxicity. Thanks for a too high (several million) average M
n of PTFE mentioned above, it cannot cross the cellular membrane, indicating it is not toxic or bioavailable. Indeed, this polymer has been extensively tested in the European Union and USA to allow commercial applications for global medical device regulations, food contact, and surgery.
77-81 Furthermore, FPs contain none or tiny monomer(s) (which are gaseous), oligomer(s), and leachable amounts and no reactive functional groups with high toxicity (
Table 2).
35 These comparisons of PLC and various regulatory assessment criteria demonstrate that, in contrast to conventional PFASs, high molar mass-FPs display quite different characteristics. Therefore, they should fall in a separate class of materials that must be determined on their own features.
More recently, the American Chemical Council led the Fluoropolymer industry Group (Fluoropolymergroup) to investigate a similar study on 14 additional fluorinated (co)polymers.90 FPs and the Stockholm Convention persistent organic pollutants (POP) criteria meet the persistence criterion only, but not the bioaccumulative, toxic, or mobile criteria. Actually, their physico-chemical properties prevent bioavailability, bioaccumulation, toxicity, and degradation. Presently, 96 % of FPs fulfill these 13 PLC criteria.
4.2.2.4. Recycling, End of Life and Reuse of FPs
Recycling is the re-introduction of utilized compounds (or polymers) into the cycle of products (i.e., polymers in the context). They are collected, sorted and refined to be re-used as materials or energy source. Recycling should help to preserve resources and to avoid waste.128-130 Indeed, the recycling of plastics is a real challenge131-133 since only ca. 9% of polymers is recycled, less than three time more that of FPs.134 The global plastics production was 460 million tonnes (Mt) in 2021,131 predicted to reach 1120 Mt annually by 2050132 and should increase up to 1231 Mt by 2060. In the 2000-2019 period, the growth of plastics has outpaced that of economic growth by almost 40%. MacLeod et al.133 highlighted the global threat induced by the plastic pollution, based on the high environmental persistence of plastics. In contrast to commodity polymers, the consumption of FPs represents a quite small volume (estimated to 330,300 metric tonnes in 202164, hence representing less than 0.1% among all polymers). In 2015, its global consumption was 270 kt evidencing a 22.2 % increase since then. Actually, the global situation on the fate of FP waste is as follows: 83.5% of incineration, 13.1% landfill and 3.4% of recycling,134-135 briefly summarized hereafter.
i). Different techniques of recycling. FP waste from commercially available and industrial waste manufacturers are either pre-sorted or arise from dismantling processing or can also be incinerated for energy recovery. Fractions of pre-sorted FP waste are devoted to recycling, either to be exported for recycling in various countries134-136 or to domestic recyclers. Other recycling includes sintering, re-grinding or chemical recycling of FP materials. Four main ways of recycling are possible:128 i) primary (or mechanical) recycling; ii) secondary recycling; iii) tertiary recycling and iv) quaternary (or energy) recycling.
ii) Decomposition and recycling of FPs
Several examples are supplied here after:
PTFE. The thermal degradation and pyrolysis of PTFE was studied by many authors. In 1947, it was pioneered by Lewis and Naylor (under vacuum at 600 °C);
137 9 years later, by Wall and Michaelson (at 450-510 °C, under the presence of various gases),
138 then reported by Simon and Kaminski
139 (who pyrolyzed PTFE at 500–600 °C in a fluidized bed reactor, the primary products of decomposition being TFE and
•CF
2• bisradicals) and comprehensively described by Ellis et al.,
140 followed by Schlipf and Schwalm,
141 further up dated by Puts and Crouse,
142-143 carefully reviewed by Lakshman and Chakraborty in 2015 in a book.
144 Puts and Crouse,
142-143 could deeply detect and quantify the released fluorinated compounds (especially fluoroolefins and octafluorocyclobutane, OFCB) in the pyrolysis of PTFE from 35 °C to 800 °C in presence or absence of various metals or salts. These authors highlighted that, in absence of salts, TFE was produced in 98% while the nature of the salt induced other released gases with the influence of inorganic oxides of Al, Cr, Co, Cu, Fe, Ga, In, La, Mn, Ni, V, Zn and Zr (
Scheme 2).
142-143
Industrially, while various thermal processes (smoldering, pyrolysis, open burning, etc) were claimed in the patent literature (recently summarized),
136 reuse of fluoromonomers have scarcely been reported, as scaled up in a pilot plant at Dyneon Company,
145-146 (
Figure 7) via a robust process so-called “
FP upcycling technology” yielding more than 90% TFE/HFP.
This technology was scaled-up into a new demonstration plant (capacity is presently >500 tonnes year).
Recycling of other thermoplastics. The Arkema Company141-142 claims to use PVDF copolymers as processing and recycling aid (PPRA) for polyethylene and polypropylene films, pipes, cables, and injection molded parts. Such a PPRA increases output and flow, enhances surface finish, reduces extruder pressure and allows a steady gauge control and a processing at lower temperatures. This company has involved a process which enables 20-30% only of recycled materials before losing some feature and being reprocessed up to 90 or even 100% recycled materials to make such above items.147 Materials already containing the PPRA recycle behave almost the same as a virgin material in which polymer processing aid (PPA) was added as a master batch at the extruder.148 PVDF and VDF copolymers are currently assisting the reprocessing of high-volume polyolefins as a PPRA. In addition, Takahara’s group 149 reported that PVDF used for fishing lines could not be degraded by UV radiation and biodegradation and thus, may be recycled after use.
Recycling of Fluorinated Elastomers. The recycling of fluorinated elastomers has been reported in a few studies, well-summarized by Schuster et al.150 These authors reported only two relevant methods to achieve the recycling of poly(VDF-ter-HFP-ter-TFE) terpolymers (also named FKM) in an industrially acceptable way by i) milling FKM into fine powders to be mixed to virgin FKM and ii) the mechanical devulcanization of FKM, followed by successive compounding with virgin rubber. Both techniques give suitable thermostable products by preserving the mechanical features of original FKM. Indeed, these authors’ review cites many patents mainly while the quoted articles just refer to the degradation and not to de-vulcanization. These authors concluded that recycling FKM is possible and leads to products with competitive properties to those obtained in presence of virgin FKM. But, as known, Schuster et al.150 stated that fluorinated elastomers are usually crosslinked and thus recycling is rather complex in addition to the fact that they also contain fillers and additives.
Degradation and recycling of perfluorosulfonic acid membranes. Another key-functional FP is a copolymer based on TFE and a perfluoroalkyl sulfonyl fluoride vinyl ether further processed into proton exchange membranes for fuel cells, PEMFC, such as Nafion®, Flemion®, Fumion and Aquivion®, called perfluorosulfonic acid (PFSA) membranes (
Figure 8).
151 These high performance polymers are also involved in chloro-alkali process to produce chlorine and sodium hydroxide from brine, desalination for drinkable waters, and electrolyzers able to produce “clean” hydrogen from water. Though the thermal degradation of Nafion® N117 membrane was reported by Feng et al.
152 or by Zaton et al.
153, its recycling is really challenging.
Nowadays, no alternative is foreseen to be able to substitute such highly performance materials,9,59,63,83-84 essential to the functioning of the hydrogen value chain and electrolyzers. These are produced and used in a highly controlled industrial environment, where their emissions are negligible and, due to their high initial price, their reusability and recyclability are actively investigated. So far, a patent from Grot154 (by dissolving the membrane and separating the components), a report from Park 155 and a British Research and Innovation project, called Frankenstack156 (dealing with the recovery and reuse at the end of the lifecycle membrane) are the only documents describing the recycling of PFSA membrane.
4.2.2.5. Chemical recycling to monomer and reuse of the released fluoromonomers. The chemical recycling of FP to fluoromonomer (CRM) is a real challenge. One example is illustrated by
Scheme 2 that represents the depolymerization of PTFE into TFE or other fluorinated compounds according to the conditions. Actually, the generated TFE could be involved in various reactions enabling to close the loop: i) in radical homopolymerization initiated by peroxides or persulfates to lead to PTFE
157; ii) by conventional radical copolymerization of either HFP
158 or isobutyl vinyl ether (iBuVE)
159 to produce either poly(TFE-
co-HFP) copolymer (or FEP) or alternated poly(TFE-
co-iBuVE) copolymer (as commercially available Zeffle® homologues
160), and finally iii) under reversible addition−fragmentation chain-transfer (RAFT) copolymerization of TFE and iBuVE, controlled by a xanthate, to yield well-defined poly(TFE-
co-iBuVE) copolymers.
159
Anastasaki et al.
161 reported the catalyst-free depolymerization of poly(2,2,2-trifluoroethylmethacrylate), PTFEMA, at 180 °C. This polymer was previously synthesized by reversible addition−fragmentation chain-transfer polymerization (RAFT) of TFEMA controlled by a trithiocarbonate (TTC). The kinetics of depolymerization, monitored by
1H NMR spectroscopy, evidenced the unzipping reaction and evidenced that at the end of the reaction only TFEMA and the TTC remained in the flask (
Figure 9). Though it required heat, that reaction did not need any toxic reactants.
4.2.2.5. Reuse of degraded FP
Bai’s team 162 described that commercially available FKM elastomer [poly(VDF-co-HFP) or poly(VDF-ter-HFP ter-TFE) fluoroelastomers, Mn > 300,000 g.mol-1], the average molar mass in number and dispersity of which were Mn=134,000 g.mol-1 and PDI=3.7 (while the VDF:HFP molar ratio was 3:1) could undergo a tertiary recycling yielding to cooligomers. The Mn of these latter were ranging between 3,300 and 10,400 g.mol-1. This reaction occurred in presence of sodium hydroxide, hydrogen peroxide and triethyl ammonium chloride. These transparent dicarboxyl telechelic cooligomers were first chemically changed into diacrylates and then photocrosslinked. The resulting network exhibited suitable mechanical and hydrophobic properties.162
A more recent work on the use of FEP waste for transparent soils was achieved by the coating of specific terpolymers onto such waste (thanks to Fluorine-Fluorine interactions). The growing of lettuce roots was monitored by optical system and the roots were able to live in such an environment. 163
4.2.2.6. Incineration
Incineration is the last method to process end of life of FPs. Recent studies on the disposal of end-of-life PTFE have highlighted the incineration to be an appropriate way to dispose of FP too, with no environmental concern. It is a high-temperature flaming process, happening in open air space, whereas smoldering is a flameless combustion process that occurs on the surface of a condensed fuel. While both methods can be utilized to decompose fluorinated waste, the main difference is that smoldering is self-sustaining and, hence, is more energy efficient compared to incineration which needs a continuous energy input.
The incineration or combustion, differs from thermolysis in that a source of fuel is used in order to purposefully favor a complete degradation of FPs (as a source of trifluoroacetic acid or acetate, TFA, and chlorodifluoroacetic acid, CDFA).140 Furthermore, due to the high temperatures and oxidizing conditions used, it is unlikely to produce environmentally significant levels of TFA or TFA precursors. On the other hand, low-temperature burning of domestic waste, as an important source of furans and polychlorinated dioxins to the atmosphere, may analogously be a huge source of fluorinated acids.
Incineration has been adopted by various countries.
134-135,164-165 In the case of Norway,
165 though the municipal solid waste incineration (MSWI) conditions are achieved at about 850 °C, emissions of FP degradation products from household waste incineration have not been investigated yet. However, on the laboratory scale, the decomposition of PTFE and other FPs was comprehensive studied in the 700-1050 °C temperature range, yielding various main released products such as CF
4, CHF
3, C
2F
6, TFE, HFP and OFCB (
Table 3).
124, 140,165-171
Most of these substances are non-toxic, but highly toxic ones like perfluoroisobutylene (PFIB) or fluorophosgene may possibly be released under some severe conditions.
Wang et al. 172 suggested that PFASs may be generated from FP waste via a MSWI process, probably at temperatures lower than 500 °C. Thanks to its high thermal and chemical stabilities, PTFE is inert in the environment and Taylor et al.173 found that municipal waste incinerators operating with an average gas temperature of 1000 °C can be used to totally decompose PTFE.
In contrast, in Germany, Aleksandrov et al.
174 reported that the incineration of PTFE, using best available techniques (BAT), did not release any PFAS. By comparing with the possible formation of 31 PFAS compounds as references, these authors noted that PTFE could almost fully decomposed into fluorine (as HF) and concluded that the municipal incineration of PTFE should be considered as an acceptable form of waste treatment. They tested for the presence of 31 different PFASs and 11 of these were detected but deemed to be due to contamination from the environment. A constant mass flow of wood pellets was utilized while these authors added PTFE into the reactor to maintain a consistent thermal profile, as shown in
Figure 10.
Furthermore, the Dutch Institute for Public Health and Environment (RIVM) 164 drew slightly fewer concrete conclusions, mentioning that, although it can be assumed that the polymers are destroyed with the gasification process, this does not provide enough information on the kind and degree of by-products formed and on the rate of mineralization.
In EU, the overall situation of the fate of collected FP waste involved in recycling, recovery, reuse and landfill, proposed in the Conversio Report, is illustrated in
Figure 11134-135 indicating that, globally ca. 23.5 kt of FP waste were collected in 2020 (< 0.01% of the total waste). To compare, ca. 29,450 kt of plastics were collected in 2020 (<5% of the total collected waste excluding mineral fractions). Moreover, about 84% (20.4 kt) of the total FP collected waste in Europe in 2020 is either thermally or (co-)incinerated destructed while 3.1 kt (13.1%) were landfilled. Finally, 0.81 kt were collected separately for recycling whereas a significant amount was exported for recycling (e.g. to Asian countries).
130
Beside incineration, more severe degradation of FPs can be obtained by various methods including smoldering, pyrolysis. These are efficient to treat fluorinated waste,136 the first one being self-sustaining. As a high-temperature process used for thermal decomposition, pyrolysis is similar to incineration except it is achieved in an inert atmosphere. For an efficient degradation, a temperature greater than 900 °C is preferred. These techniques enable to lead to total destruction of released hazardous PFASs. Several studies have tested the efficiency of these methods to determine if they reach temperatures high enough for a sufficient duration enabling a complete degradation.174-175 Other techniques of incineration 136 such as mineralization (vide infra) of FPs during thermal treatment, or a plasma-based water treatment, are also being investigated as they may be safer and more efficient to treat waste.
4.2.2.7. End-of-life
Several authors have studied the end of life of FPs.136 Actually, when a FP has fulfilled its intended use and will be disposed of, the fate of FPs must be investigated.
Many reports have concluded that FPs such as PTFE do not degrade in the environment and do not release any hazardous compounds toward mammals, human beings and for Environment.102,123,165,176,177 Thus, the downstream, end-of-life process of incineration should lead to more studies.
In addition, though FPs match the PLC criteria (section 4.2.2.3.), circular economy of FPs deserves more interest, and to our knowledge, Wahlström et al.
165 have comprehensively proposed an overall situation including several flows (
Figure 12) ranging from the manufacture of FPs to their use and their recycling (also analyzing the depolymerization of PTFE into TFE as explained in sections above).
The Conversio report
134 extensively provided the results of the treatment of FP waste by industry segments (automotive, aerospace, semiconductors, electronics
76 and chemical industries) in the EU in 2020 regarding collected waste, energy recovery, landfill and recycling as well as co-treatment of FP and associated waste streams.
Figure 13 represents the overall circular economy situation of FPs in EU, involving pre-consumer processing losses during the manufacturing of FP products and applications.
134-135 Most FP are (co-)incinerated in MSWI plants or dedicated hazardous waste incineration plants which are treating different wastes from chemical waste producers. Indeed, two main ways of recycling have been used (
Figure 13): the mechanical and the chemical ones enabling to recycle melt processible FPs (such as PVDF or PFA) or non-melt processible ones (as achieved at Dyneon
145-146 or Karlsruhe Institute of Technology
174) or virgin raw FPs.
The processing of FP materials such as the machining of PTFE rods and cubes for the manufacturing of various milled and drilled parts results pre-consumer FP processing losses. Actually, ca. 20 - 25% of FP producers claim to get their own internal re-processing steps for their process losses. These are the cases for Dyneon, 145-146 Arkema147-148 and other companies. Then, 30 - 35% report to send their pre-consumer FP waste to external material re-processing companies while 15% exported their pre-consumer wastes to other companies inside the EU. 5 - 10% mention that their FP processing losses are exported outside the EU for re-processing, e.g., to Asian countries. 130 Finally, 5% of them state that they do not have any information on their process losses. These companies usually sub-contract waste companies.
4.2.2.8. Mineralization
A totally degradation of FPs is desired to avoid any release of oligomers that imparts severe persistent and toxic issues. The mineralization, that yields to fluoride anions, appears as an attractive and environmentally friendly method. As reported for low molar mass-PFASs,44 the mineralization of FPs has been deeply studied by Hori’s group since more than 10 years, by means of subcritical (or superheated) water.178 These conditions can be reached at the critical temperature (374 °C) and pressure (> 22.1 MPa) of water178-184 for which this fluid displays low viscosity, high diffusivity, and ability to hydrolyze and mineralize many organic compounds. Indeed, reactions requiring subcritical water are considered environmentally benign with the goal at recycling the fluorine element. In the case of FPs, from this technique, Hori’s team mineralized PVDF,179-180 (decomposed into F– and CO2) as well as VDF copolymers: poly(VDF-co-HFP),180 poly(VDF-co-CTFE),179 poly(VDF-co-PMVE)181 and poly(VDF-co-MAF)182 copolymers (where MAF stands for methacrylic acid) and poly(VDF-ter-HFP-ter-TFE) terpolymer183. This led to a quasi-complete mineralization of PVDF performed at 250 ºC as well as for poly(VDF-co-HFP) and poly(VDF-co-CTFE) copolymers.179-180
Scheme 3 supplies a suggested mechanism of the decomposition of poly(VDF-
co-HFP) copolymer. Advantageously, by reacting Ca
2+ cations onto such released fluoride anions, these authors examined the CaF
2 formation
180-183 to close the loop on the fluorine element, since CaF
2 is the source for all fluorinated compounds.
These authors also extended that strategy to the mineralization of ETFE180 and PFSA membranes184 in much more attractive conditions than those reporting the degradation of PFSA membranes generating perfluoroalkanoic acids151 and perfluoroalkane sulfonic acids.185
A different approach from another Japanese team
186 involved molten alkaline metal hydroxide at 400-600 °C to mineralize PTFE. This two step-process allowed an efficient mineralization by chemical recycling. However, that process appears surprising since PTFE can be etched by liquid sodium and also degrades from 500 °C as seen in section 4.2.2.4. First, PTFE (as well as PVDF, PCTFE, and poly(VDF-
co-HFP) copolymer) was decomposed into soluble alkaline fluorides via a degradation in such molten hydroxides at high temperatures and atmospheric pressure. Then, CaF
2, considered the main source of the organofluorine chemistry, was produced by treatment of the former aqueous solution with CaCl
2. When PTFE was heated with a large excess of NaOH at 500 °C, 74% yield of CaF
2 was obtained (
Scheme 4) with respect to the initial PTFE amount.
Indeed, such high temperatures are not far from thermal conditions to favor the unzipping depolymerization of PTFE 102,137-144,157 and, consequently, for other less thermostable FPs than PTFE, the degradation should also happen, even without any base. These authors noted that i) there was no decomposition with molten NaOH below 400 °C whereas ii) from 600 °C yields of CaF2 fell down to 46% (from 67% and 74% at 450 and 500 °C, respectively).
More recently, Sheldon et al.
187 reported that a nucleophilic magnesium reagent (
Figure 14 and
Scheme 5) could enable defluorination of PTFE powder under mild conditions (room temperature and 1 atm), releasing a molecular soluble magnesium fluoride coordination product (2) that was separated from the surface-modified FP. This kinetically stabilized species could be utilized as fluoride carrier and appeared more reactive than inorganic metal fluorides, MF(s) or MF
2(s), which suffer from high lattice enthalpies and high stability. This proof-of-concept evidences that the Fluorine atoms in PTFE can be harvested and reused in coordination synthesis.