Recovery of non-steroidal anti-inflammatory. drugs from wastes using ionic liquid-based. three-phase partitioning systems

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Supporting Information Recovery of non-steroidal anti-inflammatory drugs from wastes using ionic liquid-based three-phase partitioning systems Francisca A. e Silva 1, Magda Caban 2, Mariam Kholany 1, Piotr Stepnowski 2, João A. P. Coutinho 1, Sónia P. M. Ventura 1* 1 CICECO - Aveiro Institute of Materials, Department of Chemistry, University of Aveiro, 3810-193 Aveiro, Portugal. 2 Department of Environmental Analysis, Institute for Environmental and Human Health Protection, Faculty of Chemistry, University of Gdańsk, ul. Wita Stwosza 63, 80-308 Gdańsk, Poland. Equally contributing authors *Corresponding author: E-mail: spventura@ua.pt Campus Universitário de Santiago, Departamento de Química, Universidade de Aveiro, 3810-193 Aveiro, Portugal

Table S1. General information of the pills used as real matrices in this study; identification and content of the NSAIDs, name of the medicine, list of excipients and MA holder [information available on the website of the Portuguese National Authority of Medicines and Health Products (INFARMED, I.P.) - www.infarmed.pt]. API Medicine name (NSAIDs content) Excipients MA holder NAP Naproxeno Generis (naproxen 250 mg) Magnesium stearate, microcrystalline cellulose, colloidal silica, povidone Generis Farmacêutica, Amadora, Portugal KET Profenid Retard (ketoprofen 200 mg) Tablet core: calcium hydrogen phosphate dihydrate, hydroxyethyl cellulose, magnesium stearate Coating: cellulose acetate phthalate, ethyl phthalate Sanofi Aventis, Porto Salvo, Portugal IBU Brufen (ibuprofen 200 mg) Microcrystalline cellulose, crosslinked sodium carboxymethylcellulose, lactose monohydrate, colloidal silica dioxide, sodium lauryl sulfate, magnesium stearate, hypromellose (hydroxypropyl methylcellulose) 2910, hypromellose 2910, talc and titanium dioxide Abbott Laboratórios, Amadora, Portugal

Table S2. Validation parameters for the HPLC-DAD analytical method. Retention Time (min) Concentration range (µg.ml -1 ) Minimum of 6 concentrations Injection volume (μl) Wavelength (nm) R 2 Linearity range (µg.ml -1 ) LOQ LOD Accuracy intra-day (%) Accuracy inter-day (%) Precision intra-day (RSD, %) Precision inter-day, (%) Ibuprofen Naproxen Ketoprofen 16.48 a 12.73 12.27 10 750 a 0.05-50 10 a 25 230 a 230 0.9999 a 1.0000 10-750 a 0.5-50.00 10 a 0.50 1 a 0.20 83.1-101.0 a 92.9-101.6 10-750 0.05-50 10 25 270 245 1.0000 1.0000 10-750 0.05-50.00 10 0.05 1 0.02 80.5-104.9 98.2-112.6 10-750 0.05-50 10 25 270 245 1.0000 1.0000 10-750 0.10-50.00 10 0.10 1 0.05 83.0-99.5 89.2-100.5 88.7-109.7 a 87.2-109.3 81.9-114.3 0.15-3.00 a 0.70-4.00 0.04-1.73 0.20-1.90 0.02-0.50 0.10-2.00 0.01-1.93 a 0.00-0.64 0.00-0.14 a Values taken from e Silva, F. A.; Caban, M.; Stepnowski, P.; Coutinho, J. A. P.; Ventura, S. P. M. Recovery of ibuprofen from pharmaceutical wastes using ionic liquids. Green Chem. 2016, 18, 3749-3757. DOI: 10.1039/c6gc00261g.

Table S3. Tie-lines (TLs) and corresponding values of tie-line lengths (TLLs) information for the IL-based ABS at 25 (±1) ºC utilized in the NSAIDs extraction. ABS [IL] T a [salt] T b [water] T c [IL] M d [salt] M e [IL] B f [salt] B g [water] B h TLL [N 4444 ]Cl + citrate buffer (ph 7) 68.44 1.74 29.82 29.76 30.11 0.65 51.46 47.89 84.07 [BzCh]Cl + citrate buffer (ph 7) 58.34 7.72 33.94 34.88 30.05 8.95 54.73 36.32 68.18 [C 4 mim]cl + citrate buffer (ph 7) 51.05 8.13 40.82 29.93 29.93 7.82 52.75 39.43 62.13 55.21 6.01 38.78 33.02 28.12 7.23 53.81 38.96 67.73 55.62 5.82 38.55 35.25 26.64 5.72 56.82 37.46 71.35 [C 4 mim]cl + citrate buffer (ph 8) 52.27 7.91 39.81 29.95 30.04 7.10 52.69 40.22 63.60 [C 4 mim]cl + potassium citrate tribasic (ph 9) 52.95 7.17 39.88 30.10 29.94 6.25 53.72 40.03 65.94 a Weight fraction composition (in wt%) of IL in the top phase. b Weight fraction composition (in wt%) of salt in the top phase. c Weight fraction composition (in wt%) of water in the top phase. d Weight fraction composition (in wt%) of IL in the biphasic mixture. e Weight fraction composition (in wt%) of salt in the biphasic mixture. f Weight fraction composition (in wt%) of IL in the bottom phase. g Weight fraction composition (in wt%) of salt in the bottom phase. h Weight fraction composition (in wt%) of water in the bottom phase.

Table S4. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using the ABS composed of 30 wt% of [C 4 mim]cl + 30 wt% of potassium citrate buffer (ph 7), and with distinct NSAIDs contents (in mg NSAID per g ABS). NSAID content / (mg NSAID per g ABS) Ibuprofen 1 2 4 EE NSAID ± σ, % 86.7 ± 1.3 87.9 ± 0.7 97.8 ± 2.9 R T ± σ, % 98.2 ± 0.1 98.8 ± 0.0 99.2 ± 0.3 Naproxen EE NSAID ± σ, % 90.4 ± 2.6 98.1 ± 2.3 92.8 ± 6.9 R T ± σ, % 98.2 ± 0.1 98.5 ± 0.0 98.7 ± 0.7 Ketoprofen EE NSAID ± σ, % 93.7 ± 4.0 91.9 ± 0.1 99.2 ± 3.5 R T ± σ, % 98.7 ± 0.1 98.9 ± 0.1 99.1 ± 0.5

Table S5. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using distinct IL-based ABS. IL [C 4 mim]cl [N 4444 ]Cl [BzCh]Cl Ibuprofen EE NSAID ± σ, % 97.8 ± 2.9 88.8 ± 8.4 90.1 ± 6.6 R T ± σ, % 99.2 ± 0.3 100 100 Naproxen EE NSAID ± σ, % 92.8 ± 6.9 84.9 ± 5.6 86.6 ± 8.5 R T ± σ, % 98.7 ± 0.7 100 99.8 ± 0.0 Ketoprofen EE NSAID ± σ, % 99.2 ± 3.5 90.2 ± 9.6 99.6 ± 7.9 R T ± σ, % 99.1 ± 0.5 100 99.6 ± 0.0

Table S6. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using the ABS composed of 30 wt% of [C 4 mim]cl + 30 wt% of potassium citrate buffer at distinct temperatures (±1 ºC) and ph 7. Temperature (ºC) 15 25 35 45 Ibuprofen EE NSAID ± σ, % 90.0 ± 2.4 97.8 ± 2.9 91.5 ± 2.2 91.3 ± 0.5 R T ± σ, % 97.8 ± 0.5 99.2 ± 0.3 99.2 ±0.1 99.3 ±0.0 Naproxen EE NSAID ± σ, % 91.2 ± 2.0 92.8 ± 6.9 92.5 ± 0.4 96.4 ± 2.2 R T ± σ, % 97.4 ± 0.9 98.7 ± 0.7 99.1 ± 0.1 99.2 ± 0.0 Ketoprofen EE NSAID ± σ, % 94.5 ± 1.6 99.2 ± 3.5 94.8 ± 1.0 100 R T ± σ, % 97.7 ± 0.7 99.1 ± 0.5 99.3 ± 0.1 99.4 ± 0.1

Table S7. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using ABS composed of 30 wt% of [C 4 mim]cl + 30 wt% of potassium citrate buffer or potassium citrate tribasic, at distinct ph values. ph 7 8 9 Ibuprofen EE NSAID ± σ, % 97.8 ± 2.9 94.2 ± 4.8 85.1 ± 3.8 R T ± σ, % 99.2 ± 0.3 99.0 ± 0.2 99.1 ± 0.2 Naproxen EE NSAID ± σ, % 92.8 ± 6.9 91.7 ± 0.8 86.5 ± 0.6 R T ± σ, % 98.7 ± 0.7 98.8 ± 0.3 99.0 ± 0.2 Ketoprofen EE NSAID ± σ, % 99.2 ± 3.5 95.3 ± 3.9 89.1 ± 0.8 R T ± σ, % 99.1 ± 0.5 99.1 ± 0.2 99.1 ± 0.3

Table S8. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using the ABS composed of [C 4 mim]cl + potassium citrate buffer (ph 7) at variable mixture compositions (in wt%)/tlls. ([IL] M, [Salt] M ) / (wt%) TLL (30, 30) 62.13 (33, 28) 67.73 (35, 26.5) 71.35 Ibuprofen EE NSAID ± σ, % 97.8 ± 2.9 85.6 ± 3.7 80.3 ± 2.6 R T ± σ, % 99.2 ± 0.3 98.2 ± 1.4 99.4 ± 0.2 Naproxen EE NSAID ± σ, % 92.8 ± 6.9 86.5 ± 3.1 82.5 ± 3.0 R T ± σ, % 98.7 ± 0.7 98.1 ± 1.4 99.4 ± 0.2 Ketoprofen EE NSAID ± σ, % 99.2 ± 3.5 93.0 ± 1.2 85.1 ± 2.9 R T ± σ, % 99.1 ± 0.5 99.0 ± 0.8 99.4 ± 0.2

Table S9. Comparison between the proposed stability study protocol and the original OECD 111e one. Parameter OECD 111e Present protocol Purpose Test substance application Concentration of tested compound Temperature 50 C Estimating hydrolysis as abiotic degradation path in environment. Compounds with good solubility in water are required. 10-2 to 10-3 M for environmental conditions ( 10-6 M). Time of incubation 5 days (preliminary test) 5 days Sample ph 4, 7 and 9 Buffer solution CLARK and LUBS, Citrate buffers of KOLTHOFF and VLEESCHHOUWER, Borate and phosphate mixtures of SÖRENSEN Determining ILs influence on the stability of drugs in extraction processes. Compounds with good solubility in water are not mandatory. It will depend upon compounds solubility in IL enriched matrix. Not confined. Similar concentrations to those instilled by the extraction process are preferable. Temperature at which the IL-based ABS was conducted. Other temperatures may be included if a temperature effect study is targeted. ph at which the IL-based ABS was conducted. Other ph values may be included if a ph effect study is targeted. Buffer (or salt) used as phase-forming agent in the ABS. Also samples without salt addition may be included to control salt effect on analyte stability. Sub-samples taking time t 0 and after 5 days. St 0 (control) and after 5 days (St 25 and St 50 ).

Table S10. Extraction efficiencies (EE NSAID, %) and recovery toward the top phase (R T, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using the IL-TPP investigated. Ibuprofen [C 4 mim]cl [N 4444 ]Cl [BzCh]Cl EE NSAID ± σ, % 92.3 ± 5.1 89.8 ± 5.1 86.3 ± 5.5 R T ± σ, % 97.8 ± 0.7 100 99.8 ± 0.1 Naproxen EE NSAID ± σ, % 86.6 ± 5.0 89.7 ± 3.1 84.9 ± 3.9 R T ± σ, % 97.8 ± 0.3 100 99.7 ± 0.0 Ketoprofen EE NSAID ± σ, % 99.5 ± 6.2 83.8 ± 7.7 86.8 ± 4.1 R T ± σ, % 98.1 ± 0.3 100 98.3 ± 1.0

Table S11. Isolation efficiencies (IE NSAID, %) plus the corresponding standard deviations (σ) of the three target NSAIDs obtained using the distinct approaches based on the precipitation with an antisolvent. Ratio of top phase and antisolvent volume Citric acid aqueous solution at 25 wt% IE IBU ± σ, % IE NAP ± σ, % IE KET ± σ, % 1:4 78.7 ± 2.2 79.1 ± 3.0 - Aluminium sulphate aqueous solution at 15 wt% 1:4 - - 76.2 ± 1.8 1:6 - - 80.9 ± 0.7 1:8 - - 83.4 ± 4.0 1:10 - - 87.1 ± 0.2 1:12 - - 87.9 ± 0.3

Figure S1. Visual appearance of IL-based TPP developed in the present study for the recovery of active ingredients, namely ibuprofen (IBU), ketoprofen (KET) and naproxen (NAP) from solid state pills.