Validation of an extraction method for microplastics from human materials.

INTRODUCTION: Since the beginning of industrial production in 1950, plastic production has continued to grow strongly worldwide and is now at 322 million tonnes in the year 2015. From these very high production volumes ever larger quantities are found in the environment. There the plastics degradate to microplasticity and spread ubiquitously in the world. The present work deals with the possible uptake of microplastic particles in human organisms. For the detection of these plastic particles, an extraction method was developed and validated. MATERIALS AND METHODS: Biological materials consist of human blood (healthy volunteers, n = 4) and different tissues of pigs and cattles. Various lysis solutions were tested for degradation efficiency of biological material and for effects on the plastics. The mass loss, surfaces and structure variations as well as the physicochemical spectrum of the material were observed after treatment by atomic force (AFM) and electron microscopy (EM) and Fourier transform infrared spectrometry (FTIR). RESULTS: The different plastic types as polyamide (PA), polycarbonate (PC), polyethylene (PE), polypropylene (PP), polystyrene (PS) and polyvinyl chloride (PVC) could be clearly differentiated and identified by FTIR. Regarding the surface control, especially PVC showed detectable alterations: After extraction an irregular surface structure caused by protuberances or bubbles could be observed. However, instead of these alterations an equivalent count of plastic particles was found in correlation to the applied plastic amount (recovery rate overall was 99,12±0,67%). CONCLUSION: The applied method can be used for plastic extractions from human or animal tissues without remarkable effects on the plastics.

Transformation of atrazine by photolysis and radiolysis: kinetic parameters, intermediates and economic consideration.

Four techniques, UV254 nm photolysis, vacuum ultraviolet (VUV172 nm) photolysis, combined UV254 nm/VUV185 nm photolysis and gamma (γ) radiolysis were used to induce the transformation of atrazine in aqueous solution. The effects of dissolved oxygen (atrazine concentration 1 × 10-4 mol L-1 and 4.6 × 10-7 mol L-1) and matrix (high purity water/purified wastewater, atrazine concentration 4.6 × 10-7 mol L-1) and the electric energy requirements were investigated. The calculation of the energy input in cases of the photolyses was based on the lamp's power. In radiolysis, the absorbed dose (J kg-1) was the basis. In UV photolysis, atrazine transforms to atrazine-2-hydroxy; this product practically does not degrade during UV photolysis; due to this reason, the mineralisation is very slow. This and some other products of atrazine decomposition degrade only in radical reactions. Dissolved oxygen usually slightly enhances the degradation rate. At 10-7 mol L-1 concentration level, the matrix, high purity water/purified wastewater, has not much influence on the degradation rates in UV photolysis and radiolysis. In the VUV and UV/VUV systems, considerable matrix effects were observed. Comparing the electric energy requirements of the four degradation processes, radiolysis was found to be the economically most feasible method, requiring 1-2 orders of magnitude less electric energy than UV/VUV, VUV and UV photolysis.

Electrochemical decomposition of fluorinated wetting agents in plating industry waste water.

Electrochemical decomposition of fluorinated surfactants (PFAS, perfluorinated alkyl substances) used in the plating industry was analyzed and the decomposition process parameters optimized at the laboratory scale and production scale of a 500-liter reactor using lead electrodes. The method and system was successfully demonstrated under production conditions to treat PFAS) with up to 99% efficiency in the concentration range of 1,000-20,000 µg/l (1 ppm-20 ppm). The treatment also reduced hexavalent chromium (Cr(6+)) ions to trivalent chromium (Cr(3+)) ions in the wastewater. If the PFAS-containing wastewater is mixed with other wastewater streams, specifically from nickel plating drag out solution or when pH values >5, the treatment process is ineffective. For the short chain PFAS, (perfluorobutylsulfonate) the process was less efficient than C6-C8 PFAS. The process is automated and has safety procedures and controls to prevent hazards. The PFAS were decomposed to hydrogen fluoride (HF) under the strong acid electrochemical operating conditions. Analytical tests showed no evidence of organic waste products remaining from the process. Conventional alternative PFAS removal systems were tested on the waste streams and compared with each other and with the-E-destruct (electrochemical oxidation) process. For example, ion exchange resin (IX resin) treatment of wastewater to complex and remove PFAS was found to be seven times more efficient when compared to the conventional activated carbon absorption (C-treat) process. However, the E-destruct process is higher in capacity, exhibits longer service life and lower operating costs than either IX or C-treat methods for elimination of PFAS from these electroplating waste streams.

Helical Figure-of-Eight Loop Dicopper(I) Compounds: Syntheses, Structures, and Dynamics.

The synthesis of a series of nine large macrocyclic ligands with two N(2)S(2) (thioether and Schiff-base imine) binding sites each, with different bridges between the donor atoms of each site (ethylene, o-xylylene, propylene, butylene) and different spacer groups between the two binding sites (p-xylylene, 2,5-dimethyl-p-xylylene, 2,5-dimethoxy-p-xylylene), and the synthesis of a similar ligand with a preorganized double-helical geometry, based on a paracyclophane spacer group, are reported, together with the syntheses and characterizations of the corresponding dicopper(I) compounds. The solid state structures of the dicopper(I) complexes have two tetrahedral copper(I) sites, separated by ca. 8 Å, and a figure-of-eight loop configuration of the ligand with a parallel arrangement of the two substituted benzene spacer groups (benzene.benzene distance of ca. 3.5 Å). All the dicopper(I) compounds have the same double-helical configuration ("twisted ring figure-of-eight loop"). NMR spectroscopy indicates that the monocyclic metal-free ligands have an open, cyclic structure in solution, while the dicopper(I) compounds are folded as in the solid. In acetonitrile there is a fast dynamic equilibrium between two enantiomeric forms of the double-helical dicopper(I) compounds. The fact that copper(I)-donor atom bond breaking is involved in this process is supported by (1)H NMR data and by the X-ray crystal structure analysis of a putative intermediate with each of the two copper(I) centers coordinated to one acetonitrile and three donors of the macrocycle. A second fast dynamic, solvent independent process (epimerization) has been identified in nitromethane and acetonitrile, involving helix inversion with full conservation of the copper(I) coordination.

Novel Ring Contraction Reaction for the Synthesis of Functionalized Tetrathiamacrocyclic Ligand Molecules.

Chlorination of [14]aneS(4)-ol (1,4,8,11-tetrathiatetradecan-6-ol) and cis/trans-[14]aneS(4)-diol (cis/trans-1,4,8,11-tetrathiatetradecane-6,13-diol) yields the corresponding dichloro-substituted macrocycles [14]aneS(4)-Cl (1,4,8,11-tetrathiatetradecane 6-chloride) and cis/trans-[14]aneS(4)-Cl(2) (cis/trans-1,4,8,11-tetrathiatetradecane 6,13-dichloride) in good yield. Thiomethylation of the chlorides produces the ring-contracted pendent thioether macrocycles [13]aneS(4)-CH(2)SCH(3) (1,4,7,10-tetrathiatridecane-5-(methylthio)methane) and cis/trans-anti-[12]aneS(4)-(CH(2)SCH(3))(2) (1,4,7,10-tetrathiadodecane-5,11-bis((methylthio)methane)). The mechanism of the ring contraction reaction is discussed in terms of the reactivity of the monochlorinated macrocycle toward ring contraction and the stereochemistry of the chlorinated intermediates and the thiomethylated products, which are based on the X-ray crystal structure analyses of trans-[14]aneS(4)-Cl(2) and trans-anti-[12]aneS(4)-(CH(2)SCH(3))(2).