Landfills are potential sources for PFASs and treatment techniques for landfill leachate are urgently needed. Foam fractionation is an aeration technique which utilizes the tendency of PFASs to escape the liquid phase and build foam. The foam is harvested and with it the contamination. Landfill leachate from Hovgården, Uppsala Sweden contained PFASs of higher concentration than desired and investigations into whether foam fractionation could reduce PFASs amounts were initiated. Landfill leachate containing sum PFASs of 5500 ng/L on average were aerated in two different aeration foam collection pilot set-ups for the research. The pilot set-ups were divided into two models: a batch pilot and a continuous pilot. The batch pilot was run for 60 minutes testing parameters such as column volume, air flow rate, dilution and using additives as NaCl, FeCl3 and dish soap. The continuous pilot used contact times of 5, 10 and 20 minutes with constant air flow rate and column volume and no additives. All batch experiments showed reduced concentrations of PFASs, from 62 up to 91%, with an average sum PFASs removal efficiency of 77%. Air flow rates of 4 and 6 L/min were more effective than 2 L/min to reduce the amount of PFASs. Smaller volumes got higher removal efficiency. The dilution experiments showed mixed and somewhat contradictory results, where the nondiluted experiment had removal efficiency of sum PFASs of average 77% while the 50% diluted had an average sum PFASs removal efficiency of 84%. The experiment with the greatest dilution (75%) had the lowest average sum PFASs removal efficiency as suspected, at 68%. Regarding additives, the experiments with added 0.155 and 0.313% NaCl in the leachate were most effective at removing PFASs. The dish soap and FeCl3 additives also contributed to higher PFASs reduction. The experiment with the addition of dish soap had an average sum PFASs removal efficiency of 88% compared to 77% without additives, and the highest concentration of FeCl3 (0,09% of the leachate) had an average sum PFASs removal efficiency of 85%. All continuous experiments showed reduced reduced PFASs concentrations with sum PFASs removal efficiencies ranging from 72 up to 94%, with an average of 86%. The majority of the PFASs were reduced within the first time steps for all experiments, but for the last amount to be removed the contact time needed to be longer. The column contact time of 20 min had the highest average sum PFASs removal efficiency. The conclusion is that PFASs are reduced during the treatment in the pilots and that the reduction is dependent on the chain length and functional groups of the substances, and increased with additives and increased air flow rate. The volume treated and the concentration of raw water also influenced the removal efficiency.

The aim of this work was to develop an alkali activated matrix based mainly on fly ash, to determine the ability to fix lead in these matrices, the impact of added lead on mechanical properties and to reveal the way of lead fixation in these matrices. The matrices consisted mainly of fly ash (four from fluidized bed combustion, one pulverized coal combustion) with an admixture of blast furnace slag and sodium silicate as an activator. Lechates were prepared on the basis of the ČSN EN - 12457-4 standard, lead concentrations in them were measured using an atomic emission spectrometer with inductively coupled plasma. The strengths of the samples were measured after 28 days. Images, element maps and element spectra were taken to determine the structure using a scanning electron microscope with an electron dispersion spectrometer, the samples were analyzed on an infrared spectrometer with a Furier transform, X-ray diffraction analysis and electron spectroscopy for chemical analysis were also used. The individual measurements showed that lead is accumulated in the form of hydroxide. The impact of lead doping on strength of the matrix was different for individual samples. Matrices from both types of fly ash released minimal amounts of lead into leachates, so it is possible to use them to fixate lead.

The enrichment of ore produces large amounts of sulfur and metal-rich residual waste called tailings, which need to be deposited and stored for a long time. When the tailing is oxidized, large amounts of protons and metals are dissolved and diffuse to the groundwater. This poses a major environmental threat to biological life forms in the downstream ecosystem (Karltorp, 2008). In this study, leachate plumes and geological structures surrounding the tailings impoundment at the Kringelgruvan mine in northern Sweden have been successfully mapped using geophysical methods. Three methods have been used in parallel, slingram, ground penetrating radar (GPR) and electrical resistivity measurements, known as continuous vertical electrical sounding (CVES). The resulting data from GPR and CVES have been co-analyzed using Matlab. Algorithms have been produced that plots underground structures from CVES and compares them with interpreted structures from GPR. Studies have shown that the GPR is more sensitive than CVES to local variations of substructures when used in shallow soil cover, while CVES gives considerably more information regarding localization of the leachates and other electrically conductive materials, such as ore. Slingram EM31 has been shown to be the most time-efficient method to localize groundwater flow.

Ammonium-nitrate based explosives (NH4NO3) used within the operations of Kiruna iron ore mine release nitrate (NO3-) into the environment, potentially having adverse effects on local river-systems. One way of reducing NO3- impacts to the environment is through a woodchip denitrifying bioreactor (DBR). Waste rock leachate is collected and passed through the bioreactor, where denitrifying microbial communities reduce NO3- to nitrogen gas (N2) using a carbon energy source. However, the efficiency of the DBR present in Kiruna iron ore mine has declined since the start of its operation leading to lower values of NO3-removal throughout the years.  Denitrification being a temperature dependent process, a heating device was installed to warm up the water prior to the DBR treatment to counterbalance this decrease. The effect of which has been assessed within this thesis. Chemical analyses encompassing NO3-, nitrite (NO2-), ammonium (NH4+), total organic carbon (TOC), phosphorus compounds (tot-P, PO4-P), and bacterial abundance were then investigated along a flowpath in the DBR. Overall, the results have shown that with an increase in temperature prior to the treatment, TOC, tot-P, PO4-P release was improved. Moreover, NO3- removal doubled compared to the previous year. TOC, tot-P and PO4-P are the result of the hydrolysis process, transforming the woodchips in available carbon source and providing nutrients for the bacteria to perform denitrification. Similarly, the bacterial abundance presented a significant increase with temperature. This suggest that both hydrolysis and bacteria growth enhancement with temperature ultimately participated in the improvement of the denitrification reaction. Moreover, a long-lasting effect of temperature on NO3- removal was observed during a following cold period as NO3- removal stayed above 45% after two months without heating. It is suggested that the cost of heating can be reduced by inducing “heat pulse” instead of continuous heating. Adding a heating system prior to treatment represents a promising solution for the future of sustainable mining, particularly for mines located in extreme climates such as Kiruna. / NITREM

Leachate from landfills is contaminated in many ways and per- and polyfluoroalkyl substances (PFAS)-contamination is one of them. Recent studies have demonstrated the environmental and human concerns of PFAS. Therefore, the treatment of leachate is important. One technique to reduce the PFAS concentration is by using aeration and foam fractionation. Hovgården is a landfill northeast of Uppsala, where previous measurements have shown high levels of PFAS in the leachate. Earlier small-scale experiments using aeration foam fractionation as a treatment technique for PFAS removal have been done successfully, but with upcoming requirements of PFAS concentrations there is a need to investigate whether an upscaling is possible or not. In this study, this has been investigated by pumping PFAS contaminated leachate from the landfill in to a 0.046 square metre plastic cylinder and aerated the leachate with an airflow of ten L min-1. A total of six experiments were conducted were the contact time and fraction of extracted foam was parameters that was varying. Four experiments were done with a contact time of ten min and foam fraction of five, ten, twenty and thirty percent and two experiments were made with a foam fraction of five percent and a contact time of twenty respectively thirty min. The average ΣPFAS removal, i.e., the percentage difference in ΣPFAS concentrations between the influent and effluent water in the different runs varied between 31 % and 66 %. The removal of long chained PFAS (≥C6) was higher than the removal of short chained PFAS(≤C5) even if all experiments did reduce the PFAS concentration. Carbon chains with a functional group containing a carboxylic acid is called perfluorocarboxylic acids (PFCA) and with a functional group containing a sulfonic acid is called perfluoroalkane sulfonic acids (PFSA). Precursors are PFAS that after a reaction degrades into PFCA and PFSA. The average removal efficiency of PFCA were 48 %, of PFSA 59 % and of precursors 78 %. The highest removal efficiency was discovered in the experiment with a 30-min contact time and five percent foam fraction with an average ΣPFAS removal of 58 % and an average Σlong chained PFAS removal of 92 %. The lowest removal efficiency was discovered in the experiment with a 10-min contact time and 20 percent foam fraction with an average ΣPFAS removal of 41 % and an average Σlong chained PFAS removal of 67 %. In conclusion a connection between increased contact time and increased removal efficiency was discovered but no clear connections between foam fraction and removal efficiency were found. However, it cannot be stated beyond reasonable doubt that the contact time is the decisive factor. Another conclusion is that the enrichment of short chained PFAS are higher in the water and a higher enrichment of long chained PFAS in the foam. In general, a higher inlet concentration of PFAS in the influent water resulted in a higher removal efficiency.

If not purified leachate from landfills would cause damages on the environment. At most landfills in Sweden local treatment of leachate is achieved, at the rest the leachate is transported to sewertreatment. While no comprehensive legal provisions for discharge exist in Sweden there is a difference in discharges between the installations for landfill. If no comprehensive legal provisions is produced guidance must improve. Treatment of leachate and self monitoring system at fifteen installations in Sweden has been studied and compared. A study of literature about different treatment solutions has also been performed. Practical information about the landfills has been gathered through visits. Processes of treatment described in literature correspond to measures. Variations exists between the self monitoring systems at the installations both between parameters for analyses, how often controls take place and were testpoints are situated. Knowledge of reactions and techniques for treatment of compounds common in leachate exist. Further research about compounds whose effect we do not know for certain must be achieved. / Lakvattenrening och egenkontrollprogram vid femton deponier i Sverige har studerats och jämförts. En litteraturstudie angående olika reningstekniker har även utförts. Information om deponierna och reningsprocesserna har inhämtats via studiebesök och miljörapporter. Vid jämförelse av rening har olika processer studerats separat. Den beskrivning av processerna som finns i litteraturen stämmer väl med uppmätta resultat. Exempel på detta är ammoniumhalter som reduceras i luftad damm, halter totalkväve som minskar genom rening i Satsvis Biologisk Reaktorteknik och reducerad halt suspenderat material som inträffar vid rening genom markfilter. Egenkontrollprogrammen vid de olika deponierna varierar dels i avseende på vilka parametrar som kontrolleras och dels hur ofta kontroller utförs och var provpunkter är belägna. För de vanligast förekommande ämnen som existerar i lakvatten finns kunskap om reaktioner och fungerande tekniker för rening. Problem uppstår för de ämnen vilkas reaktioner och förändringar man ej känner till. Farhågor finns dessutom att det i lakvatten finns föreningar vars existens och verkan vi ej känner till. På grund av detta krävs ytterligare forskning på lakvatten.

Research was conducted 2014-2016 to determine how tobacco thrips (Frankliniella fusca) (Hinds) resistance to neonicotinoid insecticides impact thrips resistance to neonicotinoid insecticides in cotton, Gossypium hirsutum (L.).Studies included bioassays to determine severity and mechanism of resistance and evaluation of host plant characteristics in multiple cotton varieties. Another aspect of research focused on the neonicotinoid insecticide clothianidin and its leaching ability as a seed treatment on corn by evaluating soil type, water regime, and amount found in tissue.

Tidigare studier har visat på höga halter av per- och polyfluorerade alkylsubstanser (PFAS) ilakvatten från avfallsanläggningar. Avfallsanläggningar i Sverige har idag inga krav på attrena bort PFAS från lakvatten, och anläggningarna har generellt inte ett reningssystem som äranpassat för att rena den typen av ämnen. EU stramar hela tiden åt kraven kring utsläpp ochanvändning av PFAS och det kan därför vara bra för en avfallsanläggning att ha översikt påhur mycket PFAS det släpps ut från deponi- och avfallsverksamheten och vilka eventuellaåtgärder som skulle kunna vidtas för detta problem. I denna uppsats används analysresultat av22 PFAS ämnen från nio provtagningspunkter på Gärstad avfallsanläggning, för attundersöka avfallsanläggningens utsläpp av PFAS. Resultaten för studien visar att deuppmätta värdena för summa PFAS 22 för provpunkterna ligger mellan 410 ng/l – 58 000ng/l. PFAS ämnen med kortare kedja (4 – 8 kol) har uppmätts i högre halter än de med längrekedja (9 – 13 kol). Resultaten visade även högre halter av perfluorerade karboxylater (PFCA)än perfluorerade sulfonsyror (PFSA). / Previous studies have shown high levels of per- and polyfluorinated alkyl substances (PFAS)in leachate from waste facilities. Waste facilities in Sweden currently have no requirements topurify PFAS from leachate, and the facilities generally do not have a treatment system that isadapted to purify this type of substances. The EU is constantly tightening the requirementsregarding the release and use of PFAS, and it can therefore be good for a waste facility tokeep track of how much PFAS is released from landfill and waste operations and whatpossible measurements could be taken for this problem. In this essay, analysis results of 22PFAS substances from nine sampling points at Gärstad waste facility have been used, toinvestigate the waste facility's discharge of PFAS. The results of studies show that themeasured values for total PFAS 22 at the sampling spots are between 410 ng/l - 58,000 ng/l.PFAS substances with a shorter chain (4 – 8 carbons) have been measured at higherconcentrations than those with a longer chain (9 – 13 carbons). The results also showedhigher levels of perfluorinated carboxylic acids (PFCAs) than perfluorinated sulfonic acids(PFSAs).

The landfill leachate is commonly treated for non-biodegradable organic matters, ammonia and colour. Experimental investigations using polyaluminium chlorite (PAC) and UV/O3 have been conducted for the determination of optimal pH value, reaction time and PAC concentration for the removal of chemical oxygen demand (COD) and colour. In pre-treatment coagulation stages, the highest COD and colour removal efficiencies were observed at the concentration of PAC ≥ 3,000 mglG1 and pH values between 7 and 8. However, these experiments also indicated significant removal efficiency for PAC starting with concentrations of 1,500 mglG1. The efficiency of COD and colour removal were approximately 30% and 70%, respectively. Similar efficiencies have been observed also during the second treatment stage where UV/O3 processes were used to treat coagulated leachate. After UV/O3 application, the pH of leachate reached the optimum value of 7.5 whereas the highest COD and colour removal efficiency was 55% and 72%, respectively, and the optimal reaction time was achieved after 80 min. / Nước rỉ rác sinh ra từ bãi chôn lấp chất thải rắn cần được xử lý các thành phần chất hữu cơ khó phân hủy sinh học, xử lí amoni và độ màu. Một số kết quả thử nghiệm về xử lý COD và màu của nước rỉ rác bằng việc sử dụng phương pháp keo tụ với PAC và quá trình UV/O3 đã được thực hiện cùng với việc xác định các giá trị pH tối ưu, thời gian phản ứng và nồng độ PAC tối ưu. Hiệu suất xử lý cao nhất đạt được khi nồng độ của PAC ≥ 3.000 mg/l, pH trong khoảng từ 7 đển 8 trong giai đoạn tiền xử lý. Tuy nhiên, hiệu quả loại bỏ COD và màu bắt đầu tăng rõ khi nồng độ PAC từ 1.500 mg/l trở lên. Hiệu quả loại bỏ COD và màu tương ứng là khoảng 30% và 70%. Các giá trị pH này phù hợp cho quá trình phản ứng UV/O3 được sử dụng sau giai đoạn keo tụ. Sau quá trình xử lý bằng hệ UV/O3, pH của nước rỉ rác tối ưu được xác định là 7,5 (hiệu suất xử lý COD và màu cao nhất tương ứng là 55% và 72%), thời gian phản ứng tối ưu là 80 phút.

No description available.