Ecohydrological separation in wet, low energy northern environments? A preliminary assessment using different soil water extraction techniques

Funded by European Research Council ERC. Grant Number: project GA 335910 VEWA

Öljyvahinkojätteiden käsittely Kymenlaakson alueella alusonnettomuuden jälkeen

Työn tavoitteena oli selvittää Suomenlahdella tapahtuvasta alusöljyvahingosta syntyvän öljyisen jätteen käsittelymahdollisuudet ja -kapasiteetit sekä loppusijoitusmahdollisuudet ja -kapasiteetit Kymenlaakson alueella. Lisäksi tavoitteena oli selvittää, miten öljy-vahinkojätettä voidaan esikäsitellä välivarastoinnin aikana puhdistuksen ja loppusijoituksen tehostamiseksi. Työn alussa on perehdytty öljyvahinkojätteen muodostumiseen vaikuttaviin tekijöihin: öljylaatujen ominaisuuksiin, öljyn kulkeutumiseen rannalle, ranta- ja saaristomaisemaan, öljyntorjuntaan jarantojen puhdistamiseen. Työssä on kuvattu öljyvahinkojätteen käsittelymenetelmien periaatteet ja menetelmien rajoituksia käsitellä öljyvahinkojätettä. Lisäksityö sisältää tutkimusta Suomen aluevesillä ja maailmalla tapahtuneista öljyonnettomuuksista. Onnettomuuksista on selvitetty erityisesti öljyvahinkojätteen määrä, koostumus ja käsittely. Työn loppuosassa on esitelty Kymenlaakson alueen laitosten mahdollisuuksia käsitellä öljyvahinkojätettä. Tietoa onkerätty haastattelemalla puhelimitse laitosten edustajia keväällä 2007. Alueella voidaan polttaa leijupedissä puhtaaseen polttoaineeseen sekoitettua öljyistä orgaanista ainesta ja puhdistustyössä käytettyjä varusteita arviolta 19 000 t/a, homogenoitua öljyistä orgaanista ainesta voidaan polttaa rumpu-uunissa arviolta 1200 t/a. Alueen polttokapasiteetti kasvaa, kun työn aikana rakenteilla oleva jätteenpolttolaitos valmistuu ja jätettä voidaan polttaa laitoksen arinalla. Lisäksi erityisesti öljyisiä maa-aineksia voidaan alipainekäsitellä, bitumistabiloida, kompostoida sekä pestä. Saadut tutkimustulokset ovat hyödynnettävissä erityisesti Kymenlaakson alueella. Tiedot käsittelymenetelmistä ja niiden rajoitteista ovat hyödynnettävissä valtakunnallisesti.

Öljyvahinkojätteiden käsittely alusonnettomuuden jälkeen Kymenlaakson alueen näkökulmasta

Työn tavoitteena oli selvittää Suomenlahden rannalta merkittävän suuruisen alusöljyvahingon jälkeen kerättävän öljyisen jätteen käsittelymahdollisuudet ja -kapasiteetit sekä loppusijoitusmahdollisuudet ja -kapasiteetit Kymenlaakson alueen näkökulmasta. Tarkoituksena oli selvittää, missä jätteiden käsittely voidaan toteuttaa sekä, miten öljyisiä jätteitä voidaan esikäsitellä välivarastoinnin aikana puhdistuksen ja loppusijoituksen tehostamiseksi. Tutkimuksen kohteena oli sekä rannalta kerättävät kiinteät öljyiset ainekset että öljyinen merivesi. Työn alussa on perehdytty jätehuoltovastuuseen, eli kenen vastuulla öljyalusonnettomuuksissa syntyvät öljyiset jätteet ovat. Työssä on esitelty lyhyesti öljyvahinkojätteille teknisesti soveltuvien käsittelymenetelmien periaatteet ja menetelmien rajoituksia käsitellä öljyvahinkojätetteitä. Työssä on myös mainittu aiemmin Suomea koskettaneiden tai maailmalla tapahtuneiden alusöljyvahinkojen jätemääriä ja tapauksissa käytettyjä jätteiden käsittelymenetelmiä. Työ painottuu esittelemään Kymenlaakson alueen laitosten, Riihimäen Ekokem Oy Ab:n ja siirrettävien laitteistojen mahdollisuuksia käsitellä öljyisiä jätteitä. Lisäksi on esitelty öljyisen meriveden käsittelyyn soveltuvia laitoksia Kymenlaakson alueen näkökulmasta. Tietoja on kerätty puhelimitse ja sähköpostitse yritysten edustajilta vuoden 2007 aikana. Kymenlaakson alueella voidaan polttaa voimalaitosten leijupedeissä puhtaaseen polttoaineeseen sekoitettuja öljyisiä orgaanisia aineksia ja murskautuvia puhdistustyössä käytettyjä varusteita noin 10 000 t/a, homogenoitua öljyistä orgaanista ainesta voidaan polttaa Leca-soratehtaan rumpu-uunissa noin 1 200 t/a. Alueen polttokapasiteetti kasvaa, kun työn aikana rakenteilla oleva jätteenpolttolaitos valmistuu ja jätettä voidaan polttaa laitoksen arinalla. Haihtuvilla öljy-yhdisteillä pilaantuneita maa-aineksia voidaan alipainekäsitellä, jos yhdisteet eivät ole haihtuneet jo merellä. Erityisesti öljyiset maaainekset voidaan käsitellä alhaisilla öljypitoisuuksilla (öljypitoisuus noin alle 1-2 %) bitumistabiloimalla, aumakompostoimalla tai pesemällä siirrettävällä pesulaitteistolla. Kymenlaakson alueelle voidaan tuoda myös alueen ulkopuolelta siirrettäviä laitteistoja. Siirrettävät termodesorptiolaitteistot on tehty pilaantuneen maa-aineksen ensisijaiseen käsittelyyn, mutta samalla voidaan käsitellä myös muita jätejakeita, joilla on pieni partikkelikoko (alle 5-10 cm). Savaterra Oy:n siirrettävän termodesorptiolaitteiston kapasiteettiarvio on 100 000 t/a. Myös Niska & Nyyssönen Oy:llä on siirrettävä termodesorptiolaitteisto. Doranova Oy:n siirrettävän pesulaitteiston kapasiteettiarvio on 30 000- 50 000 t/a öljyistä maa-ainesta. Tutkimuksessa on ollut mukana myös Riihimäen Ekokem Oy Ab:n jätevoimala, jonka kapasiteettiarvio on 40 000-45 000 t/a erityisesti öljyisille orgaanisille aineksille, varusteille ja kuolleille eläimille. Riihimäen Ekokem Oy Ab:n ongelmajätelaitoksen rumpuuuneissa voidaan käsitellä arviolta 80 000-100 000 t/a öljyisiä maa-aineksia eli kiinteitä jätteitä, joiden partikkelikoko on suunnilleen alle 10 cm, ja 20 000 t/a nestemäisiä öljyisiä jätteitä. Työn loppupuolella on esitelty myös öljyisen meriveden käsittelyyn soveltuvia laitoksia ja niiden rajoituksia käsitellä kyseistä jätettä. Kyseisten laitosten kapasiteetit selviävät usein vasta onnettomuuden sattuessa. Kaikkiin annettuihin kapasiteettiarvioihin vaikuttaa merkittävästi jätteen koostumus. Raportin lopussa on esitelty alustava toimintasuunnitelma öljyvahinkojätteen käsittelemiseksi. Suunnitelmaan sisältyvät eri jätejakeille laaditut kaaviot, joista voi nähdä muun muassa eri jätekoostumuksille teknisesti soveltuvat käsittelymenetelmät ja käsittelymenetelmiä suorittavat yritykset. Öljyalusonnettomuuden sattuessa soveltuviin yrityksiin tulee ottaa yhteyttä ja selvittää kyseisellä hetkellä vapaana oleva käsittelykapasiteetti. Raportissa on myös esitelty käsittelykustannuksiin vaikuttavia tekijöitä ja arvioitu aiheutuvia kuljetuskustannuksia. Saadut tutkimustulokset ovat hyödynnettävissä erityisesti Kymenlaakson alueella. Tiedot käsittelymenetelmistä ja niiden rajoitteista ovat hyödynnettävissä valtakunnallisesti.

Extraction of soil water by plants: development and validation of a model

A quantitative model of water movement within the immediate vicinity of an individual root is developed and results of an experiment to validate the model are presented. The model is based on the assumption that the amount of water transpired by a plant in a certain period is replaced by an equal volume entering its root system during the same time. The model is based on the Darcy-Buckingham equation to calculate the soil water matric potential at any distance from a plant root as a function of parameters related to crop, soil and atmospheric conditions. The model output is compared against measurements of soil water depletion by rice roots monitored using γ-beam attenuation in a greenhouse of the Escola Superior de Agricultura "Luiz de Queiroz"/Universidade de São Paulo(ESALQ/USP) in Piracicaba, State of São Paulo, Brazil, in 1993. The experimental results are in agreement with the output from the model. Model simulations show that a single plant root is able to withdraw water from more than 0.1 m away within a few days. We therefore can assume that root distribution is a less important factor for soil water extraction efficiency.

Intercomparison of soil pore water extraction methods for stable isotope analysis

Peer reviewed

Electrical Conductivity and Chemical Composition of Soil Solution: Comparison of Solution Samplers in Tropical Soils

ABSTRACT Soil solution samplers may have the same working principle, but they differ in relation to chemical and physical characteristics, cost and handling, and these aspects exert influence on the chemical composition of the soil solution obtained. This study was carried out to evaluate, over time, the chemical composition of solutions extracted by Suolo Acqua, with the hydrophilic membrane (HM) as a standard, using soils with contrasting characteristics, and to determine the relationship between electrical conductivity (EC) and concentration of ions and pH of soil solution samples. This study was carried out under laboratory conditions, using three soils samples with different clay and organic matter (OM) contents. Soil solution contents of F−, Cl−, NO−3, Br−, SO42−, Na+, NH4+, K+, Mg2+, Ca2+, were analyzed, as well as inorganic, organic, and total C contents, pH, and EC, in four successive sampling times. Soil solution chemical composition extracted by the Suolo Acqua sampler is similar to that collected by the HM, but the Suolo Acqua extracted more Na+ and soluble organic C than the HM solution. Solution EC, cation and anion concentrations, and soluble C levels are higher in the soil with greater clay and OM contents (Latossolo and Cambissolo in this case). Soil solution composition varied over time, with considerable changes in pH, EC, and nutrient concentrations, especially associated with soil OM. Thus, single and isolated sampling of the soil solution must be avoided, otherwise composition of the soil solution may not be correctly evaluated. Soil solution EC was regulated by pH, as well as the sum of cation and anion concentrations, and the C contents determined in the soil liquid phase.

Speciation of naturally-accumulated uranium in an organic-rich soil of an alpine region (Switzerland)

Very high concentrations of uranium (up to 4000 ppm) were found in a natural soil in the Dischma valley, an alpine region in the Grisons canton in Switzerland. The goal of this study was to examine the redox state and the nature of uranium binding in the soil matrix in order to understand the accumulation mechanism. Pore water profiles collected from Dischma soil revealed the establishment of anoxic conditions with increasing soil depth. A combination of chemical extraction methods and spectroscopy was applied to characterize the redox state and binding environment of uranium in the soil. Bicarbonate extraction under anoxic conditions released most of the uranium indicating that uranium occurs predominantly in the hexavalent form. Surprisingly, the uranium redox state did not vary greatly as a function of depth. X-ray absorption near edge spectroscopy (XANES), confirmed that uranium was present as a mixture of U(VI) and U(IV) with U(VI) dominating. Sequential extractions of soil samples showed that the dissolution of solid organic matter resulted in the simultaneous release of the majority of the soil uranium content (>95%). Extended X-ray absorption fine structure (EXAFS) spectroscopy also revealed that soil-associated uranium in the soil matrix was mainly octahedrally coordinated, with an average of 1.7 axial (at about 1.76 Å) and 4.6 to 5.3 equatorial oxygen atoms (at about 2.36 Å) indicating the dominance of a uranyl-like (UO22+) structure presumably mixed with some U(IV). An additional EXAFS signal (at about 3.2 Å) identified in some spectra suggested that uranium was also bound (via an oxygen atom) to a light element such as carbon, phosphorus or silicon. Gamma spectrometric measurements of soil profiles failed to identify uranium long-life daughter products in the soil which is an indication that uranium originates elsewhere and was transported to its current location by water. Finally, it was found that the release of uranium from the soil was significantly promoted at very low pH values (pH 2) and increased with increasing pH values (between pH 5 and 9).

Optimization and validation of the solid-liquid extraction technique for determination of picloram in soils by high performance liquid chromatography

The objective of this study was to optimize and validate the solid-liquid extraction (ESL) technique for determination of picloram residues in soil samples. At the optimization stage, the optimal conditions for extraction of soil samples were determined using univariate analysis. Ratio soil/solution extraction, type and time of agitation, ionic strength and pH of extraction solution were evaluated. Based on the optimized parameters, the following method of extraction and analysis of picloram was developed: weigh 2.00 g of soil dried and sieved through a sieve mesh of 2.0 mm pore, add 20.0 mL of KCl concentration of 0.5 mol L-1, shake the bottle in the vortex for 10 seconds to form suspension and adjust to pH 7.00, with alkaline KOH 0.1 mol L-1. Homogenate the system in a shaker system for 60 minutes and then let it stand for 10 minutes. The bottles are centrifuged for 10 minutes at 3,500 rpm. After the settlement of the soil particles and cleaning of the supernatant extract, an aliquot is withdrawn and analyzed by high performance liquid chromatography. The optimized method was validated by determining the selectivity, linearity, detection and quantification limits, precision and accuracy. The ESL methodology was efficient for analysis of residues of the pesticides studied, with percentages of recovery above 90%. The limits of detection and quantification were 20.0 and 66.0 mg kg-1 soil for the PVA, and 40.0 and 132.0 mg kg-1 soil for the VLA. The coefficients of variation (CV) were equal to 2.32 and 2.69 for PVA and TH soils, respectively. The methodology resulted in low organic solvent consumption and cleaner extracts, as well as no purification steps for chromatographic analysis were required. The parameters evaluated in the validation process indicated that the ESL methodology is efficient for the extraction of picloram residues in soils, with low limits of detection and quantification.

Small-scale method for the determination of selected organochlorine pesticides in soil

A small-scale method was developed for the simultaneous determination of γ-HCH, heptachlor, aldrin, dicofol, mirex, endosulfan I, endosulfan II and endosulfan sulphate in soil. The extraction and clean-up steps were combined into one step by transferring soil samples to chromatographic columns prepacked with neutral alumina. The pesticides elution was processed with n-hexane : dichloromethane (7:3) and the concentrated eluate was analysed using gas-liquid chromatography with electron capture detection. Analyses of the in vitro fortified samples with the selected pesticides were performed at three different levels. Mean recoveries for aldrin, γ-HCH and heptachlor, at levels of 2, 10 and 20 ng/g, ranged from 71 to 87%; for dicofol, at levels of 8, 40 and 80 ng/g, ranged from 97 to 103%; for endosulfan I and II, at levels of 5, 25 and 50 ng/g, ranged from 88 to 96%; for mirex, at levels of 6, 30 and 60 ng/g, ranged from 86 to 110%; and for endosulfan sulphate, at levels of 15, 75 and 150 ng/g, ranged from 93 to 104%. The method can be used for rapid determination of these pesticides in soil. © Springer-Verlag 1996.

Dissipation of DDT in a heavily contaminated soil in Mato Grosso, Brazil

After the prohibition of organochlorine-pesticide use in Brazil for controlling insect vector diseases, Mato Grosso State gathered the exceeding DDT and stored it irregularly in an open air area that belongs to the National Health Foundation, causing soil contamination. This study aimed to evaluate the contamination level and dissipation of p,p′-DDT and p,p′-DDE in this area. For that, surface soil samples were collected on 19 September 2000, 15 December 2000, 4 April 2001 and soil samples 30-40 cm; 60-70 cm and 90-100 cm deep were taken from five points in the studied area on 17 July 2001. The contaminants were determined by a small scale method which consists on extraction and clean-up steps combined into one step by transferring soil samples mixed with neutral alumina to a chromatographic column prepacked with neutral alumina and elution with hexane:dichloromethane (7:3 v:v). The eluate was concentrated and the analytes were quantified by gas chromatography with an electron-capture detector. p,p′-DDT at surface soil ranged from 3800 to 7300 mg kg -1. 30-40 cm deep soil sample concentrations varied from 0.036 to 440 mg kg -1 while 90-100 cm deep samples varied from 0.069 to 180 mg kg -1. Volatilization is probably the main dissipation process. The p,p′-DDT is moving slowly downward in the soil profile, however, the levels of this contaminant are high enough to present risk to underground waters. © 2005 Elsevier Ltd. All rights reserved.

Macroscopic root water uptake distribution using a matric flux potential approach

Hydrological models featuring root water uptake usually do not include compensation mechanisms such that reductions in uptake from dry layers are compensated by an increase in uptake from wetter layers. We developed a physically based root water uptake model with an implicit compensation mechanism. Based on an expression for the matric flux potential (M) as a function of the distance to the root, and assuming a depth-independent value of M at the root surface, uptake per layer is shown to be a function of layer bulk M, root surface M, and a weighting factor that depends on root length density and root radius. Actual transpiration can be calculated from the sum of layer uptake rates. The proposed reduction function (PRF) was built into the SWAP model, and predictions were compared to those made with the Feddes reduction function (FRF). Simulation results were tested against data from Canada (continuous spring wheat [(Triticum aestivum L.]) and Germany (spring wheat, winter barley [Hordeum vulgare L.], sugarbeet [Beta vulgaris L.], winter wheat rotation). For the Canadian data, the root mean square error of prediction (RMSEP) for water content in the upper soil layers was very similar for FRF and PRF; for the deeper layers, RMSEP was smaller for PRF. For the German data, RMSEP was lower for PRF in the upper layers and was similar for both models in the deeper layers. In conclusion, but dependent on the properties of the data sets available for testing,the incorporation of the new reduction function into SWAP was successful, providing new capabilities for simulating compensated root water uptake without increasing the number of input parameters or degrading model performance.

Nitrate leaching through climatologic water balance in a fertigated coffee plantation

Nitrate losses from soil profiles by leaching should preferentially be monitored during high rainfall events and during irrigation when fertilizer nitrogen applications are elevated. Using a climatologic water balance, based on the models of Thornthwaite and Penman Monteith for potential evapotranspiration, drainage soil water fluxes below the root zone were estimated in a fertigated coffee crop. Soil solution extraction at the depth of 1 m allowed the calculation of nitrate leaching. The average nitrate concentration in soil solution for plots that received nitrogen by fertigation at a rate of 400 kg ha-1, was 5.42 mg L-1, surpassing the limit of the Brazilian legislation of 10.0 mg L-1, only during one month. For plots receiving 800 kg ha-1 of nitrogen, the average was 25.01 mg L-1, 2.5 times higher than the above-mentioned limit. This information indicates that nitrogen rates higher than 400 kg ha-1 are potentially polluting the ground water. Yearly nitrate amounts of leaching were 24.2 and 153.0 kg ha-1 for the nitrogen rates of 400 and 800 kg ha-1, respectively. The six times higher loss indicates a cost/benefit problem for coffee fertigations above 400 kg ha-1.

Biorremediação de solos contaminados com produtos petrolíferos

Mestrado em Engenharia Química. Ramo Tecnologias de Protecção Ambiental.

Biocomplementation of SVE to achieve clean-up goals in soils contaminated with toluene and xylene

Soil vapor extraction (SVE) and bioremediation (BR) are two of the most common soil remediation technologies. Their application is widespread; however, both present limitations, namely related to the efficiencies of SVE on organic soils and to the remediation times of some BR processes. This work aimed to study the combination of these two technologies in order to verify the achievement of the legal clean-up goals in soil remediation projects involving seven different simulated soils separately contaminated with toluene and xylene. The remediations consisted of the application of SVE followed by biostimulation. The results show that the combination of these two technologies is effective and manages to achieve the clean-up goals imposed by the Spanish Legislation. Under the experimental conditions used in this work, SVE is sufficient for the remediation of soils, contaminated separately with toluene and xylene, with organic matter contents (OMC) below 4 %. In soils with higher OMC, the use of BR, as a complementary technology, and when the concentration of contaminant in the gas phase of the soil reaches values near 1 mg/L, allows the achievement of the clean-up goals. The OMC was a key parameter because it hindered SVE due to adsorption phenomena but enhanced the BR process because it acted as a microorganism and nutrient source.

Prevención, seguimiento y evaluación de la descontaminación de percloroetileno en suelo y aguas subterráneas en un terreno industrial

La contaminación de suelos y aguas subterráneas es uno de los problemas ambientales más extendidos en gran parte de los terrenos industriales de Cataluña. En este proyecto se ha analizado el proceso de gestión de la contaminación: caracterización, remediación y seguimiento de la descontaminación en suelos y aguas subterráneas por un caso de afección por organoclorados (percloroetileno) y otros contaminantes (hidrocarburos, selenio y cromo) en un emplazamiento industrial situado en una zona agroforestal (superficie de 81.462 m2). A partir de la implantación en la empresa del sistema de gestión ISO 14.001 en 1.996, se abrieron diferentes proyectos de gestión para los posibles contaminantes. Por las mismas fechas, también se detectó una afección por selenio en aguas subterráneas, ajena a la empresa de estudio. Por el momento, el único contaminante que ha requerido de un proceso de descontaminación ha sido el percloroetileno. En suelos se emplea el método “soil vapor extraction” y en aguas subterráneas el método “airstripping”. Finalmente, se ha llevado a cabo una comparación de los costes reales derivados del proceso de descontaminación del percloroetileno en contra de los costes que se hubiesen derivado la implantación de medidas de prevención de la contaminación. El resultado de la valoración indica que la descontaminación de éste compuesto requiere de una inversión económica importante, unas 10 veces más elevada que los costes derivados de las medidas de prevención.