OXIDIZED LOW-RANK COALS - IN SITU IMMOBILIZED HUMIC SUBSTANCES. Břehová 7, Praha 1, Czech Republic,

Similar documents
SUPPORTING INFORMATION FOR THE MANUSCRIPT. Phenanthrene sorption to soil humic acid and humin fractions

Hansell Gonzalez Raymat DOE Fellow Graduate Student, Ph.D. in Chemistry

Adsorption of Cd(II) ions by synthesize chitosan from fish shells

Chapter 1. Introduction

WM 00 Conference, February 27 March 2, 2000, Tucson, AZ DIFFUSION COEFFICIENTS OF CRITICAL RADIONUCLIDES FROM RADIOACTIVE WASTE IN GEOLOGICAL MEDIUM

Radionuclide Migration: Prediction Experience

Removal Efficiency of Cesium and Strontium in Seawater by Zeolite Fixed-Bed Columns

IMO LATERITIC SOIL AS A SORBENT FOR HEAVY METALS

Sorptive treatment of explosives and heavy metals in water using biochar

Adsorption of Methylene Blue on Mesoporous SBA 15 in Ethanol water Solution with Different Proportions

ACTIVATED BLEACHING CLAY FOR THE FUTURE. AndrevJ Torok ThomaE D Thomp~on Georgia Kaolin Company Elizabeth, New JerEey

CEE 697z Organic Compounds in Water and Wastewater

Removal of Sb-125 and Tc-99 from Liquid Radwaste by Novel Adsorbents

Removal Of Copper From Waste Water Using Low Cost Adsorbent

Understanding Aqueous Dispersibility of Graphene Oxide and Reduced Graphene Oxide through pka Measurements

Thermodynamic parameters of Cs + sorption on natural clays

Application of Fe 2 O 3 nanoparticles in Heavy Metal Removal

Physicochemical Processes

ROLE OF SURFACE CHEMISTRY IN ADSORPTION OF ETHYLMETHYLAMINE ON ACTIVATED CARBONS

STUDIES ON THE REMOVAL OF CATIONIC DYES FROM AQUEOUS SOLUTION BY MIXED ADSORBENTS

CHAPTER 4. Major Classes of Chemical Reactions

The Sorption Properties of Humate Injected into the Subsurface System. Hansell Gonzalez Raymat DOE Fellow Graduate Student, Ph.D.

Adsorption of chromium from aqueous solution by activated alumina and activated charcoal

CHAPTER CHROMATOGRAPHIC METHODS OF SEPARATIONS

Removal of Cu 2+, Cd 2+, Hg 2+, and Ag + from Industrial Wastewater by Using Thiol-Loaded Silica Gel

The Influence of Humic Acid and Colloidal Silica on the Sorption of U(VI) onto SRS Sediments Collected from the F/H Area

Preparation and adsorption properties of cyclodextrin modified chitosan inclusion compound crosslinked by glutaraldehyde

CHAPTER 3 WATER AND THE FITNESS OF THE ENVIRONMENT. Section B: The Dissociation of Water Molecules

Effect of Process Parameters on Adsorption of Methylene Blue from Synthetic Effluent Using Jack Fruit Seed Powder

Potential Alternative Utilization of Manganese Nodules

Adsorption at the solid/liquid interface

EXTRAPOLATION STUDIES ON ADSORPTION OF THORIUM AND URANIUM AT DIFFERENT SOLUTION COMPOSITIONS ON SOIL SEDIMENTS Syed Hakimi Sakuma

Chem 128, Final Exam May 11, 2003

Photocatalytic degradation of dyes over graphene-gold nanocomposites under visible light irradiation

BRIEFING. Pharmacopeial Discussion Group Sign Off Document Attributes EP JP USP Definition Loss on drying Readily carbonizable substances

Removal of Benzene From Aqueous Solution Using Raw Red Mud

PREPARATION OF ACTIVATED CARBON FROM PULP AND PAPER MILL WASTES TO BE TESTED FOR THE ADSORPTION OF VOCS

Aqueous Reactions and Solution Stoichiometry (continuation)

Tokyo, 3-4 February Valentina Toropova and Dmitri Davydov

Removal of Fluoride from Synthetic Water Using Chitosan as an Adsorbent

REMEDIATION OF SALT IMPACTED GROUNDWATER WITH ELECTROKINETICS. Paper by: Sean Kelly, Rick Churko, Sean Frisky, Anjum Mullick, Stuart Torr.

THE USE OF ORGANOCLAY IN MANAGING DISSOLVED ORGANIC CONTAMINANTS RELEVANT TO CONTAMINATED SEDIMENTS

Scientific Base of the Technologies for Heavy Metals and Petrochemical Hydrocarbons Detoxification by Polyelectrolyte Enhanced Biopolymer

9/24/12. Chemistry Second Edition Julia Burdge. Reactions in Aqueous Solutions

Extraction. A useful technique for purification of mixture. Dr. Zerong Wang at UHCL. Separation processes

CHM Salicylic Acid Properties (r16) 1/11

Synthetic faujasite based on coal by-products for the treatment of acid mine drainage (AMD)

GEOCHEMISTRY, GROUNDWATER AND POLLUTION,

Chapter 4 Reactions in Aqueous Solutions. Copyright McGraw-Hill

Supporting Information

Instrumental Characterization of Montmorillonite Clay by FT-IR and XRD from J.K.U.A.T Farm, in the Republic of Kenya

Chapter 6. Types of Chemical Reactions and Solution Stoichiometry

Removal of Crystal Violet from Aqueous Solution by Activated Biocharfibers. Maria A. Andreou and Ioannis Pashalidis

Ondansetron Hydrochloride Tablets

Application of Chitin and Zeolite adsorbents for treatment of low level radioactive liquid wastes

Use of ion-exchange composites based on natural zeolites for cleaning of water solutions with purpose to create environmentally safe technologies

CHAPTER 4 TYPES OF CHEMICAL REACTIONS & SOLUTION STOICHIOMETRY

MOF-76: From Luminescent Probe to Highly Efficient U VI Sorption Material

Types of chemical reactions

Buffers. A buffered solution resists changes in ph when small amounts of acids or bases are added or when dilution occurs.

Vol. 3, No. 4 December 2002 pp

Analysis of Thermal Decomposition Behavior of Coals Using High Temperature Infrared Spectrophotometer System


NOTE. Separation of chlorophenols using columns of hydroxyaluminium interlayered clays

Treatment of Heavy Metals in Contaminated Soils Around an Abandoned Mine Using Magnetically Modified Alginic Acid and XYZ

CHEM 344 Fall 2015 Final Exam (100 pts)

Sorption of Water Pollutants

Chem 115 POGIL Worksheet - Week #6 Oxidation Numbers, Redox Reactions, Solution Concentration, and Titrations

THE STUDY OF ION SORPTION PERFORMANCES OF STOICHIOMETRIC AND NON-STOICHIOMETRIC POLYELECTROLYTE COMPLEXES.

Lecture 15: Adsorption; Soil Acidity

Mercury, total-in-sediment, atomic absorption spectrophotometry, nameless, direct

Chemistry 265 December Exam 2011 Smith-Palmer

Standard Methods for the Examination of Water and Wastewater

A NEW SOLVENT FOR CO2 CAPTURE R.

Solution Properties of Marine Humic Acid. II. Formation and Effects of Metal Ions on Solution Properties

STUDY ON THE IMPROVEMENT OF THE REDUCTION CAPACITY OF ACTIVATED CARBON FIBER

ADSORPTION PROPERTIES OF As, Pb AND Cd IN SOFT SOIL AND META SEDIMENTARY RESIDUAL SOIL

Chapter Four: Reactions in Aqueous Solution

Advanced Pharmaceutical Analysis

2. (i) Infrared (radiation absorbed) by (C H) bond vibration ALLOW bond stretching OR bond bending DO NOT ALLOW molecules vibrating 2

Adsorption of Humic acid on Powdered Activated Carbon (PAC)

1901 Application of Spectrophotometry

Luke Chimuka. School of Chemistry, University of Witwatersrand

Solution-processable graphene nanomeshes with controlled

Chapter 4. Reactions in Aqueous Solution

REMOVAL OF METAL IONS FROM ACIDIC SOLUTIONS USING PEAT A LOW COST SORBENT

Studying the Effect of Crystal Size on Adsorption Properties of Clay

Final Report. Characterisation of Sample Report. Job No 2016/11/12-34 AS No. 1234A. Client Example Contact Sample. Signed Date 2017.

Adsorption of phenol from diluted aqueous solutions by activated carbons obtained from bagasse, oil palm shell and pericarp of rubber fruit

WM2016 Conference, March 6 10, 2016, Phoenix, Arizona, USA

Supporting Information. for. Angew. Chem. Int. Ed. Z Wiley-VCH 2003

Chemistry 12 Unit III Solubility Notes

Materials Research Centre, Brno University of Technology, Faculty of Chemistry, Brno, Czech Republic, EU.

Sorption of Uranium (VI) to Graphite under Potential Repository Conditions

CLASS EXERCISE 5.1 List processes occurring in soils that cause changes in the levels of ions.

CHAPTER IV HOFMANN REARRANGEMENT IN CROSSLINKED POLYMERIC MATRICES

INVESTIGATION OF SURFACE CHEMISTRY PROPERTIES OF Ga 2 O 3 /Al 2 O 3 CATALYSTS BY FT-IR SPECTROSCOPY

Current World Environment Vol. 4(2), (2009)

HUMUS CHEMISTRY. Genesis, Composition, Reactions. Second Edition. F. J. STEVENSON Department of Agronomy University of Illinois

Chapter 02 The Chemical Basis of Life I: Atoms, Molecules, and Water

Transcription:

OXIDIZED LOW-RANK COALS - IN SITU IOBILIZED HUIC SUBSTANCES G. asnerová 1, J. izera, V. achovič 3, L.Borecká 3 1 Department of Nuclear Chemistry, Czech Technical University in Prague Břehová 7, 115 19 Praha 1, Czech Republic, E-mail: masnerova@fjfi.cvut.cz Nuclear Physics Institute, Academy of Sciences of the Czech Republic, 50 68 Řež u Prahy, Czech Republic, E-mail: mizera@ujf.cas.cz 3 Institute of Rock Structure and echanics, Academy of Sciences of the Czech Republic, V Holešovičkách 41, 18 09 Praha 8, Czech Republic, E-mail: machoviv@vscht.cz Abstract Properties of oxidized low-rank coals as potential low-cost sorbents of metal ions were investigated. Lignite coal from the Northern Bohemia with a defined range of grain size was oxidized on air at 140 C for up to 00 hours to increase degree of oxygen functionalities (carboxylic and phenolic groups). For comparison, oxihumolite from the same locality and Aldrich humic acid were used. Influence of coal bitumen (the organic-soluble fraction) was investigated. Changes in composition and structure caused by the laboratory oxidation were studied by elemental analysis and DRIFT spectroscopy, respectively. Proton exchange capacities (PEC) and dissociation of functional groups of the samples were investigated by the Ba(OH) method and potentiometric titration, solubility was checked by spectrophotometry. Sorption of Cs +, Co + and Eu 3+ cations was studied by batch experiments using radiotracer method. Introduction Industrial technologies and energetics are connected with generation of enormous amounts of harmful environmental pollutants, and in agreement with safety regulations require new approaches to waste management. Technologies employed in treatment of waste streams are often expensive and/or insufficient. The nature of some wastes, namely long-life radionuclides, requires their long-term storage in suitable repositories which, in addition to the natural geological barriers within a repository site, need geochemical barriers based on suitable sorbents to immobilize the contaminants in case they penetrate through geotechnical barrier (tanks, vitrifying glass, etc.). Similarly, in situ permeable barriers based on sorbents have a potential for remediation of contaminated ground water. For largescale use, these materials would be exceedingly expensive. Natural sorbents as zeolites, metal oxides, clays, coal, chitosan, etc. have been considered as promising inexpensive alternative (1). Partial solubility and/or insufficient mechanical stability of sorbent particles deteriorate their utilization especially for dynamic column operations. It is necessary to provide physical support, and preserve or increase accessibility of the binding sites. Humic substances (HS) are a substantial component of natural organic matter produced by biomass degradation. The complex nature of interaction between cations and HS as heterogenous, polydispersive polyelectrolytes is given by the variety of functional groups (mainly carboxylic and phenolic) located in various chemical environments of the 3-D structure of a macromolecule, and ranges from purely electrostatic, non-specific interactions with the net negative charge on the surface of humic macromolecule to covalent, specific interactions, as in the formation of complexes and chelates with the functional groups (). Solubility of HS precludes their use as sorbent material without suitable immobilization, although after acid precipitation and drying, humic acid (HA) is fairly stable even in mildly alkaline solutions. In situ immobilization of HS in matrix of low-rank coals, particularly postsedimentary oxidized coals (oxihumolite or leonardite), represent one of the most abundant natural resources of immobilized HS, and potential low-cost sorbents of toxic metals and radionuclides for use in waste water treatment, groundwater remediation, and construction of active geochemical barriers (3). Since the supply of naturally oxidized coal is limited, it would be convenient to treat the more abundant energetic brown coals to obtain material with sorption properties comparable to oxihumolites. The sorption ability of coal is affected by several factors, as amount and acidity of the oxygen functionalities, their location within coal structure, size and swelling ability of coal particles, pore size distribution. Quantity and/or quality of the exchangeable functional groups can be altered by, e.g., oxidation increasing content of the oxygen functionalities, stripping off metal cations/protonation,

and sulfonation increasing the exchange capacity and extending the exchange range to lower. Extraction of the organic-soluble fraction, bitumen, can also affect the sorption properties by influence on the pore system. This work, in continuation of our previous study (4), has been aimed to investigate potential of artificially oxidized low-rank coal (lignite) as a low-cost sorbent of selected radionuclides, in comparison with oxihumolite produced naturally by postsedimentary oxidation of parent coal from the same seam. ethods Reagents and sample preparation. All solutions were prepared from analytical reagents without further purification, and ultrapure water. Samples were collected from seam Antonín (Sokolov Basin, Czech Republic) - lignite in Jiří mine, oxihumolite in arie mine, sieved (0.3-0.5 mm, samples and, respectively). Sample was oxidized on air at 140 C, samples were withdrawn after 4, 50, 80, 10 and 00 h (,,, J10,, respectively). All samples were protonized by 1 HCl. To study the role of bitumen, samples E, E, 00E were prepared from samples, and, respectively, by extraction with toluene/ethanol (1:1) in Soxhlet extractor for 5 days. Aldrich humic acid (HA) was used, purified/protonated according to a procedure described in (5). Elemental analysis. C, H, N, S were determined by standard methods, O was calculated by the difference. DRIFT. The diffuse reflectance infrared Fourier transform spectroscopy (DRIFT) utilized a Nicolet 740 spectrometer with a TGS detector and a Spectra Tech diffuse reflectance accessory. Each sample (50 mg) spectrum averaged 51 scans at resolution cm -1. Titration methods. The proton exchange capacity (PEC) was determined by back titration of excess Ba(OH) equilibrated in suspension (75 mg in 5 ml Ba(OH), 0.1 ) with a sample. Dissociation of acidic functional groups was studied by potentiometric titration using a Radiometer Titralab 80 automatic titrator. Suspension of a sample (150 mg in 30 ml, I = 0.1 by NaClO 4 ) was titrated with 0.1 NaOH under nitrogen in a cell thermostated at 5 C, at dosing rate 40 µl per 5 min. Spectrophotometry. Leaching of HS from the samples was checked by measuring absorbance (λ=54 nm) of the solution sampled after centrifugation, in quartz cuvettes, after suitable dilution. Sorption experiments. Batch experiments were performed with radiotracers 134 Cs, 60 Co, 15 Eu (simultaneously) under following conditions: V/m = 100 ml/g, I = 0.1 (NaNO 3 ), Cs, Co and Eu concentration.4 10-5,. 10-5, 1.6 10-6, respectively, 4 h shaking. Effect of was studied. Centrifugation (3500 rpm, 15 min) was used to separate phases. Activities in solution were determined by γ-spectrometry measuring the analytical lines at 1, 605 and 1173 kev for 15 Eu, 134 Cs and 60 Co, respectively. Results and Discussion Oxidative changes in coal. The elemental changes are illustrated by the van Krevelen diagram (Figure 1). They are most pronounced during the first 50 hours, the higher O content in is reached in J after 80 h oxidation. At the same time, H/C atomic ratio decreases due to cleavage of aliphatic C-H bonds (6). Extraction of bitumen (6-8 wt%) decreased content of both O and H by their concentrating in the bituminous fraction. Figure 1: Elemental analysis of coal samples - van Krevelen diagram 0.95 0.90 (H/C) at 0.85 0.80 0.75 E E J10 0.70 0.18 0.0 0. 0.4 0.6 0.8 (O/C) at

Structural changes in oxygen functionalities can be followed by the DRIFT spectroscopy using interpretation of the spectra as shown on Figure. The increase of content of carboxyl functionalities with oxidation time is reflected by increasing ratio of peak intensities at 1700 cm -1 (stretching vibrations of carbonyl groups) and 161 cm -1 (aromatic C=C bonds). The gain in phenolic groups is followed by the ratio of 300 (phenolic OH) and 9 cm -1 (aliphatic C-H bonds) peak intensities. Effect of extraction is ambiguous. For oxihumolite ( vs. E), it slightly decreases content of both types of O functionalities as expected. For extracted coal samples (E, ), decrease is observed only in phenolic groups, content of carbonyl increases with extraction, particularly for the non-oxidized sample. Possibly, oxidation takes place during extraction with hot solvents on air, and/or content of aromatic structures decreases increasing the I 1700 /I 161 intensity ratio. Figure : Relative content of carbonyl and phenolic groups determined by DRIFT spectroscopy, as function of oxidation time (squares carbonyl, circles phenolic, broken lines extracted J samples) I 1700 /I 161 1.5 1.4 1.3 1. 1.1 E I 300 /I 9 (phenolic groups) I 1700 /I 161 (carbonyl groups) E.5 1.5 I 300 /I 9 0.9 0.8 0.7 0 50 100 150 00 oxidation time, h Changes in acidobasic properties of coal samples due to oxidation are illustrated by titration curves (Figure 3) and proton exchange capacities (Table 1). Increase in O functionalities due to oxidation is reflected by shift of the curves to higher NaOH consumption, and increase in the PEC values. Comparing the PEC values with NaOH consumption at the end of titration ( > 10-11), the latter is significantly lower. Obviously, titration was not slow enough to reach equilibrium after each titrant addition due to a worse accessibility of HS functional groups in coal mineral matrix. In case of the purified (demineralized) HA, the PEC corresponds quite well with the titration curve. Extraction of bitumen changed character of titration curve and decreased PEC, especially in case of oxihumolite ( vs. E) and strongly oxidized coal (J vs. ). Figure 3: Titration curves 1 10.0 J10 E E HA blank Table 1: Proton exchange capacities Sample PEC (mmol/g) ± 0.38 4.63 ± 0.17 5.90 ± 0.01 6. ± 0.11 6.35 ± 0.04 J10 6.67 ± 0.01 7.07 ± 0.00 E 5.60 ± 0.14 E 4.53 ± 0.14 6.35 ± 0.1 HA 7.39 ± 0.08 0 1 3 4 5 6 7 8 NaOH, mmol per g of sorbent

Leaching of HS from coal as function of contact time with solution and its, checked by measuring absorbance in solution at 54 nm, is documented by Figure 4. In agreement with solubility of HA in neutral and alkaline solution, leaching increases with. It is much higher for oxihumolite than for coal samples. Oxidation for 00 h increases significantly leaching of HS, but yet it remains much lower than in case of oxihumolite. Checked by weighing dried samples after separation from solution, weight losses were about 3 and 13 % for and, respectively. Extraction decreased leaching of HS. Figure 4: Leaching of HS from the samples checked by spectrophotometry 0.16 0.14 3 7.0 6 1 1 9 Absorbance, λ = 54 nm 0.1 0.10 0.08 0.06 0.04 0.0 0.00 5.0 3.0 0.0 E E 1 1 10.0 0.0 0 10 0 30 40 50 0 10 0 30 40 50 0 10 0 30 40 50 Sorption of Cs, Co and Eu. Activities (cpm, counts per minute) in solution were used to calculate distribution coefficient K d defined by the equation K d = Ai C, i where A i is concentration of adsorbate (radionuclide) on the solid at equilibrium (cpm./g), C i is concentration of total dissolved adsorbate remaining in solution at equilibrium (cpm/ml). K d values (Figure 5) increasing in the order Cs<Co<Eu reflect increasing charge of cation and ability of coordination-covalent binding to HS sites. Oxidation of coal increased K d s with no improving after 80 h oxidation. Generally, K d s increase with due to dissociation of the binding sites. K d s of Eu (and with Co, to a certain extent) with oxihumolite and HA, in alkaline region also with other samples, decrease with due to formation of soluble HS complexes leached to solution. Effect of extraction is negligible except for non-oxidized coal ( vs. E) with Eu and Co, whose sorption in neutral and alkaline region is enhanced, probably owing to suppressed leaching of HS. Figure 5: Sorption of Cs, Co and Eu on the samples K d values vs. Cesium 4 Cobalt 4 Europium log K d 1 3 1 3 J10 E E HA 4 6 8 10 0 4 6 8 10 4 6 8 10 Summary and Conclusions As a source of naturally immobilized humic substances, low-rank coal (lignite) is a promising material to be used as a low-cost sorbent of toxic metals and radionuclides. It can be artificially oxidized to increase content of oxygen functionalities, carboxyl and phenolic groups. Oxidation on air at 140 C for 80 hours is sufficient to obtain material with content of the functional groups similar to that of the naturally oxidized coal, oxihumolite. Despite similar (or even higher) content of oxygen functionalities, sorption ability for Cs, Co and Eu of the oxidized lignite is lower in acidic solution than in case of oxihumolite, probably due to a worse accessibility of the binding sites for the cations (7). In neutral and

alkaline region, sorption properties of oxihumolite deteriorate due to leaching of the originally in situ immobilized HS into solution, while for the artificially oxidized lignite with relatively low leaching of HS, sorption increases with until mildly alkaline region. Extraction of bitumen expected to ensure a better accessibility of the binding sites was accompanied with decrease in content of the oxygen groups, thus has brought a negligible effect. However, it enhanced immobilization of HS within coal matrix improving its sorption ability in neutral and alkaline solutions. Acknowledgement The study was supported by the CTU grant No. 0311114. References 1.S. BABEL and T.A. KURNIAWAN, Journal of Hazardous aterials, B97, 19-43 (003). C.J., ILNE, D.G. KINNIBURGH and E. TIPPING, Environ. Sci. Technol., 35, 049-059 (001). 3 D.L. BODINE and F.. DOYLE, "Removal of Cu +, Cd + and n(vii) from Dilute, Aqueous Solutions by Oxidized Bituminous Coal", In: Treatment and inimization of Heavy etal- Containing Wastes (J.P. Hagar et al., eds.), TS, Warrendale, PA, 81-93 (1995). 4 V. ACHOVIČ, J. IZERA, I. SÝKOROVÁ and L. BORECKÁ, Acta ontana IRS AS CR, Series B, 10(117), 15-6 (000). 5 J.I. KI and G. BUCKAU, Characterization of Reference and Site Specific Humic Acids - Report RC 0188, Technical University ünchen, Germany (1988). 6 D.C. CRONAUER, R.G. RUBERTO, R.G. JENKINS, P.C. DAVIS, P.C. PAINTER and D.S. HOOVER, Fuel, 6, 114-113 (1983). 7 K. URAKAI, T. YAADA, K. FUDA, T. ATSUNAGA and Y. NISHIYAA, Fuel, 76, 1085-1090 (1997).