Potential use of a chemical leaching reject from a kaolin industry as agricultural fertilizer

The industrial refining of kaolin involves the removal of iron oxides and hydroxides along with other impurities that cause discoloration of the final product and depreciate its commercial value, particularly undesirable if destined to the paper industry. The chemical leaching in the industrial processing requires treatments with sodium hyposulfite, metallic zinc, or sulfuric and phosphoric acids, in order to reduce, dissolve and remove ferruginous compounds. To mitigate the environmental impact, the acidic effluent from the leaching process must be neutralized, usually with calcium oxide. The resulting solid residue contains phosphorous, zinc, and calcium, among other essential nutrients for plant growth, suggesting its use as a macro and micronutrient source. Samples of such a solid industrial residue were used here to evaluate their potential as soil fertilizer in an incubation greenhouse experiment with two soil samples (clayey and medium-textured). The small pH shift generated by applying the residue to the soil was not a limiting factor for its use in agriculture. The evolution of the concentrations of exchangeable calcium, and phosphorous and zinc extractability by Mehlich-1 extractant during the incubation period confirms the potential use of this industrial residue as agricultural fertilizer.

Koboltin ja nikkelin poisto sinkkisulfaattiliuoksesta ioninvaihdolla

Työssä tutkittiin kahden silikapohjaisen erotusmateriaalin soveltuvuutta nikkelin ja koboltin poistoon sinkkisulfaattiliuoksista. Suurin osa kokeista tehtiin ioninvaihtimella, jonka funktionaalinen ryhmä on iminodietikkahappo. Vertailuerotusmateriaalin toiminta perustui adsorptioon. Liuoksina käytettiin sekä autenttista prosessiliuosta että synteettistä ZnSO4-liousta. Ioninvaihtimen kestävyyskokeissa selvisi, että tutkittu ioninvaihdin kestää hyvin sekä 60 oC lämpötilan että happamia olosuhteita. Emäksisissä liuoksissa silikarunko ei kestä. Jo 0,1 M NaOH-liuos liuottaa merkittävästi hartsia vuorokauden aikana. Vaihtimen vetyionikapasiteetiksi saatiin titrauksella 2,3 mekv/g. Tasapainokokeilla saatiin selville, että ioninvaihdin on selektiivinen nikkelille sinkin suhteen ja että selektiivisyys kasvaa liuoksen pH:n laskiessa. Koboltille ioninvaihdin ei ole selektiivinen sinkin suhteen. Mikäli sinkin pitoisuus on tuhansia kertoja nikkelin pitoisuutta suurempi, ei ioninvaihtimen Ni-selektiivisyys riitä myöskään nikkelille. Synteettisillä ZnSO4-liuoksilla tehtyjen kolonnikokeiden perusteella havaittiin, että tutkitulla ioninvaihtimella voidaan laimeista ZnSO4-liuoksista poistaa nikkeliä selektiivisesti. Nikkelin eluointi onnistui helposti 1 M H2SO4:lla. Vertailukokeen perusteella oli ioninvaihtimen Ni/Zn-selektiivisyys referenssiadsorbentin Ni/Zn-selektiivisyyttä pienempi. Ioninvaihtokolonnin mallintaminen ei onnistunut riittävän hyvin kuvaamaan ioninvaihtimessa tapahtuvaa samanaikaista ioninvaihtoa ja adsorptiota. Sen sijaan kun kolonnissa oli vertailumateriaalina käytetty adsorbentti, saatiin kolonnikokeiden tulokset mallilla hyvin ennustettua.

Germaniumin talteenotto ioninvaihtohartseilla

Työssä tutkittiin laboratorio-olosuhteissa germaniumin talteenottoa happamista hydrometallurgisista sulfaattiliuoksista käyttäen kaupallisia ioninvaihtohartseja. Germaniumin talteenottoa tutkittiin sekä tasapaino- että kolonnikokein syöttöliuoksista joiden pH oli alueella 0,8–3,0. Tutkituista hartseista parhaiten germanium voitiin erottaa käyttäen emäsmuotoista N-metyyli-D-glukamiini-tyyppistä ioninvaihtohartsia (esim. Rohm & Haasin IRA-743). Germaniumille määritettiin adsorptioisotermit tasapainokokein sekä emäs- että happomuotoisilla hartseilla. Adsorptioisotermien perusteella parhaiten germa-niumia adsorboi emäsmuotoinen IRA-743-hartsi kun liuoksen alku-pH oli tutkitun alueen korkein. Lämpötilassa 25 °C kapasiteetti oli 114 mg Ge/g. Tasapainokokein määritettiin emäsmuotoisilla hartseilla germaniumin lisäksi myös kuparia ja kobolttia sisältävillä liuoksilla Ge:n jakaantumisvakiot sekä erotustekijät Ge/Cu ja Ge/Co. Havaittiin, että IRA-743:lla alku-pH:ssa 3,0 Ge:n jakaantumisvakiot sekä erotustekijät Ge/Cu ja Ge/Co olivat selvästi suuremmat kuin muilla tutkituilla hartseilla. Arseenin, nikkelin, sinkin ja rauta(III):n adsorboitumista emäsmuotoiseen IRA-743:een tutkittiin monimetallisella liuoksella syöttöliuoksen pH:n ollessa alueella 1,4–3,6. Kokeissa havaittiin, että hartsi adsorboi hieman Ni:a ja Zn:a tasapaino-pH:n ollessa yli 5,5. Arseenia ei tutkitulla pH-alueella havaittu adsorboituvan. Lisäksi huomattiin, että rauta alkaa saostua pH:n ollessa hieman alle kolme. Kolonnikokeissa havaittiin, että emäsmuotoinen IRA-743-hartsi toimii hyvin germaniumin talteenotossa myös kolonnissa. Pelkästään germaniumia ja kobolttia sisältäneellä liuoksella hartsin dynaamiseksi kapasiteetiksi saatiin 54 mg Ge/g. Germaniumin eluointi IRA-743:sta onnistui parhaiten 0,5 M H2SO4:lla. Kolonnikokeita IRA-743:lla ajettiin myös monimetallisilla liuoksilla, mutta silloin havaittiin hartsin kapasiteetin pienenevän hartsin myrkyttymisen takia.

Eletrodissolução de ligas de latão empregando sistemas de análise em fluxo para a determinação de cobre, zinco e chumbo por ICP-AES

An on-line electrodissolution procedure implemented in a flow injection system for determination of copper, zinc and lead in brasses alloys by ICP-AES is described. Sample dissolution procedure was carried out by using a PTFE chamber and a DC power supply with constant current. Solid sample was attached to chamber as anode and a gold tubing coupled in the chamber was used as cathode. An electrolytic solution flowing through the gold tubing closed the electric circuit with sample, in order to provide condition for electric dissolution when the DC power supply was switched on. The best results were achieved by using a 1.5 mol l-1 nitric acid solution as electrolyte and a 2.5 A current intensity. The procedure presented a good performance characterized by a relative standard deviation better than < 5% (n=5) and a sample throughput of 180 determinations per hour for Cu, Zn and Pb. Results were in agreement with those obtained by conventional acid dissolution (99% confidence level).

Pré-concentração de chumbo e cádmio em um sistema de micro extração líquido-líquido e determinação por espectrometria de absorção atômica com chama

A method for determination of lead and cadmium in aqueous samples using solvent microextraction and dithizone as complexing agent with FAAS was developed. Solvent microextraction parameters were optimized. The effect of foreign ions on the extraction yields was studied. The extraction was carried out until the aqueous to organic phase ratio achieved a 250 fold preconcentration of metals. For preconcentration times of 4 min the 3sigma detection limits, relative standard deviations (n=7) and linear calibration ranges were 1.6 mug L-1, 5.8% and 10.0 -- 80.0 mug L-1 for lead and 11.1 ng L-1, 5.9% and 0.3 -- 3.0 mug L-1 for cadmium, respectively. The solvent microextraction procedure presented here was applied to the determination of lead and cadmium in natural waters.

Reagenssin pinta-aktiivisuuden hyödyntäminen sinkin uutossa

Työssä tutkittiin sinkin uutossa käytettävän di(2-etyyliheksyyli)fosforihappo (D2EHPA) -uuttoreagenssin faasikäyttäytymistä ja miten laimentimen koostumus, lämpötila ja orgaanisen faasin sinkkipitoisuus vaikuttavat faasitasapainoon. Laimentimen vaikutuksen havaittiin olevan pientä, kun taas lämpötilan nostaminen yli huoneenlämpötilan leventää faasidiagrammin yksifaasialuetta. Pienet orgaanisen faasin sinkkipitoisuudet eivät juuri vaikuta faasitasapainoon. Sinkin ja D2EHPA:n moolisuhteen ollessa välillä 0,1–0,2 kompleksin rakenne ilmeisesti muuttuu. Sinkkipitoisuuden kasvaessa yksifaasialue muodostuu pienemmillä ammoniakkimäärillä. Suurilla orgaanisen faasin sinkkipitoisuuksilla ja ammoniakkimäärillä muodostuu orgaanisen faasin ja vesifaasin välille kolmas nestefaasi. D2EHPA:n (40 p %) vesipitoisuuden ja viskositeetin pH riippuvuutta tutkittiin, kun laimentimena oli alifaattinen hiilivetyliuotin. Nostettaessa pH yli 3,5:n uuttoreagenssi alkoi muodostaa käänteismisellejä, jolloin orgaanisen faasin vesipitoisuus ja viskositeetti kasvoivat eksponentiaalisesti. Sinkin mukana uuttautuu epäpuhtauksia kuten Al3+, Co2+, Cu2+, Na+, Ni2+, Cl- ja F-. Takaisinuuton kautta epäpuhtaudet joutuvat talteenottoelektrolyysiin, jossa ne voivat vaikuttaa tuotteen laatuun ja laskea virtahyötysuhdetta. Tarkoituksena oli tutkia väheneekö epäpuhtauksien myötäuuttautuminen jollakin tietyllä sinkin latausasteella. Fluoridin ja kuparin uuttautumisen havaittiin vähenevän vasta, kun sinkin pitoisuus orgaanisessa faasissa oli yli 20 g/L lämpötilasta riippumatta. Fluoridi uuttautuu mahdollisesti alumiinikompleksina ja/tai fluorihappona. Koboltin ja nikkelin myötäuuttautumisen havaittiin vähenevän, kun sinkin latausaste oli yli 10 g/L. Natrium ja kloridi eivät myötäuuttautuneet.

Estudo da capacidade de complexação e sua relação com algumas variáveis ambientais em cinco represas do Rio Tietê/Brasil

The copper and cadmium complexation properties in natural sediment suspensions of reservoirs of the Tietê River were studied using the solid membrane copper and cadmium ion-selective electrodes. The complexation and the average conditional stability constants were determined under equilibrium conditions at pH=6.00 ± 0.05 in a medium of 1.0 mol L-1 sodium nitrate, using the Scatchard method. The copper and cadmium electrodes presented Nernstian behavior from 1x10-6 to 1x10-3 mol L-1 of total metal concentration. Scatchard graphs suggest two classes of binding sites for both metals. A multivariate study was done to correlate the reservoirs and the variables: complexation properties, size, total organic carbon, volatile acid sulfide, E II and pH.

Composição química de um resíduo alcalino da indústria de papel e celulose (DREGS)

Dregs is an alkaline solid by-product generated in the cellulose manufacturing industry that could be used to correct soil acidity. The present study aimed to evaluate the chemical composition of this product and some of its properties. The dregs presented 354 g kg-1 of calcium, neutralization capacity of 80.3%, and pH 10.7, besides low concentration of sodium (10.2 g kg-1), lead (62.9 mg kg-1) and cadmium (5.6 mg kg-1). Thus, it is a product that can safely be used to increase the soil pH.

Processamento de pilhas do tipo botão

This work presents hydrometallurgical routes for recovering valuable elements from spent button cells, based on leaching of internal components with sulfuric acid (Li/MnO2 and Zn-air) or nitric acid (Ag-Zn), at 90 ºC for 2h. Slow evaporation of the leachate crystallized MnSO4.H2O, whereas lithium was partially recovered as LiF. Mercury present in Zn-air and Ag-Zn samples was precipitated as HgS. Silver was recovered as AgCl before mercury precipitation. Zinc and iron were precipitated as hydroxides. The amount of iron varied according to the intensity of the corrosion of the external cell case. Final wastes are neutral and colorless sodium sulfate/nitrate solutions.

Avaliação da lixiviação do cádmio e níquel provenientes da degradação de baterias níquel-cádmio em uma coluna de solo

Spent nickel-cadmium (Ni-Cd) batteries and salts of nickel and cadmium were placed in two different columns of soil for a period of two years. A leaching solution was passed through them at ambient temperature in this period. The behavior of metals in each column was then evaluated. Under the conditions of the experiment, cadmium and nickel demonstrated the potential to contaminate and affect the natural cycles of soil. The disposal of Ni-Cd batteries directly to the soil also increased the concentration of nickel (349 mg kg-1) and cadmium (2890 mg kg-1), sometimes exceeding the intervention values defined in CONAMA resolution 420/09.

Epäpuhtausmetallien talteenotto sinkkiprosessissa

There are small amounts of valuable metals, such as indium, gallium and germanium, in zinc process solutions. Their solvent extraction was studied in this work in sulphate solutions containing zinc and other metals present in industrial solutions. It was discovered, that a commercial bis(2-ethylhexyl)phosphate (D2EHPA) extractant can be used to extract indium and gallium. Indium was extracted separately at a higher acid concentration than gallium. Zinc was co-extracted faster than gallium and almost as much as gallium at the same pH. However, the scrubbing of zinc was possible using a dilute sulphuric acid and a short contact time while gallium losses were small. Both indium and gallium were stripped with sulphuric acid. Germanium was extracted with 5,8-diethyl-7-hydroxydodecane-6-oxime with the commercial name of LIX 63. Unlike other metals in the solution the extraction of germanium increased with different extractants as the acidity increased. Germanium extraction isotherm was measured for a 125 g/L sulfuric acid solution. The loaded organic phase was washed with pure water. It removed the co-extracted acid and part of the germanium and extracted impurities such as iron and copper. Germanium was stripped using a NaOH solution. A process model utilizing own experimentally determined extraction, scrubbing and stripping isotherms was made with HSC Sim software developed by Outotec Oyj. The model based on McCabe–Thiele diagrams was used in sizing the necessary amount of stages and phase ratios in a recovery process. It was concluded, that indium, gallium and germanium can be recovered in the process from a feed where their concentrations are low (<300 ppm). In an example case the feed contained also more than 20 g/L zinc and 2–8 g/L iron, aluminium and copper. The recoveries of indium, gallium and germanium were more than 90 % when 1–3 stages were used in each extraction, scrubbing and stripping section. Since the number of stages is small mixer-settlers would be well suited for this purpose.

Nutrients in the cassava (Manihot esculenta Crantz) leaf meal at three ages of the plant

The high number of cassava cultivars adapted to many different regions provides a wide variation in the chemical composition of cassava leaves meal (CLM). Therefore, the contents of some nutrients in CLM from five cultivars at three ages of the plant were investigated in order to select the cultivars and ages with superior levels of these nutrients. When the plants were 12 months old, the highest levels of crude protein (CP), beta-carotene, iron, magnesium, phosphorus and sulfur were observed. The IAC 289-70 cv. showed the highest levels of magnesium, as well as considerable contents of CP, beta-carotene, iron, zinc and sulfur, which did not differ statistically from the cultivars showing the highest levels of these nutrients.

Chemical characteristics of pequi fruits (Caryocar brasiliense Camb.) native of three municipalities in the State of Goiás - Brazil

In order to assure that the use of cerrado fruits occur in a sustainable way, studies to investigate their characteristics are extremely relevant. In this context, the present study aims to describe some chemical parameters of pequi fruits picked in three municipalities in southwestern Goiás State (Jataí, Rio Verde, and Serranópolis). In each city, two populations of pequi trees - pequizeiros, denominated areas, were selected. In each area, eight trees were selected for the fruit to be picked. The contents of phosphorus, potassium, calcium, magnesium, nitrogen, zinc, and ether extract were determined in the samples. The results demonstrate differences between the chemical characteristics studied for the fruits picked in different areas, which does not seem to vary in a significant way. Comparing the contents obtained in the present study with those required as human daily supply, further studies are recommended aiming at using the pequi fruit as a complementary alternative source of magnesium, manganese, and copper.

Heavy metals investigation in bovine tissues in Brazil

The aim of this study was to investigate the presence of arsenic, lead, and cadmium residues in samples of liver, kidney, and muscle of cattle during the years of 2002 to 2008. A total of 1017 samples from 20 Brazilian States were used. The samples were analyzed at the National Agricultural Laboratory using the atomic absorption spectrometry technique. Arsenic residues were detected in 15.7% of liver samples and 28.7% of kidney samples although no results have exceeded the MRL. With regard to lead, 16 samples of liver and 74 samples of kidney were contaminated (5.2 and 10.9%, respectively). Among these samples, only one liver and two of kidney samples had lead levels above the MRL. Cadmium was found with levels below the MRL in 12.5% of the liver samples, and only 3 samples (1%) were quantified above the MRL. Among the kidney samples, 420 (60.8% of the total tested) had cadmium residues, and five of them exceeded the limits established by legislation. It is concluded that the Brazilian meat meets the legislation requirements without putting consumer's healthy at risk since as it satisfies the national and international food-safety conditions.

Étude structure-fonction des fructose-1,6-bisphosphate aldolases métallo-dépendantes : mécanisme catalytique et développement d’antimicrobiens

Les fructose-1,6-bisphosphate aldolases (FBPA) sont des enzymes glycolytiques (EC 4.1.2.13) qui catalysent la transformation réversible du fructose-1,6-bisphosphate (FBP) en deux trioses-phosphates, le glycéraldéhyde-3-phosphate (G3P) et le dihydroxyacétone phosphate (DHAP). Il existe deux classes de FBPA qui diffèrent au niveau de leur mécanisme catalytique. Les classes I passent par la formation d’un intermédiaire covalent de type iminium alors que les classes II, métallodépendantes, utilisent généralement un zinc catalytique. Contrairement au mécanisme des classes I qui a été très étudié, de nombreuses interrogations subsistent au sujet de celui des classes II. Nous avons donc entrepris une analyse détaillée de leur mécanisme réactionnel en nous basant principalement sur la résolution de structures cristallographiques. De nombreux complexes à haute résolution furent obtenus et ont permis de détailler le rôle de plusieurs résidus du site actif de l’enzyme. Nous avons ainsi corrigé l’identification du résidu responsable de l’abstraction du proton de l’O4 du FBP, une étape cruciale du mécanisme. Ce rôle, faussement attribué à l’Asp82 (chez Helicobacter pylori), est en fait rempli par l’His180, un des résidus coordonant le zinc. L’Asp82 n’en demeure pas moins essentiel car il oriente, active et stabilise les substrats. Enfin, notre étude met en évidence le caractère dynamique de notre enzyme dont la catalyse nécessite la relocalisation du zinc et de nombreux résidus. La dynamique de la protéine ne permet pas d’étudier tous les aspects du mécanisme uniquement par l’approche cristallographique. En particulier, le résidu effectuant le transfert stéréospécifique du proton pro(S) sur le carbone 3 (C3) du DHAP est situé sur une boucle qui n’est visible dans aucune de nos structures. Nous avons donc développé un protocole de dynamique moléculaire afin d’étudier sa dynamique. Validé par l’étude d’inhibiteurs de la classe I, l’application de notre protocole aux FBPA de classe II a confirmé l’identification du résidu responsable de cette abstraction chez Escherichia coli (Glu182) mais pointe vers un résidu diffèrent chez H. pylori (Glu149 au lieu de Glu142). Nos validations expérimentales confirment ces observations et seront consolidées dans le futur. Les FBPA de classe II sont absentes du protéome humain mais sont retrouvées chez de nombreux pathogènes, pouvant même s'y révéler essentielles. Elles apparaissent donc comme étant une cible idéale pour le développement de nouveaux agents anti-microbiens. L’obtention de nouveaux analogues des substrats pour ces enzymes a donc un double intérêt, obtenir de nouveaux outils d’étude du mécanisme mais aussi développer des molécules à visée pharmacologique. En collaboration avec un groupe de chimistes, nous avons optimisé le seul inhibiteur connu des FBPA de classe II. Les composés obtenus, à la fois plus spécifiques et plus puissants, permettent d’envisager une utilisation pharmacologique. En somme, c’est par l’utilisation de techniques complémentaires que de nouveaux détails moléculaires de la catalyse des FBPA de classe II ont pu être étudiés. Ces techniques permettront d’approfondir la compréhension fine du mécanisme catalytique de l’enzyme et offrent aussi de nouvelles perspectives thérapeutiques.