No description available.

No description available.

A kinetic study of the oxidation of arsenic(III) by chromium(VI) was made in acetic acid-acetate buffers at ionic strengths 1.5M and 3.0M. The reaction rate showed a first order dependence on the arsenic(III), total chromium(VI), and acetic acid concentrations. Two possible mechanisms for the reaction have been suggested. One possibility is the formation of an arsenic-chromium adduct in which either the acid chromate or dichromate ion is involved. A second possible mechanism postulates adduct formation involving only the acid chromate ion, followed by a CrO₄= catalyzed decomposition of the adduct. In either suggested mechanism, the acetate and hydroxide ion catalyzes the decomposition of the adduct. The rate dependence on total chromium(VI) concentration is contrary to previous reports which postulate an adduct or ester mechanism. Induced reaction studies show the initial step involves the oxidation of one arsenic(III) species by chromium(VI) with the formation of tetravalent chromium as-a reactive intermediate. The stoichiometry or the overall reaction was found to be 3 As(III) + 2 Cr(VI) = 3 Aa(V) + 2 Cr(III). / M.S.

Two trials (n = 160) were conducted to evaluate the effects of the halothane gene, chromium picolinate supplementation, and sex on growth performance, carcass characteristics, and meat quality in pigs. Halothane negative (NN) and halothane carrier (Nn) pigs (barrows, gilts) were supplemented with either 0 or 200 ppb chromium picolinate from 28.7 to 107.3 kg. There were no differences between genotypes for ADG or G/F. Chromium had no significant effect on any growth, carcass, or muscle quality characteristics, although chromium-fed pigs were slightly fatter. Barrows gained faster (P < .001) and consumed more feed (P < .001) than gilts, yielding heavier (P < .001) carcasses, and heavier (P < .05) wholesale cuts. Gilts had less backfat (P < .001) and larger (P < .01) LMA, and tended to gain more efficiently than barrows. Carrier pigs had lower pH values, higher CIE L* values, higher drip loss, and lower protein solubility (P < .05), all indicators of decreased quality. Chromium supplementation resulted in pork with higher (P<.05) CIE a*, CIE b*, and Chroma C values. Halothane carrier barrows and all gilts that were not fed chromium had lower lipid muscle content than NN barrows (P < .05). Gilts had higher CIE L* and a* values (P < .001), less lipid, and higher moisture percentage (P < .02) than barrows. Chromium picolinate did not negatively affect pork muscle quality. / Master of Science

An investigation was conducted to determine if Sn atoms could be substituted for Si atoms in the compound Cr₃Si. Prom size factor considerations, the feasibility that this substitution should occur seemed reasonable. However, attempts to make the substitution were unsuccessful. A model of the Cr₃O-type compounds, of which Cr₃Si is a representative, is proposed. From this model substitution of a Sn atom for a Si atom would require the formation of a double bond. The possibility of this double bond being unable to form may explain the unsuccessful attempts to make the above substitution. / Master of Science

A hard chromium electroplating process is normally used for preventing mechanical and electrical parts such as roller, piston and mold from the harmful environments and giving the good physical properties on the surface such as increased wear resistance, increased hardness, low frictional coefficient as well as good aesthetic look on the surface of workpieces. The problem that often found in this process is the deflected workpieces after plating process due to the low plating performance during a plating period. These deflected workpieces are needed to replating it again. However, the replating method causes a large amount of resource consumptions and increases the production time. To handle this problem, the plating solution temperature is needed to maintain the plating solution temperature at a set point about 50 °C in order to improve the plating performance during the plating period and decrease the occurrence of the deflected workpieces. In this work, the mathematical models are developed to explain the dynamic behavior of the plating solution temperature during the plating time and validated with the real data from a plant. The conventional (PID) controller is applied to this process for the purpose of keeping the plating solution temperature at the set point throughout the plating time. The result demonstrates that the developed mathematical models can be used to explain the dynamic behavior of the plating solution temperature because it gives the good simulation of the plating solution temperature with a slightly different from the real data. Furthermore, the PID controller shows the high control performance for maintaining the plating solution temperature at the set point throughout the plating period with small overshoot at the beginning of every batch.

A detailed study has been carried out to investigate the dissolution characteristics of unstabilized and stabilized CrO₂ particles. It has been found that on contact of CrO₂ with aqueous solutions, it dissolves by disproportionation reaction to HCrO₄ and Cr2O₃. XPS study has shown that stabilization of CrO₂ particles with bisulfite solution leads to the formation of Cr2O₃. However, because of agglomeration of the CrO₂ particles due to their magnetic properties, not all of the surface is completely stabilized. The electrokinetic characteristics of Cr(IV) and Cr(III) oxides in aqueous solutions have been investigated. Experiments suggest that sulfite ions chemisorb strongly on Cr₂O₃ particles. Experiments have also been carried out to study the adsorption of sodium dodecyl sulfate (SDS) on Cr₂O₃ particles. With increasing SDS concentration, Cr₂O₃ becomes less positively charged and ultimately negatively charged when the surfactant concentration exceeds 10⁻³ M. This suggests that SDS specifically adsorbs onto the oxide.

Binuclear mixed biscarbene complexes of bithiophene were synthesized via the classical Fischer method of synthesis. The metal carbonyls, Mo(CO)6, Cr(CO)6, W(CO)6 and Mn(MeCp)(CO)3 were reacted with dilithiated bithiophene to afford complexes of the formula, [M(CO)5{C(OEt)C4H2S-C4H2SC(OEt})M'(CO)5] (in case of manganese, M(CO)5 is replaced with MMeCp(CO)2), where [M] and [M'] are the metal carbonyls in different combinations. Quenching was achieved with triethyl oxonium tetrafluoroborate. In all the reactions the products included monocarbene complexes, biscarbene complexes and the decomposition products. C-C coupling reactions produced unexpected biscarbene complexes of Cr, W, and Mo having extended bithiophene spacers. The complexes were of the formula, [M(CO)5{C(OEt)C4H2S-C4H2SC(R)-C(R)C4H2S-C4H2SC(OEt})M'(CO)5] (R = O, OH or OEt). These complexes were characterized with NMR, infrared spectroscopy and some with mass spectrometry. Furthermore, three biscarbene complexes of the metal combinations Mo(CO)6 and Cr(CO)6, W(CO)6 and Cr(CO)6, and Mn(MeCp)(CO)3 and Cr(CO)6 were all reacted with 3-hexyne. The result was the benzannulation or the Dötz products. / Chemistry / M. Sc. (Chemistry)

No description available.

<p>The production of ferrochromium alloys at Vargön Alloys AB contributes to formation of unwanted ferrochromium dust, which contains toxic Cr(VI). The dust is since summer 2005 treated with an iron-sulphate solution to reduce Cr(VI) to the non-toxic Cr(III). A year later the treatment technique was improved and disposal occurs in cells on the landfill. The cells can be up to 300 m3 and the edges can be made out of fro example concrete. Tests are conducted on the treated dust when it is disposed. The analyses show low contents of Cr(VI), which indicates that the reduction is successful. Analyses of leakage water from a small scale cell however showed an increasing content of Cr(VI) and pH under the first two months.</p><p>This thesis has evaluated the new treatment method. An investigation was conducted to determine if the same changes have occurred in the full scale cells. Half of the 18 collected samples from the disposed dust showed high or very high contents of Cr(VI). The other half had a almost no detectable content. pH was over 12. No correlation between Cr(VI)-content and pH, conductivity, age or water content in the disposed dust could be shown.</p><p>An experiment was also performed in small scale to reduce the number of influencing parameters. The results showed that if the dust has access to oxygen the Cr(VI) content increases during the first days from a few mg/kg dry substance to over 20 mg/kg dry substance, a level which was maintained during the rest of the experiment period. The content of Cr(VI) was almost constant at 4 mg/kg dry substance when oxygen was eliminated during the whole experiment period. When the water content was below 5 %, the content of chromium did not increase more.</p><p>Since almost all newly created Cr(VI) is reduced to Cr(III) by the addition of ferrous sulphate, recreation of Cr(VI) occurs. Today there is now possibility to follow the changes in the dust from untreated to after disposed. The addition of iron-sulphate is based upon an average Cr(VI) content in the dust and the variation of disposal occasions can be significant. To determine if the increase in Cr(VI) is caused of an incorrect addition of solution a smaller disposal cell can be constructed. The initial content of Cr(VI) can be controlled and the dust can be examined during the time it ages. If the dosage could be improved the addition can be optimized. It is also important to minimize the infiltration and accelerate the drying of the slurry since the Cr(VI) content can increase the as long as the water content is high the Cr(VI) content can increase.</p> / <p>Vid produktionen av ferrolegeringar på Vargön Alloys AB bildas ferrokromstoft som en oönskad biprodukt, vilken innehåller hälsofarligt sexvärt krom. Sedan sommaren 2005 behandlas stoftet med järnsulfatlösning för att reducera Cr(VI) till mindre hälsofarliga Cr(III). Ett år senare förbättrades tekniken och deponering sker sedan dess i iordningställda celler på deponin. Cellerna rymmer cirka 300 m3 och har kanter av bland annat betongstöd. Provtagning sker på det behandlade stoftet i samband med deponeringen. Analyserna visar mycket låga halter av Cr(VI), vilket tyder på att reduktionen lyckas. Analyser av lakvatten från en småskalig provcell visade däremot att Cr(VI)-halter och pH ökade under de två första månaderna.</p><p>Detta arbete har utvärderat den nya behandlingsmetoden. Undersökning huruvida samma förändring har skett i fullskaliga celler har utförts. Utav de 18 prov som inhämtades från det deponerade stoftet visade hälften på höga eller mycket höga Cr(VI)-halter och resterande hade nästan omätbara halter. I det deponerade stoftet var pH genomgående drygt 12. Inget samband mellan Cr(VI)-halt och pH, konduktivitet, ålder eller vatteninnehåll i deponerat stoft erhölls.</p><p>Försök utfördes även i liten skala i för att minska antalet påverkande parametrar. Utan tillgång till syre var Cr(VI)-halten cirka 4 mg/kg torrsubstans under hela försöksperioden. Försöken visade att om stoftet har tillgång till syre ökar Cr(VI) från några mg/kg torrsubstans till dryga 20 mg/kg torrsubstans efter bara några dagar. Halten förblev konstant under resten av försökstiden. Ett samband som sågs var att när Cr(VI)- halten har stagnerat är vatteninnehållet i provet under 5 %.</p><p>Eftersom nästan allt krom reduceras till Cr(III) vid tillsatsen av järnsulfatlösning har det nyreducerade Cr(VI) återbildats. I nuläget går det inte att följa hur stoftet förändras från obehandlat och vad som händer när det åldras efter att det har behandlats och deponerats. Tillsatsen av järnsulfat doseras efter en medelhalt Cr(VI)-innehåll i stoftet och variationen i Cr(VI)-halt mellan deponeringstillfällen kan vara stor. För att avgöra om ökningen av Cr(VI) beror på felaktig tillsatts av järnsulfatlösning kan en mindre deponeringscell anläggas. Ingående Cr(VI)-halter kan kontrolleras och stoftet kan undersökas medan det åldras på deponin. Visar det sig att dosering behöver förbättras kan tillsatsen optimeras. Det är även viktigt att minska infiltrationen samt påskynda torkningen av slurryn eftersom så länge vattenhalten är hög kan Cr(VI)-halterna öka.</p>