934 resultados para batch changeover


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Työssä tutkittiin pienpuhdistamon ylijäämälietteen ominaisuuksia ja käyttäytymistä pienpuhdistamon ylijäämälietteen tiivistys- tai kuivausmenetelmän kehittämisen teoriapohjaksi. Työ sisältää myös lietteiden tiivistysmenetelmien kustannustarkastelua. Kokeellisessa osuudessa käytettiin työn teettäjän Oy KWH Pipe Ab:n valmistamien pienpuhdistamojen ylijäämälietettä. Tutkittava ylijäämäliete oli peräisin asukasvastineluvultaan 5–95 pienistä aktiivilietelaitepuhdistamoista. Tiivistys- tai kuivausmenetelmän kehittämisen tarkoituksena on saavuttaa kustannussäästöjä pienpuhdistamon ylijäämälietteen kuljetusmatkojen vähentämisen kautta. Soveltuvia vertailtavia sovelluksia ovat staattiseen laskeuttamiseen perustuvat menetelmät, mekaaniset ruuvi- ja linkokuivaimet, kuivauslava ja flotaatio. Tarkasteltavien menetelmien tuli olla käytöltä ja huollolta sekä käyttökuluiltaan edullisia ja yksinkertaisia. Ylijäämälietteiden ominaisuuksia ja käyttäytymistä tutkittiin kirjallisuuslähteistä ja käytännön kokein. Kokeissa tarkasteltiin ylijäämälietteen laskeutumis- ja nousuominaisuuksia, redox-potentiaalin vaihtelua seisovassa näytteessä ja flotaation onnistumista testattavalle lietteelle. Kokeet tehtiin kullakin kerralla eri ajankohtana otetuille lietenäytteille, käytettyjä puhdistamoja oli useita ja mitoitus, kuormitus sekä jäteveden laatu vaihteli paljon.

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This dissertation is based on four articles dealing with modeling of ozonation. The literature part of this considers some models for hydrodynamics in bubble column simulation. A literature review of methods for obtaining mass transfer coefficients is presented. The methods presented to obtain mass transfer are general models and can be applied to any gas-liquid system. Ozonation reaction models and methods for obtaining stoichiometric coefficients and reaction rate coefficients for ozonation reactions are discussed in the final section of the literature part. In the first article, ozone gas-liquid mass transfer into water in a bubble column was investigated for different pH values. A more general method for estimation of mass transfer and Henry’s coefficient was developed from the Beltrán method. The ozone volumetric mass transfer coefficient and the Henry’s coefficient were determined simultaneously by parameter estimation using a nonlinear optimization method. A minor dependence of the Henry’s law constant on pH was detected at the pH range 4 - 9. In the second article, a new method using the axial dispersion model for estimation of ozone self-decomposition kinetics in a semi-batch bubble column reactor was developed. The reaction rate coefficients for literature equations of ozone decomposition and the gas phase dispersion coefficient were estimated and compared with the literature data. The reaction order in the pH range 7-10 with respect to ozone 1.12 and 0.51 the hydroxyl ion were obtained, which is in good agreement with literature. The model parameters were determined by parameter estimation using a nonlinear optimization method. Sensitivity analysis was conducted using object function method to obtain information about the reliability and identifiability of the estimated parameters. In the third article, the reaction rate coefficients and the stoichiometric coefficients in the reaction of ozone with the model component p-nitrophenol were estimated at low pH of water using nonlinear optimization. A novel method for estimation of multireaction model parameters in ozonation was developed. In this method the concentration of unknown intermediate compounds is presented as a residual COD (chemical oxygen demand) calculated from the measured COD and the theoretical COD for the known species. The decomposition rate of p-nitrophenol on the pathway producing hydroquinone was found to be about two times faster than the p-nitrophenol decomposition rate on the pathway producing 4- nitrocatechol. In the fourth article, the reaction kinetics of p-nitrophenol ozonation was studied in a bubble column at pH 2. Using the new reaction kinetic model presented in the previous article, the reaction kinetic parameters, rate coefficients, and stoichiometric coefficients as well as the mass transfer coefficient were estimated with nonlinear estimation. The decomposition rate of pnitrophenol was found to be equal both on the pathway producing hydroquinone and on the path way producing 4-nitrocathecol. Comparison of the rate coefficients with the case at initial pH 5 indicates that the p-nitrophenol degradation producing 4- nitrocathecol is more selective towards molecular ozone than the reaction producing hydroquinone. The identifiability and reliability of the estimated parameters were analyzed with the Marcov chain Monte Carlo (MCMC) method. @All rights reserved. No part of the publication may be reproduced, stored in a retrieval system, or transmitted, in any form or by any means, electronic, mechanical, photocopying, recording, or otherwise, without the prior permission of the author.

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A flow injection spectrophotometric procedure is proposed for the determination of paracetamol (acetaminophen) in pharmaceutical formulations. Powdered and liquid samples were previously dissolved/diluted in 0.05 mol L-1 hydrochloric acid solution and a volume of 250 µL was injected directly into a carrier stream of this same acid solution, flowing at 2.5 mL min-1. Paracetamol reacts with sodium hypochlorite forming N-acetyl-p-benzoquinoneimine which then reacts with sodium salicylate in sodium hydroxide solution yielding a blue indophenol dye which was measured at 640 nm in the pH range of 9.5-10.0. Paracetamol was determined in pharmaceutical products in the 1.0 to 100.0 mg L-1 (3.3x10-6 a 6.6x10-4 mol L-1) concentration range, with a detection limit of 0.5 mg L-1 (1.6x10-6 mol L-1). The recovery of this analyte in five samples ranged from 98.0 to 103.6 %. The analytical frequency was 80 determinations per hour and the RSDs were less than 1% for paracetamol concentrations of 25.0, 50.0 and 75.0 mg L-1 (n=10). A paired t-test showed that all results obtained for paracetamol in commercial formulations using the proposed flow injection procedure and a spectrophotometric batch procedure agree at the 95% confidence level.

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Tässä diplomityössä tutkitaan kolmiulotteisen konenak6järjestelmän soveltuvuutta matkapuhelimien alikokoonpanojen testaukseen massatuotannossa. Tavoitteena oli saada tietoa 3D järjestelmän käytettävyydestä suorituskyvyn ja kapasiteetin suhteen sekä selvittää järjestelmän joustavuutta testattavia tuotteita vaihdettaessa. Haluttiin myös selvittää, että ratkaiseeko 3D järjestelmä käytössä olevan 2D järjestelmän kanssa ilmenneitä ongelmia Järjestelmän suorituskykyä tutkittiin tekemällä testiajoja, joista saatuja tuloksia analysoitiin tilastollisella laadunvalvontaohjelmistolla. Varsinaisen kehitystyön teki konenäköjärjestelmiin erikoistunut alihankkija, jolla on kokemusta 3D testauksesta muilta teollisuuden aloilta. Matkapuhelimien alikokoonpanojen testauksessa laatukriteerit ja tarkkuusvaatimukset ovat kuitenkin liian kovia saavutettaviksi 3D lasertriangulaatioon perustuvaa testausjärjestelmää käytettäessä

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The historical development of atomic spectrometry techniques based on chemical vapor generation by both batch and flow injection sampling formats is presented. Detection via atomic absorption spectrometry (AAS), microwave induced plasma optical emission spectrometry (MIP-OES), inductively coupled plasma optical emission spectrometry (ICP-OES) , inductively coupled plasma mass spectrometry (ICP-MS) and furnace atomic nonthermal excitation spectrometry (FANES) are considered. Hydride generation is separately considered in contrast to other methods of generation of volatile derivatives. Hg ¾ CVAAS (cold vapor atomic absorption spectrometry) is not considered here. The current state-of-the-art, including extension, advantages and limitations of this approach is discussed.

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Poly (ethylene) glycol (PEG) and bovine serum albumin (BSA), as additive agents, were used to enhance the activity of immobilized microbial lipase in organic solvent. Controlled pore silica (CPS) was selected as matrix and different immobilization procedures were evaluated: directly lipase binding on CPS and simultaneous addition of lipase and additive agent on the same support. The highest coupling yield (59.6%) was attained when the immobilization procedure was performed at lipase loading of 150 U/g support in the presence of PEG-1.500. This immobilized system was used in esterification reactions under repeated batch cycles and the biocatalyst half-life was found to increase 2.7 times when compared with the control.

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Normally, the determination of equilibrium constants (k d) in batch experiments uses a high solution to soil ratio, which does not represent field conditions. In this study we present an alternative method to evaluate adsorption constants, using micro-columns of soil at higher soil to solution ratios. The centrifugation force and equilibration time were investigated. The triadimenol distribution along the column profile is controlled by diffusion and equilibration times greater than 24 h are needed to achieve reproducibility. The centrifugation force must be superior to 670 g in order to guarantee enough extraction of the liquid solution from the soil columns.

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The effect of synthetic zeolites on stabilizing Zn-contaminated soil using 0.01 mol L-1 CaCl2 leaching solution in batch experiments was investigated. The zeolites were synthesized from coal ash by hydrothermal treatment with alkaline solution. The additive enhanced the sorption capacity of the soil and reduced leaching. Zinc leaching was reduced by more than 80% using a minimum of 10% additive. The higher cation exchange capacity of the zeolite/soil mixtures and higher pH were responsible for stabilizing Zn in soil. The poly(2-aminobenzenesulfonic acid)-coated mercury thin-film electrode was used for the determination of zinc.

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The application of biocatalysis is a promising field related to new technologies for organic synthesis. The development of immobilization techniques is very important due to the multiple or repetitive use of a single batch of enzymes and the ability to stop the reaction rapidly, at any stage, by removing the enzymes. In most cases, after immobilization, enzymes and microorganisms maintain or even increase their activity and stability. This work presents an overview of the common methods for lipase immobilization in polymers and applications of these systems to obtain compounds of synthetic interest.

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In this study, the preparation of the xerogel anilinepropylsilica is reported. The ability of the xerogel for extracting Al(III), Cr(III) and Fe(III) from ethanol was investigated at 25 ºC. The xerogel adsorption capacities were obtained from the adsorption isotherms by using the batch method. Flame atomic absorption spectrometry (FAAS) was used to estimate the concentration of metal ions in solution. The adsorption affinity follows the series Cr(III) > Fe(III) > Al(III) and the maximum adsorption capacities of the metal ions were 0.61, 0.52 and 0.43 mmol g-1, respectively.

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The present study consists in evaluating the NaX zeolite efficiency in removing Cu2+ from aqueous solutions, for future use of NaX in removing metals from wastewaters. The experiments were performed in batch systems (with shaking and continous stirring) and for different time intervals (1 to 24 h). Three particle sizes were employed: < 850 µm, 850 µm - 1 mm and 3 mm. It has been concluded that it is possible to employ the NaX zeolite for metal removal and the particle size plays an important role in the adsorption process. Specifically, NaX zeolites of smaller particle size achieved the maximum adsorption capacity of 152.36 mg of Cu2+/g of zeolite at pH = 4.5.

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Two samples of residues from iron mining plants have been investigated for their retention capacity of As, Cu, Cr, and Pb. The sample with the higher content of iron oxides showed the highest capacity to retain metals. The adsorption affinity series changes from Pb>Cu>Cr~As to As>Pb>Cu>Cr or As>Cu>Cr>Pb, depending on the material and the concentration of the initial solution. In the competitive environment, the Pb adsorption decreases and the As, Cu and Cr adsorption increases. Sequential extraction procedures, carried out after adsorption batch experiments, showed that the most important adsorption process occurs in the oxide fraction and that the major part of the absorbed metal is remobilized from exchangeable and oxide fractions.

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The driving force of boron adsorption on some tropical soils was evaluated by means of thermodynamic parameters. The batch method was employed, and the reaction was monitored at different pH values. The Langmuir equation successfully fitted the experimental results and provided reasonable isotherm parameters. Boron adsorption increased as a function of the pH of the soil solution and the concentration of added boron. The reaction was favorable and proceeded spontaneously, being strongly exoergic, as indicated by a negative free energy (deltaG) and a separation factor (K R) < 1. The boron adsorption phenomenon and the soil-solution interface were thermodinamically described using a theoretical model.

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The production of cashew apple wine has the purpose of minimizing the wastage in the Brazilian cashew production. Knowing that the cashew apple fermentation produces a good cashew wine, a study of alcoholic fermentation kinetics of the cashew apple and the physico-chemical characterization of the product were made. The cashew wine was produced in an stirred batch reactor. The results of the physico-chemical analysis of volatiles, residual sugars, total acidity and pH of cashew wine showed that their concentrations were within the standard limits established by the Brazilian legislation for fruit wines.

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There is great interest nowadays in the use of preparative liquid chromatography as an effective tool for the production of enantiomerically pure, or enriched, compounds for the pharmaceutical industry. To make the chromatographic process economically attractive, attention is now focused on the choice of the chromatographic operating mode to minimize eluent consumption and to maximize productivity. Among the alternatives to the traditional batch chromatography, attention is now shifting towards simulated moving bed (SMB) technologies and a review covering the latest developments in this area seems timely. Several aspects of this important analytical technique are presented and details concerning the SMB technology for process optimization are outlined.