Development of descriptor tools for the characterization of Australian sugar mill evaporator scale

Cleaning of sugar mill evaporators is an expensive exercise. Identifying the scale components assists in determining which chemical cleaning agents would result in effective evaporator cleaning. The current methods (based on x-ray diffraction techniques, ion exchange/high performance liquid chromatography and thermogravimetry/differential thermal analysis) used for scale characterisation are difficult, time consuming and expensive, and cannot be performed in a conventional analytical laboratory or by mill staff. The present study has examined the use of simple descriptor tests for the characterisation of Australian sugar mill evaporator scales. Scale samples were obtained from seven Australian sugar mill evaporators by mechanical means. The appearance, texture and colour of the scale were noted before the samples were characterised using x-ray fluorescence and x-ray powder diffraction to determine the compounds present. A number of commercial analytical test kits were used to determine the phosphate and calcium contents of scale samples. Dissolution experiments were carried out on the scale samples with selected cleaning agents to provide relevant information about the effect the cleaning agents have on different evaporator scales. Results have shown that by simply identifying the colour and the appearance of the scale, the elemental composition and knowing from which effect the scale originates, a prediction of the scale composition can be made. These descriptors and dissolution experiments on scale samples can be used to provide factory staff with an on-site rapid process to predict the most effective chemicals for chemical cleaning of the evaporators.

Development of descriptor tools for the characterisation of Australian sugar mill evaporator scale

Cleaning of sugar mill evaporators is an expensive exercise. Identifying the scale components assists in determining which chemical cleaning agents would result in effective evaporator cleaning. The current methods (based on x-ray diffraction techniques, ion exchange/high performance liquid chromatography and thermogravimetry/differential thermal analysis) used for scale characterisation are difficult, time consuming and expensive, and cannot be performed in a conventional analytical laboratory or by mill staff. The present study has examined the use of simple descriptor tests for the characterisation of Australian sugar mill evaporator scales. Scale samples were obtained from seven Australian sugar mill evaporators by mechanical means. The appearance, texture and colour of the scale were noted before the samples were characterised using x-ray fluorescence and x-ray powder diffraction to determine the compounds present. A number of commercial analytical test kits were used to determine the phosphate and calcium contents of scale samples. Dissolution experiments were carried out on the scale samples with selected cleaning agents to provide relevant information about the effect the cleaning agents have on different evaporator scales. Results have shown that by simply identifying the colour and the appearance of the scale, the elemental composition and knowing from which effect the scale originates, a prediction of the scale composition can be made. These descriptors and dissolution experiments on scale samples can be used to provide factory staff with an on-site rapid process to predict the most effective chemicals for chemical cleaning of the evaporators.

On-line scale monitoring device

Developments in evaporator cleaning have accelerated in the past 10 years as a result of an extended period of research into scale formation and scale composition. Chemical cleaning still provides the most cost effective method of cleaning the evaporators. The paper describes a system that was designed to obtain on-line samples of evaporator scale negating the need to open up hot evaporator vessels for scale collection. This system was successfully implemented in a number of evaporators at a sugar mill. This paper also describes a recent experience in a sugar factory in which the cleaning procedure was slightly modified, resulting in effective removal of intractable scale.

On-line scale monitoring device

Developments in evaporator cleaning have accelerated in the past 10 years as a result of an extended period of research into scale formation and scale composition. Chemical cleaning still provides the most cost effective method of cleaning the evaporators. The paper describes a system that was designed to obtain on-line samples of evaporator scale negating the need to open up hot evaporator vessels for scale collection. This system was successfully implemented in a number of evaporators at a sugar mill. This paper also describes a recent experience in a sugar factory in which the cleaning procedure was slightly modified resulting in effective removal of intractable scale.

Removal of cyanobacteria and cyanotoxins from drinking water by powdered activated carbon adsorption/ultrafiltration

Tese dout., Ciências e Tecnologias do Ambiente, Universidade do Algarve, 2009

Eficácia da imersão e da escovação mecânica combinada com diferentes agentes de limpeza de prótese na redução da viabilidade de biofilme multiespécies

Pós-graduação em Reabilitação Oral - FOAR

Molhabilidade de material reembasador: efeito dos agentes químicos de limpeza

Risk of mechanical injuries contraindicate brushing and elect chemical agents as appropriate for daily cleaning of dentures relined with resilient materials. It was evaluated the effect of denture cleansers on the wettability of denture relining material (Dentusoft, Dental Medrano). We used 20 discs of acrylic resin thermoactivated VipiCril ® with 30mm diameter and 4mm thick, covered by 2mm Dentusoft ®. Divided into 4grupos were stored in artificial saliva at 37 +1 º C for 30 days, immersed daily for 15minutes in distilled water (GI), Corega ® Tabs (GII), a solution of sodium bicarbonate (GIII) or solution of sodium hypochlorite (GIV) after which, on the soft liner were poured 2 ml of type IV gypsum (Durone IV, Dentsply). Reached the final setting of the gypsum specimens were sectioned vertically and medially, settled water with sandpaper No. 400 and mounted on suitable device for reading (in the right and left) of the contact angle Carl Zeiss microscope (precision, 001). The results were submitted to analysis, showed non-normal distribution, opting for non-parametric test. Kruskal Wallis test performed at 5% significance, there was statistical difference between the groups with lower average contact angle for GII. It was concluded that the chemical cleaning Corega Tabs ® allowed a better adaptation of relining the gypsum studied.

Mg/Ca ratios in planktonic foraminifera

The primary Mg/Ca ratio of foraminiferal shells is a potentially valuable paleoproxy for sea surface temperature (SST) reconstructions. However, the reliable extraction of this ratio from sedimentary calcite assumes that we can overcome artifacts related to foraminiferal ecology and partial dissolution, as well as contamination by secondary calcite and clay. The standard batch method for Mg/Ca analysis involves cracking, sonicating, and rinsing the tests to remove clay, followed by chemical cleaning, and finally acid-digestion and single-point measurement. This laborious procedure often results in substantial loss of sample (typically 30-60%). We find that even the earliest steps of this procedure can fractionate Mg from Ca, thus biasing the result toward a more variable and often anomalously low Mg/Ca ratio. Moreover, the more rigorous the cleaning, the more calcite is lost, and the more likely it becomes that any residual clay that has not been removed by physical cleaning will increase the ratio. These potentially significant sources of error can be overcome with a flow-through (FT) sequential leaching method that makes time- and labor-intensive pretreatments unnecessary. When combined with time-resolved analysis (FT-TRA) flow-through, performed with a gradually increasing and highly regulated acid strength, produces continuous records of Mg, Sr, Al, and Ca concentrations in the leachate sorted by dissolution susceptibility of the reacting material. Flow-through separates secondary calcite from less susceptible biogenic calcite and clay, and further resolves the biogenic component into primary and more resistant fractions. FT-TRA reliably separates secondary calcite (which is not representative of original life habitats) from the more resistant biogenic calcite (the desired signal) and clay (a contaminant of high Mg/Ca, which also contains Al), and further resolves the biogenic component into primary and more resistant fractions that may reflect habitat or other changes during ontogeny. We find that the most susceptible fraction of biogenic calcite in surface dwelling foraminifera gives the most accurate value for SST and therefore best represents primary calcite. Sequential dissolution curves can be used to correct the primary Mg/Ca ratio for clay, if necessary. However, the temporal separation of calcite from clay in FT-TRA is so complete that this correction is typically <=2%, even in clay-rich sediments. Unlike hands-on batch methods, that are difficult to reproduce exactly, flow-through lends itself to automation, providing precise replication of treatment for every sample. Our automated flow-through system can process 22 samples, two system blanks, and 48 mixed standards in <12 hours of unattended operation. FT-TRA thus represents a faster, cheaper, and better way to determine Mg/Ca ratios in foraminiferal calcite.

Recuperación de energía de la salmuera

Como consecuencia del proceso de desalación, se produce el vertido al mar de un agua de rechazo hipersalino o salmuera. La salinidad de este vertido es variable, dependiendo del origen de la captación y del proceso de tratamiento. Muchos de los hábitats y biocenosis de los ecosistemas marinos se encuentran adaptados a ambientes de salinidad casi constante y son muy susceptibles a los incrementos de salinidad originados por estos vertidos. Junto con el vertido de salmuera otro de los principales inconvenientes que plantean las plantas desaladoras es el alto consumo energético, con todas las desventajas que esto supone: alto coste del agua desalada para los consumidores, contaminación del medio... El desarrollo de los métodos de vertido, herramientas de gestión de la salmuera, estudios del comportamiento de la pluma salina… ha buscado la mitigación de estos efectos sobre los ecosistemas marinos. El desarrollo en membranas de ósmosis inversa, diseño de bombas y sistemas de recuperación de energía ha permitido también la reducción del consumo energético en las plantas de desalación. Sin embargo, estos campos parecen haber encontrado un techo tecnológico difícil de rebasar en los últimos tiempos. La energía osmótica se plantea como uno de los caminos a investigar aplicado al campo de la reducción del consumo energético en desalación de agua de mar, a través del aprovechamiento energético de la salmuera. Con esta tesis se pretende cumplir principalmente con los siguientes objetivos: reducción del consumo energético en desalación, mitigar el impacto del vertido sobre el medio y ser una nueva herramienta en la gestión de la salmuera. En el presente documento se plantea el desarrollo de un nuevo proceso que utiliza el fenómeno de la ósmosis directa a través de membranas semipermeables, y busca la sinergia desalación depuración, integrando ambos, en un único proceso de tratamiento dentro del ciclo integral del agua. Para verificar los valores de producción, calidad y rendimiento del proceso, se proyecta y construye una planta piloto ubicada en la Planta Desaladora de Alicante II, escalada de tal manera que permite la realización de los ensayos con equipos comerciales de tamaño mínimo. El objetivo es que el resultado final sea extrapolable a tamaños superiores sin que el escalado afecte a la certeza y fiabilidad de las conclusiones obtenidas. La planta se proyecta de forma que el vertido de una desaladora de ósmosis inversa junto con el vertido de un terciario convencional, se pasan por una ósmosis directa y a continuación por una ósmosis inversa otra vez, ésta última con el objeto de abrir la posibilidad de incrementar la producción de agua potable. Ambas ósmosis están provistas de un sistema de pretratamiento físico-químico (para adecuar la calidad del agua de entrada a las condiciones requeridas por las membranas en ambos casos), y un sistema de limpieza química. En todos los ensayos se usa como fuente de disolución concentrada (agua salada), el rechazo de un bastidor de ósmosis inversa de una desaladora convencional de agua de mar. La fuente de agua dulce marca la distinción entre dos tipos de ensayos: ensayos con el efluente del tratamiento terciario de una depuradora convencional, con lo que se estudia el comportamiento de la membrana ante el ensuciamiento; y ensayos con agua permeada, que permiten estudiar el comportamiento ideal de la membrana. Los resultados de los ensayos con agua salobre ponen de manifiesto problemas de ensuciamiento de la membrana, el caudal de paso a través de la misma disminuye con el tiempo y este efecto se ve incrementado con el aumento de la temperatura del agua. Este fenómeno deriva en una modificación del pretratamiento de la ósmosis directa añadiendo un sistema de ultrafiltración que ha permitido que la membrana presente un comportamiento estable en el tiempo. Los ensayos con agua permeada han hecho posible estudiar el comportamiento “ideal” de la membrana y se han obtenido las condiciones óptimas de operación y a las que se debe tender, consiguiendo tasas de recuperación de energía de 1,6; lo que supone pasar de un consumo de 2,44 kWh/m3 de un tren convencional de ósmosis a 2,28 kWh/m3 al añadir un sistema de ósmosis directa. El objetivo de futuras investigaciones es llegar a tasas de recuperación de 1,9, lo que supondría alcanzar consumos inferiores a 2 kWh/m3. Con esta tesis se concluye que el proceso propuesto permite dar un paso más en la reducción del consumo energético en desalación, además de mitigar los efectos del vertido de salmuera en el medio marino puesto que se reduce tanto el caudal como la salinidad del vertido, siendo además aplicable a plantas ya existentes y planteando importantes ventajas económicas a plantas nuevas, concebidas con este diseño. As a consequence of the desalination process, a discharge of a hypersaline water or brine in the sea is produced. The salinity of these discharges varies, depending on the type of intake and the treatment process. Many of the habitats and biocenosis of marine ecosystems are adapted to an almost constant salinity environment and they are very susceptible to salinity increases caused by these discharges. Besides the brine discharge, another problem posed by desalination plants, is the high energy consumption, with all the disadvantages that this involves: high cost of desalinated water for consumers, environmental pollution ... The development of methods of disposal, brine management tools, studies of saline plume ... has sought the mitigation of these effects on marine ecosystems. The development of reverse osmosis membranes, pump design and energy recovery systems have also enabled the reduction of energy consumption in desalination plants. However, these fields seem to have reached a technological ceiling which is difficult to exceed in recent times. Osmotic power is proposed as a new way to achieve the reduction of energy consumption in seawater desalination, through the energy recovery from the brine. This thesis mainly tries to achieve the following objectives: reduction of energy consumption in desalination, mitigation of the brine discharge impact on the environment and become a new tool in the management of the brine. This paper proposes the development of a new process, that uses the phenomenon of forward osmosis through semipermeable membranes and seeks the synergy desalination-wastewater reuse, combining both into a single treatment process within the integral water cycle. To verify the production, quality and performance of the process we have created a pilot plant. This pilot plant, located in Alicante II desalination plant, has been designed and built in a scale that allows to carry out the tests with minimum size commercial equipment. The aim is that the results can be extrapolated to larger sizes, preventing that the scale affects the accuracy and reliability of the results. In the projected plant, the discharge of a reverse osmosis desalination plant and the effluent of a convencional tertiary treatment of a wastewater plant, go through a forward osmosis module, and then through a reverse osmosis, in order to open the possibility of increasing potable water production. Both osmosis systems are provided with a physicochemical pretreatment (in order to obtain the required conditions for the membranes in both cases), and a chemical cleaning system. In all tests, it is used as a source of concentrated solution (salt water), the rejection of a rack of a conventional reverse osmosis seawater desalination. The source of fresh water makes the difference between two types of tests: test with the effluent from a tertiary treatment of a conventional wastewater treatment plant (these tests study the behavior of the membrane facing the fouling) and tests with permeate, which allow us to study the ideal behavior of the membrane. The results of the tests with brackish water show fouling problems, the flow rate through the membrane decreases with the time and this effect is increased with water temperature. This phenomenon causes the need for a modification of the pretreatment of the direct osmosis module. An ultrafiltration system is added to enable the membrane to present a stable behavior . The tests with permeate have made possible the study of the ideal behavior of the membrane and we have obtained the optimum operating conditions. We have achieved energy recovery rates of 1.6, which allows to move from a consumption of 2.44 kWh/m3 in a conventional train of reverse osmosis to 2.28 kWh / m3 if it is added the direct osmosis system. The goal of future researches is to achieve recovery rates of 1.9, which would allow to reach a consumption lower than 2 kWh/m3. This thesis concludes that the proposed process allows us to take a further step in the reduction of the energy consumption in desalination. We must also add the mitigation of the brine discharge effects on the marine environment, due to the reduction of the flow and salinity of the discharge. This is also applicable to existing plants, and it suggests important economic benefits to new plants that will be built with this design.

The antibacterial effects for Salmonella Enteritidis phage type 4 of different chemical disinfectants and cleaning agents tested under different conditions

A selection of commercially available disinfectants, sanitizers and water sanitizers based on iodophor, quaternary ammonium compounds (QACs) and phenolic compounds were tested for their activity against a phage type 4 strain of Salmonella serotype Enteritidis in the presence of a variety of organic materials. In general the phenolic preparations were the most effective followed by the QACs and the iodophors. They were all inactivated to different degrees by chick fluff, chicken faeces, feed and wood shavings. The inactivation was greatest when Salmonella organisms were pre-dried in feed. Under these conditions formaldehyde and glutaraldehyde were still active. There was some evidence that induced resistance to stress conditions including culture at 42°C and anaerobic culture increased resistance to one of the water sanitizers.

The efficacy of chemical agents in cleaning and disinfection programs

Abstract Background Due to the growing number of outbreaks of infection in hospital nurseries, it becomes essential to set up a sanitation program that indicates that the appropriate chemical agent was chosen for application in the most effective way. Method For the purpose of evaluating the efficacy of a chemical agent, the minimum inhibitory concentration (MIC) was reached by the classic method of successive broth dilutions. The reference bacteria utilized were Bacillus subtilis var. globigii ATCC 9372, Bacillus stearothermophilus ATCC 7953, Escherichia coli ATCC 25922, Staphylococcus aureus ATCC 25923. The strains of Enterobacter cloacae IAL 1976 (Adolfo Lutz Institute), Serratia marcescens IAL 1478 and Acinetobactev calcoaceticus IAL 124 (ATCC 19606), were isolated from material collected from babies involved in outbreaks of infection in hospital nurseries. Results The MIC intervals, which reduced bacteria populations over 08 log10, were: 59 to 156 mg/L of quaternarium ammonium compounds (QACs); 63 to 10000 mg/L of chlorhexidine digluconate; 1375 to 3250 mg/L of glutaraldehyde; 39 to 246 mg/L of formaldehyde; 43750 to 87500 mg/L of isopropanol or ethanol; 1250 to 6250 mg/L of iodine in polyvinyl-pyrolidone complexes, 150 to 4491 mg/L of chlorine-releasing-agents (CRAs); 469 to 2500 mg/L of hydrogen peroxide; and, 2310 to 18500 mg/L of peracetic acid. Conclusions Chlorhexidine showed non inhibitory activity over germinating spores. A. calcoaceticus, was observed to show resistance to the majority of the agents tested, followed by E. cloacae and S. marcescens.

Chemical shoreline cleaning agents for oil spills : update state-of-the-art on mechanisms of action and factors influencing performance /

"EPA contract no. 68-C8-0062, Work assignment no. 3-48, SAIC project no. 01-0895-03-1000."

Dependence of ultra-thin gate oxide reliability on surface cleaning approach

In this paper, we investigate the effect of silicon surface cleaning prior to oxidation on the reliability of ultra-thin oxides. It is demonstrated that chemical preoxide grown in H2SO4/H2O2 (SPM) solution prior to oxidation provides better oxide integrity than both HF-based solution dipping and preoxide grown in RCA SC1 or SC2 solutions. It is also found that the oxides with SPM preoxide exhibit better hot-carrier immunity than the RCA cleaned oxides.