Determining the Reaction Rate of Electrochemical Process for Purification of Polluted Water

Abstract Aims: Turbidity in higher than standard levels, indicates failure in the water treatment plant. An electrochemical disinfection process takes place through electricity transition between two or more electrodes. This research aimed to determine the reaction rate of electrochemical process for purification of polluted water. Materials & Methods: This is a bench scale, experimental study performed in a batch system on synthetic wastewater. 1700ml of prepared synthetic wastewater was put in an electrolytic cell and constant 600mA current was flowed into the cell content through merged aluminum electrodes for 1 hour. Samples were taken from the batch in the beginning and every 10 minutes and were analyzed for, turbidity, Coliform bacteria (probably, confirmed and E. coli) and Heterotrophic Plat Count. Fisher exact test was used to analyze data. Findings: All the parameters of turbidity, HPC, total coliform, confirmed coliform and E. coli were decreased during the time. The electrochemical process reduced the average of turbidity below 3NTU after 50 minutes (91.05 removal). The HPC number reduced from 130n/ml to 2.4n/ml (98.15 removal) after 50 minutes. No coliforms were seen after 40 minutes of the electrochemical process. Conclusion: 40 minutes of electrochemical process in 600mA by aluminum electrodes is the optimum condition for removing the turbidity, Coliform bacteria (total, confirmed and E. coli) and HPC from polluted water

Determining the Reaction Rate of Electrochemical Process for Purification of Polluted Water

Aims Turbidity in higher than standard levels, indicates failure in the water treatment plant. An electrochemical disinfection process takes place through electricity transition between two or more electrodes. This research aimed to determine the reaction rate of electrochemical process for purification of polluted water. Materials & Methods This is a bench scale, experimental study performed in a batch system on synthetic wastewater. 1700ml of prepared synthetic wastewater was put in an electrolytic cell and constant 600mA current was flowed into the cell content through merged aluminum electrodes for 1 hour. Samples were taken from the batch in the beginning and every 10 minutes and were analyzed for, turbidity, Coliform bacteria (probably, confirmed and E. coli) and Heterotrophic Plat Count. Fisher exact test was used to analyze data. Findings All the parameters of turbidity, HPC, total coliform, confirmed coliform and E. coli were decreased during the time. The electrochemical process reduced the average of turbidity below 3NTU after 50 minutes (91.05% removal). The HPC number reduced from 130n/ml to 2.4n/ml (98.15% removal) after 50 minutes. No coliforms were seen after 40 minutes of the electrochemical process. Conclusion 40 minutes of electrochemical process in 600mA by aluminum electrodes is the optimum condition for removing the turbidity, Coliform bacteria (total, confirmed and E. coli) and HPC from polluted water

Annular flow of high-viscosity epoxy in circular pipes

Paper presented at the 7th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Turkey, 19-21 July, 2010.A combined experimental and numerical investigation was done to study the flow of viscous epoxy propelled through circular tubes by compressed air. Epoxy moved through a pipe in annular flow and spread uniformly on the inner surface of the pipe, forming a thin, uniform coating. The objectives of the study were to determine the effect of varying process parameters such as air flow rate, temperature, and pressure, on the movement of epoxy within a pipe; to visualize epoxy flows through straight pipe sections and around elbows; and to detemine how pipe geometry length and orientation affect epoxy flow. High pressure air from a compressor was used to drive a slug of epoxy through clear poly-vinyl chloride (PVC) pipes. The epoxy was mixed from two parts, resin and hardener, and hardened in an irreversible exothermic reaction. A video camera was used to record the movement of the epoxy inside the pipe. Once the epoxy had hardened sections were taken through the pipe and the thickness of the coating measured Tests were done varying a variety of experimental parameters including air pressure, airflow rate, piping configuration and epoxy temperature. A one dimensional numerical algorithm was developed to model the fluid flow of epoxy and air within the pipe, the heat transfer between air, epoxy and walls, as well as the curing rate of the epoxy as it is moving alongside the pipe. Results from the model were used to predict the epoxy front velocity and coating thickness and were compared to the experimental observations. Heating the epoxy was found to slow its motion, since the epoxy sets faster at a higher temperature and its viscosity becomes greater. Before curing occurs, the viscosity decreases as the temperature is increased. The viscosity then increases when hardening takes place. The coating was significantly thicker at the bottom of a horizontal pipe than at the top due to sagging of the epoxy coating after it had been applied, resulting in flow from the top to the bottom of the pipe. Sagging could be reduced by maintaining airflow until curing was almost complete and the epoxy had hardened enough to prevent it from moving easily. The most important parameters controlling the speed of the epoxy and coating thickness were the air flow rate and temperature, since they determine the shear forces on the epoxy layer and the rate at which the epoxy cures. Raising air temperature increases the reaction rate and therefore decreases the time required for the epoxy to cure inside the pipe.ksb201

Using a novel optimization algorithm for parameter extraction of photovoltaic cells and modules

Summarization: The critical worldwide revolution towards clean energy has prompted the improvement of studies on the fabrication of high-performance solar cells. In this regard, rendering an accurate model of the solar cell for performance evaluation in the simulation could be essential. So far, several models have been proposed for the solar cell, including single-diode model (SDM), double-diode model (DDM), and three-diode model (TDM). By increasing the number of diodes considered in the equivalent circuit in order to deliver a more accurate model, the number of unknown parameters which must be identified will be increased as well. Therefore, presenting an efficient algorithm to estimate these parameters becomes an interesting issue in recent years. In this study, an improved optimization algorithm, called springy whale optimization algorithm (SWOA), is proposed to estimate the model parameters of solar cells. SWOA is a generalization of the WOA and has the advantages of high convergence speed, global search capability, and high robustness over it. In order to inquire the efficiency of SWOA, this algorithm is posed to estimate the parameters of models of solar cells and photovoltaic (PV) modules as well; the simulation results authenticate the supremacy of the proposed algorithm. Furthermore, the effectiveness of SWOA algorithm in the practical application has been evaluated using commercial modules, including polycrystalline (SW255), multi-crystalline (KC200GT), and monocrystalline (SM55). This assessment is carried out for various operating conditions under different irradiance and temperature conditions, which yield variations in the parameters of the PV model. The results obtained from various experimental setups confirm the high performance and robustness of the proposed algorithm.Presented on: European Physical Journal Plu

Autoantibodies Targeting a Collecting Duct-Specific Water Channel in Tubulointerstitial Nephritis

Tubulointerstitial nephritis is a common cause of kidney failure and may have diverse etiologies. This form of nephritis is sometimes associated with autoimmune disease, but the role of autoimmune mechanisms in disease development is not well understood. Here, we present the cases of three patients with autoimmune polyendocrine syndrome type 1 who developed tubulointerstitial nephritis and ESRD in association with autoantibodies against kidney collecting duct cells. One of the patients developed autoantibodies targeting the collecting duct-specific water channel aquaporin 2, whereas autoantibodies of the two other patients reacted against the HOXB7 or NFAT5 transcription factors, which regulate the aquaporin 2 promoter. Our findings suggest that tubulointerstitial nephritis developed in these patients as a result of an autoimmune insult on the kidney collecting duct cells