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The performance of the anion bed in a two-bed deionization process was investigated. Experiments and simulation were carried out with a feed solution concentration of about 0.005N. The prepared solutions were dilute acid of HCl, H 2 SO 4 and a mixture of the two. The bed height was about 40 cm and the flow rate in the range of 75-150 ml/min. Both the binary and ternary models were used to predict the column performance. In both models, it was found that the equilibrium parameters do not affect significantly the breakthrough behavior. This is due to the accompanied neutralization reaction which results in the irreversible form of the rate equation. The experimental and theoretical breakthrough curves show very good agreement especially for the early part of the data. Results of this study suggest that a pseudo-binary or pseudo-ternary model can be used to model the fixed bed deionization process by ion exchange.
The performance of the anion bed in a two-bed deionization process was investigated. Experiments and simulation were carried out with a feed solution concentration of about 0.005N. The prepared solutions were dilute acid of HCl, H 2 SO 4 and a mixture of the two. The bed height was about 40 cm and the flow rate in the range of 75-150 ml/min. Both the binary and ternary models were used to predict the column performance. In both models, it was found that the equilibrium parameters do not affect significantly the breakthrough behavior. This is due to the accompanied neutralization reaction which results in the irreversible form of the rate equation. The experimental and theoretical breakthrough curves show very good agreement especially for the early part of the data. Results of this study suggest that a pseudo-binary or pseudo-ternary model can be used to model the fixed bed deionization process by ion exchange.
The article contains sections titled: 1. Introduction 2. Definition 2.1. Ionic Purity ‐ Conductivity and Resistivity 2.2. Organic Purity 2.3. Particulate Purity 3. Technologies used for Ultrapure Water Processing 3.1. Ion Exchange Resins 3.1.1. Mixed‐Bed Ion Exchangers 3.1.2. Homogeneous Beds 3.2. Membranes 3.2.1. Reverse Osmosis 3.2.2. Ultrafiltration and Nanofiltration 3.2.3. Electrodeionization 3.3. Adsorption ‐ Activated Carbon Beds 3.4. Degasification 3.5. Clarifiers and Chemical Precipitators 3.6. Chemical Chlorine Removal 3.7. Ultraviolet Treatment 3.8. Membrane Contactors 3.9. Piping Materials, Gaskets 4. Analysis 4.1. Ion Chromatography 4.2. pH Measurement 4.3. Conductivity 4.4. Ion‐Selective Electrodes 4.5. Determination of Total Dissolved Solids 4.6. Determination of Total Organic Carbon 4.7. Particle Counters 4.8. Colorimetric Analyzers for Silica and Phosphate 4.9. Dissolved Oxygen Electrodes 4.10. Capillary Electrophoresis 4.11. ORP Chlorine Analyzers 4.12. Nonvolatile Residue Monitors 4.13. Use of On‐line Analyzers and Manually Collected Samples 5. Applications 5.1. Microelectronics Industry 5.2. Pharmaceutical Industry 5.3. Power Industry 5.3.1. Nuclear Power Plants 5.3.2. Fossil Fuel‐Fired Plants 5.4. Chemical Industry 5.4.1. Boiler Feedwater Make‐up 5.4.2. Process Water 6. Future Developments
At present, aqueous rechargeable Zn–MnO2 batteries have attracted widespread attention as green potential application for renewable energy storage devices. MnO2 cathode has great potential for application, but its proton reaction results in side reactions of cathode, electrolyte consumption, and dramatic pH value changes, suffering from capacity degradation. To address the issues caused by proton deficit, a proton–limited domain strategy is proposed by integrating solid acids (Sulfonic acid type polystyrene–divinylbenzene, SATP) with proton exchange reactions into MnO2. SATP can act as a new proton source increasing the amount of H+ and reducing the generation of zinc hydroxide sulfate, by–product of proton at the cathode interface, via proton exchange reactions of ‐HSO3– group. As a result, Zn–MnO2/SATP battery delivered with excellent rate performance (218.4 mAh g–1 at 2 A g–1) and high cycling stability (the retained capacity of 115.8 mAh g–1 after 500 cycles at a current density of 1 A g–1. This work provides an innovative strategy for high performance aqueous Zn–MnO2 batteries.
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