Abstract
Hydrogen can be one of the key elements as source of future energy requirement. Water splitting reaction is an important route for generation of hydrogen as maximum fraction of hydrogen constitute in water. The present work describes the experimental investigation for generation of hydrogen through water splitting reaction in flow conditions with the aid of metal aluminum and sodium hydroxide as an activator. The hydrogen generation through water splitting reaction at various concentrations of NaOH, viz. 0.5 N and 1 N and the flow rates ranging from 0.2 to 10 ml/min was studied. The yield of hydrogen generated is reported for each NaOH concentration and flow rate. The yield of hydrogen generated at all the considered concentrations and flow rates was found to be greater than 98 %. The shrinking core model has been modified and developed for predicting the conversion of aluminum in the reaction system as per the prevailing conditions and rate controlling mechanism. The RMSE value of predicted conversion of Al was found to be 0.0351 which signify that the model agrees well with the experimental data.
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Articles in the same Issue
- Synthesis and Modification of Zeolite ZSM-5 Catalyst with Solutions of Calcium Carbonate (CaCO3) and Sodium Carbonate (Na2CO3) for Methanol to Gasoline Conversion
- Hydrogen Generation in an Annular Micro-Reactor: An Experimental Investigation and Reaction Modelling by Shrinking Core Model (SCM)
- Fluidization in Supercritical Water: Heat Transfer between Particle and Supercritical Water
- Optimization of Process Parameters for Reactive Separation of Gallic Acid
- Intensification of the Production of 2-Ethyl-Hexyl Acrylate: Batch Kinetics and Reactive Distillation
- Hydrogen Generation in Water Splitting Reaction Using Aluminum: Effect of NaOH Concentration and Reaction Modelling Using SCM
- NOx process inhibition and energy efficiency improvement in new swirl modification device for steel slag based on coal combustion
- Study of Pyrolysis Behavior of Shenhua Coal Pretreated by Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate
- Catalytic Gasification – A Critical Analysis of Carbon Dioxide Methanation on a Ru/Al2O3 Catalyst
- A Green Process for Synthesis of Geraniol Esters by Immobilized Lipase from Candida Antarctica B Fraction in Non-Aqueous Reaction Media: Optimization and Kinetic Modeling
Articles in the same Issue
- Synthesis and Modification of Zeolite ZSM-5 Catalyst with Solutions of Calcium Carbonate (CaCO3) and Sodium Carbonate (Na2CO3) for Methanol to Gasoline Conversion
- Hydrogen Generation in an Annular Micro-Reactor: An Experimental Investigation and Reaction Modelling by Shrinking Core Model (SCM)
- Fluidization in Supercritical Water: Heat Transfer between Particle and Supercritical Water
- Optimization of Process Parameters for Reactive Separation of Gallic Acid
- Intensification of the Production of 2-Ethyl-Hexyl Acrylate: Batch Kinetics and Reactive Distillation
- Hydrogen Generation in Water Splitting Reaction Using Aluminum: Effect of NaOH Concentration and Reaction Modelling Using SCM
- NOx process inhibition and energy efficiency improvement in new swirl modification device for steel slag based on coal combustion
- Study of Pyrolysis Behavior of Shenhua Coal Pretreated by Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate
- Catalytic Gasification – A Critical Analysis of Carbon Dioxide Methanation on a Ru/Al2O3 Catalyst
- A Green Process for Synthesis of Geraniol Esters by Immobilized Lipase from Candida Antarctica B Fraction in Non-Aqueous Reaction Media: Optimization and Kinetic Modeling