Hydrogen Generation Through Aluminum, Aluminum Alloys In Aqueous Solution

Similar documents
Available online at ScienceDirect. Procedia Engineering 113 (2015 ) 8 12

METALS AND THEIR COMPOUNDS

2023 Reduction of D-(+)-camphor with lithium aluminium hydride to an isomeric mixture of (+)-borneol and ( )-isoborneol

Rapid hydrogen generation from aluminum water system by adjusting water ratio to various aluminum/aluminum hydroxide

85 Q.51 Which of the following carbonates would give the metal when heated with carbon? (1) MgCO 3 (2) PbCO 3 (3) K 2 CO 3 (4) CuCO 3

TWEED RIVER HIGH SCHOOL 2006 PRELIMINARY CHEMISTRY. Unit 2 Metals

Mon. Tues. Wed. Thurs. Fri. AM or PM B

Iron filings (Fe) 56g IRON + SULPHUR IRON SULPHIDE

Extraction of Al and Na from red mud by magnesium oxide sodium carbonate sinter process

Preparation of Cyclohexene From Cyclohexanol

A Study on Strength Properties of Geopolymer Concrete with Addition of G.G.B.S

Hydrogen Generation by Accelerating Aluminum Corrosion in Water with Alumina

Resource Guide. Section 4: Ni-Resist

GENARAL INTRODUCTION TO METALLURGY :Std: XI-CHEMISTRY

GRAVIMETRIC DETERMINATION OF SULFATE IN AN UNKNOWN SOLUTION

Table of Contents. Preface...

Partner: Cathy 22 March Separation and Qualitative Determination of Cations and Anions

Metals And Their Properties- Physical and Chemical

STRENGTH STUDIES ON SILICA FUME BASED GEOPOLYMER MORTAR WITH COIR FIBRE

Utilization of Alumina Waste and Silica Waste for Geopolymer Production

Chemical Activation of Low Calcium Fly Ash Part 1: Identification of Suitable Activators and their Dosage

Polyvidone Polyvinylpyrrolidone H 2 C H C N

Session 4.1: Solid Storage Technology. Dr. N. Eigen (GKSS) 25 th 29 th September 2006 Ingolstadt. Session 1.2: Introductory Lectures. K.

STRENGTH PROPERTIES OF GEOPOLYMER MORTAR CONTAINING BINARY AND TERNARY BLENDS OF BENTONITE

Chapter 20 CHEMISTRY. Metallurgy and the Chemistry of Metals. Dr. Ibrahim Suleiman

In the 21st century, with more understanding of the importance

TREATMENT OF DAIRY WASTE WATER BY MORINGA OLEIFERA AS NATURAL COAGULANT

PERFORMANCE ANALYSIS OF BENCHMARK PLANT FOR SELECTIVE LITHIUM RECOVERY FROM SEAWATER

CONSERVATION OF MATTER AND CHEMICAL PROPERTIES

TENSILE STRENGTH OF FLY ASH BASED GEOPOLYMER MORTAR

1. Scaling. H.O.: H-5/21, KRISHNA NAGAR, DELHI Tel.: , Fax:

Mitigation of Alkali-Silica Reaction in Mortar with Limestone Addition and Carbonation

to the presentation Teaching Thermodynamics: Chemical Potential from the Beginning Regina Rüffler, Georg Job

Effect of Anodizing Potential on the Surface Morphology and Corrosion Property of AZ31 Magnesium Alloy

Electricity and Chemistry

Utilization of micro silica as partial replacement of OPC & SRC in concrete

AP Chemistry A. Allan Chapter 18 - The Representative Elements: Groups 1A through 4A

Aluminum-Based Hydrogen Generator for a Mini-Type Proton Exchange Membrane Fuel Cell with an Innovative Flow Field Plate

Chemical Admixtures for Concrete. ACCELERATORS Özge Andiç Çakır, PhD

POTASSIUM SILICATE FOLIAR FERTILIZER GRADE FROM GEOTHERMAL SLUDGE AND PYROPHYLLITE

Pre- Lab Questions: Synthesis and Crystallization of Alum

FUNDAMENTAL STUDY ON MICROSTRUCTURE OF CeO 2 -DOPED (Na 0.5 Bi 0.5 )TiO 3 CERAMICS

Deposition of Silica Aluminum Using an Alkali Solution of Fly Ash

5-4 Chemical changes Trilogy

Technical Presentation on Spent Pot lining Management & Red Mud

Hydrogen Sulphide and Mercaptan Removal

Available online at ScienceDirect. 9th International Conference on Applied Energy, ICAE2017, August 2017, Cardiff, UK

Microstructural Evolution of Ti-Mo-Ni-C Powder by Mechanical Alloying

Injection Moulding and Heat Treatment of Ni-Cr-Si-B Alloy Powder

Sulphur Removal From Sulcis Coal By Sequential Leaching With Koh Followed By H 2 o 2

CHLOR-ALKALI INDUSTRY

High Purity Alumina and Zeolite from Local Low Grade Kaolin

PREPARATION AND PROPERTIES OF Al Fe AND Al Fe Cr ALLOYS. Petra HANUSOVÁ 1, Pavel NOVÁK 2

PERFORMANCE OF ALKALINE SOLUTIONS ON GRADES OF GEOPOLYMER CONCRETE

Applications of electrochemistry

METHOD 3 - GAS ANALYSIS FOR THE DETERMINATION OF DRY MOLECULAR WEIGHT. NOTE: This method does not include all of the

Preparation of cerium oxide nanoparticles (CNPs). Preparations of CNPs produced

Soda Ash ( Sodium carbonate) Manufacture

Desorption of Hydrogen from Palladium Plating

Iraqi Journal of Chemical and Petroleum Engineering Vol.9 No.3 (December 2007) ISSN:

Analysis of Calcium Carbonate Tablets

Comparison of hydrogen storage properties of pure Mg and milled pure Mg

Supporting Information. Low temperature synthesis of silicon carbide nanomaterials using

NaOH alkali-activated class F fly ash: NaOH molarity, Curing conditions and mass ratio effect

New Developments in Measuring Low Silicon in Process Piping Using Handheld X-ray Fluorescence (XRF)

Abstract Concrete is most used construction material. enhance the strength to the concrete. Fibers act as crack

EVALUATION OF A CHEMICAL CLEANING FORMULATION FOR THE STEAM GENERATOR OF NUCLEAR POWER PLANTS

Development of a Microcompact Fuel-cell Vehicle Equipped with a Hydrogen Generator

MAHESH TUTORIALS I.C.S.E.

Localized Corrosion of a 7075 Aluminum Alloy Exposed to KCl

CHAPTER 6. Natural Mineral Mineral Content Elements In The Minerals Bauxite Aluminium oxide Aluminium, oxygen. Cassiterite Tin oxide Tin, oxygen

Acid leaching technology for obtaining a high-purity of silica for Photovoltaic area

*20GSD5201* Double Award Science: Chemistry. Unit C2 Higher Tier TUESDAY 9 JUNE 2015, AFTERNOON [GSD52] *GSD52* *G5802* TIME 1 hour 15 minutes.

Characterization of Coatings on Grey Cast Iron Fabricated by Hot-dipping in Pure Al, AlSi11 and AlTi5 Alloys

Hydrogen Production by Bio-ethanol reforming for Small-scale Fuel Cell Applications

2.3 Chemical Changes corrosion Kinds of Corrosion

Journal of Chemical and Pharmaceutical Research, 2017, 9(1): Research Article

Metal Powder - the Raw Material of Future Production

MA-SHS of ZrC and ZrB2 in Air from The Zr/B/C Powder. the original is available online at Instructions for use

Compounds & Reactions Week 1. Writing Formulas & Balancing Equations. Write the chemical formula for each molecular (covalent) compound.

NOx processing experiences for removal in the CO 2 plant for the Oxyfuel combustion process

Study on the Recovery of Some Metals from Spent Desulfurization Catalyst

Technical Process Bulletin

Properties of aqueous alkaline sodium borohydride solutions and by-products formed during hydrolysis

ELECTRIDEPOSITION AND WEAR BEHAVIOR OF NANO-STRUCTURED Cr-WC COMPOSITE COATINGS FROM A TRIVALENT CHROMIUM BATH

Direct reduction of low grade nickel laterite ore to produce ferronickel using isothermal temperature gradient

TITANIUM DIOXIDE. SYNONYMS Titania; CI Pigment white 6; CI (1975) No ; INS No. 171 DEFINITION DESCRIPTION FUNCTIONAL USES CHARACTERISTICS

VIBRATIONAL STUDIES OF Na 2 SO 4, K 2 SO 4, NaHSO 4 AND KHSO 4 CRYSTALS

Visualization and Control of Particulate Contamination Phenomena in a Plasma Enhanced CVD Reactor

EXPERIMENTAL STUDY ON COIR FIBRE REINFORCED FLYASH BASED GEOPOLYMER CONCRETE WITH 12M & 10M MOLAR ACTIVATOR

Oxidation and Reduction

EFFECTS OF CURRENT DENSITY ON SIZE AND SURFACE MORPHOLOGY OF HIGH SPEED DIRECT NANO-CRYSTALLINE NICKEL PLATING ON TITANIUM SURFACE

THE NUCLEAR FUEL CYCLE

Topic 2.7 EXTRACTION OF METALS. Extraction of Iron Extraction of Aluminium Extraction of Titanium Recycling

S.E. (Chemical) (First Semester) EXAMINATION, 2012 PROCESS CALCULATIONS (2008 PATTERN) Time : Three Hours Maximum Marks : 100

Recovery of Cu, Zn, Ni and Cr from Plating Sludge by Combined Sulfidation and Oxidation Treatment

(a) To find out which is the more reactive metal, zinc or tin, the following experiment could be carried out. piece of zinc shiny surface

Recovery of Energetic Components from Propellant with Hydrolyzable/Degradable Binders

Supplementary Material for Chitin and chitosan dissolving. in ionic liquids as reversible sorbents of CO 2

Design, development and performance of a new solid mercury dispenser for fluorescent lighting

Transcription:

International Journal of ChemTech Research CODEN( USA): IJCRGG ISSN : 0974-4290 Vol.5, No.2, pp 1062-1067, April-June 2013 ICGSEE-2013[14 th 16 th March 2013] International Conference on Global Scenario in Environment and Energy Hydrogen Generation Through Aluminum, Aluminum Alloys In Aqueous Solution Anurag Tiwari, Amit Keshav, A.B. Soni Department of Chemical Engineering, NIT Raipur, Raipur 492010,India. Abstract : Hydrogen has been identified as an alternative to substitute the non-sustainable fossil fuel. Ongoing research is underway to develop environmentally friendly and economical hydrogen production technologies that are essential for the hydrogen economy. One of the promising ways to produce hydrogen is to use aluminum or its alloys to reduce water or hydrocarbons to generate hydrogen. In the present work production of hydrogen using aluminum and aluminum alloys (Al/Si) with aqueous alkaline solutions has been performed. Effect of aluminum concentration, aluminum alloy concentration, corrosion time and ph on generation of hydrogen has been studied. SEM is used to study the changes in surface properties of metal occurring due to corrosion. The obtained result shows that Al/Si alloy produces more hydrogen than aluminum, although with a low reaction efficiency reaching a hydrogen production yield upto 14 % at ph 12. In principle, this method does not consume alkali because the aluminate salts produced in the hydrogen generation undergo a decomposition reaction that regenerates the alkali. This process is based on aluminum corrosion, consuming only water and aluminum which are cheaper raw materials than other compounds used for in situ hydrogen generation, such as chemical hydrides. As a consequence, this process could be a feasible alternative for CO 2 free hydrogen production for fuel cell application. Keywords : Hydrogen, aluminum alloy, Al/Si alloy, corrosion. Introduction The current fossil-fuel based economy is generally considered unsustainable due to resource as well as environmental constraints. One possible alternative is the development of a hydrogen-based economy, as hydrogen is an abundant and environmentally friendly fuel. However, it should be noted that free hydrogen does not occur naturally, and needs to be generated by various means. Hydrogen should therefore not be considered a primary energy source (eg. coal), but rather, an energy carrier. The need for high pressure storage systems is one impediment to the large-scale utilization of hydrogen as a fuel. The production of on-demand hydrogen, thereby bypassing the storage system requirement, could greatly aid in making the hydrogen economy a reality. A lot of researchers have recently focused their interests on the generation of hydrogen by the hydrolysis of metal or metal hydrides 1-4,5. Hydrogen can be generated from hydrolysis reaction through corrosion of active metals such as, Al, Na, Zn, Mg etc. in an alkaline water 3,6,7. These metals are considered to be one of the most attractive hydrogen production systems at very low cost. Among them, Al is the second most abundant element in the Earth`s crust following silicon, and it is electrochemically very active (EAl3+/Al = - 1.66). So, Al can be used as a safe, simple, low-cost, and practical material for hydrogen production.

Anurag Tiwari et al/int.j.chemtech Res.2013,5(2) 1063 Production of hydrogen using corrosion produces on-demand hydrogen for fuel cells through the use of aluminum which reacts with water under certain conditions to produce hydrogen using the following reaction. 2Al + 6H 2 O + 2NaOH = 2NaAl(OH) 4 + 3H 2 (1) NaAl(OH) 4 = NaOH + Al(OH) 3 (2) 2Al + 6H 2 O = 2 Al(OH) 3 + 3H 2 (3) This can be used for applications as small as portable handheld devices, onboard generation for vehicles, or as large as a hydrogen refueling center. However, the utilization of aluminum for generating ondemand hydrogen is critically dependent on the control of the rate of hydrogen generation from the reaction. Decreasing the aluminum particle size can result in increased reaction rates due to higher reactant surface area. It should be noted that in general, aluminum-water reactions for hydrogen generation have been extensively studied and reported in literature. However, there is a dearth of literature on the use of aluminum particles at the nano-scale in particular. Experiment were conducted to identify the salient parameters that influence the mixture proportions (Aluminum/Aluminum alloy powder, NaOH, Deionized water) on the properties of low cost hydrogen production through corrosion of Aluminum and Aluminum alloy. Corrosion properties of Aluminum and Aluminum alloy powder or what percentage of corrosion occurred from the reaction was also studied. Experimental Procedure Different proportions of materials was added to deionized water and influence of processing parameters i.e. curing time, curing temperature, water content of mixture and corrosion etc. was studied and analyzed. To study the effect of alkaline solution, sodium-based solutions were chosen because they were cheaper as well as more reactive than others like potassium-based solutions. The sodium hydroxide solids were in flakes form (3 mm), with a density of 1.33, 98% purity, and obtained from Finar Chemical Ltd, Ahmedabad INDIA. The sodium hydroxide (NaOH) solution was prepared by dissolving either the flakes or the pellets in water. The mass of NaOH solids in a solution varied depending on the concentration of the solution expressed in terms of molar, M. The reactor was a triple-neck 200 ml round-bottomed glass vessel. The reaction was initiated by introducing aluminum and aluminum alloy particles through the central vessel neck into the alkaline solution poured in the vessel from beforehand. After particle introduction, the neck was immediately corked to prevent any gas leakage. Tubing (40 cm length and 8 mm I.D.) inserted in one of the adjacent neck corks routed the evolving hydrogen gas through water bath at room temperature in order to cool it and was collected into an inverted 1000 ml measuring cylinder. The evolving hydrogen displaced the water in the measuring cylinder, and the changing water level in the measuring cylinder was measured as a function of time. The rate of change of the water level provided an indication of the rate of hydrogen generation from the reaction, and the difference between the initial and final water levels in the measuring cylinder indicated the total hydrogen yield. For experiments using less than 5 ml of solution, the aluminum particles were introduced into the empty glass vessel first, and the alkaline solution was injected into the vessel subsequently. Solid byproducts of the hydrogen generation reactions were analyzed with Scanning Electron Microscopy (SEM) for crystalline species identification. For SEM analysis of the byproducts, the solid mixture remaining in the reactor was filtered using a vacuum pump and a funnel provided with a filter plate. Solids were dried in an oven at 75 C under air for approximately 24 h to remove humidity. Result And Discussion Using the triple-neck glass vessel reactor, multiple experiments were conducted in order to gain familiarity with the reaction under consideration, confirm basic trends described in literature, and draw qualitative conclusions about certain factors affecting the rate and yield of the reaction. 76.7 ml of hydrogen was produced in 15 minutes using 0.1 gm Al powder with water having ph 7.2 at the room temperature (34 o C) (Figure 1). The initial reaction rate was found to be very slow. As the time proceeds, the rate of reaction goes on increasing. The reason behind this result was that rate of corrosion of hydrogen was low initially and as time proceeds, it increases.

Anurag Tiwari et al/int.j.chemtech Res.2013,5(2) 1064 Figure 1: Hydrogen production using 0.1 gm Al powder at ph =7.2. The characteristic morphology of original Aluminum powder is shown in SEM image Figure (6). It can be seen that it consists of a series of spherical vitreous particle of different size (diameters ranging from 10 µm to 200 µm). Although usually hollow, some of these spheres may contain other particle of smaller size in their interiors. Figure (6) also shows the changes detected in Aluminum powder microstructure after the attack. Some of the reacted Aluminum particles coexisting with the unreacted spheres and even with the particles partially covered with reaction products may be seen in the picture. Figure (2) shows the rate of hydrogen production using 0.1gm aluminum powder with 75 ml of aqueous NaOH of ph 12.1. Analyzing the above experiment, it may be concluded that the rate of production of H 2 during the first second (i.e.; 0-1) is very high i.e. the rate of corrosion of Al is very high. From first minute to sixth minute, the production rate goes on decreasing after that it increases slightly then again it decreases and after 12th minute, the production remains constant with time. The production rate of hydrogen is about 151 ml in 15 minutes. Figure (6) shows the SEM analysis of the surface after corrosion at ph 12.1. Figure 2: Hydrogen production using 0.1 gm Al Powder at ph 12.1 Figure (3) shows the effect of increase of Al concentration on the amount of hydrogen produced. 0.2 gm of Aluminum powder was treated with 75 ml of NaOH solution at 12.1 ph. Analyzing the above experiment it may be concluded that the initial production rate of H 2 was very high, i.e. 85 ml to 223 ml as time was raised from 1 to 4 minutes. After that it goes on decreasing as the time proceeds. Figure (6) shows the SEM analysis of the present case.

Anurag Tiwari et al/int.j.chemtech Res.2013,5(2) 1065 Figure 3: Hydrogen production using 0.2 gm Al Powder at ph 12.1 Figure ( 4-5) shows the effect of aluminum silicone alloys on the production of hydrogen. 0.1gm aluminum alloy powder was contacted with 75 ml of aqueous NaOH of ph 12.1. It may be seen that the rate of production of H 2 during the first second (i.e.; 0-1) is very high i.e. the rate of corrosion of Al is very high. From third minute to sixth minute, the production rate goes on decreasing after that it increases slightly then again it decreases and after 12th minute, the production remains constant with time. And the production rate of hydrogen is about 476 ml in 15 minutes. SEM Image of surface microstructure is shown in Figure (6). Effect of increasing Aluminum alloy concentration is also reported in Figure (5). It can be seen that the rate of production of H 2 using 0.2gm Al alloy is higher than 0.2gm Al i.e. alloy of Al corrode more than Al. The SEM microstructure is shown in Figure (6). Figure 4: Hydrogen production using 0.1 gm Al Alloy Powder in 75 ml of Aqueous Solution of NaOH Figure 5: Hydrogen production using 0.2 gm Al Alloy Powder in 75 ml of Aqueous Solution of NaOH

Anurag Tiwari et al/int.j.chemtech Res.2013,5(2) 1066 a) b) c) d) e) f) Figure 6: SEM of Microstructures Morphology of Aluminum surfaces (a) As Received fine particles and (b) After leaching with water at ph 7.2 for 15 min (c) 0.1gm Al Leached With aq. NaOH (solution ph 12.1) (d) 0.2gm Al Leached With aq. NaOH (solution ph 12.1 ) (e) 0.1gm Al Alloy (f) 0.2gm Al Alloy Table (1) show the overview of the amount of hydrogen produced using various conditions studied in the present paper.

Anurag Tiwari et al/int.j.chemtech Res.2013,5(2) 1067 Table 1: Overview of hydrogen production using aluminum corrosion S.No. Amt. of Al/Al alloy ph Amt. of H 2 (cm 3 ) 1. 0.1 gm Al powder (only water) 7.2 73 2. 0.1 gm Al powder (Alkaline) 12.1 152 3. 0.2 gm Al powder (Alkaline) 12.1 319 4. 0.1 gm Al alloy powder (Alkaline) 12.1 457 5. 0.2 gm Al alloy powder (Alkaline) 12.1 530 Conclusion SEM, analysis shows the corrosion in Aluminum and Aluminum alloy by addition of NaOH. SEM analysis gives the microstructure of the surface, which shows the corrosive part of the content. The high activity of aluminum makes it able to extract hydrogen from different sources including water or alkaline water hence, aluminum and it s alloys are rather useful for hydrogen production. Higher ph shows more basic solution, hence better result is obtained at solution having higher ph. Higher quantity of Al alloys gives better result as compare to higher quantity of using aluminum powder because corrosion occurs more in Al alloys solution which produces higher hydrogen rate. References 1. M. Fan, F. Xu, Li Sun, International Journal of Hydrogen Energy (2007) 2809-2815. 2. Foulkes FR, Kirk DW, Hinatsu JT. International journal of Hydrogen Energy (1999) 665. 3. H.Z. Wang, D.Y.C. Leung, M.K.H Leung, M. Ni. A review on hydrogen production using aluminum and aluminum alloys. Renewable and Sustainable Energy Reviews (2009). 4. A. Bauen, J. International journal of power sources. (2006) 893 901. 5. L. Soler, J. Macan as, M. Mu noz, J. Casado, Int. J. Hydrogen Energy (2006) 129 139. 6. SM Kotay, D. Das, Biohydrogen as a renewable energy resource prospects and potentials. Int J Hydrogen Energy (2008) 258 63. 7. U.B. Demirci, O. Akdim, P. Miele, Ten-year efforts and a no-go recommendation for sodium borohydride for on-board automotive hydrogen storage. Int J Hydrogen Energy (2009) 2638 45. *****