Battery Digest Article

Total Page:16

File Type:pdf, Size:1020Kb

Battery Digest Article ISSUE NUMBER 11 FEBRUARY 1997 ISSN # 1086-9727 Concentrated Battery Business and Technology Summaries for Decision Makers Considerations for Primary Cell Selection1 by Sol Jacobs * The technical press pays a lot of atten- bon-zinc chloride system, a heavy-duty By far, the leading primary battery tion to rechargeable, or secondary bat- version of the Leclanche cell, consti- technology, in terms of units sold in the teries, mainly because of the growing United States, is the alkaline system, number of portable-computing and based on manganese dioxide, zinc and communications applications. But there a caustic potassium hydroxide-zinc are categories of applications that can Primary Battery Specific Energy oxide electrolyte. Alkaline-cell technol- be addressed only by the less glam- ogy offers greater capacity for a given orous class of primary batteries. Alkaline cell size compared with Leclanche types, but it typically costs 50% more Li/12 These applications can be organized and weighs about 25% more. into groups that help to rationalize the Li/(CFX)x choice of primary battery technology. There have been some apparent Li/SO2 However, an overview of existing bat- improvements in alkaline cell perfor- tery technologies is a necessary first Li/MnO2 mance in recent years, but these have step in the decision-making process. been a result of changes in packaging Li/SOCL2 0 250 500 750 and manufacturing techniques rather The types of primary battery than any improvements to the basic chemistries available today include Watthours/kg. chemical system. traditional zinc-carbon-ammonium chloride (Leclanche cell), zinc-carbon- In the past, alkaline batteries were The Lithium Thionyl Chloride battery zinc chloride, alkaline (the leading type made with complex sealing systems has the highest energy density of pro- for consumer use), zinc-air and a and thick steel outer cases and end duction primary batteries. Just as with variety of lithium-based chemistries. caps. Several years ago, a method was other chemistries such as lithium ion, developed that allowed manufacturers lithium thyonyl shloride performance is The chemical systems employed in the to use thinner packaging materials and manufacturer dependent. Tadiran’s most widely used primary battery types more volumetrically efficient seals. have the highest energy density, voltage have been around for quite some time. That created room for more active and temperature range. The zinc-carbon-ammonium chloride material within a given standard cell “dry,” or Leclanche cell, system is size and increased capacity. more than 75 years old and still accounts for a little less than 10 per- The next change to come in alkaline- cent of all of the primary battery units tutes a similar portion of U.S. primary cell technology may actually be a step sold in the United States. The zinc-car- battery consumption. backward in capacity, but for a good Issue No. 11, Feb., 1997, © 1997 by Teksym Corp. Maple Plain, MN, 55359, Phone 612-479-6190, Fax 612-479-3657, E Mail [email protected], Page 1 cause. Mercury, an environ- mental pollutant, is used in alkaline batteries as an anti-passivation stabilizer for the zinc electrode. Without mercury, chemical processes within the battery cause the zinc to function less efficiently as discharge proceeds because of passivation of zinc surface, thus limiting useful battery life. In the interest of keeping as much mercury out of the envi- ronment as possible, several states have developed propos- als to reduce the mercury con- tent of alkaline batteries. The current target for mercury con- tent is 250 ppm. The European Union has developed similar rules, also with the allowable mercury content of 250 ppm. Major producers of alkaline cells are conducting research to find gen is absorbed into the electrolyte metals. Lithium is also the lightest environmentally suitable replacements through a gas-permeable, liquid-tight non-gaseous metal. Batteries based on for mercury. By the time mercury is membrane. With the removal of a seal- lithium chemistries have the highest phased out, it is likely the end user will ing tab, oxygen from the air is intro- specific energy (energy per unit not notice any changes in alkaline bat- duced into the cell. A zinc-air battery weight) and energy density (energy per tery performance. typically reaches full operating voltage unit volume) of all types. The high within 5 seconds of being unsealed. energy density is a result of lithium’s Mercury cells were once widely used The zinc-air system, while sealed, has high potential and the fact that lithium in many applications that required excellent shelf life, with a self-dis- reacts strongly with water. miniature or subminiature size and rel- charge rate of only 2 percent per year. atively low drain. Coin-sized versions That precludes the use of any aqueous Now, zinc-air battery technology, origi- (water-containing) electrolyte—-but nally developed in the mid-1980’s, has Zinc-air batteries are available in but- that turns out to be a benefit. Because become a high-capacity, high-energy- ton sizes for direct replacement of the oxygen and hydrogen in water dis- density replacement for mercury. other button types, but recently intro- sociate in the presence of a potential Compared with mercury cells of the duced coin-sized versions are designed above 2 V, cells using aqueous elec- same physical size, zinc-air batteries, for pagers as well as personal medical trolytes are limited in voltage. Lithium with a nominal Open Circuit Voltage equipment, such as cardiac monitors cells, all of which use a non-aqueous (OCV) of 1.4 V, are up to 40 percent and transmitters. electrolyte, have nominal OCVs of lighter and have twice the capacity. between 2.7 and 3.6 V. However, the Zinc-air batteries offer much higher Of all the primary battery chemistries, use of non-aqueous electrolytes results energy density than any alkaline bat- lithium has stirred the most interest in those cells having a relatively high tery type. among members of the electronics internal impedance. industry. Lithium is an ideal material Batteries using zinc-air technology are for battery anodes because its intrinsic Lithium batteries also have extended energized only when atmospheric oxy- negative potential exceeds that of all operating-temperature ranges, made Page 2 Issue No. 11, Feb., 1997, © 1997 by Teksym Corp. Maple Plain, MN, 55359, Phone 612-479-6190, Fax 612-479-3657, E Mail [email protected] possible by the absence of Manganese dioxide lithium cells are water and the chemical also available in standard cylindrical Lithium Thionyl Chloride and physical stability of and coin sizes. They are in many ways Components and Materials the materials. Some lithi- equivalent to poly (carbon monofluo- ☛ Anode: Made of battery grade lithium foil, um-based systems, ride) cells in terms of construction, which is pressed on to the inner surface of the including Tadiran’s inor- energy density, safety and OCV, but cell can provide a mechanically sound and reli- ganic system, can operate typically have only about half the ser- able electrical connection. at temperatures as low as vice life. However, manganese dioxide- -55°C and as high as lithium cells are well-suited to applica- ☛ Separator: Between the anode and cathode, +150°C. While incinera- tions having relatively high continu- prevents internal shorts while enabling ions to tion or other exposure to ous- or pulse-current requirements, move freely between the electrodes. It is made of very high temperature can since the cell internal impedance is non woven glass. cause the casings of lithi- somewhat lower than for other types. ☛ Cathode: Made of highly porous teflon-bond- um batteries to fail cata- ed carbon powder. Thyonyl chloride cathodic strophically, other battery A proprietary lithium-iodine technolo- reduction occurs on the cathode surface when a types behave similarly gy is offered by some manufacturers, load is connected. The high porosity of the car- under similar conditions. and that approach offers very good bon results in a true surface area compatible with safety, since it uses only solid con- the current capability of the cell. Under the broad category stituents. The separator in a lithium- ☛ Electrolyte: A solution of lithium aluminum of primary lithium battery iodine cell can “heal” itself if cracks tetrachloride in thionyl chloride, which is highly types, there are several occur. This battery type powers the ionic conductive over the entire temperature chemical systems in majority of implanted cardiac pace- range. This temperature range and negligible mainstream use, each makers. The major drawback to the mass transport loss in the electrochemical sys- with its own set of perfor- lithium-iodine system is its high inter- tem contribute to the outstanding voltage stability mance and safety charac- nal impedance, which limits its use to of lithium thionyl chloride cells. The low freezing teristics. They are poly very low-drain applications. point (-105°C) and relatively high boiling point (carbon monofluoride) (>79°C) of the electrolyte result in a battery capa- lithium, or (CF)X-Li; Sulfur dioxide-lithium cells are used ble of operating over a wide temperature range. manganese dioxide lithium, almost exclusively in military/aero- ☛ Current Collector: A metal surface provides or MnO2Li; thionyl space applications and have somewhat the electrical connection between the porous car- chloride lithium, or SOCi2 lower energy density than manganese bon cathode and the positive terminal of the bat- Li; sulfur dioxide lithium, dioxide-lithium or poly (carbon mono- tery. or SO2Li; and iodine fluoride) lithium cells. Their service ☛ Can and Cover: Made of nickel-plated cold- lithium, or I2Li. life and energy density are less than rolled steel, the can is designed to withstand the half that of thionyl chloride lithium mechanical stresses that would be encountered Poly (carbon monofluo- cells.
Recommended publications
  • Hydrogel Leclanché Cell: Construction and Characterization
    energies Article Hydrogel Leclanché Cell: Construction and Characterization Greg Jenson 1,2,* , Gurjap Singh 2,3 , Jay K. Bhama 2,4,5 and Albert Ratner 2,3 1 Department of Surgery, University of Iowa Hospitals and Clinics, Iowa City, IA 52242, USA 2 Bhama-Ratner Artificial Heart & MCS Advancement Lab, University of Iowa Department of Mechanical Engineering, 3131 Seamans Ctr, Iowa City, IA 52242, USA; [email protected] (G.S.); [email protected] (J.K.B.); [email protected] (A.R.) 3 Department of Mechanical Engineering, University of Iowa, Iowa City, IA 52242, USA 4 Baptist Health Medical Center, Little Rock, AR 72205, USA 5 Division of Cardiovascular Surgery, University of Arkansas for Medical Sciences, University of Arkansas for Medical Sciences, 4301 W Markham, Little Rock, AR 72205, USA * Correspondence: [email protected] Received: 10 December 2019; Accepted: 21 January 2020; Published: 28 January 2020 Abstract: A liquid-to-gel based Leclanché cell has been designed, constructed and characterized for use in implantable medical devices and other applications where battery access is limited. This well-established chemistry will provide reliable electrochemical potential over a wide range of applications and the novel construction provides a solution for the re-charging of electrodes in hard to access areas such as an internal pacemaker. The traditional Leclanché cell, comprised of zinc (anode) and manganese dioxide (cathode), conductive carbon powder (acetylene black or graphite), and aqueous electrolyte (NH4Cl and ZnCl2), has been suspended in an agar hydrogel to simplify construction while maintaining electrochemical performance. Agar hydrogel, saturated with electrolyte, serves as the cell support and separator allowing for the discharged battery suspension to be easily replaced once exhausted.
    [Show full text]
  • 247. the Leclanche Cell Copy
    Notes from the Oesper Collections The Leclanché Cell William B. Jensen Department of Chemistry, University of Cincinnati Cincinnati, OH 45221-0172 The previous three issues of Museum Notes have described the Edison nickel-iron alkaline storage cell (1), the Daniel gravity cell (2), and the Grove and Bun- sen cells (3) respectively. This issue will deal with yet a fifth cell of historical importance found among the collection of voltaic cells donated to the Oesper Col- lections some years ago by the Chemistry Department of Oberlin College – the primary Leclanché cell. First described by the French scientist, Georges Leclanché, (figure 1) in 1868 (4, 5), this cell is based on the net cell reaction: Zn(s) + 2MnO2(s) + 2(NH4)Cl(aq) + 2H2O(l) → ZnCl2(aq) + 2Mn(OH)3 + 2NH3(aq) + ΔEel in which Zn(0) is oxidized to Zn(II) at the anode, Mn(IV) is reduced to Mn(III) at the cathode, and the resulting net cell potential is roughly 1.4 V. Figure 1. A portrait medallion commemorating Georges Like the Edison cell described earlier, the Leclan- Leclanché (1838-1882). ché cell was a single-fluid system that employed a saturated aqueous solution of ammonium chloride [(NH4)Cl] as the electrolyte. As originally conceived, the MnO2(s) and an inert rectangular carbon cathode came sealed in a large porous ceramic spacer (figures 2-3) and the Zn anode as a separate rod. Both of these were placed in a large rectangular glass battery jar and the jar half-filled with the (NH4)Cl(aq) electrolyte. To increase the conductivity of the MnO2(s), it was in- termixed with an equal quantity of powdered carbon.
    [Show full text]
  • On Manganese (IV) Oxide (Mno2) in a Leclanche Dry Cell
    Available online a t www.pelagiaresearchlibrary.com Pelagia Research Library Der Chemica Sinica, 2012, 3(1):182-191 ISSN: 0976-8505 CODEN (USA) CSHIA5 2+ Adsorption of zinc ion (Zn ) on manganese (IV) oxide (MnO 2) in a leclanche dry cell Adejoh Adu Zakariah* and Aloko Duncan Folorunsho Department of Chemical Engineering, University of Abuja, Nigeria _____________________________________________________________________________________________ ABSTRACT This work was carried out to study the adsorption of zinc nitrate (Zn(NO 3)2) on manganese (IV) oxide (MnO 2) in a leclanche dry cell. The aim of the study is to optimize the process for the adsorption of zinc ion on MnO 2 in a leclanche dry cell using a second order factorial method. Potentiometric titration method was the adsorption method used. Considering the temperature effect on electric surface charge, pH respond during titration, concentration effect on adsorption and surface charge and the nature of cation, results obtain show that adsorption is inversely proportional to temperature, in other words, as temperature of cation increases, the adsorption capacity on MnO 2 decreases at a given concentration. Also at a given temperature adsorption capacity increases as the concentration of the adsorbent increases. The highest adsorption capacity was observed at 0.1M for Zn 2+ at 28 oC . Key words : Adsorption, zinc nitrate (Zn(NO 3)2), manganese (IV) oxide, potentiometric, concentration, adsorbent. _____________________________________________________________________________________________ INTRODUCTION An electrochemical cell is a device designed to produce electrical energy as the primary output product with the cell itself undergoing a chemical transformation (reaction). Conversely, in cell some chemical reaction can be made to occur through ionic mechanism by passing electric energy into the cell (as a form of secondary input).
    [Show full text]
  • Introduction to Batteries
    Introduction to Batteries Course No: E03-002 Credit: 3 PDH A. Bhatia Continuing Education and Development, Inc. 22 Stonewall Court Woodcliff Lake, NJ 07677 P: (877) 322-5800 [email protected] CHAPTER 2 BATTERIES LEARNING OBJECTIVES Upon completing this chapter, you will be able to: 1. State the purpose of a cell. 2. State the purpose of the three parts of a cell. 3. State the difference between the two types of cells. 4. Explain the chemical process that takes place in the primary and secondary cells. 5. Recognize and define the terms electrochemical action, anode, cathode, and electrolyte. 6. State the causes of polarization and local action and describe methods of preventing these effects. 7. Identify the parts of a dry cell. 8. Identify the various dry cells in use today and some of their capabilities and limitations. 9. Identify the four basic secondary cells, their construction, capabilities, and limitations. 10. Define a battery, and identify the three ways of combining cells to form a battery. 11. Describe general maintenance procedures for batteries including the use of the hydrometer, battery capacity, and rating and battery charging. 12. Identify the five types of battery charges. 13. Observe the safety precautions for working with and around batteries. INTRODUCTION The purpose of this chapter is to introduce and explain the basic theory and characteristics of batteries. The batteries which are discussed and illustrated have been selected as representative of many models and types which are used in the Navy today. No attempt has been made to cover every type of battery in use, however, after completing this chapter you will have a good working knowledge of the batteries which are in general use.
    [Show full text]
  • Evaluation of Rapid Electric Battery Charging Techniques
    UNLV Theses, Dissertations, Professional Papers, and Capstones 2009 Evaluation of rapid electric battery charging techniques Ronald Baroody University of Nevada Las Vegas Follow this and additional works at: https://digitalscholarship.unlv.edu/thesesdissertations Part of the Power and Energy Commons Repository Citation Baroody, Ronald, "Evaluation of rapid electric battery charging techniques" (2009). UNLV Theses, Dissertations, Professional Papers, and Capstones. 156. http://dx.doi.org/10.34917/1392506 This Thesis is protected by copyright and/or related rights. It has been brought to you by Digital Scholarship@UNLV with permission from the rights-holder(s). You are free to use this Thesis in any way that is permitted by the copyright and related rights legislation that applies to your use. For other uses you need to obtain permission from the rights-holder(s) directly, unless additional rights are indicated by a Creative Commons license in the record and/ or on the work itself. This Thesis has been accepted for inclusion in UNLV Theses, Dissertations, Professional Papers, and Capstones by an authorized administrator of Digital Scholarship@UNLV. For more information, please contact [email protected]. EVALUATION OF RAPID ELECTRIC BATTERY CHARGING TECHNIQUES By Ronald Baroody Bachelor of Science University of Nevada, Las Vegas 2005 A thesis submitted in partial fulfillment of the requirements for the Master of Science in Engineering Department of Electrical and Computer Engineering Howard R. Hughes College of Engineering Graduate
    [Show full text]
  • A Mathematical Model of a Lithium/Thionyl Chloride Primary Cell T
    University of South Carolina Scholar Commons Faculty Publications Chemical Engineering, Department of 1989 A Mathematical Model of a Lithium/Thionyl Chloride Primary Cell T. I. Evans Texas A & M University - College Station T. V. Nguyen Texas A & M University - College Station Ralph E. White University of South Carolina - Columbia, [email protected] Follow this and additional works at: https://scholarcommons.sc.edu/eche_facpub Part of the Chemical Engineering Commons Publication Info Journal of the Electrochemical Society, 1989, pages 328-339. © The Electrochemical Society, Inc. 1989. All rights reserved. Except as provided under U.S. copyright law, this work may not be reproduced, resold, distributed, or modified without the express permission of The Electrochemical Society (ECS). The ra chival version of this work was published in the Journal of the Electrochemical Society. http://www.electrochem.org/ DOI: 10.1149/1.2096630 http://dx.doi.org/10.1149/1.2096630 This Article is brought to you by the Chemical Engineering, Department of at Scholar Commons. It has been accepted for inclusion in Faculty Publications by an authorized administrator of Scholar Commons. For more information, please contact [email protected]. 328 J. Electrochem. Soc., Vol. 136, No. 2, February 1989 The Electrochemical Society, Inc. Table A-I. Concentration, density, and mole fraction of LiAICI4-SOCI2 (p +_ 0.0001) = (0.594484 • 0.000934). XLjAlCI4 solutions at 25~ based on the experiment of Venkatasetty and Saathoff (5) + (1.64388 --+ 0.00004) (R 2 = 0.99997) These lines are valid in the range 0 < XLIA~C14< 0.11, 0 < C Concentration Density < 1.50 mol/liter and 1.64 < p < 1.71 g/cm ~ and at 25~ At (mol/liter) (g/cm~) XLiAIC14a higher concentrations linear extrapolation cannot be done with confidence.
    [Show full text]
  • Development of Cathode Materials for Magnesium Primary Cell K
    View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by KnowledgeCuddle Publication (E-Journals) International Journal of Research in Advance Engineering, (IJRAE) Vol. 2, Issue 5, Sep-Oct-2016, Available at: www.knowledgecuddle.com/index.php/IJRAE Development of cathode materials for magnesium primary cell K. Narthana1, M. Selvam1, K. Saminathan, V. Rajendran and Karan V.I.S. Kaler2 aCentre for nano science and technology, K S Rangasamy College of technology, Tiruchengode -637 215, Tamil Nadu, India bSchulich School of Engineering , Department of Electrical and Computer Engineering, University of Calgary, Calgary, Alberta, Canada. Abstract: The Zinc Sulfide nanoparticles were synthesized by simple chemical reaction of ZnCl2 and Sulphur powder in aqueous solution. The main advantage of this method is the use of non-toxic precursors and water as solvent. The BZ1 and NZ2 samples reveal an average particle size respectively 510 and 43.7 nm. The structural, morphological, chemical composition and optical properties of the nanoparticles were investigated by X-ray diffraction, Scanning electron Microscopy, and Energy-dispersive X-ray Spectroscopy, Ultra Violet Spectroscopy and Electrochemical studies. The NZ2 sample showed a high discharge capacity of 362 mAh g -1, whereas the BZ1 sample showed a discharge capacity of 120 mAh g -1. The discharge capacity of NZ2 sample based cathode was 33.1 % higher than BZ1 sample based cathode. Thus, the above studies confirm that zinc sulfide nano powders show promise application as a cathode material for Mg/ZnS primary cell. Key words: BZ1 sample, NZ2 sample, Discharge capacity, Electro chemical studies, Band gap *Corresponding author: [email protected] I.
    [Show full text]
  • Battery Recycling: Defining the Market and Identifying the Technology Required to Keep High Value Materials in the Economy and out of the Waste Dump
    Battery Recycling: defining the market and identifying the technology required to keep high value materials in the economy and out of the waste dump By Timothy W. Ellis Abbas H. Mirza Page 1 of 33 Introduction: The accumulation of post consumer non-Lead/Acid batteries and electrochemical (n-PbA) cells has been identified as a risk in the waste stream of modern society. The n-PbA’s contain material that is environmentally unsound for disposal; however, do represent significant values of materials, e.g. metals, metal oxides, and carbon based material, polymers, organic electrolytes, etc. The desire is to develop systems whereby the nPbA’s are reprocessed in a hygienic and environmentally astute manner which returns the materials within the n-PbA’s to society in an economically and environmentally safe and efficient manner. According to information published in the Fact File on the “Recycling of Batteries” by the Institution of Engineering and Technology (www.theiet.org) the following, Table 1, describes the recycling market. Table 1: Recoverable Metals from Various Battery Types Battery Type Recycling Alkaline & Zinc Carbon Recycled in the metals industry to recover steel, zinc, ferromanganese Nickel – (Cadmium, Metal Hydride) Recycled to recover Cadmium and Nickel with a positive market value Li-Ion Recycled to recover Cobalt with a positive market value Lead-Acid Recycled in Lead industry with a positive market value Button Cells Silver is recovered and has a positive market value; Mercury is recovered by vacuum thermal processes A literature search on “Recycling and Battery” on the STN Easy data base produced over 2500 hits.
    [Show full text]
  • Electric Current Is a Flow of Charge
    Page 1 of 7 KEY CONCEPT Electric current is a flow of charge. BEFORE, you learned NOW, you will learn • Charges move from higher to • About electric current lower potential • How current is related to • Materials can act as conductors voltage and resistance or insulators • About different types of • Materials have different levels electric power cells of resistance VOCABULARY EXPLORE Current electric current p. 28 How does resistance affect the flow of charge? ampere p. 29 Ohm’s law p. 29 PROCEDURE MATERIALS electric cell p. 31 • pencil lead 1 Tape the pencil lead flat on the posterboard. • posterboard 2 Connect the wires, cell, bulb, and bulb • electrical tape holder as shown in the photograph. • 3 lengths of wire 3 Hold the wire ends against the pencil lead • D cell battery about a centimeter apart from each other. • flashlight bulb Observe the bulb. • bulb holder 4 Keeping the wire ends in contact with the lead, slowly move them apart. As you move the wire ends apart, observe the bulb. WHAT DO YOU THINK? • What happened to the bulb as you moved the wire ends apart? • How might you explain your observation? Electric charge can flow continuously. Static charges cannot make your television play. For that you need a different type of electricity. You have learned that a static charge contains a specific, limited amount of charge. You have also learned that a static charge can move and always moves from higher to lower VOCABULARY potential. However, suppose that, instead of one charge, an electrical Don’t forget to make a four square diagram for the pathway received a continuous supply of charge and the difference in term electric current.
    [Show full text]
  • Zinc–Carbon Battery - Wikipedia 3/17/20, 1050 AM
    Zinc–carbon battery - Wikipedia 3/17/20, 1050 AM Zinc–carbon battery A zinc–carbon battery is a dry cell primary battery that delivers about 1.5 volts of direct current from the electrochemical reaction between zinc and manganese dioxide. A carbon rod collects the current from the manganese dioxide electrode, giving the name to the cell. A dry cell is usually made from zinc, which serves as the anode with a negative electrical polarity, while the inert carbon rod is the positive electrical pole cathode. General-purpose batteries may use an aqueous paste of ammonium chloride as electrolyte, possibly mixed with some zinc chloride solution. Heavy-duty types use a paste primarily composed of zinc chloride. Zinc–carbon batteries were the first commercial dry batteries, developed from the technology of the wet Leclanché cell. They Zinc–carbon batteries of various made flashlights and other portable devices possible, because sizes the battery can function in any orientation. They are still useful in low drain or intermittent use devices such as remote controls, flashlights, clocks or transistor radios. Zinc–carbon dry cells are single-use primary cells. Contents History Construction Chemical reactions Zinc-chloride "heavy duty" cell Storage Durability Environmental impact See also References External links https://en.wikipedia.org/wiki/Zinc–carbon_battery Page 1 of 7 Zinc–carbon battery - Wikipedia 3/17/20, 1050 AM History By 1876, the wet Leclanché cell was made with a compressed block of manganese dioxide. In 1886, Carl Gassner patented a "dry" version by using a zinc cup as the anode and a paste of plaster of Paris (and later, wheat flour) to jellify the electrolyte and to immobilize it.
    [Show full text]
  • Physical Chemistry LD
    Physical Chemistry LD Electrochemistry Chemistry Galvanic elements Leaflets C4.4.4.2a Leclanché cell Time required: 120 – 150 min + over night Aims of the experiment To construct a galvanic cell. To examine the Leclanché cell as a galvanic cell. To follow the path from galvanic cell to battery. The zinc-carbon battery and its characteristic curve. Principles casing In 1780, the Italian researcher and physician L. Galvani no- insula- ticed that a frog leg jerks when it comes into contact with iron tor and copper. He presumed that there was an electric effect at work. 20 years later, A. Volta developed the first battery (pri- metal mary cell) in the form of the voltaic pile. Further developments cup in the “wet battery field” followed. However, none of these cells were suitable for everyday use since the electrolyte was zinc in the form of a liquid. They are therefore not useful for mobile use for such things as pocket flash lights, mobile telephones, etc. Finally, in 1866 the first dry battery was patented, at that NH4Cl time still in wet form, by French physical chemist G. Leclan- ché. In the process, the electrolyte solution was turned into a gel using binders so that mobile use was possible. MnO2/C The Leclanché cell has a (clamping) voltage of 1.5 V. The graphite anode is made of zinc and the cathode is made of manga- electrode nese dioxide and carbon. A thickened ammonium chloride solution is used as the electrolyte. Additionally, zinc chloride is used in order to increase the energy density (charging density) (see Fig.
    [Show full text]
  • Leclanche´ and Zinc Chloride Cell Systems
    FUEL CELLS AND BATTERIES Dr.HASSAN ABDUL‐ZEHRA ZINC-CARBON BATTERIES (Leclanche´ and Zinc Chloride Cell Systems) Dry Cells Invented by George Leclanche, a French Chemist in the 1860’s, The common dry cell or LeClanche cell, has become a familiar household item. An active zinc anode in the form of a can house a mixture of MnO2 and an acidic electrolytic paste, consisting of NH4Cl, ZnCl2, H2O and starch powdered graphite improves conductivity. The inactive cathode is a graphite rod. Anode (oxidation): 2+ - Zn(s) → Zn (aq) + 2e Cathode (reduction): The cathodic half-reaction is complex and even today, is still being studied. MnO2(s) is reduced 2+ to Mn2O3(s) through a series of steps that may involve the presence of Mn and an acid-base + - reaction between NH4 and OH : + - 2MnO2 (s) + 2NH4 (aq) + 2e → Mn2O3(s) + 2NH3(aq) + H2O (l) The ammonia, some of which may be gaseous, forms a complex ion with Zn2+, which crystallize in contact Cl- ion: 2+ - Zn (aq) + 2NH3 (aq) + 2Cl (aq) → Zn(NH3)2Cl2(s) Overall Cell reaction: 2MnO2 (s) + 2NH4Cl(aq) + Zn(s) → Zn(NH3)2Cl2(s) + H2O (l) + Mn2O3(s) Ecell = 1.5 V Uses: common household items, such as portable radios, toys, flashlights, Advantage; Inexpensive, safe, available in many sizes Disadvantages: At high current drain, NH3(g) builds up causing drop in voltage, short shelf life + because zinc anode reacts with the acidic NH4 ions. Features: • Inexpensive, widely available • Inefficient at high current drain • Poor discharge curve (sloping) • Poor performance at low temperatures The major advantages and disadvantages of Leclanche´ and Zinc-Chloride batteries are listed in Table 1 below.
    [Show full text]