Ferrocenes and Isoindolines As Reagents for Redox Flow Battery Electrolytes and Moieties in Chromophores, Chelates, and Macrocycles
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Liquid Junction Potentials at Mixed Electrolyte Salt
LIQUID JUNCTION POTENTIALS AT MIXED ELECTROLYTE SALT BRIDGES. A Thesis 2ubmitted in Part-Fulfilment of the Requirements for the Degree of Master of Science of Rhodes University. BY NOEL PHILLIP FINKELSTEIN. RHODES UNIVERSITY, GRAHAli-1STmVN. September, 1956. ( i) ACKNOJLEDGJ:!Ji.fuNTS. It is with sincere gratitude that the following acknowledgements are made: DR . E.T. VE~DISR , M.Sc., (S.A.); Docteur es Sciences Physiques (France), for his able dir$ction, guidance, and constant encoura~ement. PROFESSOR W.F. BA~KER, B.Sc., Ph.D., F.R.I.C. F.n.s.s. Af., for his encouragement and interest. PHOFESSOR J.A. GLEDHILL , Ph.D., (S.A.), Ph.D., (Yale), for long hours of in valuable discussion. Mr. F. van der VI/A Tim, for his skilful and patient assistance with the technical aspects of the work. Mr. D.A. CLUR, B.Sc., (Hons.) for much in valuable discusssion, and many useful suggestions. Mrs. J. FINKELSTbiN, for her assistance with the clerical side of the pre paration of the thesis. Mr. H.T. DREYER, who was responsible for the diagrams. THE SOUTH AFRICAN COUNCIL FOH SCI~NTI?IC AND INDUSTRIAL RESJ:;AllCH for a grant held during this research. ( ii) CONTENTS . £ (( 'i j . AC KNO':-.ILED£}]-1ENTS (1) 1. GLOSSARY OF ABBREVIATIONS AND SYMBOLS. 1. 2. INTRODUCTimT. 3 . 3. CRITICAL SURVEY ON PREVIOUS WORK ON LIQUID JUNCTION POTEN~IALS. 5· 3.1. The Theory of Liquid Junction Pot- entials . 5· 3. 2. The ~l i m ination of the Error due to Liquid Junction Potentials . g. 3~3. The Measurement of Liquid Junction Potentials . -
Galvanic Cell Notation • Half-Cell Notation • Types of Electrodes • Cell
Galvanic Cell Notation ¾Inactive (inert) electrodes – not involved in the electrode half-reaction (inert solid conductors; • Half-cell notation serve as a contact between the – Different phases are separated by vertical lines solution and the external el. circuit) 3+ 2+ – Species in the same phase are separated by Example: Pt electrode in Fe /Fe soln. commas Fe3+ + e- → Fe2+ (as reduction) • Types of electrodes Notation: Fe3+, Fe2+Pt(s) ¾Active electrodes – involved in the electrode ¾Electrodes involving metals and their half-reaction (most metal electrodes) slightly soluble salts Example: Zn2+/Zn metal electrode Example: Ag/AgCl electrode Zn(s) → Zn2+ + 2e- (as oxidation) AgCl(s) + e- → Ag(s) + Cl- (as reduction) Notation: Zn(s)Zn2+ Notation: Cl-AgCl(s)Ag(s) ¾Electrodes involving gases – a gas is bubbled Example: A combination of the Zn(s)Zn2+ and over an inert electrode Fe3+, Fe2+Pt(s) half-cells leads to: Example: H2 gas over Pt electrode + - H2(g) → 2H + 2e (as oxidation) + Notation: Pt(s)H2(g)H • Cell notation – The anode half-cell is written on the left of the cathode half-cell Zn(s) → Zn2+ + 2e- (anode, oxidation) + – The electrodes appear on the far left (anode) and Fe3+ + e- → Fe2+ (×2) (cathode, reduction) far right (cathode) of the notation Zn(s) + 2Fe3+ → Zn2+ + 2Fe2+ – Salt bridges are represented by double vertical lines ⇒ Zn(s)Zn2+ || Fe3+, Fe2+Pt(s) 1 + Example: A combination of the Pt(s)H2(g)H Example: Write the cell reaction and the cell and Cl-AgCl(s)Ag(s) half-cells leads to: notation for a cell consisting of a graphite cathode - 2+ Note: The immersed in an acidic solution of MnO4 and Mn 4+ reactants in the and a graphite anode immersed in a solution of Sn 2+ overall reaction are and Sn . -
Academic Year 2017- 2018 First Term Biology Revision Sheet
Academic Year 2017- 2018 First Term Biology Revision Sheet Name: ____________________________ Date: _______________ Grade 9 Section: ______________ Q1: Choose the letter of the best answer ___ 1.What is the main function of the Golgi apparatus? A. communicates with another cell B. convert solar energy to chemical energy C. process and deliver proteins D. copy genetic material. ___2. Which of the following organelles can be found in cytoplasm and on the surface of the endoplasmic reticulum A. mitochondria B. centrosomes C. ribosomes D.centrioles ___ 3. What type of membrane allows some, but not all materials A. diffusible B. permeable C. impermeable D. selectively permeable ____4. What materials makes up a cell membrane? A. Phospholipids and cholesterol B. Cholesterol and protein C. Phospholipid, cholesterol and protein D. Phospholipid, protein and amino acid Page 1 of 7 ____5. What type of receptor is within a cell? A. Membrane receptor B. Intracellular receptor C. Intercellular receptor D. Ligand receptor ____6. Which part of phospholipid is hydrophobic? A. Glycerol B. fatty acid tail C. entire phospholipid molecule D. phosphate group only ____7. A ligand produces a response in a cell if it finds the right kind of A. carbohydrate. B. hormone. C. membrane. D.receptor. ____8. What is the term for the diffusion of water across a semipermeable membrane? A. osmosis B.equilibrium C.transport D.isotonic ____9.The movement of molecules down a concentration gradient through transport proteins in the cell membrane is a type of A. selective transport. B.osmosis C.energy expenditure. D.facilitated diffusion. ___10.Nucleus act as a A. -
1.4 Solar Cell Losses and Design in This Final Introduction Video on Photo
1.4 Solar cell losses and design In this final introduction video on photovoltaic energy conversion, we will discuss the various parts of a solar cell and the losses that occur in a solar cell. The losses in solar cells will provide an important framework to put everything we learn over the course of the next couple of weeks in context. The learning objective for this video are to understand the main function of the various parts of a solar cell. We will discuss the main losses that occur in solar cells and we will come to understand how these losses lead to the design rules for solar cells. Shown here is a standard silicon wafer based solar cell. These are the most common type of solar cells, accounting for about 93 % of the total production in 2015. We will base this solar cell on a p-type silicon absorber even though some silicon cells can be made with an n-type absorber layer. The purpose of this absorber layer, as its name implies, is to absorb light. Through this absorption, minority and majority charge charge carriers are formed. In the case of a p-type absorber, electrons are the minority carriers and holes are the majority carriers. Next is the emitter layer. The emitter layer is crucial for charge carrier separation and collection. The emitter layer functions as an selective membrane, that allows minority charge carriers, in this case electrons, to move through, but resists the movement of majority carriers, in this case holes. Without the emitter layer, generated charge carriers would simply move around in the absorber layer until they recombine. -
United States Patent to 11, 3,996,141 Updike 45 Dec
United States Patent to 11, 3,996,141 Updike 45 Dec. 7, 1976 54 DALYSIS MEMBRANE 2,971,850 2/1961 Barton ............................. 195/63 X 3, 158,532 11/1964 Pall et al. ... ... 210/503 X 75 Inventor: Stuart J. Updike, Madison, Wis. 3,282,702 1 1/1966 Schreiner ........................ 195/63 X (73) Assignee: Wisconsin Alumni Research 3,327,859 6/1967 Pall .............. ........ 210/266 3,526,481 9/1970 Rubricius ........... ... 210/321 X Foundation, Madison, Wis. 3,766,013 10/1973 Forgione et al. .................... 195/63 22) Filed: Jan. 17, 1974 3,809,613 5/1974 Vieth et al. ...................... 195/68 X 3,824, 150 7/1974 Lilly et al. ... ... 195/DIG. l l X 21 ) Appl. No.: 434,231 3,846,236 1 1/1974 Updike ......................... 23/258.5 X Related U.S. Application Data Primary Examiner-Frank A. Spear, Jr. (63) Continuation-in-part of Ser. No. 191,720, Oct. 22, Attorney, Agent, or Firm-McDougall, Hersh & Scott 1971, Pat. No. 3,846,236. 57 ABSTRACT 52 U.S. Cl. ................................ 210/501; 427/245 (51) Int. Cl. ......................................... B01D 13/04 A semi-permeable membrane containing a catalyst for 58 Field of Search .............. 210/22, 23, 321,500, conversion of hydrogen peroxide introduced from one side of the semi-permeable membrane to molecular 210/501, 502; 23/258.5; 195/18, 63; oxygen which is released from the opposite side of the 106/194; 264/41, 49; 427/245 semi-permeable membrane. The catalyst is preferably 56) References Cited in the form of a ruthenium oxide or sulfide and prefer UNITED STATES PATENTS ably in assymetrical distribution in the membrane. -
Chapter 13: Electrochemical Cells
March 19, 2015 Chapter 13: Electrochemical Cells electrochemical cell: any device that converts chemical energy into electrical energy, or vice versa March 19, 2015 March 19, 2015 Voltaic Cell -any device that uses a redox reaction to transform chemical potential energy into electrical energy (moving electrons) -the oxidizing agent and reducing agent are separated -each is contained in a half cell There are two half cells in a voltaic cell Cathode Anode -contains the SOA -contains the SRA -reduction reaction -oxidation takes place takes place - (-) electrode -+ electrode -anions migrate -cations migrate towards the anode towards cathode March 19, 2015 Electrons move through an external circuit from the anode to cathode Electricity is produced by the cell until one of the reactants is used up Example: A simple voltaic cell March 19, 2015 When designing half cells it is important to note the following: -each half cell needs an electrolyte and a solid conductor -the electrode and electrolyte cannot react spontaneously with each other (sometimes carbon and platinum are used as inert electrodes) March 19, 2015 There are two kinds of porous boundaries 1. Salt Bridge 2. Porous Cup · an unglazed ceramic cup · tube filled with an inert · separates solutions but electrolyte such as NaNO allows ions to pass 3 through or Na2SO4 · the ends are plugged so the solutions are separated, but ions can pass through Porous boundaries allow for ions to move between two half cells so that charge can be equalized between two half cells 2+ 2– electrolyte: Cu (aq), SO4 (aq) 2+ 2– electrolyte: Zn (aq), SO4 (aq) electrode: zinc electrode: copper March 19, 2015 Example: Metal/Ion Voltaic Cell V Co(s) Zn(s) Co2+ SO 2- 4 2+ SO 2- Zn 4 Example: A voltaic cell with an inert electrode March 19, 2015 Example Label the cathode, anode, electron movement, ion movement, and write the half reactions taking place at each half cell. -
Electrochemical Cells - Redox Reactions Can Be Used in a Controlled Manner to Make a Battery
Chapter 17 Worksheet #2 Name __________________________ Electrochemical Cells - Redox reactions can be used in a controlled manner to make a battery. A galvanic cell (voltaic cell or battery) converts the chemical energy of the reactants into electrical energy. BATTERY: Anode - AN OX, RED CAT Cathode - Salt Bridge - A tube containing a salt (such as KCl or NaNO3) solution that is used to connect two half-cells in an electrochemical cell; allows the passage of ions (maintains charge neutrality), but prevents the mixing of half-cell electrolytes. Shorthand notation for a galvanic cell: Zn(s)│Zn2+(aq)║Cu2+(aq)│Cu(s) where the anode is on the left, the cathode on the right, │ indicates the interface between the metal and solution, and ║ indicates the salt bridge. In many cells, the electrode itself does not react but serves only as a channel to direct electrons to or from the solution where a reaction involving other species takes place. The electrode itself is unaffected. Platinum and graphite are inert in most (but not all) electrochemical reactions. The Cu electrode could be replaced by a platinum or graphite electrode in the Zn/Cu battery: Zn(s)│Zn2+(aq)║Cu2+(aq)│Pt(s) Construct a battery from the reaction: Cr(s) + Pb2+(aq) Cr3+(aq) + Pb(s) Construct a galvanic cell using platinum electrodes and the reaction: - - + 2+ 10 Br (aq) + 2 MnO4 (aq) + 16 H (aq) 5 Br2(ℓ) + 2 Mn (aq) + 8 H2O(ℓ) A salt bridge is not required in a battery in which the reactants are physically separated from each other. -
Electrochemistry: Elektrolytic and Galvanic Cell Co08 Galvanic Series (Beketov, Cca 1860)
1/26 Electrochemistry: Elektrolytic and galvanic cell co08 Galvanic series (Beketov, cca 1860): Li, Ca, Al, Mn, Cr Zn, Cd Fe, Pb, [H2], Cu, Ag, Au ≈ ≈ ⊕ Cell = system composed of two electrodes and an electrolyte. electrolytic cell: electric energy chemical reaction ! galvanic cell: chemical reaction electric energy ! reversible galvanic cell (zero current) Electrodes anode = electrode where oxidation occurs Cu Cu2+ + 2 e ! − 2 Cl Cl2 + 2 e − ! − cathode = electrode where reduction occurs 2 Cu + + 2 e Cu credit: Wikipedia (free) − ! Cl2 + 2 e 2 Cl − ! − Oxidation and reduction are separated in a cell. The charge flows through the circuit. 2/26 Anode and cathode co08 electrolytic cell galvanic cell '$ '$ - - ⊕&% &% ⊕ Cl2 Cu2+ Cu2+ Pt Cl ! ! 2 Cu Cl Cl − Cu − CuCl2(aq) CuCl2(aq) anode cathode anode cathode “anions go to the anode” 3/26 Galvanic cells: electrodes, convention co08 Electrodes(= half-cells) may be separated by a porous separator, polymeric mem- brane, salt bridge. Cathode is right (reduction) ⊕ Anode is left (oxidation) negative electrode (anode) positive electrode (cathode) ⊕ liquid junction phase boundary . (porous separator) j salt bridge .. semipermeable membrane k Examples: 3 Cu(s) CuCl2(c = 0.1 mol dm ) Cl2(p = 95 kPa) Pt j − j j ⊕ Ag s AgCl s NaCl m 4 mol kg 1 Na(Hg) ( ) ( ) ( = − ) j j j 1 NaCl(m = 0.1 mol kg ) AgCl(s) Ag(s) j − j j ⊕ 2 3 4 3 3 3 Pt Sn +(0.1 mol dm ) + Sn +(0.01 mol dm ) Fe +(0.2 mol dm ) Fe j − − jj − j ⊕ 4/26 Equilibrium cell potential co08 Also: electromotive potential/voltage, electromo- tive force (EMF). -
Biological Fuel Cells and Membranes
membranes Review Biological Fuel Cells and Membranes Zahra Ghassemi and Gymama Slaughter * Bioelectronics Laboratory, Department of Computer Science and Electrical Engineering, University of Maryland Baltimore County, 1000 Hilltop Circle, Baltimore, MD 21250, USA; [email protected] * Correspondence: [email protected]; Tel.: +1-410-455-8483 Academic Editor: Tongwen Xu Received: 31 October 2016; Accepted: 5 January 2017; Published: 17 January 2017 Abstract: Biofuel cells have been widely used to generate bioelectricity. Early biofuel cells employ a semi-permeable membrane to separate the anodic and cathodic compartments. The impact of different membrane materials and compositions has also been explored. Some membrane materials are employed strictly as membrane separators, while some have gained significant attention in the immobilization of enzymes or microorganisms within or behind the membrane at the electrode surface. The membrane material affects the transfer rate of the chemical species (e.g., fuel, oxygen molecules, and products) involved in the chemical reaction, which in turn has an impact on the performance of the biofuel cell. For enzymatic biofuel cells, Nafion, modified Nafion, and chitosan membranes have been used widely and continue to hold great promise in the long-term stability of enzymes and microorganisms encapsulated within them. This article provides a review of the most widely used membrane materials in the development of enzymatic and microbial biofuel cells. Keywords: biofuel cells; microbial fuel cells; semi-permeable membrane; chitosan; Nafion 1. Introduction A conventional fuel cell is an electrochemical power source that continuously converts the stored chemical energy in a fuel to electrical energy as long as there is a continuous supply of fuel. -
What Is the Difference Between Osmosis and Diffusion?
What is the difference between osmosis and diffusion? Students are often asked to explain the similarities and differences between osmosis and diffusion or to compare and contrast the two forms of transport. To answer the question, you need to know the definitions of osmosis and diffusion and really understand what they mean. Osmosis And Diffusion Definitions Osmosis: Osmosis is the movement of solvent particles across a semipermeable membrane from a dilute solution into a concentrated solution. The solvent moves to dilute the concentrated solution and equalize the concentration on both sides of the membrane. Diffusion: Diffusion is the movement of particles from an area of higher concentration to lower concentration. The overall effect is to equalize concentration throughout the medium. Osmosis And Diffusion Examples Examples of Osmosis: Examples of osmosis include red blood cells swelling up when exposed to fresh water and plant root hairs taking up water. To see an easy demonstration of osmosis, soak gummy candies in water. The gel of the candies acts as a semipermeable membrane. Examples of Diffusion: Examples of diffusion include perfume filling a whole room and the movement of small molecules across a cell membrane. One of the simplest demonstrations of diffusion is adding a drop of food coloring to water. Although other transport processes do occur, diffusion is the key player. Osmosis And Diffusion Similarities Osmosis and diffusion are related processes that display similarities. Both osmosis and diffusion equalize the concentration of two solutions. Both diffusion and osmosis are passive transport processes, which means they do not require any input of extra energy to occur. -
Stability of Positive Electrolyte Containing Trishydroxymethyl Aminomethane Additive for Vanadium Redox Flow Battery
Int. J. Electrochem. Sci., 7 (2012) 4388 - 4396 International Journal of ELECTROCHEMICAL SCIENCE www.electrochemsci.org Stability of Positive Electrolyte Containing Trishydroxymethyl Aminomethane Additive for Vanadium Redox Flow Battery Sui Peng1, Nangfang Wang1,2, Chao Gao1, Ying Lei1, Xingxing Liang1, Suqin Liu1,* , Younian Liu1 1 Key Laboratory of Resources Chemistry of Nonferrous Metals, Ministry of Education, College of Chemistry and Chemical Engineering, Central South University, Changsha 410083, China 2 School of Chemistry and Chemical Engineering, Hunan Institute of Engineering, xiangtan 411104, China *E-mail: [email protected] Received: 10 March 2012 / Accepted: 24 March 2012 / Published: 1 May 2012 Trishydroxymethyl aminomethane (Tris) was used as an additive of the positive electrolyte for all vanadium redox battery (VRB) and cycling and electrochemical stabilities of the positive electrolyte were investigated. The 50 cyclic voltammetry (CV) cycles suggested that the positive electrolyte with the Tri additive after charge-discharge cycles has good cycle stability compared to that before the charge-discharge cycles. The VRB employing the vanadium electrolyte with the Tris additive as positive electrolyte exhibited better charge-discharge behavior and less discharge capacity fade rate with cycles compared with the blank electrolyte system. The UV/visible spectroscopy showed that the vanadium concentration in the positive electrolyte containing Tri additive during 40 charge-discharge cycles remains unchanged. The X-ray photoelectron spectroscopy (XPS) verified that the positive electrolyte with the Tri additive has no etching and oxidation effect on the carbon felt electrode. Keywords: Vanadium redox flow battery; additive; stability; electrochemical stability 1. INTRODUCTION All vanadium redox flow battery (VRB) is a promising energy conversion device that employs V(V)/ V(II)/V(III) and V(IV)/V(V) couples in the negative and positive half-cells respectively to store chemical potential energy [1-3]. -
Evaluation of Thin Film Composite Forward Osmosis Membranes
Drink. Water Eng. Sci., 14, 45–52, 2021 https://doi.org/10.5194/dwes-14-45-2021 © Author(s) 2021. This work is distributed under the Creative Commons Attribution 4.0 License. Evaluation of thin film composite forward osmosis membranes: effect of polyamide preparation conditions Aya Mohammed Kadhom1, Mustafa Hussein Al-Furaiji2, and Zaidun Naji Abudi1 1Environmental Engineering Department, College of Engineering, Mustansiriyah University, Baghdad, Iraq 2Environment and Water Directorate, Ministry of Science and Technology, Baghdad, Iraq Correspondence: Mustafa Hussein Al-Furaiji ([email protected]) Received: 11 October 2020 – Discussion started: 15 October 2020 Revised: 23 December 2020 – Accepted: 5 January 2021 – Published: 8 February 2021 Abstract. The forward osmosis (FO) process has been considered for desalination as a competitive option with respect to the traditional reverse osmosis process. The interfacial polymerization (IP) reaction between two monomers (i.e., m-phenylenediamine, MPD, and 1,3,5-benzenetricarbonyl chloride, TMC) is typically used to prepare the selective polyamide layer that prevents salts and allows water molecules to pass. In this research, we investigated the effect of preparation conditions (MPD contact time, TMC reaction time, and addition of an amine salt) on the FO performance in terms of water flux and salt flux. The results showed that increasing MPD contact time resulted in a significant increase in the water flux and salt flux. However, increasing TMC reaction time caused a decline in both the water flux and the salt flux. The optimum condition that gave the highest water flux (64 L m−2 h−1) was found to be as 5 min for MPD and 1 min for TMC.