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History of the Chlor-Alkali Industry
2 History of the Chlor-Alkali Industry During the last half of the 19th century, chlorine, used almost exclusively in the textile and paper industry, was made [1] by reacting manganese dioxide with hydrochloric acid 100–110◦C MnO2 + 4HCl −−−−−−→ MnCl2 + Cl2 + 2H2O (1) Recycling of manganese improved the overall process economics, and the process became known as the Weldon process [2]. In the 1860s, the Deacon process, which generated chlorine by direct catalytic oxidation of hydrochloric acid with air according to Eq. (2) was developed [3]. ◦ 450–460 C;CuCl2 cat. 4HCl + O2(air) −−−−−−−−−−−−−−→ 2Cl2 + 2H2O(2) The HCl required for reactions (1) and (2) was available from the manufacture of soda ash by the LeBlanc process [4,5]. H2SO4 + 2NaCl → Na2SO4 + 2HCl (3) Na2SO4 + CaCO3 + 2C → Na2CO3 + CaS + 2CO2 (4) Utilization of HCl from reaction (3) eliminated the major water and air pollution problems of the LeBlanc process and allowed the generation of chlorine. By 1900, the Weldon and Deacon processes generated enough chlorine for the production of about 150,000 tons per year of bleaching powder in England alone [6]. An important discovery during this period was the fact that steel is immune to attack by dry chlorine [7]. This permitted the first commercial production and distribu- tion of dry liquid chlorine by Badische Anilin-und-Soda Fabrik (BASF) of Germany in 1888 [8,9]. This technology, using H2SO4 for drying followed by compression of the gas and condensation by cooling, is much the same as is currently practiced. 17 “chap02” — 2005/5/2 — 09Brie:49 — page 17 — #1 18 CHAPTER 2 In the latter part of the 19th century, the Solvay process for caustic soda began to replace the LeBlanc process. -
Energy and Exergy Analyses of Different Aluminum Reduction Technologies
sustainability Article Energy and Exergy Analyses of Different Aluminum Reduction Technologies Mazin Obaidat 1, Ahmed Al-Ghandoor 1, Patrick Phelan 2, Rene Villalobos 2 and Ammar Alkhalidi 3,* ID 1 Department of Industrial Engineering, The Hashemite University, Az-Zarqa 13133, Jordan; [email protected] (M.O.); [email protected] (A.A.-G.) 2 Ira A. Fulton Schools of Engineering, Arizona State University, Tempe, AZ 85287, USA; [email protected] (P.P.); [email protected] (R.V.) 3 Energy Engineering Department, German Jordanian University, Amman 11180, Jordan * Correspondence: [email protected]; Tel.: +962-7-9611-2506 Received: 23 February 2018; Accepted: 11 April 2018; Published: 17 April 2018 Abstract: This paper examines and compares different aluminum reduction technologies found in the literature as alternatives to the current Hall–Heroult technology. The main inefficiencies in the current Hall–Heroult technology were identified and the advantages of the different proposed technologies over the Hall–Heroult technology were determined. The comparison between the different technologies, namely Hall–Heroult, wetted drained cathode, inert anode, and carbothermic, was based on energy and material requirements, and environmental impact. In order to combine all of the evaluation criteria into one numerical value, the exergy concept was utilized as a decision tool. The results emphasize that in order to analyze any conversion system, the exergy of energy, material, environmental impact, and their associated chain production should be taken into consideration. Keywords: exergy; aluminum; Hall–Heroult; inert anode; wetted drained cathode; carbothermic 1. Introduction Aluminum’s unique properties of low density and corrosion resistance make it a very important metal and a metal of choice to modern manufacturing. -
GREEN SYNTHESIS and CHARACTERIZATION of SODIUM Supported by CYANIDE from CASSAVA (Manihot Esculenta CRANTZ)
GREEN SYNTHESIS AND CHARACTERIZATION OF SODIUM Supported by CYANIDE FROM CASSAVA (Manihot esculenta CRANTZ) E. B. AttahDaniel1*, P. O. Enwerem2, P. G. Lawrence1, C. U. Ofiwe 3, S. O. O. Olusunle4 and A. R. Adetunji5 1Department of Chemical Sciences, Federal University Wukari, PMB 1020, Taraba State, Nigeria 2Department of Chemistry, River State University, PMB 5080, Mkpoluorowurukwo, Port Harcourt, Nigeria 3National Agency for Science & Engineering Infrastructure, Centre of Excellence, Nanotechnology and Advanced Material, Akure x, Ondo State, Nigeria 4Engineering Materials Development Institute, PMB 611 Akure, Ondo State, Nigeria 5Department of Materials and Metallurgical Engineering, Obafemi Awolowo University, Ile Ife, Nigeria *Corresponding author: [email protected] Received: January 09, 2020 Accepted: February 24, 2020 Abstract: This study was carried out to develop a green, simple and cost-effective route for synthesis of sodium cyanidevia aquohydrolysis of linamarin a cyanogenic glucoside found in cassava (Manihot esculenta Crantz). Two procedures were employed and compared, the acid hydrolysis method and direct (aquo) hydrolysis. The CN– ion released was reacted with Na+ via ion exchange to replace the hydroxyl ion (OH–) and yielded NaCN. The NaCN was crystallized via evaporation in an air ventilated oven by maintaining the temperature of the reaction solution at 100oC. The crystalized salt was quantified using the modified Vogel’s Argentometric method of cyanide quantification. The concentrations were found to be 10.56 mg/g for whole tuber, 13.92 mg/g for tuber tissue and 4.5 mg/g for cassava peels. Analyte grade sodium cyanide purchased off shelf was used as a reference. The crystals were characterized using, X-ray diffraction analysis; the X-ray diffractogram confirmed the products from acid hydrolysis was a cyanogen (CN2CN2) while the product from direct hydrolysis was sodium cyanide. -
ELECTROWINNING of TITANIUM from TITANIUM TETRACHLORIDE: PILOT PLANT EXPERIENCE and PRODUCTION PLANT PROJECTIONS George Gobel, Jo
ELECTROWINNING OF TITANIUM FROM TITANIUM TETRACHLORIDE: PILOT PLANT EXPERIENCE AND PRODUCTION PLANT PROJECTIONS George Gobel, John Fisher and Linden E. Snyder The Dow Chemical Company, Midland, Michigan Howmet Turbine Components Corporation, Whitehall, Michigan Introduction High purity electrolytic titanium is being successfully produced on a pilot plant basis by D-H Titanium Company, a joint venture of The Dow Chemical Company and Howmet Turbine Components Corporation. The technology is an out growth of work originating at the U.S. Bureau· of Mines, Boulder City, Nevada. [l] The project is aimed at commercialization of this prior bench-scale research. Full-scale prot_otype components are being operated in a single ,anode 5,000 AMP cell producing approximately 45 kg./day of metal. Construction of industrial scale multiple anode cells is presently'underway that will culminate in opera tion of a one half to one million kg. per year demonstration plant in 1981. Previous research in the field has been extensive. Major efforts at prototype scale-up have been conducted by the New Jersey Zinc Co. (2 land Titanium Metals Corporation o.f America. [3] In both processes the diaphragm, which is required to ~nable selective oxidation of the chloride ion, was generated in the cell. A substantial fraction of the cathodic current was directed to a screen or perforate plate that divided the cell into anolyte and catholyte areas. As metal deposited restricting the plate openings an efficient semipermeable membrane was set-up which excluded Ti+2, Ti+3 interactions at the anode and cathode. High purity titanium was produced by both companies, how ever, the methods employed had several 'inherent shortcomings. -
Electrolysis of Water - Wikipedia 1 of 15
Electrolysis of water - Wikipedia 1 of 15 Electrolysis of water Electrolysis of water is the decomposition of water into oxygen and hydrogen gas due to the passage of an electric current. This technique can be used to make hydrogen gas, a main component of hydrogen fuel, and breathable oxygen gas, or can mix the two into oxyhydrogen, which is also usable as fuel, though more volatile and dangerous. It is also called water splitting. It ideally requires a potential difference of 1.23 volts to split water. Simple setup for demonstration of Contents electrolysis of water at home History Principle Equations Thermodynamics Electrolyte selection Electrolyte for water electrolysis Pure water electrolysis Techniques Fundamental demonstration Hofmann voltameter Industrial High-pressure High-temperature An AA battery in a glass of tap water Alkaline water with salt showing hydrogen Polymer electrolyte membrane produced at the negative terminal Nickel/iron Nanogap electrochemical cells Applications Efficiency Industrial output Overpotential Thermodynamics https://en.wikipedia.org/wiki/Electrolysis_of_water Electrolysis of water - Wikipedia 2 of 15 See also References External links History Jan Rudolph Deiman and Adriaan Paets van Troostwijk used, in 1789, an electrostatic machine to make electricity which was discharged on gold electrodes in a Leyden jar with water.[1] In 1800 Alessandro Volta invented the voltaic pile, and a few weeks later the English scientists William Nicholson and Anthony Carlisle used it for the electrolysis of water. In 1806 -
5. Electrolytic Processes
5. Electrolytic Processes 5.1 Introduction • The fact that electrical energy can produce chemical changes and the processes based on it, called the “electrolytic processes”, are widely used for extraction of pure metals from their ores (such as aluminum, zinc, copper, magnesium, sodium etc.), manufacturing of various chemicals (such as caustic soda, potassium permanganate, hydrogen, oxygen, chlorine etc.), electro deposition of metals including electroplating, electrotyping, electroforming, building up of worn-out parts in metallurgical, chemical and other industries. 5.2 Principle of electrolysis • As discussed in the definition of electrolyte, whenever any electrolyte gets dissolved in water, its molecules split into cations and anions moving freely in the electrolytic solution. • Now two metal rods are immersed in the solution and an electrical potential difference applied between the rods externally preferably by a battery. These partly immersed rods are technically referred as electrodes. • The electrode connected with negative terminal of the battery is known as cathode and the electrode connected with positive terminal of the battery is known as anode. • The freely moving positively charged cations are attracted by cathode and negatively charged anions are attracted by anode. - e- e Battery Impure Copper Pure Copper C A a n t SO4- o Cu+ h d + o SO4- Cu e Cu+ d e Cu+ Electrolyte (CuSO4) Impurities Figure 5.1 Electrolysis Prof. Rajan Detroja, EE Department Utilization of Electrical Energy and Traction (2160907) 1 5. Electrolytic Processes • In cathode, the positive cations take electrons from negative cathode and in anode, negative anions give electrons to the positive anode. For continually taking and giving electrons in cathode and anode respectively, there must be flow of electrons in the external circuit of the electrolytic. -
4.3 Synthetic Graphite
BRNO UNIVERSITY OF TECHNOLOGY VYSOKÉ UČENÍ TECHNICKÉ V BRNĚ FACULTY OF ELECTRICAL ENGINEERING AND COMMUNICATION FAKULTA ELEKTROTECHNIKY A KOMUNIKAČNÍCH TECHNOLOGIÍ DEPARTMENT OF ELECTRICAL AND ELECTRONIC TECHNOLOGY ÚSTAV ELEKTROTECHNOLOGIE THE EFFECT OF ELECTRODE BINDERS TO ELECTROCHEMICAL PROPERTIES OF NEGATIVE ELECTRODE MATERIALS BACHELOR'S THESIS VLIV POJIV NA ELEKTROCHEMICKÉ VLASTNOSTI ZÁPORNÝCH ELEKTRODOVÝCH HMOT BAKALÁŘSKÁ PRÁCE AUTHOR András Zsigmond AUTOR PRÁCE SUPERVISOR Ing. Jiří Libich, Ph.D. VEDOUCÍ PRÁCE BRNO 2016 BRNO UNIVERSITY OF TECHNOLOGY Faculty of Electrical Engineering and Communication Department of Electrical and Electronic Technology Bachelor thesis Bachelor's study field Microelectronics and Technology Student: András Zsigmond ID: 154915 Year of study: 3 Academic year: 2015/16 TITLE OF THESIS: The Effect of Electrode Binders to Electrochemical Properties of Negative Electrode Materials INSTRUCTION: Get acquaint with Lithium-Ion batteries and their charactericti electrochemicla properties. Study operation principle of Litihum-Ion battery along with intercalaction process. Lead experiments which involve different kinds of binders and their using in electrodes. REFERENCE: Podle pokynů vedoucího práce. Assigment deadline: 8. 2. 2016 Submission deadline: 2. 6. 2016 Head of thesis: Ing. Jiří Libich, Ph.D. Consultant: doc. Ing. Jiří Háze, Ph.D. Subject Council chairman WARNING: The author of this bachelor thesis claims that by creating this thesis he/she did not infringe the rights of third persons and the personal and/or property rights of third persons were not subjected to derogatory treatment. The author isfully aware of the legal consequences of an infringement of provisions asper Section 11 and following of Act No 121/2000 Coll. on copyright and rights related to copyright and on amendments to some other laws (the Copyright Act) in the wording of subsequent directives including the possible criminal consequences asresulting from provisions of Part 2, Chapter VI, Article 4 of Criminal Code 40/2009 Coll. -
Electrolytic Concentration of Caustic Soda Carl Rene Vander Linden Iowa State College
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1950 Electrolytic concentration of caustic soda Carl Rene Vander Linden Iowa State College Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Chemical Engineering Commons Recommended Citation Vander Linden, Carl Rene, "Electrolytic concentration of caustic soda " (1950). Retrospective Theses and Dissertations. 14031. https://lib.dr.iastate.edu/rtd/14031 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. INFORMATION TO USERS This manuscript has been reproduced from the microfilm master. UMI films the text directly from the original or copy submitted. Thus, some thesis and dissertation copies are in typewriter face, while others may be from any type of computer printer. The quality of this reproduction is dependent upon the quality of the copy submitted. Broken or indistinct print, colored or poor quality illustrations and photographs, print bleedthrough, substandard margins, and improper alignment can adversely affect reproduction. In the unlikely event that the author did not send UMI a complete manuscript and there are missing pages, these will be noted. Also, if unauthorized copyright material had to be removed, a note will indicate the deletion. Oversize materials (e.g., maps, drawings, charts) are reproduced by sectioning the original, beginning at the upper left-hand comer and continuing from left to right in equal sections with small overiaps. -
Industrial Process Industrial Process
INDUSTRIAL PROCESS INDUSTRIAL PROCESS SESSION 4 Electrolysis SESSION 4 Electrolysis Session 4 Electrolysis Illustration of an electrolysis apparatus used in a school laboratory. In chemistry and manufacturing, electrolysis is a method of using a direct electric current (DC) to drive an otherwise non-spontaneous chemical reaction. Electrolysis is commercially highly important as a stage in the separation of elements from naturally occurring sources such as ores using an electrolytic cell. The voltage that is needed for electrolysis to occur is called the decomposition potential. Contents 1 History 2 Overview o 2.1 Process of electrolysis o 2.2 Oxidation and reduction at the electrodes o 2.3 Energy changes during electrolysis o 2.4 Related techniques 3 Faraday's laws of electrolysis o 3.1 First law of electrolysis o 3.2 Second law of electrolysis 1 4 Industrial uses 5 Competing half-reactions in solution electrolysis 6 Electrolysis of water 7 Electrocrystallization 8 Experimenters History The word electrolysis comes from the Greek ἤλεκτρον [ lektron] "amber" and λύσις [lýsis] "dissolution". 1785 – Martinus van Marum's electrostatic generator was used to reduce tin, zinc, and antimony from their salts using electrolysis.[1] 1800 – William Nicholson and Anthony Carlisle (view also Johann Ritter), decomposed water into hydrogen and oxygen. 1807 – Potassium, sodium, barium, calcium and magnesium were discovered by Sir Humphry Davy using electrolysis. 1833 - Michael Faraday develops his two laws of electrolysis, and provides a mathematical -
Electrolysis
Electricity Current and the transport of charge Electrolysis DETERMINATION OF THE FARADAY CONSTANT Production of hydrogen by means of electrolysis and determining the volume of the hydrogen V. Determining the charge Q by measuring the current as a function of time I(t). Calculating the Faraday constant F. UE3020700 07/15 UD BASIC PRINCIPLES Electrolysis is the name given to the splitting or dissocia- tion of a chemical bond due to the action of an electric current. The process of electrical conduction is associat- ed with decomposition of the substance in question such that the charge transported Q and the quantity in moles n of material which has undergone dissociation are propor- tional to one another. The constant of proportionality is called the Faraday constant F and is a fundamental phys- ical constant. To be more precise regarding the proportionality between the charge Q and the number of moles n of dissociated material, we actually need to take into account a multiplier z, the valen- cy number for the dissociated ions. The following is true: (1) Q F n z Once that quantity is known, the Faraday constant can there- fore be determined by measuring the charge Q and the num- ber of moles n involved in an electrolytic process. In this experiment, the electrolysis of water will cause a certain quantity of hydrogen and oxygen to be produced. In order to determine the quantity of charge Q transported during this process, the change in electric current over time I(t) will be measured and then the charge Q can be derived by integration: (2) Q I() t dt . -
Exploitation Strategic Plan and Business Model - Final
Exploitation strategic plan and business model - final Deliverable 8.4 © Copyright 2019 The INTMET Consortium Project Funded by the European Commission under the Horizon 2020 Framework Programme. Grant Agreement No 689515 EXPLOITATION PLAN-FINAL D8.4 PROGRAMME H2020 – Environment and Resources GRANT AGREEMENT NUMBER 689515 PROJECT ACRONYM INTMET DOCUMENT Deliverable 8.4 TYPE (DISTRIBUTION LEVEL) ☒ Public ☐ Confidential ☐ Restricted DUE DELIVERY DATE M36 DATE OF DELIVERY January 31 2019 STATUS AND VERSION NUMBER OF PAGES WP / TASK RELATED WP 8, task 8.4, 8.5 WP / TASK RESPONSIBLE MinPol AUTHOR (S) Prof. Dr. Horst Hejny, Dr. Angelika Brechelmacher, Prof. Dr. Günter Tiess PARTNER(S) CONTRIBUTING FILE NAME Exploitation strategic plan and business model - final DOCUMENT HISTORY VERS ISSUE DATE CONTENT AND CHANGES 1.0 30/01/2019 First Revision 1.1 31/01/2019 Small corrections ClC final 31/01/2019 for submission DOCUMENT APPROVERS PARTNER APPROVER CLC Francisco Sánchez 2 | 34 EXPLOITATION PLAN-FINAL D8.4 TABLE OF CONTENTS 1. PURPOSE ............................................................................................................................................................................................... 6 2. BUSINESS MODEL .................................................................................................................................................................................. 7 2.1 BASIC IDEA ............................................................................................................................................................................................... -
METALS PRODUCTION Theodore R. Beck Electrochemical Technology
METALS PRODUCTION F- /J Theodore R. Beck Electrochemical Technology Corp. Abstract Existing procedures for design of electrochemical plants can be used for design of lunar processes taking into consideration the differences in environmental conditions. These differences include: 1/6 Earth gravity, high vacuum, solar electrical and heat source, space radiation heat sink, long days and nights, and different availabilityand economics of materials, energy, and labor. Techniques have already been developed for operation of relatively small scale hydrogen-oxygen fuel cell systems used in the U.S. lunar landing program. Design and operation of lunar aqueous electrolytic process plants appears to be within the state-of-the-art. Finding or developing compatible materials for construction and designing of fused-magma metal winning cells will present a real engineering challenge. 111-41 Introduction Electrochemical processes are candidates for exploiting lunar rocks to obtain oxygen, metals of construction, and by-product glasses and ceramic materials. Since the Apollo landings, NASA has supported some preliminary studies on electrochemical processing of lunar rocks. One of the first was a laboratory investigation at the Bureau of Mines by Kesterke on electrowinning of oxygen from • o 1 sthcate rocks. Electrolyses were performed with volcanic scoria, fluxed with fluorides to obtain operating temperatures in the range of 1050° to 1250°C, and a current of about 50 amperes. Oxygen was obtained at a current efficiency of about 55%. Solid cathode deposits were formed consisting of metal dendrites of iron, aluminum, silicon, etc., in an electrolyte matrix. Waldron. Ersffeld, and Criswell reviewed the role of chemical engineering in space manufacturing in 1979.