Heterogeneous Production of Perchlorate and Chlorate By

Total Page:16

File Type:pdf, Size:1020Kb

Heterogeneous Production of Perchlorate and Chlorate By HETEROGENEOUS PRODUCTION OF PERCHLORATE AND CHLORATE BY OZONE OXIDATION OF Cl- by SIXUAN WANG B.E. A Thesis In CIVIL ENGINEERING Submitted to the Graduate Faculty of Texas Tech University in Partial Fulfillment of The Requirements for The Degree of MASTER OF SCIENCE IN CIVIL ENGINEERING Approved Dr. Andrew W. Jackson Chairperson of the Committee Dr. Todd A. Anderson Peggy Gordon Dean of Graduate School August, 2011 Copyright © 2011, Sixuan Wang Texas Tech University, Sixuan Wang, August 2011 ACKNOWLEDGEMENTS This research project would not finish without the support of many people. I would like to express my gratitude to all those who gave me help and support to complete this thesis. I want to thank Dr. Andrew Jackson, the chair of my committee for giving me the chance, guidance, and encouragement. I would like to take this opportunity to thank my committee members, Dr. Todd Anderson, for his continuous support and encouragement all the way. I would also take this opportunity to thank my friends and colleagues Dr. Rao, Nubia, Felipe, Tony and Tim for their continuous help, sharing during these two years of research in Environmental lab. I am very thankful to the Strategic Environmental Research and Development Program (SERDP) for providing the necessary funds for this project. ii Texas Tech University, Sixuan Wang, August 2011 TABLE OF CONTENTS ACKNOWLEDGEMENTS .......................................................................................... ii ABSTRACT .................................................................................................................. v LIST OF TABLES ...................................................................................................... vii LIST OF FIGURES ................................................................................................... viii I. INTRODUCTION ..................................................................................................... 1 1.1 Occurrence of Natural Perchlorate ...................................................................... 3 1.2 Natural Perchlorate Production Mechanisms ...................................................... 4 - 1.2.1 ClO4 Production by UV Irradiation of Oxychlorine Aqueous Species ....... 4 - - 1.2.2 ClO4 Production by Ozone Oxidation of Cl in Aqueous and Dry Systems 6 - 1.2.3 ClO4 Production by Ozone Oxidation of Aqueous Chlorine/Oxy-Chlorine Species ................................................................................................................... 6 1.3 Chlorate Background Information ...................................................................... 7 1.4 Objectives ............................................................................................................ 8 II. MATERIALS AND METHODS ............................................................................. 9 2.1 Experiment Set-up ............................................................................................. 12 2.1.1 Reactor Surface Area Experiment .............................................................. 14 2.1.2 Humidity Experiment ................................................................................. 14 2.1.3 HCl Oxidation Experiment ......................................................................... 16 2.2 Control system................................................................................................... 17 2.3 Chemicals and reagents ..................................................................................... 18 2.4 Measurements of ozone concentrations ............................................................ 18 2.5 Analyses of chlorine oxyanions ........................................................................ 18 2.5.1 Perchlorate Analysis ................................................................................... 18 2.5.2 Chlorate Analysis ....................................................................................... 19 2.5.3 Chloride Analysis ....................................................................................... 20 iii Texas Tech University, Sixuan Wang, August 2011 III. RESULTS ............................................................................................................. 21 3.1 Production of Perchlorate and Chlorate from Ozone Oxidation of non-Aqueous Chloride ................................................................................................................... 21 - - 3.2 The Effect of Reaction Time on ClO4 Generation by Ozone Oxidation of Cl 21 - - 3.3 The Impact of Initial Cl mass on ClO4 production .......................................... 30 - 3.4 The Impact of Moisture on ClO4 production.................................................... 35 - 3.5 The Impact of Reactor Surface Area on ClO4 Production ............................... 37 - - 3.6 Formation of ClO4 and ClO3 by Ozone Oxidation of HCl Gas ....................... 44 IV. DISCUSSION ....................................................................................................... 47 4.1 Perchlorate Generation by Ozone Oxidation of Cl- .......................................... 47 4.2 Effect of Reaction Time .................................................................................... 47 4.3 Effect of Initial Cl- Mass ................................................................................... 48 4.4 Effect of Reactor Surface Area ......................................................................... 49 4.5 Effect of Humidity ............................................................................................ 50 - - 4.6 ClO4 Formation by O3 Oxidation of Gas Phase Cl .......................................... 51 V. CONCLUSION ...................................................................................................... 52 REFERENCE .............................................................................................................. 55 iv Texas Tech University, Sixuan Wang, August 2011 ABSTRACT - Perchlorate (ClO4 ) an atmospherically produced species, is widely distributed in the environment at low concentrations. Studies have demonstrated the - potential for atmospheric formation of ClO4 and evaluated some mechanisms for - - ClO4 formation by UV irradiation and ozone oxidation of aqueous Cl and oxy- chlorine species as well as the dry oxidation of Cl salts. However, there has been no - systematic evaluation of the controlling factors that impact ClO4 formation by ozone mediated oxidation of dry Cl-. The objective of this study was to determine the - factors that control ClO4 formation by ozone oxidation of chloride in heterogeneous - - systems. Experiments were conducted to evaluate production of ClO4 and ClO3 formation by heterogeneous oxidation by evaluating the ozone oxidation at constant NaCl mass for different oxidation periods, ozone oxidation of varying NaCl masses for a constant oxidation period (1 day), the impact of humidity below the deliquescence point, the impact of reactor and salt surface area, and the physical form - - of Cl (NaCl and HCl). The mass of ClO4 formed in the reactor increased roughly linearly (R2 = 0.98; R2 = 0.83) with respect to reaction time for a constant mass of Cl. - - - ClO4 mass did not consistently vary with an increase in Cl mass while ClO3 increased 3 orders of magnitude (0.043 μg- 37.93 μg) over the 4 order range of Cl- - masses reacted. The manner in which ClO4 formed mass in the humidity system was - similar to how it was produced in the low humidity system; however, ClO3 mass increased by 2 orders of magnitude in the humidity system compared to the dry - - system. ClO4 and ClO3 mass production were linearly related to reactor surface area v Texas Tech University, Sixuan Wang, August 2011 for constant ratio of Cl mass to reactor area but no increase in production was - observed for an increase in Cl surface area at constant Cl mass. ClO4 production form HCl gas was relatively equal to that produced from HCl for similar oxidation time periods and masses. This work suggested that Cl in a variety of forms can be - - heterogeneously oxidized by ozone to produce ClO4 and ClO3 at varying ratios dependent on the oxidation conditions. The ratios appear to be influenced by the total mass of Cl oxidized and associate reaction times. It also appears that the reactor surface area may play a role in the oxidation process perhaps by surface catalyzation. Additional work is required to full evaluate this production mechanisms role in - atmospheric production of ClO4 . vi Texas Tech University, Sixuan Wang, August 2011 LIST OF TABLES 2.1 Experimental Matrix of System Parameters ..................................................... 9 - - - - 3.1 Average ClO4 and ClO3 detected in the reactor, and ClO4 , ClO3 - and Cl in the trapping flask after ozone oxidation of 1.8g of NaCl. .......................... 23 - - - - 3.2 Average ClO4 and ClO3 detected in the reactor, and ClO4 , ClO3 - and Cl in the trapping solution after ozone oxidation of 0.18g of NaCl. ................... 25 - - 3.3 Representation of average ClO4 and ClO3 detected in the reactor, - - - and ClO4 , ClO3 and Cl in the trapping solution of 1day ozone oxidation of different NaCl mass. ............................................................................................... 33 - - 3.4 Average ClO4 and ClO3 Detected in the Reactor and Trapping Solution for 1 Day Oxidation of Cl- Have Different Reactor Surface Area. .............. 39 vii Texas Tech University,
Recommended publications
  • Sodium Chloride (Halite, Common Salt Or Table Salt, Rock Salt)
    71376, 71386 Sodium chloride (Halite, Common Salt or Table Salt, Rock Salt) CAS number: 7647-14-5 Product Description: Molecular formula: NaCl Appearance: white powder (crystalline) Molecular weight: 58.44 g/mol Density of large crystals: 2.17 g/ml1 Melting Point: 804°C1 Density: 1.186 g/ml (5 M in water)2 2 Solubility: 1 M in H2O, 20°C, complete, clear, colorless 2 pH: 5.0-8.0 (1 M in H2O, 25°C) Store at room temperature Sodium chloride is geologically stable. If kept dry, it will remain a free-flowing solid for years. Traces of magnesium or calcium chloride in commercial sodium chloride adsorb moisture, making it cake. The trace moisture does not harm the material chemically in any way. 71378 BioUltra 71386 BioUltra for molecular biology, 5 M Solution The products are suitable for different applications like purification, precipitation, crystallisation and other applications which require tight control of elemental content. Trace elemental analyses have been performed for all qualities. The molecular biology quality is also tested for absence of nucleases. The Certificate of Analysis provides lot-specific results. Much of the sodium chloride is mined from salts deposited from evaporation of brine of ancient oceans, or recovered from sea water by solar evaporation. Due to the presence of trace hygroscopic minerals, food-grade salt has a small amount of silicate added to prevent caking; as a result, concentrated solutions of "table salt" are usually slightly cloudy in appearance. 71376 and 71386 do not contain any anti-caking agent. Applications: Sodium chloride is a commonly used chemical found in nature and in all body tissue, and is considered an essential nutrient.
    [Show full text]
  • Self-Diffusion of Sodium, Chloride and Iodide Ions in Methanol-Water Mixture
    Self-Diffusion of Sodium, Chloride and Iodide Ions in Methanol-Water Mixture E. Hawlicka* Institute of Applied Radiation Chemistry, Technical University, Wroblewskiego 15, 93-590, Lodz, Poland Z. Naturforsch. 41 a, 939-943 (1986); received April 25, 1986 The self-diffusion coefficients of Na+, C l- and I- in methanol-water solutions at 35 ± 0.01 °C have been measured in their dependence on the salt molarity in the range 1 • 10-4— 1 • 10-2 mol dm -3. The ionic self-diffusion coefficients in infinitely diluted solutions have been computed. The influence of the solvent composition on the solvation of the ions is discussed. A preferential hydration of Na+, Cl - and I “ ions in water-methanol mixtures has been found. In spite of the great interest in the porperties of aqueous solution with a Nal(Tl) scintillation crystal water-organic solvent electrolyte solutions, data on of the well-type (2 x 2"). the ionic mobilities in such systems are scarce. For the self-diffusion measurements the open-end Usually the ionic mobility is calculated from the capillary method was used. The details of the equivalent conductance and the transference num­ experimental procedure have been described in [6], ber. Ionic transference numbers have been reported The labelling of the sodium ions with 22Na or for water and 17 organic solvents [1], but only for a 24Na and the iodide ions with i25I or 1311, respective­ few water-organic solvents mixtures. ly, did not make any difference in the results. Similar information can be obtained from the ionic self-diffusion coefficients, which have been reported for a few water-organic solvent systems Results [2-5], The aim of the present work was to determine the All self-diffusion experiments have been carried self-diffusion coefficients of sodium, chloride and out at 25.0 ± 0.05 °C.
    [Show full text]
  • Sodium Chlorate Process Liquor De-Chromed SN
    SAFETY DATA SHEET This SDS adheres to the standards and regulatory requirements of the United States and may not meet the regulatory requirements in other countries. 1. Identification Product identifier Sodium Chlorate Process Liquor De-chromed SN Other means of identification De-chromed blend of Crystallizer Feed Liquor and Mother Liquor, NaClO3 Recommended use For internal transfer between ERCO Worldwide sodium chlorate manufacturing facilities for process purposes Recommended restrictions None known Manufacturer/Importer/Supplier/Distributor information Manufacturer Company name ERCO Worldwide Address 335 Carlingview Drive Unit 1 Etobicoke, M9W 5G8 Canada Telephone Information #: (416) 239-7111 (M- F: 8:00 am – 5:00pm EST) Website http://www.ercoworldwide.com E-mail [email protected] Emergency phone number Canada & USA: 1-800-424-9300 (CHEMTREC) Supplier Refer to Manufacturer 2. Hazard(s) Identification Physical hazards Oxidizing liquids Category 2 Health hazards Acute toxicity, oral Category 4 Environmental hazards Not currently regulated by OSHA, refer to Section 12 for additional information. OSHA defined hazards This mixture does not meet the classification criteria according to OSHA HazCom 2012. Label elements Signal word Danger Hazard statement May intensify fire; oxidizer. Harmful if swallowed. Page 1 of 15 Issue Date: 11/18/2020 Sodium Chlorate Process Liquor De-chromed SN Precautionary statement Prevention Keep away from heat, hot surfaces, sparks, open flames and other ignition sources. No smoking. Keep away from clothing and other combustible materials. Wear protective gloves, protective clothing, eye protection, face protection. Response IF ON SKIN: Wash with plenty of water. Take off contaminated clothing and wash it before reuse. In case of fire: Use water to extinguish.
    [Show full text]
  • Salt Effect on Vapor-Liquid Equilibria for Acetone-Water System'
    SALT EFFECT ON VAPOR-LIQUID EQUILIBRIA FOR ACETONE-WATER SYSTEM' E1ZO SADA, TOSHIO OHNO** AND SHIGEHARU KITO Department of Chemical Engineering, Nagoya University, Nagoya, Japan Vapor-liquid equilibrium data of acetone-water system saturated with sodium chloride, potassium chloride, sodium nitrate, and calcium chloride dihydrate are determined under atmospheric pressure. These vapor-liquid equilibrium data are correlated by a method which gives approximately the behavior of salt in the liquid. The standard deviation of correlated results is 2.32%. To carry out this correlation, the vapor pressures of aqueous solutions saturated with salts are also determined. Investigations concerned with the effect of salt the portion between Cx and Hj is brought to the addition on the vapor-liquid equilibria of binary- vapor pressure of sample solution. Whenthe system systems are of theoretical and industrial importance, attains equilibrium (about one hour is needed), and not a little knowledge of vapor-liquid equilibrium the heights of Hl5 H2, and H3 aremeasured, and the data in this field is already available2}. However, vapor pressure is calculated from the following most investigations are limited to presentation of equation. P '---(Hi-H,W+(Hg-H,W experimental data with no attempt to develop a cor- LO -% r relation. Among these, only a few correlations />*" (1) are proposed, for example, by Johnson and Furter5), As the density of sample solution is usually an order and Hashitani and Hirata3). In this paper, the vapor-liquid equilibrium data of magnitude lower than for mercury, it does not decrease the accuracy of measurementto use the for the acetone-water system saturated with each density of pure water at measuring temperature in of four kinds of salt, i.e.
    [Show full text]
  • Production of Hexavalent Chromium for Use in Chlorate Cells
    Europaisches Patentamt J European Patent Office © Publication number: 0 266 128 A2 Office europeen des brevets EUROPEAN PATENT APPLICATION © Application number: 87309335.5 © Int. CIA C25B 1/26 @ Date of filing: 22.10.87 ® Priority: 29.10.86 CA 521737 © Applicant: Tenneco Canada Inc. 2 Gibbs Road © Date of publication of application: Islington OntarioM9B 1R1(CA) 04.05.88 Bulletin 88/18 0 Inventor: Dobosz, Leszek Michal © Designated Contracting States: 68 MacDonald Street CH ES FR LI SE Toronto Ontario M8V 1Y4(CA) © Representative: Hamilton, Raymond et al c/o Albright & Wilson Limited 1 Knightsbridge Green London SW1X 7QD(GB) © Production of hexavalent chromium for use in chlorate cells. © By-product hypochlorite from the electrolytic production of chlorates, notably sodium chlorate, is used to form hexavalent chromium for use in the electrolysis process by oxidation of trivalent chromium compounds by the hypochlorite. The hypochlorite maybe the condensate produced by treatment of the chlorate cell by-product gas stream and/or present in the cell liquor. < 00 CO CO (VI a. UJ Xerox Copy Centre 0 266 128 PRODUCTION OF HEXAVALENT CHROMIUM FOR USE IN CHLORATE CELLLS The present invention relates to the fomation of hexavalent chromium useful in the electrolytic production of aqueous chlorate solutions. An aqueous solution of sodium chlorate and sodium chloride is conventionally produced by the electrolysis of aqueous sodium chloride in diaphragmless electrolytic cells. The extent of electrolysis is 5 controlled to produce an effluent from the cell in which the sodium chlorate and sodium chloride have the desired ratio, usually in the range (expressed as a weight ratio) of about 1 :1 to about 20:1 and preferably in the range of about 2:1 to about 15:1.
    [Show full text]
  • Guidelines for Drinking-Water Quality, Fourth Edition
    12. CHEMICAL FACT SHEETS Assessment date 1993 Principal reference WHO (2003) Chlorine in drinking-water In humans and experimental animals exposed to chlorine in drinking-water, no specific adverse treatment-related effects have been observed. IARC has classified h ypochlorite in Group 3 (not classifiable as to its carcinogenicity to humans). Chlorite and chlorate Chlorite and chlorate are disinfection by-products resulting from the use of chlorine dioxide as a disinfectant and for odour and taste control in water. Chlorine dioxide is also used as a bleaching agent for cellulose, paper pulp, flour and oils. Sodium chlorite and sodium chlorate are both used in the production of chlorine dioxide as well as for other commercial purposes. Chlorine dioxide rapidly decomposes into chlorite, chlorate and chloride ions in treated water, chlorite being the predominant species; this reaction is favoured by alkaline conditions. The major route of environmental ex- posure to chlorine dioxide, sodium chlorite and sodium chlorate is through drinking- water. Chlorate is also formed in sodium hypochlorite solution that is stored for long periods, particularly at high ambient temperatures. Provisional guideline values Chlorite: 0.7 mg/l (700 µg/l) Chlorate: 0.7 mg/l (700 µg/l) The guideline values for chlorite and chlorate are designated as provisional because use of chlorine dioxide as a disinfectant may result in the chlorite and chlorate guideline values being exceeded, and difficulties in meeting the guideline value must never be a reason for compromising adequate disinfection. Occurrence Levels of chlorite in water reported in one study ranged from 3.2 to 7.0 mg/l; however, the combined levels will not exceed the dose of chlorine dioxide applied.
    [Show full text]
  • Action of Ammonium Chloride Upon Silicates
    Bulletin No. 207 Series E, Chemistry and Physics, 36 DEPARTMENT OF TEiE INTERIOR UNITED STATES GEOLOGICAL SURVEY CHARLES D. WALCOTT, DIRECTOR THE ACTION OF AMMONIUM CHLORIDE UPON SILICATES BY AND GKKOKG-IE Srj::ir, WASHINGTON GOVERNMEN.T PllINTING OFFICE 1902 CONTENTS. Page. Introductory statement......--..-..---.--.------.--.-..--.-.-----------. 7 Analcite-.....-.-.-.--.-.....-.--.'--------....--.-.--..._.-.---.-...---.--. 8 Leucite .....................'.................-....................^-..... 16 The constitution of analcite and leucite.........-..--.-..--...--.---------. 17 Pollucite---. ............................................................ 21 Natrolite--------------------------..-..-----------------.------ --------- 22 Scolecite ................,.:............-.....-.................--.--.... 24 Prehnite .....--.-............--.------------------------------ --------- 25 The trisilicic acids-.--.-.--..---..........-._-----...-.........-...----.- 26 Stilbite.............-..................-....-.-.-----...--.---.......... 29 Henlandite .......... .......................---.-..-.-..-...-----.--..--.. 81 Chabazite............................................................... 32 Thoinsonite...-.-.-..-...._.................---...-.-.-.----..-----..--.. 34 Lanmontite -.-.------.-..-------------.-..-.-..-.-------.-.-----........ 35 Pectolite ......:......... ......................................'.......;.., 36 Wollastonite ....'............................ ................:........... 39 Apophyllite. _.--._..._-....__.....:......___-------------....----..-...._
    [Show full text]
  • Dangers of Unspent Aircraft Oxygen Generators
    Safety Advisory Dangers of Unspent Aircraft Oxygen Generators U.S. Chemical Safety and Hazard Investigation Board No. 2007-I-NC-01-SA | June 2007 Key Message This Safety Advisory is issued to alert aircraft maintenance and hazardous waste facility personnel to the hazards associated with the transportation and storage of expired, unspent aircraft chemical oxygen generators. Aircraft oxygen generators are dangerous devices that, if mishandled, can cause fires, property damage, and personal injury. Aircraft oxygen generators that have exceeded their service life should be expended before shipping by any transport mode. Introduction On October 5, 2006, at about 10 pm, a fire occurred at the EQ Industrial Services (EQ) hazardous waste treatment, storage, and disposal facility in Apex, North Carolina. The fire resulted in the evacuation of thousands of Apex residents and the complete destruction of the hazardous waste building at EQ’s Apex facility. The U.S. Chemical Safety and Hazard Investigation Board (CSB) investigation concluded that aircraft oxygen generators most likely contributed to the rapid spread of the fire to other areas in the EQ facility. The CSB issues this Safety Advisory to focus attention on the need for aircraft maintenance facilities to expend chemical oxygen generators that have exceeded their service life, and for hazardous waste facility operators and shippers to exercise due care when handling unspent chemical oxygen generators. Incident Description At about 10 pm on October 5, 2006, a citizen driving past the EQ facility in Apex, North Carolina, called 911 when he saw a plume of smoke and smelled a strong chlorine odor coming from the facility.
    [Show full text]
  • CDG Solution 3000TM Safety Data Sheet
    Emergency Telephone Number: 800-424-9300 24 hours/day, 7 days/week Emergency Telephone Number: 800-424-9300 24 hours, 7 days/week CDG Solution 3000TM Safety Data Sheet Section 1 – Chemical Product and Company Identification Product Identifier: Chlorine Dioxide 0.3% Aqueous Solution SDS No. CD-004 Other Means of Identification: Chlorine Oxide Solution Chlorine Peroxide Solution Chlorine (IV) Oxide Solution Chloroperoxyl Solution Recommended Use: Biocide Company: CDG Environmental, LLC 301 Broadway, Suite 420 Bethlehem, PA 18015 888-610-2562 484-821-0780 Emergency Phone Number: 800-424-9300 SDS # CD-004 CDG Solution 3000 Page 1 of 12 Emergency Telephone Number: 800-424-9300 24 hours, 7 days/week Section 2 – Hazards Identification GHS Classification: Skin Irritation: Category 2 Eye Irritation: Category 2B Acute Toxicity – Inhalation: Category 4 Signal Word: Warning Pictogram: Hazard Statements: Causes skin irritation Causes eye irritation Harmful in inhaled Precautionary Wash exposed areas thoroughly after handling. Statements: Wear protective gloves. Avoid breathing fume/gas/mist/vapors/spray. Use only outdoors or in a well-ventilated area. If on skin: Wash with plenty of water. If skin irritation occurs: Get medical attention. If in eyes: Rinse cautiously with water for several minutes. Remove contact lenses, if present and easy to do. Continue rinsing. If eye irritation persists: Get medical attention. If inhaled: Remove person to fresh air and keep comfortable for breathing. Call a doctor if you feel unwell. Specific treatment (see First
    [Show full text]
  • WFOOT General Assembly
    Headquarters: World Via de Pratello, 8 Federation of Bologne (Italy) Ozone WEB: www.wfoot.org Therapy Email: [email protected] Guangzhou, June 12th, 2017 Some medical ozone associations are promoting the use of ozonated saline solution as a method classifiable as Ozone Therapy. This is documented also by the “Second edition of Madrid Declaration on Ozone Therapy” edited by ISCO3 (International Scientific Committee on Ozone Therapy) that included this technique in their training courses. The World Federation of Ozone Therapy – WFOT, very worried about this fact, has made a deep study through its scientific advisory committee that concludes: - Ozonated saline following the recommendation from the above related document, introduces in the body a very low amount of ozone dissolved in certain quantity of saline solution, compared with systemic indirect endovenous ozone therapy (SIEVOT), also known as major autohemotherapy. This small quantity doubtfully would induce any significant biological response, through the generation of ROS and LOPs. We must say that it is not an Ozone Therapy technique based on the ozone chemistry well documented by the German, Cuban and Italian schools, in which ozone is the only molecule that interacts with the body fluids. - The ozonation of saline solution (0,9% NaCl) induces the generation of dangerous oxidized chlorine derivatives, not present in other techniques of medical ozone administration. Ozonated saline solutions showed to induce mutagenicity and toxicity in clinical reports. Ozonated saline solutions lacks of any kind of approved preclinical studies to support its safety, as ozone has, which were developed in Cuba and following the recommendations of the World Health Organization – WHO.
    [Show full text]
  • Potassium Chloride 1311
    ASHP INJECTABLE DRUG INFORMATION Potassium CHLORIDE 1311 Potassium Chloride AHFS 40:12 Products chloride injection thoroughly with the infusion solution before administration. The usual maximum concentration is 40 mEq/L. Potassium chloride is available as concentrated solutions of 1.5 and Extravasation should be avoided.1(5/06) 4 2 mEq/mL in 10-, 20-, 30-, and 40-mEq sizes in water for injection in ampuls, vials, and syringes. It is also available in a 30-mL (60-mEq) Great care is required when adding potassium chloride to multiple-dose vial containing methylparaben 0.05% and propyl- infusion solutions, whether in flexible plastic containers or paraben 0.005% as preservatives and 250-mL pharmacy bulk pack- in rigid bottles. Adding potassium chloride to running infu- ages. The pH may have been adjusted with hydrochloric acid and sion solutions hanging in the use position, especially in flex- if necessary potassium hydroxide during manufacture. The concen- ible containers, has resulted in the pooling of potassium chlo- trated solutions must be diluted for use.1(5/06) ride and a resultant high-concentration bolus of the drug being administered to patients, with serious and even fatal conse- Potassium chloride is also available premixed in infusion 4 quences. Attempts to mix adequately the potassium chloride solutions in concentrations of 10, 20, 30, and 40 mEq/L. in flexible containers by squeezing the container in the hanging pH position were unsuccessful. It is recommended that drugs be The pH is usually near 4.6 with a range from 4 to 8.1(5/06) 17 admixed with solutions in flexible containers when positioned with the injection arm of the container uppermost.
    [Show full text]
  • Battle of the Acids Weak Acids and Bases SCIENTIFIC
    Battle of the Acids Weak Acids and Bases SCIENTIFIC Introduction Not all acids are created equal. This demonstration compares the “frothing and foaming” activity of different acids with calcium carbonate and examines their behavior in the presence of their conjugate bases to distinguish strong versus weak acids. The use of a “rainbow acid” universal indicator produces a rainbow spectrum of color changes as the mixtures react. Concepts • Strong acid • Weak acid • Conjugate base • pH Materials (for each demonstration) Acetic acid, CH3COOH, 1 M, 400 mL Water, distilled or deionized Calcium carbonate, CaCO3, 40 g Demonstration tray, large Hydrochloric acid, HCl, 1 M, 400 mL Graduated cylinder, 250-mL “Rainbow acid” universal indicator, 5 mL Hydrometer cylinders, 600-mL, 4 (includes accompanying color chart) Pipet, Beral-type Sodium acetate, NaCH3CO2, 16 g Weighing dishes or small beakers, 6 Sodium chloride, NaCl, 12 g Safety Precautions Hydrochloric acid and acetic acid solutions are toxic and corrosive. Avoid contact with skin and eyes. “Rainbow-acid” universal indicator solution is an alcohol-based solution and is flammable. Avoid contact with flames or other ignition sources. Wear chemical splash goggles, chemical-resistant gloves, and a chemical-resistant apron. Please review current Material Safety Data Sheets for additional safety, handling, and disposal information. Preparation To save time in the presentation, pre-measure the amounts of solids needed for the demonstration. Weigh out 12 g of sodium chloride, 16 g of sodium acetate, and 4 × 10-g samples of calcium carbonate in separate, labeled weighing dishes or small beakers. Procedure 1. Obtain 4 large hydrometer cylinders or tall-form beakers and place them on a large demonstration tray.
    [Show full text]