Product Stewardship Summary Sodium Hydroxide
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Inventory Size (Ml Or G) 103220 Dimethyl Sulfate 77-78-1 500 Ml
Inventory Bottle Size Number Name CAS# (mL or g) Room # Location 103220 Dimethyl sulfate 77-78-1 500 ml 3222 A-1 Benzonitrile 100-47-0 100ml 3222 A-1 Tin(IV)chloride 1.0 M in DCM 7676-78-8 100ml 3222 A-1 103713 Acetic Anhydride 108-24-7 500ml 3222 A2 103714 Sulfuric acid, fuming 9014-95-7 500g 3222 A2 103723 Phosphorus tribromide 7789-60-8 100g 3222 A2 103724 Trifluoroacetic acid 76-05-1 100g 3222 A2 101342 Succinyl chloride 543-20-4 3222 A2 100069 Chloroacetyl chloride 79-04-9 100ml 3222 A2 10002 Chloroacetyl chloride 79-04-9 100ml 3222 A2 101134 Acetyl chloride 75-36-5 500g 3222 A2 103721 Ethyl chlorooxoacetate 4755-77-5 100g 3222 A2 100423 Titanium(IV) chloride solution 7550-45-0 100ml 3222 A2 103877 Acetic Anhydride 108-24-7 1L 3222 A3 103874 Polyphosphoric acid 8017-16-1 1kg 3222 A3 103695 Chlorosulfonic acid 7790-94-5 100g 3222 A3 103694 Chlorosulfonic acid 7790-94-5 100g 3222 A3 103880 Methanesulfonic acid 75-75-2 500ml 3222 A3 103883 Oxalyl chloride 79-37-8 100ml 3222 A3 103889 Thiodiglycolic acid 123-93-3 500g 3222 A3 103888 Tetrafluoroboric acid 50% 16872-11-0 1L 3222 A3 103886 Tetrafluoroboric acid 50% 16872-11-0 1L 3222 A3 102969 sulfuric acid 7664-93-9 500 mL 2428 A7 102970 hydrochloric acid (37%) 7647-01-0 500 mL 2428 A7 102971 hydrochloric acid (37%) 7647-01-0 500 mL 2428 A7 102973 formic acid (88%) 64-18-6 500 mL 2428 A7 102974 hydrofloric acid (49%) 7664-39-3 500 mL 2428 A7 103320 Ammonium Hydroxide conc. -
(Oxy)Hydroxide Electrocatalysts for Water Oxidation Bryan R
www.acsami.org Research Article Effect of Selenium Content on Nickel Sulfoselenide-Derived Nickel (Oxy)hydroxide Electrocatalysts for Water Oxidation Bryan R. Wygant, Anna H. Poterek, James N. Burrow, and C. Buddie Mullins* Cite This: ACS Appl. Mater. Interfaces 2020, 12, 20366−20375 Read Online ACCESS Metrics & More Article Recommendations *sı Supporting Information ABSTRACT: An efficient and inexpensive electrocatalyst for the oxygen evolution reaction (OER) must be found in order to improve the viability of hydrogen fuel production via water electrolysis. Recent work has indicated that nickel chalcogenide materials show promise as electrocatalysts for this reaction and that their performance can be further enhanced with the generation of ternary, bimetallic chalcogenides (i.e., Ni1−aMaX2); however, relatively few studies have investigated ternary chalcogenides created through the addition of a second chalcogen (i.e., NiX2−aYa). To address this, we fi studied a series of Se-modi ed Ni3S2 composites for use as OER electrocatalysts in alkaline solution. We found that the addition of Se results in the creation of Ni3S2/NiSe composites composed of cross-doped metal chalcogenides and show that the addition of 10% Se reduces the overpotential required to reach a current density of 10 mA/cm2 by 40 mV versus a pure nickel sulfide material. Chemical analysis of the composites’ surfaces shows a reduction in the amount of nickel oxide species with Se incorporation, which is supported by transmission electron microscopy; this reduction is correlated with a decrease in the OER overpotentials measured for these samples. Together, our results suggest that the incorporation of Se into Ni3S2 creates a more conductive material with a less-oxidized surface that is more electrocatalytically active and resistant to further oxidation. -
The Influence of Sodium Hydroxide Concentration on the Phase, Morphology and Agglomeration of Cobalt Oxide Nanoparticles and Application As Fenton Catalyst
Digest Journal of Nanomaterials and Biostructures Vol.14, No.4, October-December 2019, p. 1131-1137 THE INFLUENCE OF SODIUM HYDROXIDE CONCENTRATION ON THE PHASE, MORPHOLOGY AND AGGLOMERATION OF COBALT OXIDE NANOPARTICLES AND APPLICATION AS FENTON CATALYST E. L. VILJOENa,*, P. M. THABEDEa, M. J. MOLOTOa, K. P. MUBIAYIb, B. W. DIKIZAa aDepartment of Chemistry, Vaal University of Technology Private, Bag X021, Vanderbijlpark 1900, South Africa bSchool of Chemistry, University of the Witwatersrand, 1 Jan Smuts Avenue, Braamfontein Johannesburg 2000, South Africa The concentration of NaOH was varied from 0.2 M to 0.7 M during the preparation of the cobalt oxide/cobalt oxide hydroxide nanoparticles by precipitation and air oxidation. Cubic shaped and less well defined Co3O4 nanoparticles formed at 0.2 M NaOH. An increase in the NaOH concentration increased the number of well-defined cubic shaped nanoparticles. Agglomerated CoO(OH) particles with different shapes formed at the highest NaOH concentration. The cubic shaped Co3O4 nanoparticles were subsequently used as catalyst for the Fenton degradation of methylene blue and it was found that the least agglomerated nanoparticles were the most catalytically active. (Received June 25, 2019; Accepted December 6, 2019) Keywords: Cobalt oxide, Nanoparticles, Precipitation, pH, Fenton reaction 1. Introduction Controlling the size and the shape of nanoparticles using simple, inexpensive precipitation methods without sophisticated capping molecules, remains a challenge. Literature has indicated that the concentration of the base (pH) is an important parameter to control the size, shape and phase of metal oxide nanoparticles. Obodo et al.[1] used chemical bath deposition at atmospheric pressure and 70 °C to precipitate Co3O4 crystallites on a glass substrate and they showed that the crystallite sizes were larger at a higher pH of 12 in comparison to when a pH of 10 was used. -
SODIUM HYDROXIDE @Lye, Limewater, Lyewater@
Oregon Department of Human Services Office of Environmental Public Health (503) 731-4030 Emergency 800 NE Oregon Street #604 (971) 673-0405 Portland, OR 97232-2162 (971) 673-0457 FAX (971) 673-0372 TTY-Nonvoice TECHNICAL BULLETIN HEALTH EFFECTS INFORMATION Prepared by: ENVIRONMENTAL TOXICOLOGY SECTION OCTOBER, 1998 SODIUM HYDROXIDE @Lye, limewater, lyewater@ For More Information Contact: Environmental Toxicology Section (971) 673-0440 Drinking Water Section (971) 673-0405 Technical Bulletin - Health Effects Information Sodium Hydroxide Page 2 SYNONYMS: Caustic soda, sodium hydrate, soda lye, lye, natrium hydroxide CHEMICAL AND PHYSICAL PROPERTIES: - Molecular Formula: NaOH - White solid, crystals or powder, will draw moisture from the air and become damp on exposure - Odorless, flat, sweetish flavor - Pure solid material or concentrated solutions are extremely caustic, immediately injurious to skin, eyes and respiratory system WHERE DOES IT COME FROM? Sodium hydroxide is extracted from seawater or other brines by industrial processes. WHAT ARE THE PRINCIPLE USES OF SODIUM HYDROXIDE? Sodium hydroxide is an ingredient of many household products used for cleaning and disinfecting, in many cosmetic products such as mouth washes, tooth paste and lotions, and in food and beverage production for adjustment of pH and as a stabilizer. In its concentrated form (lye) it is used as a household drain cleaner because of its ability to dissolve organic solids. It is also used in many industries including glassmaking, paper manufacturing and mining. It is used widely in medications, for regulation of acidity. Sodium hydroxide may be used to counteract acidity in swimming pool water, or in drinking water. IS SODIUM HYDROXIDE NATURALLY PRESENT IN DRINKING WATER? Yes, because sodium and hydroxide ions are common natural mineral substances, they are present in many natural soils, in groundwater, in plants and in animal tissues. -
This Dissertation Has Been 62—2136 M Icrofilm Ed Exactly As Received GIELISSE, Peter Jacob M., 1934- INVESTIGATION of PHASE EQ
This dissertation has been 62—2136 microfilmed exactly as received GIELISSE, Peter Jacob M., 1934- INVESTIGATION OF PHASE EQUILIBRIA IN THE SYSTEM ALUMINA-BORON OXIDE-SILICA. The Ohio State University, Ph.D., 1961 M ineralogy University Microfilms, Inc., Ann Arbor, Michigan INVESTIGATION OP PHASE EQUILIBRIA IN THE SYSTEM ALUMINA-BORON OXIDE-SILICA DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of the Ohio State University By Peter Jacob M. Gielisse, M. S. The Ohio State University 1961 Approved by Adviser Department of Mineralogy ACKNOWLEDGMENTS The writer wishes to extend his sincere thanks to the many people without whose help the preparation of this dissertation would have been impossible. He is indebted in particular to his adviser, Dr. Wilfrid R. Foster, for his invaluable aid, advice and many kindnesses; to the other members of the faculty of the Department of Mineral ogy, Drs. Ernest G. Ehlers, Henry E. Wenden, and Rodney T Tettenhorst; and to his friend and colleague, Thomas J. Rockett. Acknowledgment is also made for financial support re ceived under contract No. AF 33(616)-3189, sponsored by Aeronautical Research Laboratories, Air Force Research Division, Wright Patterson Air Force Base, Ohio; as well as for aid received through a Mershon National Graduate Fellowship awarded to the writer by the Mershon Committee on Education in National Security for 1960-‘61'. It goes without saying that he is also most grate ful to his wife, Anna, for her excellent help and encour agement over the years. TABLE OF CONTENTS Page INTRODUCTION ...................................... -
Carbon Dioxide Capture from Atmospheric Air Using Sodium
Environ. Sci. Technol. 2008, 42, 2728–2735 Carbon Dioxide Capture from Nearly all current research on CCS focuses on capturing CO2 from large, stationary sources such as power plants. Atmospheric Air Using Sodium Such plans usually entail separating CO2 from flue gas, compressing it, and transporting it via pipeline to be Hydroxide Spray sequestered underground. In contrast, the system described in this paper captures CO2 directly from ambient air (“air § capture”). This strategy will be expensive compared to capture JOSHUAH K. STOLAROFF, from point sources, but may nevertheless act as an important DAVID W. KEITH,‡ AND complement, since CO emissions from any sector can be GREGORY V. LOWRY*,† 2 captured, including emissions from diffuse sources such as Chemical and Petroleum Engineering, University of Calgary, aircraft or automobiles, where on-board carbon capture is and Departments of Civil and Environmental Engineering very difficult and the cost of alternatives is high. Additionally, and Engineering and Public Policy, Carnegie Mellon in a future economy with low carbon emissions, air capture University, Pittsburgh, Pennsylvania 15213 might be deployed to generate negative net emissions (1). This ability to reduce atmospheric CO2 concentrations faster Received October 15, 2007. Revised manuscript received than natural cycles allow would be particularly desirable in February 05, 2008. Accepted February 06, 2008. scenarios where climate sensitivity is on the high end of what is expected, resulting in unacceptable shifts in land usability and stress to ecosystems. In contrast to conventional carbon capture systems for Previous research has shown that air capture is theoreti- cally feasible in terms of thermodynamic energy require- power plants and other large point sources, the system described ments, land use (2), and local atmospheric transport of CO2 in this paper captures CO2 directly from ambient air. -
Sodium Hydrosulfide
SAFETY DATA SHEET 1. Identification Product identifier Sodium Hydrosulfide Solution Other means of identification Product number GENLP-TDC-001-CAN Recommended use Product is a unique alkaline material, playing a vital role in many industrial processes. Recommended restrictions Use in accordance with supplier's recommendations. Manufacturer/Importer/Supplier/Distributor information Importer TDC Energy Canada, LTD. Address 1916 Farmerville Hwy Ruston, LA 71270 Telephone Customer Service (800) 422-6274 Email [email protected] CHEMTREC: 800-424-9300 (Domestic – North America) CHEMTREC: +1-703-527-3887 (International) 2. Hazard identification Physical hazards Corrosive to metals Category 1 Health hazards Acute toxicity, oral Category 3 Skin corrosion/irritation Category 1B Serious eye damage/eye irritation Category 1 Environmental hazards Hazardous to the aquatic environment, acute Category 1 hazard Label elements Signal word Danger Hazard statement May be corrosive to metals. Toxic if swallowed. Causes severe skin burns and eye damage. Very toxic to aquatic life. Precautionary statement Prevention Keep only in original container. Do not breathe mist or vapour. Wash thoroughly after handling. Do not eat, drink or smoke when using this product. Avoid release to the environment. Wear protective gloves/protective clothing/eye protection/face protection. Response If swallowed: Immediately call a poison centre/doctor. Rinse mouth. Do NOT induce vomiting. If on skin (or hair): Take off immediately all contaminated clothing. Rinse skin with water/shower. Wash contaminated clothing before reuse. If inhaled: Remove person to fresh air and keep comfortable for breathing. If in eyes: Rinse cautiously with water for several minutes. Remove contact lenses, if present and easy to do. -
Nahs Technical Guide
TECHNICAL GUIDE FOR SOLUTIONS OF SODIUM HYDROSULFIDE TECHNICAL GUIDE FOR SOLUTIONS OF SODIUM HYDROSULFIDE TABLE OF CONTENTS TOPIC PAGE Overview 1 Health Hazards and First Aid 2 Flammability and Fire Response / Storage 3 Handling (PPE) 4 Equipment Transfers/Recommendations 5 Shipping 13 Releases 14 APPENDIX This Page Intentionally left Blank Appendix A H2S Monitors Appendix B Hydrogen Sulfide Toxicity Chart Appendix C Density, Boiling and Freezing Points of Appendix D Sodium Hydrosulfide Viscosity of Typical 45% Sodium Appendix E Hydrosulfide Solution Sodium Hydrosulfide Site Assessment Appendix F Checklist TECHNICAL GUIDE FOR SOLUTIONS OF SODIUM HYDROSULFIDE Overview Sodium Hydrosulfide, chemical formula NaHS, is a highly alkaline salt solution with a pH of 11.5 to 12.5. The solution is typically yellow to dark green and has a rotten-egg odor due to the Hydrogen Sulfide (H2S) content. The product strength ranges from 20% to 45% by weight and weighs 9 to 11 pounds per gallon (specific gravity from 1.13 to 1.30 g/cm3). Solutions of NaHS are considered stable in normal transportation. The vapor space over NaHS solutions contains highly toxic Hydrogen Sulfide gas. The Hydrogen Sulfide gas is colorless and it is heavier than air. It will remain close to the ground and collect in low lying areas. The amount of Hydrogen Sulfide gas evolved from NaHS solutions is noticeably increased when the pH of the solution is below the pH of 10.2. This happens when the solution comes into contact with acidic materials or other materials that have a pH lower than 10.2. Dilution of the material will also create a minimal amount of Hydrogen Sulfide gas due to the lower pH of water coming in contact with the solution. -
Exposure to Potassium Hydroxide Can Cause Headache, Eye Contact Dizziness, Nausea and Vomiting
Right to Know Hazardous Substance Fact Sheet Common Name: POTASSIUM HYDROXIDE Synonyms: Caustic Potash; Lye; Potassium Hydrate CAS Number: 1310-58-3 Chemical Name: Potassium Hydroxide (KOH) RTK Substance Number: 1571 Date: May 2001 Revision: January 2010 DOT Number: UN 1813 Description and Use EMERGENCY RESPONDERS >>>> SEE LAST PAGE Potassium Hydroxide is an odorless, white or slightly yellow, Hazard Summary flakey or lumpy solid which is often in a water solution. It is Hazard Rating NJDOH NFPA used in making soap, as an electrolyte in alkaline batteries and HEALTH - 3 in electroplating, lithography, and paint and varnish removers. FLAMMABILITY - 0 Liquid drain cleaners contain 25 to 36% of Potassium REACTIVITY - 1 Hydroxide. CORROSIVE POISONOUS GASES ARE PRODUCED IN FIRE DOES NOT BURN Reasons for Citation Hazard Rating Key: 0=minimal; 1=slight; 2=moderate; 3=serious; f Potassium Hydroxide is on the Right to Know Hazardous 4=severe Substance List because it is cited by ACGIH, DOT, NIOSH, NFPA and EPA. f Potassium Hydroxide can affect you when inhaled and by f This chemical is on the Special Health Hazard Substance passing through the skin. List. f Potassium Hydroxide is a HIGHLY CORROSIVE CHEMICAL and contact can severely irritate and burn the skin and eyes leading to eye damage. f Contact can irritate the nose and throat. f Inhaling Potassium Hydroxide can irritate the lungs. SEE GLOSSARY ON PAGE 5. Higher exposures may cause a build-up of fluid in the lungs (pulmonary edema), a medical emergency. FIRST AID f Exposure to Potassium Hydroxide can cause headache, Eye Contact dizziness, nausea and vomiting. -
Sodium Hydrosulfide (Nahs) Recommended Procedures for Truck Unloading
Sodium Hydrosulfide (NaHS) Recommended Procedures for Truck Unloading TDC, LLC 1916 Farmerville Hwy. Ruston LA 71270 The following presentation was designed to provide specific information on unloading trucks containing Sodium Hydrosulfide (NaHS). This presentation has been developed as a guide only. THINK SAFETY AT ALL TIMES! STAY ON TOP OF SAFE HANDLING PROCEDURES Safety is Everyone’s Business Training Requirements Personnel handling hazardous chemicals should be trained in accordance with the applicable federal and state requirements These training requirements include, but may not be limited to: • Hazard Communications - 29 CFR 1910.1200 • Personal Protective Equipment - 29 CFR 1910.132 • Respiratory Protection - 29 CFR 1910.134 • Occupational Noise Exposure - 29 CFR 1910.95 • Hazmat - 49 CFR 172.700 Shipping Requirements Sodium Hydrosulfide (NaHS) is classified as a corrosive and toxic liquid. The Proper Shipping Description is: UN2922 Corrosive liquids, toxic, n.o.s., 8(6.1), PG II (sodium hydrosulfide solution) Bulk shipments are placarded “Corrosive”. KNOW THE PRODUCT! Read the MSDS MSDS Review ¾ Sodium Hydrosulfide (NaHS) is very alkaline (pH 11.5- 12.5) and very corrosive to the skin. ¾ Solution is typically yellow to dark green with a strong hydrogen sulfide (rotten egg) odor. ¾ Solutions are 20% to 45% strength and weigh 9.6 – 10.9 ppg. ¾ The vapor space over NaHS solutions contains highly toxic hydrogen sulfide (H2S). This gas is colorless and heavier than air. The level of H2S above the solution is increased by solution contact with acidic materials, heating the solution and dilution, which lowers the pH of the solution. NaHS is manufactured by reacting Hydrogen Sulfide Gas (H2S) with Sodium Hydroxide (Caustic Soda) (NaOH). -
United States Patent Office Patented Nov
3,352,642 United States Patent Office Patented Nov. 14, 1967 2 stabilized during storage for long periods of time with 3,352,642 out degradation of its oxidizing properties. STABLZATION OF OZONE Lawrence J. Heidt, Arlington, and Vincent R. Landi, In accordance with these and other objects, the present rookine, Mass., assignors to Massachusetts in invention involves the stabilization of ozone through the stitute of Technology, Cambridge, Mass., a corpo use of base, and in particular, sodium hydroxide and ration of Massachusetts other sources of hydroxyl-ion. This is a wholly new and No Drawing. Fied June 29, 1964, Ser. No. 378,990 Surprising approach to the problem of stabilizing ozone. 15 Clains. (Cl. 23-222) In fact, it has heretofore been generally believed that sodium hydroxide would have the opposite effect upon This invention relates to a method for the stabilization O oZone. For example, the Encyclopedia of Chemical Tech of ozone and in particular to a method whereby ozone nology, vol. 9, p. 735, reports that the ozone decomposi can be stored and transported with a much slower rate tion reaction is greatly accelerated by increasing the of decomposition than was heretofore thought possible. hydroxyl-ion concentration. Other references are made Ozone (O3) is an unstable blue gas which is formed in the same volume and article on ozone to the supposedly photochemically in nature in the earth's stratosphere but 5 detrimental effect of sodium hydroxide on the stability which exists only in great dilution with air or oxygen at of ozone. It is also reported in the article that the de ground levels. -
Implementation of Mathematical Equation for Calculating Alumina Extraction from Bauxite Tailing Digestion
International Conference on Applied Mathematics, Simulation and Modelling (AMSM 2016) Implementation of Mathematical Equation for Calculating Alumina Extraction from Bauxite Tailing Digestion Saini Hu Mineral and Coal Technology Research and Development CenterJalan Jenderal Sudirman No. 623 Bandung-Indonesia Abstract—Research on bauxite digesting using pressurized Washing is one of methods that are usually used to upgrade reactor at a capacity of 86,66 kg of feed/batch had been alumina content of bauxite by separating primary mineral conducted. Bauxite with -150 mesh of particle size is reacted impurities like clay, silica, iron, and titanium that are with 42,15 kg of caustic soda with concentration of 433,49 g/l at attached on the surface of crude bauxite [3]. Trommol screen the temperature of 140oC for 1.0 to 2.5 hours using steam as is common equipment to wash and screen coarse bauxite heating media. Lime added are varied from 3 to 9 kg. After from very fine particles size by supporting pressurized spray processing for a certain period of time, slurry product is water. By using water spraying and screening, smaller transferred into a Mixer. To evaluate percent yield of Al2O3 particles attached on the surface of crude bauxite is easy to extraction from this process, measuring the height of slurry separate. Therefore, there are two products of washing, level in the Mixer, densities of the slurry, filtrate, and solid namely washed bauxite having +2mm of particle size with residue are conducted. Head sample of bauxite, filtrate and high content of alumina and tailing having –2mm of particle residue are analysed by using wet method to get Al2O3 content size with lower content of alumina.