Origins of Rotational Barriers in Hydrogen Peroxide and Hydrazine
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Supporting Information For
Electronic Supplementary Material (ESI) for Chemical Communications This journal is © The Royal Society of Chemistry 2011 Supporting Information for: 2- Quadruple-CO3 Bridged Octanuclear Dysprosium(III) Compound Showing Single-Molecule Magnet Behaviour Experimental Section Synthetic procedures All chemicals were of reagent grade and were used without any further purification. Synthesis of pyrazine-2-carbohydrazide The pyrazine-2-carboxylic acid methyl ester was prepared by a literature procedure described elsewhere. A mixture of pyrazine-2-carboxylic acid methyl ester (1.38 g, 10 mmol) and hydrazine hydrate (85%, 15 ml) in methanol (20 ml) was refluxed overnight, at a temperature somewhat below 80°C. The resulting pale-yellow solution set aside 12 hrs. During this period, a colorless product, i.e. pyrazine-2-carbohydrazide, precipitated from the reaction mixture as a crystalline solid (yield = 0.84 g, 61%). Synthesis of (E)-N'-(2-hyborxy-3-methoxybenzylidene)pyrazine-2-carbohydrazide Pyrazine-2-carbohydrazide (2 mmol, 0.276 g) was suspended together with o-vanillin (2 mmol, 0.304 g) in methanol (20 ml), and the resulting mixture was stirred at the room temperature overnight. The pale yellow solid was collected by filtration (yield = 0.56 g, 83%). Elemental analysis (%) calcd for C13H12N4O3: C, 57.35, H, 4.44, N, 20.58: found C, 57.64, H, 4.59, N, 20.39. IR (KBr, cm-1): 3415(w), 3258(w), 1677(vs), 1610(s), 1579(m). 1530(s), 1464(s), 1363(m), 1255(vs), 1153(s), 1051(w), 1021(s), 986(w), 906(m), 938(w), 736(s), 596(m), 498(w). Synthesis of the complex 1 The solution of DyCl3⋅6H2O (56.5 mg, 0.15 mmol) and the H2L (40.5 mg, 0.15 mmol) in 15 ml CH3OH/CH2Cl2 (1:2 v/v) was stirred with triethylamine (0.4 mmol) for 6h. -
Hydrous Hydrazine Decomposition for Hydrogen Production Using of Ir/Ceo2: Effect of Reaction Parameters on the Activity
nanomaterials Article Hydrous Hydrazine Decomposition for Hydrogen Production Using of Ir/CeO2: Effect of Reaction Parameters on the Activity Davide Motta 1, Ilaria Barlocco 2 , Silvio Bellomi 2, Alberto Villa 2,* and Nikolaos Dimitratos 3,* 1 Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Cardiff CF10 3AT, UK; [email protected] 2 Dipartimento di Chimica, Università degli Studi di Milano, 20133 Milano, Italy; [email protected] (I.B.); [email protected] (S.B.) 3 Dipartimento di Chimica Industriale e dei Materiali, Alma Mater Studiorum Università di Bologna, 40136 Bologna, Italy * Correspondence: [email protected] (A.V.); [email protected] (N.D.) Abstract: In the present work, an Ir/CeO2 catalyst was prepared by the deposition–precipitation method and tested in the decomposition of hydrazine hydrate to hydrogen, which is very important in the development of hydrogen storage materials for fuel cells. The catalyst was characterised using different techniques, i.e., X-ray photoelectron spectroscopy (XPS), transmission electron microscopy (TEM), scanning electron microscopy (SEM) equipped with X-ray detector (EDX) and inductively coupled plasma—mass spectroscopy (ICP-MS). The effect of reaction conditions on the activity and selectivity of the material was evaluated in this study, modifying parameters such as temperature, the mass of the catalyst, stirring speed and concentration of base in order to find the optimal conditions of reaction, which allow performing the test in a kinetically limited regime. Citation: Motta, D.; Barlocco, I.; Bellomi, S.; Villa, A.; Dimitratos, N. Keywords: iridium; cerium oxide; hydrous hydrazine; hydrogen production Hydrous Hydrazine Decomposition for Hydrogen Production Using of Ir/CeO2: Effect of Reaction Parameters on the Activity. -
Introduction to the Preparation and Properties of Hydiogen Peroxide
CHAPTER 1 Introduction to the Preparation and Properties of Hydiogen Peroxide 1 Introduction The following chapter will discuss the preparation of hydrogen peroxide, historically, the present day and future vistas for its in situ preparation. A brief introduction to the physical properties of hydrogen peroxide will also be made for the sake of completeness. Finally, the chapter will conclude with a practical approach to the safe handling of peroxygen species, destruction of residual peroxygens, and the toxicological and occupational health considerations required when handling hydrogen peroxide. 2 Industrial Manufacture of Hydrogen Peroxide The industrial manufacture of hydrogen peroxide can be traced back to its isolation in 18 18 by L. J. Thenard. Thenard reacted barium peroxide with nitric acid to produce a low concentration of aqueous hydrogen peroxide; the process can, however, be significantly improved by the use of hydrochloric acid. The hydrogen peroxide is formed in conjunction with barium chloride, both of which are soluble in water. The barium chloride is subsequently removed by precipitation with sulfuric acid (Figure 1.1). Hence, Thenard gave birth to the first commercial manufacture of aqueous hydrogen peroxide, although it took over sixty years before Thenard’s wet chemical process was employed in a commercial capacity.2 The industrial production of hydrogen peroxide using the above route was still operating until the middle of the 20th century. At the turn of the 19th century, approximately 10000 metric tonnes per annurn of barium peroxide were converted to about 2000 metric tonnes of hydrogen peroxide. Thenard’s process has, however, some major drawbacks which quenched the expectant explosion of its use in an aqueous form. -
Preparing to Manufacture Hydrogen Peroxide
PREPARING TO MANUFACTURE HYDROGEN PEROXIDE Part of the Hydrogen Peroxide Propulsion Guide The early laboratory preparation of hydrogen peroxide was based on the technique that Thenard used during the initial preparation of hydrogen peroxide. In this technique, barium nitrate, purified by recrystallization, was decomposed by heating in air in a porcelain retort. The resulting oxide was further oxidized by heating in a stream of oxygen to a dull red heat. The barium peroxide which formed was then dampened, ground, and dissolved in hydrochloric acid (nitric acid was used in Thenard’s initial experiments). A slight excess of sulfuric acid was then added to precipitate barium sulfate and regenerate hydrochloric acid. The procedure of barium peroxide solution and sulfate precipitation was repeated several times in the same solution to increase the peroxide concentration (concentrations of up to 33 percent by weight hydrogen peroxide could be achieved in this manner). The concentrated solution containing water, hydrogen peroxide, and hydrochloric acid, along with accumulated impurities, was cooled with ice and saturated with barium peroxide; iron and manganese impurities in the solution were then precipitated out as phosphates. The hydrochloric acid was removed by the addition of silver sulfate and the sulfate ion was removed by the subsequent addition of barium oxide. Further concentration was accomplished by vacuum distillation until “no further density increase occurs.” Thenard reported that 100 w/o hydrogen peroxide (on the basis of density data and the measurement of the volume of oxygen released) could be obtained by this technique. The first record of commercial production of hydrogen peroxide appeared in the 1865 to 1875 period. -
Periodic Trends in the Main Group Elements
Chemistry of The Main Group Elements 1. Hydrogen Hydrogen is the most abundant element in the universe, but it accounts for less than 1% (by mass) in the Earth’s crust. It is the third most abundant element in the living system. There are three naturally occurring isotopes of hydrogen: hydrogen (1H) - the most abundant isotope, deuterium (2H), and tritium 3 ( H) which is radioactive. Most of hydrogen occurs as H2O, hydrocarbon, and biological compounds. Hydrogen is a colorless gas with m.p. = -259oC (14 K) and b.p. = -253oC (20 K). Hydrogen is placed in Group 1A (1), together with alkali metals, because of its single electron in the valence shell and its common oxidation state of +1. However, it is physically and chemically different from any of the alkali metals. Hydrogen reacts with reactive metals (such as those of Group 1A and 2A) to for metal hydrides, where hydrogen is the anion with a “-1” charge. Because of this hydrogen may also be placed in Group 7A (17) together with the halogens. Like other nonmetals, hydrogen has a relatively high ionization energy (I.E. = 1311 kJ/mol), and its electronegativity is 2.1 (twice as high as those of alkali metals). Reactions of Hydrogen with Reactive Metals to form Salt like Hydrides Hydrogen reacts with reactive metals to form ionic (salt like) hydrides: 2Li(s) + H2(g) 2LiH(s); Ca(s) + H2(g) CaH2(s); The hydrides are very reactive and act as a strong base. It reacts violently with water to produce hydrogen gas: NaH(s) + H2O(l) NaOH(aq) + H2(g); It is also a strong reducing agent and is used to reduce TiCl4 to titanium metal: TiCl4(l) + 4LiH(s) Ti(s) + 4LiCl(s) + 2H2(g) Reactions of Hydrogen with Nonmetals Hydrogen reacts with nonmetals to form covalent compounds such as HF, HCl, HBr, HI, H2O, H2S, NH3, CH4, and other organic and biological compounds. -
Dihydrazides - the Versatile Curing Agent for Solid Dispersion Systems
Dihydrazides - The Versatile Curing Agent for Solid Dispersion Systems Abe Goldstein A&C Catalysts, Inc Abstract This paper will introduce dihydrazides, a relatively obscure class of curing agents useful in virtually all thermoset resin systems. First described in 1958, by Wear, et al.(1) dihydrazides are useful curing agents for epoxy resins, chain extenders for polyurethanes, and excellent crosslinking agents for acrylics. In one-part epoxy systems, depending on the backbone chain of the chosen dihydrazide, Tg's over 150°C and pot life over 6 months as cure time of less than a minute can be seen. In acrylic emulsions, dihydrazides can be dissolved into the water phase and serve as an additional crosslinker, as the emulsion coalesces and cures. As a chain extender for poylurethanes, dihydrazides can be used to increase toughness and reduce yellowing. Introduction O O | | | | Dihydrazides are represented by the active group: H2NHNC(R) CNHNH2, where R is can be any polyvalent organic radical preferably derived from a carboxylic acid. Carboxylic acid esters are reacted with hydrazine hydrate in an alcohol solution using a catalyst and a water extraction step. The most common dihydrazides include adipic acid dihydrazide (ADH), derived from adipic acid, sebacic acid dihydrazide (SDH), valine dihydrazide (VDH), derived from the amino acid valine, and isophthalic dihydrazide (IDH). The aliphatic R group can be of any length. For example, when R group is just carbon, the resulting compound is carbodihydrazide (CDH), the fastest dihydrazide. Or R as long as C-18 has been reported as in icosanedioic acid dihydrazide (LDH). Some of the more common dihydrazides are represented in Figure 1. -
Hydrazine, Monomethylhydrazine, Dimethylhydrazine and Binary Mixtures Containing These Compounds
Fluid Phase Behavior from Molecular Simulation: Hydrazine, Monomethylhydrazine, Dimethylhydrazine and Binary Mixtures Containing These Compounds Ekaterina Elts1, Thorsten Windmann1, Daniel Staak2, Jadran Vrabec1 ∗ 1 Lehrstuhl f¨ur Thermodynamik und Energietechnik, Universit¨at Paderborn, Warburger Straße 100, 33098 Paderborn, Germany 2 Lonza AG, Chemical Research and Development, CH-3930 Visp, Switzerland Keywords: Molecular modeling and simulation; vapor-liquid equilibrium; Henry’s law constant; Hy- drazine; Monomethylhydrazine; Dimethylhydrazine; Argon; Nitrogen; Carbon Monoxide; Ammonia; Water Abstract New molecular models for Hydrazine and its two most important methylized derivatives (Monomethyl- hydrazine and Dimethylhydrazine) are proposed to study the fluid phase behavior of these hazardous compounds. A parameterization of the classical molecular interaction models is carried out by using quan- tum chemical calculations and subsequent fitting to experimental vapor pressure and saturated liquid density data. To validate the molecular models, vapor-liquid equilibria for the pure hydrazines and binary hydrazine mixtures with Water and Ammonia are calculated and compared with the available experimen- tal data. In addition, the Henry’s law constant for the physical solubility of Argon, Nitrogen and Carbon Monoxide in liquid Hydrazine, Monomethylhydrazine and Dimethylhydrazine is computed. In general, the simulation results are in very good agreement with the experimental data. ∗ corresponding author, tel.: +49-5251/60-2421, fax: +49-5251/60-3522, email: [email protected] 1 1 Introduction On October 24, 1960, the greatest disaster in the history of rocketry, now also known as Nedelin disaster, occurred [1–3]. At that time, the Soviet newspapers published only a short communique informing that Marshall of Artillery Mitrofan Nedelin has died in an airplane crash. -
Sulfur Dioxide in Workplace Atmospheres (Bubbler)
Withdrawn Provided For Historical Reference Only SULFUR DIOXIDE IN WORKPLACE ATMOSPHERES (BUBBLER) ♦ Method Number: ID-104 Matrix: Air OSHA PEL Sulfur Dioxide (Final Rule Limit): 2 ppm (Time Weighted Limit) 5 ppm (Short-Term Exposure Limit) Sulfur Dioxide (Transitional Limit): 5 ppm (Time Weighted Limit) Collection Device: A calibrated personal sampling pump is used to draw a known volume of air through a midget-fritted glass bubbler containing 10 to 15 mL of 0.3 N hydrogen peroxide. Recommended Air Volume: 15 to 60 L Recommended Sampling Rate: 1 L/min Analytical Procedure: Samples are directly analyzed with no sample preparation by ion chromatography as total sulfate. Detection Limit Qualitative: 0.0041 ppm (60-L air volume) Quantitative: 0.010 ppm (60-L air volume) Precision and Accuracy Validation Level: 2.5 to 10.0 ppm (60-L air volume) CVT 0.012 Bias -0.046 Overall Error ±7% Method Classification: Validated Method Chemist: Ted Wilczek, Edward Zimowski Date (Date Revised): 1981 (December, 1989) Commercial manufacturers and products mentioned in this method are for descriptive use only and do not constitute endorsements by USDOL-OSHA. Similar products from other sources can be substituted. Branch of Inorganic Methods Development OSHA Technical Center Salt Lake City, Utah 1 of 9 Note: OSHA no longer uses or supports this method (November 2019). Withdrawn Provided For Historical Reference Only 1. Introduction This method describes the collection and analysis of airborne sulfur dioxide (SO2) using midget-fritted glass bubblers (MFGBs) in the workplace. It is applicable for both short-term (STEL) and time weighted average (TWA) exposure evaluations. -
Ethane / Nitrous Oxide Mixtures As a Green Propellant to Substitute Hydrazine: Validation of Reaction Mechanism C
Ethane / Nitrous Oxide Mixtures as a Green Propellant to Substitute Hydrazine: Validation of Reaction Mechanism C. Naumann*, C. Janzer, U. Riedel German Aerospace Center (DLR), Institute of Combustion Technology Pfaffenwaldring 38-40, 70569 Stuttgart, Germany Abstract The combustion properties of propellants like ethane / nitrous oxide mixtures that have the potential to substitute hydrazine or hydrazine / dinitrogen tetroxide in chemical propulsion systems are investigated. In support of CFD- simulations of new rocket engines powered by green propellants ignition delay times of ethane / nitrous oxide mixtures diluted with nitrogen have been measured behind reflected shock waves at atmospheric and elevated pressures, at stoichiometric and fuel-rich conditions aimed for the validation of reaction mechanism. In addition, ignition delay time measurements of ethene / nitrous oxide mixtures and ethane / O2 / N2 - mixtures with an O2:N2 ratio of 1:2 as oxidant at the same level of dilution are shown for comparison. Finally, the ignition delay time predictions of a recently published reaction mechanism by Glarborg et al. are compared with the experimental results. Introduction waves at initial pressures of pnominal = 1, 4, and 16 bar. Hydrazine and hydrazine derivatives like The results are compared to ignition delay time monomethyl hydrazine (MMH) and unsymmetrical measurements of stoichiometric C2H4 / N2O mixtures dimethyl hydrazine (UDMH) are used for spacecraft (see [6], [7], [8]). Complementary, ignition delay times propulsion applications in various technological of the corresponding oxygen based reactive mixture contexts despite their drawback of being highly toxic. C2H6 / (1/3 O2 + 2/3 N2) have been measured, too. Today, hydrazine consumption for European space Thereafter, the predictions of a recently published activities is on the order of 2-5 tons per year. -
HYDRAZINE Method Number: 108 Matrix: Air Target Concentration
HYDRAZINE Method number: 108 Matrix: Air Target concentration: 10 ppb (13 µg/m3) and 1 ppm (1.3 mg/m3) OSHA PEL: 1 ppm (1.3 mg/m3) ACGIH TLV: 10 ppb (13 µg/m3) Procedure: Samples are collected closed-face by drawing known volumes of air through sampling devices consisting of three-piece cassettes, each containing two sulfuric acid treated 37-mm glass fiber filters separated by the ring section. The filters are extracted with a buffered EDTA disodium solution. An aliquot of the extract is derivatized with a benzaldehyde solution to form benzalazine from any hydrazine in the samples. The benzalazine is quantitated by LC using a UV detector. Recommended air volume and sampling rate: 240 L at 1.0 L/min Reliable quantitation limit: 0.058 ppb (0.076 µg/m3) Standard error of estimate at the target concentration: 7.5% at 10 ppb Target Concentration 5.2% at 1 ppm Target Concentration Status of method: Evaluated method. This method has been subjected to the established evaluation procedures of the Organic Methods Evaluation Branch. Date: February 1997 Chemist: Carl J. Elskamp Organic Methods Evaluation Branch OSHA Salt Lake Technical Center Salt Lake City, UT 84165-0200 1 of 19 T-108-FV-01-9702-M 1. General Discussion 1.1 Background 1.1.1 History In 1980, an air sampling and analytical procedure to determine hydrazine was validated by the OSHA Analytical Laboratory. (Ref. 5.1) The method (OSHA Method 20) is based on a field procedure developed by the U.S. Air Force that involves collection of samples using sulfuric acid coated Gas Chrom R and colorimetric analysis using p¯dimethylaminobenzaldehyde. -
Unsymmetrical Dimethylhydrazine (UDMH) Technical Data Sheet
Technical Performance Chemicals Product Hydrazine Information Unsymmetrical Dimethylhydrazine (UDMH) Unsymmetrical dimethylhydrazine (1,1-dimethylhydrazine) chemicals). It has also been used in acidic gas absorbers and is a clear, colorless hygroscopic liquid. It has an ammonia- as a fuel additive stabilizer. like odor which closely resembles that of aliphatic amines. UDMH is miscible with water, hydrazine, Handling, Storage and Safety dimethylenetriamine, ethanol, amines and most petroleum fuels. The experience accumulated by the chemical and aerospace industries indicates that with rigid adherence to proper UDMH is mildly alkaline and is a very strong reducing precautions, UDMH can be handled safely. Because UDMH agent. Its high chemical reactivity, easily-controlled vapors have such a very wide range of explosive limits and functionality and strong hydrogen bonding are its most useful because UDMH liquid is extremely reactive with many properties. materials, the safety precautions outlined are necessary to avoid fire or explosions. Table 1 Specifications In addition, prolonged exposure to UDMH vapor, contact % by with skin, or ingestion may produce harmful or fatal effects. Component Weight 1,1-dimethylhydrazine, min 98.0 Storage : UDMH may be stored in the DOT-approved Amines and water, max 2.0 container in which it is shipped. (See Shipping Information below.) Store away from heat, sparks, open flame and Table 2 Typical Physical Properties oxidants. Store only in well-ventilated areas. Do not contaminate. Density @ 25'C (g/ml) 0.784 (lb/gal) 6.6 Since UDMH is stable, it can be stored without loss of Viscosity @ 20'C (cp) 0.56 purity. Keep the container closed securely. -
Guidelines for the Preservation of Raw Milk by Use of the Lactoperoxidase System
GUIDELINES FOR THE PRESERVATION OF RAW MILK BY USE OF THE LACTOPEROXIDASE SYSTEM CAC/GL 13-1991 INTRODUCTION Milk is an easily perishable raw material. Contaminating bacteria may multiply rapidly and render it unsuitable for processing and/or unfit for human consumption. Bacterial growth can be retarded by refrigeration, thereby slowing down the rate of deterioration. Under certain conditions refrigeration may not be feasible due to economical and/ or technical reasons. Difficulties in applying refrigeration are specially a problem for certain areas in countries setting up or expanding their milk production. In these situations, it would be beneficial to have access to a method, other than refrigeration, for retarding bacterial growth in raw milk during collection and transportation to the dairy processing plant. In 1967 the FAO/WHO Expert Panel on Milk Quality concluded that the use of hydrogen peroxide might be an acceptable alternative in the early stages of development of an organized dairy industry, provided that certain conditions were complied with. However, this method has not achieved any general acceptance as it has several drawbacks, most important of which is the difficulty of controlling its use: it may be misused to disguise milk of basic hygienic quality produced under poor hygienic conditions. The toxicological aspects of the use of relatively high concentrations of hydrogen peroxide in milk have also been questioned. A chemical method for preserving milk would still be of great advantage in certain situations. The search for such a method has therefore continued. Interest has recently been focused on the indigenous antibacterial systems in milk to determine if these could be applied practically to preserve raw milk.