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Ammonium Nitrate-sulfate Mixture

Ammonium Nitrate-Sulfate Mixture Solid Not pertinent Not pertinent 1.800... [Pg.208]

Ammonium Nitrate-Sulfate Mixture Self contained breathing apparatus must be used when fighting fires. At all other times a dust mask is adequate. Move to fresh air. Flush with water for at least 15 minutes. [Pg.272]

Ammonium Nitrate-Sulfate Mixture Data not available Data not available 58 mg/kg Data not available... [Pg.372]

Ammonium Nitrate- Sulfate Mixture Not pertinent Not pertinent Not pertinent Not pertinent Water Steam, inert gases, foam, dry chemical Will increase the intensity of fire when in contact with combustible material Not pertinent No ... [Pg.406]

Ammonium Hydrogendifluoride. 1727 60 Ammonium Nitrate -Sulfate Mixture 2069 43... [Pg.704]

Nitro or nitrate explosives, normally shock-insensitive, are rendered extremely sensitive by addition of traces of potassium or potassium-sodium alloy. Ammonium nitrate, and nitrate-sulfate mixtures, picric acid, and even nitrobenzene respond in this way. [Pg.1727]

Ammonium nitrate-fuel oil (ANFO) mixture, in salt mining, 22 806 Ammonium nitrate limestone, 2 726 Ammonium nitrate sulfate, 2 724-725... [Pg.51]

A three-necked round-bottom flask is fitted with a dropping funnel, a thermometer, and a magnetic stirrer and is heated in a water bath to 30°. Tetralin (1.32 g, 0.01 mole) and 50 ml of 3.5 Anitric acid solution are placed in the flask and brought to temperature. Ceric ammonium nitrate (21.9 g, 0.04 mole) is dissolved in 100 ml of 3.5 N nitric acid, and the solution is added dropwise to the reaction mixture at a rate such that the temperature does not rise and only a pale yellow color is evident in the reaction mixture. At the completion of the reaction (1 to 2 hours), the mixture should be colorless. The solution is cooled to room temperature, diluted with an equal volume of water, and extracted twice with ether. The ether solution is dried with anhydrous sodium sulfate, filtered, and the ether is evaporated. The residue may be distilled to yield a-tetralone (bp 113-11676 mm or 170749 mm) or may be converted directly to the oxime, which is recrystallized from methanol, mp 88-89°. [Pg.14]

Interaction with fused ammonium nitrate or with metal nitrates, phosphates or sulfates may be explosively violent [1]. Lithium and sodium carbonates may also react vigorously [2], The mixture with magnesium sulfate has been described as a noisy but low power bursting charge for pyrotechny [3],... [Pg.1761]

Ebara [Electron beam ammonia reaction] A dry process for removing sulfur and nitrogen oxides from flue-gas. A beam of high energy electrons is injected into the gas, to which a stoichiometric quantity of ammonia has been added. The product, a mixture of ammonium sulfate and ammonium nitrate, is collected downstream by an electrostatic precipitator or a bag filter. Developed by Ebara Corporation, Japan, and piloted in Indianapolis in 1986. [Pg.95]

Victor A process for making a mixed ammonium nitrate - ammonium sulfate fertilizer (ASN) which is less liable to explode than ammonium nitrate. Ammonium sulfate is mixed with nitric acid and the mixture ammoniated in an evaporator. Developed by Gewerkschaft Victor - Chemische Werke and used by that company at Castrop Rauxel, Germany. See also Uhde - Hibernia. [Pg.284]

Fig. 1. Schematic flowsheet of uranium processing (acid leach and ion exchange) operation. Numbers refer to the numbers that appear in the boxes on the flowsheet. Operations (3), (6), (9), and (11) may be done by thickening or filtration. Most often, thickeners are used, followed by filters. The pH of the leach slurry <4) is elevated to reduce its corrosive effect and to improve the ion-exchange operation on the uranium liquor subsequently separated, In tile ion exchange operation (7), resin contained in closed columns is alternately loaded with uranium and then eluted. The resin adsorbs the complex anions, such as UC fSO 4-. in which the uranium is present in the leach solution. Ammonium nitrate is nsed for elution, obtained by recycling the uranium filtrate liquor after pH adjustment. Iron adsoibed with the uranium is eluted with it. Iron separation operation (8) is needed inasmuch as the iron hydroxide slurry is heavily contaminated with calcium sulfate and coprecipitated uranium salts. Therefore, the slurry is recycled to the watering stage (3). Washed solids from 1,6). the waste barren liquor from (7), and the uranium filtrate from (11) are combined. The pH is elevated to 7.5 by adding lime slurry before the mixture is pumped to the tailings disposal area. (Rio Algom Mines Limited, Toronto)... Fig. 1. Schematic flowsheet of uranium processing (acid leach and ion exchange) operation. Numbers refer to the numbers that appear in the boxes on the flowsheet. Operations (3), (6), (9), and (11) may be done by thickening or filtration. Most often, thickeners are used, followed by filters. The pH of the leach slurry <4) is elevated to reduce its corrosive effect and to improve the ion-exchange operation on the uranium liquor subsequently separated, In tile ion exchange operation (7), resin contained in closed columns is alternately loaded with uranium and then eluted. The resin adsorbs the complex anions, such as UC fSO 4-. in which the uranium is present in the leach solution. Ammonium nitrate is nsed for elution, obtained by recycling the uranium filtrate liquor after pH adjustment. Iron adsoibed with the uranium is eluted with it. Iron separation operation (8) is needed inasmuch as the iron hydroxide slurry is heavily contaminated with calcium sulfate and coprecipitated uranium salts. Therefore, the slurry is recycled to the watering stage (3). Washed solids from 1,6). the waste barren liquor from (7), and the uranium filtrate from (11) are combined. The pH is elevated to 7.5 by adding lime slurry before the mixture is pumped to the tailings disposal area. (Rio Algom Mines Limited, Toronto)...
Defluorinated Phosphate Rock. There is substantial production of defluorinated phosphate rock for fertilizer use in Japan (about 100,000 mt/year). Ground, high-grade rock is mixed with small proportions of sodium carbonate or sulfate and wet-process acid. The mixture is calcined at a temperature of 1350°C in an oil-fired rotary kiln 45.0 m in length and 2.7 m in diameter. The product contains 38-42 percent P205 of which more than 90 percent is soluble in neutral ammonium nitrate solution and is an effective fertilizer on acid soils. During the production of defluorinated phosphate rock, substantially all fluorine is driven off. Sodium bifluoride (NaHF2) is recovered as a byproduct. A similar product is made in the United States, but it is mainly used for animal feed supplement. [Pg.1133]


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See also in sourсe #XX -- [ Pg.291 ]




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Ammonium Nitrate Mixtures

Ammonium nitrate

Ammonium sulfate

Ammonium sulfate nitrate

Nitrating mixture

Nitration Mixture

Nitration ammonium

Sulfates ammonium sulfate

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