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1104 results about "Alkali metal oxide" patented technology

The alkali metals react with oxygen to form several different compounds: suboxides, oxides, peroxides, superoxides, and ozonides. They all react violently with water.

Methods of vitrifying waste with low melting high lithia glass compositions

The invention relates to methods of vitrifying waste and for lowering the melting point of glass forming systems by including lithia formers in the glass forming composition in significant amounts, typically from about 0.16 wt % to about 11 wt %, based on the total glass forming oxides. The lithia is typically included as a replacement for alkali oxide glass formers that would normally be present in a particular glass forming system. Replacement can occur on a mole percent or weight percent basis, and typically results in a composition wherein lithia forms about 10 wt % to about 100 wt % of the alkali oxide glass formers present in the composition. The present invention also relates to the high lithia glass compositions formed by these methods. The invention is useful for stabilization of numerous types of waste materials, including aqueous waste streams, sludge solids, mixtures of aqueous supernate and sludge solids, combinations of spent filter aids from waste water treatment and waste sludges, supernate alone, incinerator ash, incinerator offgas blowdown, or combinations thereof, geological mine tailings and sludges, asbestos, inorganic filter media, cement waste forms in need of remediation, spent or partially spent ion exchange resins or zeolites, contaminated soils, lead paint, etc. The decrease in melting point achieved by the present invention desirably prevents volatilization of hazardous or radioactive species during vitrification.
Owner:SAVANNAH RIVER NUCLEAR SOLUTIONS

Method of synthesizing IM-5 molecular sieve by using composite template

The invention provides a method of synthesizing IM-5 molecular sieve by using a composite template. The method comprises the following steps: (1) dissolving an inorganic base, an aluminum source and two templates in deionized water and carrying out uniform mixing so as to prepare a mixed solution; (2) adding a silicon source into the mixed solution obtained in step (1), optionally adding an additive and carrying out uniform mixing so as to prepare colloid or a solid-liquid mixture; (3) transferring the colloid or the solid-liquid mixture obtained in step (2) to a crystallization kettle, carrying out hydrothermal crystallization at a temperature of 120 to 200 DEG C for 1 to 10 d, carrying out cooling after crystallization and rinsing, filtering and drying the obtained mixed liquor so as to obtain raw powder of the IM-5 molecular sieve. A mole ratio of reactants satisfies the equation of SiO2: Al2O3: M2O: R1: R2: H2O = 60: 0.4-6: 6-21: 0.6-18: 0.6-12: 300-1800, wherein M2O is an alkali metal oxide, R1 is a first template, and R2 is a second template. The method provided in the invention widens the range of mixing ratios of raw materials, improves yield of a single kettle and enables time for crystallization to be further shortened and enlarged production to be easier.
Owner:CHINA PETROLEUM & CHEM CORP +1

Technology device and method for preparing propylene by dehydrogenating propane or propane-enriched low carbon hydrocarbon

The invention provides a technology device and method for preparing propylene by dehydrogenating propane or propane-enriching low carbon hydrocarbon. The device comprises a reacting/regenerating part and a product fractionating part. A reacting/regenerating system is divided into a parallel type arrangement scheme and a coaxial type arrangement scheme by a fluidized bed reacting/regenerating technology, wherein a raising pipe of the parallel type reacting/regenerating system is an internal or external raising pipe, and a raising pipe of the coaxial type reacting/regenerating system is an external raising pipe. The method comprises the steps: leading raw materials and reaction products to enter into a raising pipe reactor after heat exchange; performing a dehydrogenating conversion reaction under the conditions that the reaction temperature is 500-700 DEG C, the pressure is 0.1-0.4MPa, and the ratio of a microspherical catalyst to oil is 5-60, wherein the microspherical catalyst consists of chromium, rare earth oxides, alkali metal oxides and a gamma-Al2O3 carrier, preferably, the temperature is 550-670 DEG C, the pressure is 0.1-0.15MPa, and the ratio of the microspherical catalyst to oil is 6-14; leading the reaction products and the raw materials to enter into a gas-oil separator to separate a gas phase, a liquid phase from a water phase after heat exchange and cooling; leading the separated gas to enter into a gas compressor to be compressed and be transported to an absorbing/stabilizing part; pumping the liquid to an absorbing tower; transporting the liquefied gas from a return tank at the top of a stabilizing tower to a propylene/propane separating tower by a charging pump of a propylene tower; discharging the fine propylene separated from the top of the tower out of the device as a product; discharging the separated byproduct hydrogen out of the device; and returning products at bottom of the tower to the reacting/regenerating part to be recycled.
Owner:卓润生 +1
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