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272 results about "Barium Ion" patented technology

Mesoporous X-type molecular sieve, adsorbent based on molecular sieve, and preparation and application thereof

The invention relates to a preparation method of a mesoporous X-type molecular sieve and a method for preparing an adsorbent by using the molecular sieve as an active component. The prepared adsorbent based on the mesoporous X-type molecular sieve is used as a paraxylene adsorptive separation adsorbent. The method for preparing the mesoporous X-type molecular sieve comprises the following steps: by using water glass as a silicon source and aluminum hydroxide as an aluminum source, adding a template, and carrying out hydrothermal synthesis to obtain the mesoporous X-type molecular sieve. The mesoporous molecular sieve and kaolin are proportionally molded to obtain 0.3-0.8mm granules, and the granules are subjected to barium ion or (and) potassium ion exchange until the exchange degree is greater than 99%, thereby obtaining the adsorbent which has excellent adsorptive separation capacity for paraxylene in C8 aromatic hydrocarbons. Compared with the prior art, the active component mesoporous X-type molecular sieve of the adsorbent, which is prepared by using the template, has the crystal form structure of the X-type molecular sieve and the pore distribution of the mesoporous and microporous dual models; the mesoporous pore size distribution is 2nm or so; and thus, the problem of overlow mass transfer rate in the adsorbent can be solved.
Owner:SHANGHAI LVQIANG NEW MATERIALS CO LTD +1

Method for preparing barium-activated lithium iron phosphate cathode material

ActiveCN102347486AShape is easy to controlGood for particle size controlCell electrodesLithium iron phosphateAlcohol
The invention relates to a method for preparing a barium-activated lithium iron phosphate cathode material. The method is characterized by comprising the steps of: mixing raw materials of a lithium source, a ferrum source, a phosphate source and a barium source according to the proportion of Li:Ba:Fe:P of 1mol:(0.0003mol):1mol:1mol, performing high-speed ball-milling (at the rotating speed of 200r/min) on the mixed raw materials in an absolute ethyl alcohol (AR) medium and drying at 105-120 DEG C to obtain a precursor; and placing the dried precursor in a high-temperature furnace and calcining for 24h at a high temperature of 500-750DEG C in an ordinary pure nitrogen atmosphere to obtain the barium-activated lithium iron phosphate cathode material. The chemical general formula of the material can be represented as Li Ba FePO4. As a bit of substituent barium is doped, the appearance and the particle size of the product are favorably controlled, and a stable lithium iron phosphate compound is obtained. Barium ions replace lithium ions in an occupation manner, the crystal lattice of the compound is activated, the diffusion coefficient of the lithium ions is increased, and the first discharge capacity of the cathode material reaches 145.52mAh/g. The potential of a charge-discharge platform of the cathode material is about 3.5V compared with that of a lithium electrode, the initial discharge capacity exceeds 162mAh/g, and the capacity is attenuated by about 3.2% after 100 times of charge-discharge circles. Compared with the undoped LiFePO4 contrast embodiment, the cathode material has greatly increased specific capacity and cyclical stability. As the price of barium is more than 100 times lower than the price of lithium, the production cost can be reduced by more than 10 times.
Owner:桐乡乐维新材料有限公司

Method for improving utilization efficiency of ozone and reducing COD of wastewater

The invention provides a method for increasing the utilization efficiency of ozone and reducing the COD of wastewater. According to the method, a chemical agent for removing a hydroxyl radical capture agent generated in base catalysis ozone advanced oxidation is added into the wastewater so as to achieve the purposes. Calcium ions, barium ions and the like are added into a base catalysis ozone oxidation system, so that the hydroxyl radical capture agent becomes precipitate to be separated from the water and loses the capacity for capturing hydroxyl radicals, and accordingly the utilization efficiency of ozone is improved. In addition, part of organic acid generated by the calcium ions, the barium ions and the like and the ozone oxidation wastewater precipitates to be separated from the water, so that the consumption of ozone is reduced, and the utilization efficiency of the ozone treatment wastewater is indirectly improved. By means of the method, the reaction rate of ozone can be obviously increased, the utilization efficiency of ozone can be obviously improved, reaction time can be shortened, cost can be reduced, organic matter in the wastewater can be thoroughly mineralized, and the COD and the total phosphorus content of the wastewater can be significantly reduced.
Owner:BEIJING WEICHUANGLI TECH CO LTD

Treatment method for recycling hydrofluoric acid waste liquor

The invention discloses a treatment method for recycling hydrofluoric acid waste liquor. The treatment method comprises the following steps of: analyzing the content of silicon in hydrofluoric acid waste liquor; adding a compound of sodium, potassium or barium, which is more than the content of silicon by once, into the hydrofluoric acid waste liquor in a treatment slot, so that the fluorine and silicon is combined with sodium, potassium or barium in the hydrofluoric acid waste liquor for a reaction to generate fluosilicate solids of sodium fluosilicate, potassium fluosilicate or barium fluosilicate; extracting the upper layer of liquor after settling the fluosilicate solids, and conveying back to the original process for use after adding high-concentration hydrofluoric acid to achieve a hydrofluoric acid concentration value satisfying the use of the original use. The hydrofluoric acid waste liquor is only added with a little sodium, potassium or barium ions to prepare the hydrofluoric acid which can be recycled, so that less chemical drug is consumed, the wastewater emission is greatly lowered, the hydrofluoric acid usage amount of the original process is saved and the extra purchase cost is saved, and therefore, the treatment steps are simplified, the treatment cost is lowered and environment-friendly benefits are achieved.
Owner:巫协森 +1

Method for quickly measuring sulfate radical content in magnesium method desulfurization process

The invention discloses a method for quickly measuring sulfate radical content in a magnesium method desulfurization process. The method consists of the processes of filtration, constant volume determination, acidification, precipitation and back titration and comprises the following steps of: filtering a fetched sample by using filter paper; filling quantitative filtered clear solution with constant volume into a volumetric flask; filling proper constant volume clear solution in a beaker, and adding diluted hydrochloric acid of 1:1 concentration for acidifying; adding excessive barium chloride into the acidified clear solution to perform precipitation; filtering and fully washing the sediment, and titrating the total weight of barium, calcium and magnesium ions by using ethylene diamine tetraacetic acid (EDTA) coordination agent under the condition that chrome black T is used as an indicator; and meanwhile, calculating the content of the barium ions by measuring the total weight of the calcium and the magnesium so as to calculate the content of the sulfate radicals. The method has the advantages that: the control of solution concentration and measuring process conditions is accurate, the measurement of the content of the calcium and the magnesium is completed at the same time, and the preparation of barium and magnesium mixed solution is not needed; the accuracy of the sulfate radical detection is improved, and the detection time is shortened; and the method is suitable for quickly measuring the sulfate radical content in the debugging and operating process of a magnesium oxide method desulfurization system.
Owner:CECEP L&T ENVIRONMENTAL TECH

Method for preparing ornithine aspartate powder injection for injection

The invention discloses a method for preparing ornithine aspartate powder injection for injection. The method comprises the following steps of: taking arginine, adding the solution of barium hydroxide, stirring to dissolve the arginine, and heating to hydrolyze so as to completely transform the arginine into ornithine; adding aspartate, uniformly stirring, adding a precipitator, filtering to remove barium ion precipitate, and regulating the pH value of the solution to neutrality; adding an inert organic solvent for crystallization, filtering and pumping, adding water for injection to dissolve the crystals, adding active carbon for needle for decoloration and depyrogenation, coarsely filtering to remove carbon, and filtering to make the solution sterile and clarified by using a 0.22 mu m millipore filter; and adding ethanol for crystallization, obtaining ornithine aspartate sterile powder, packaging the powder into a sterilized vial, capping, and rolling an aluminum cover to obtain the ornithine aspartate sterile powder injection for injection. The method has the advantages of increasing the yield, preparing the ornithine aspartate by the one-pot method, along with easy operation, simple and convenient operation, low cost, short production period, and suitability for mass production.
Owner:HUBEI HOPE PHARMA

High-gravity reactive precipitation process for the preparation of barium titanate powders

The invention relates to a process for the preparation of fine barium titanate (BaTiO3) powders. The process comprises introducing an aqueous solution (I) containing salts of barium and titanium, and an aqueous basic solution (II) containing an inorganic or organic base separately and simultaneously into a high-gravity reactor with the high-gravity level of 1.25G to 12,500G and performing the reaction of the solution (I) with the solution (II) at a temperature of from 60 to 100° C. The solution (I) is preheated to a temperature ranging from 60° C. to 65° C. and the solution (II) is preheated to a temperature ranging from 60° C. to 100° C. respectively prior to the reaction, in which the Ba/Ti molar ratio in the solution (I) is more than 1 and the concentration of the base in the solution (II) is such that the reaction mixture is maintained at a constant OH concentration, preferably a pH value of about 14. The reaction product is separated by filtering and washed with deionized water to remove the impurity ions and excessive barium ions, and then dried to obtain BaTiO3 powders. Said powders consist essentially of crystalline, primary particles having a uniform particle size ranging from 5 to 200 nm, an approximately spherical morphology and a high sintering activity.
Owner:BEIJING UNIV OF CHEM TECH
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