Patents
Literature
Patsnap Copilot is an intelligent assistant for R&D personnel, combined with Patent DNA, to facilitate innovative research.
Patsnap Copilot

83 results about "Maghemite" patented technology

Maghemite (Fe₂O₃, γ-Fe₂O₃) is a member of the family of iron oxides. It has the same spinel ferrite structure as magnetite and is also ferrimagnetic. Maghemite can be considered as an Fe(II)-deficient magnetite with formula (Feᴵᴵᴵ₈)A[Fe₄₀/₃ᴵᴵᴵ□₈/₃]BO₃2 where □ represents a vacancy, A indicates tetrahedral and B octahedral positioning.

Superparamagnetic Nanoparticles Based on Iron Oxides with Modified Surface, Method of Their Preparation and Application

The subject of the invention is superparamagnetic nanoparticle probes based on iron oxides, to advantage magnetite or maghemite, with modified surface, coated with mono-, di- or polysaccharides from the group including D-arabinose, D-glucose, D-galactose, D-mannose, lactose, maltose, dextrans and dextrins, or with amino acids or poly(amino acid)s from the group including alanine, glycine, glutamine, asparagine, histidine, arginine, L-lysine, aspartic and glutamic acid or with synthetic polymers based on (meth)acrylic acid and their derivatives selected from the group containing poly(N,N-dimethylacrylamide), poly(N,N-dimethylmethacrylamide), poly(N,N-diethylacrylamide), poly(N,N-diethylmethacrylamide), poly(N-isopropylacrylamide), poly(N-isopropylmethacrylamide), which form a colloid consisting of particles with narrow distribution with polydispersity index smaller than 1.3, the average size of which amounts to 0.5-30 nm, to advantage 1-10 nm, the iron content is 70-99.9 wt. %, to advantage 90 wt. %, the modification agent content 0.1-30 wt. %, to advantage 10 wt. %.
The particles of size smaller than 2 nm with polydispersity index smaller than 1.1 can be obtained by a modified method of preparation.
Superparamagnetic nanoparticle probes according to the invention are prepared by pre-precipitation of colloidal Fe(OH)3 by the treatment of aqueous 0.1-0.2M solution of Fe(III) salt, to advantage FeCl3, with less than an equimolar amount of NH4OH, at 21° C., under sonication, to which a solution of a Fe(II) salt, to advantage FeCl2, is added in the mole ratio Fe(III)/Fe(II)=2 under sonication and the mixture is poured into five- to tenfold, to advantage eightfold, molar excess of 0.5M NH4OH. The mixture is left aging for 0-30 min, to advantage 15 min, and then the precipitate is repeatedly, to advantage 7-10 times, magnetically separated and washed with deionized water. Then 1-3 fold amount, to advantage 1.5 fold amount, relative to the amount of magnetite, of 0.1 M aqueous solution of sodium citrate is added and then, dropwise, 1-3 fold amount, to advantage 1.5 fold amount, relative to the amount of magnetite, of 0.7 M aqueous solution of sodium hypochlorite. The precipitate is repeatedly, to advantage 7-10 times, washed with deionized water under the formation of colloidal maghemite to which, after dilution, is added dropwise, to advantage under 5-min sonication, an aqueous solution of a modification agent, in the weight ratio modification agent/iron oxide=0.1-10, to advantage 0.2 for amino acids and poly(amino acid)s and 5 for saccharides.
The particles smaller than 2 nm with polydispersity index smaller than 1.1 are prepared by mixing at 21° C. 1 volume part of 10-60 wt. %, to advantage 50 wt. %, of an aqueous solution of a saccharide, disaccharide or polysaccharide, such as D-arabinose, D-glucose, D-galactose, D-mannose, lactose, maltose, dextran and dextrins, and 1 volume part of aqueous solution of a Fe(II) and Fe(III) salt, to advantage FeCl2 and FeCl3, where the molar ratio Fe(III)/Fe(II)=2. A 5-15%, to advantage 7.5%, solution of NH4OH is added until pH 12 is attained and the mixture is heated at 60° C. for 15 min. The mixture is then sonicated at 350 W for 5 min and then washed for 24 h by dialysis in water using a membrane with molecular weight cut-off 14,000 until pH 7 is reached. The volume of solution is reduced by evaporation so that the final dry matter content is 50-100 mg/ml, to advantage 80 mg per 1 ml.
Superparamagnetic nanoparticle probes according to the invention can be used for labelling cells used in magnetic resonance imaging for monitoring their movement, localization, survival and differentiation especially in detection of pathologies with cell dysfunction and of tissue regeneration and also for labelling and monitoring cells administered for cell therapy purposes, in particular embryonal stem cells, fetal stem cells, stem cells of an adult human including bone marrow stem cells, olfactory glial cells, fat tissue cells, in the recipient organism by magnetic resonance.
The preparation of labelled cells proceeds by adding to the complete culture medium 5-20 μl, to advantage 10 μl, of a colloid containing 0.05-45 mg iron oxide per ml, to advantage 1-5 mg iron oxide per ml of the medium, and culturing the cells for a period of 1-7 days, to advantage for 1-3 days, at 37° C. and 5% of CO2.
Owner:INST OF MACROMOLECULAR CHEM ASCR V V I +1

Compound maghemite ore dressing method

ActiveCN106076606AAdvantages of beneficiation methodIndicators are stableWet separationMaghemiteHigh intensity
The invention discloses a compound maghemite ore dressing method. The compound maghemite ore dressing method comprises the following steps: feeding compound maghemite ore into an ore grinding-grading-low-intensity magnetic separation operation segment to obtain low intensity magnetic separation concentrate and low-intensity magnetic separation tailings; feeding the low-intensity magnetic separation concentrate into a fine sieving operation segment to obtain finely-sieved concentrate C1; feeding the low-intensity magnetic separation tailings into a high-intensity magnetic separation operation segment, and throwing out high-intensity magnetic separation tailings T1 to obtain high-intensity magnetic separation concentrate; combining coarse fraction low-intensity magnetic separation concentrate with the high-intensity magnetic separation concentrate, and feeding the mixture into a pre-grading-two-stage ore grinding-reverse flotation operation segment to obtain reverse flotation concentrate C2, and throwing out reverse flotation concentrate T2. In the method, staged ore grinding and high-intensity tailing throwing are adopted, so that discarding as soon as possible is realized; the low-intensity magnetic separation concentrate is obtained by fine sieving, so that collection as soon as possible is realized; oversize finely-sieved and high-intensity coarse concentrate is ground, so that the amount of ore ground at a second segment is lowered greatly, and energy-saving and consumption lowering are facilitated; an oversize finely-sieved product is reground and floated, so that the flotation grade is raised, and the adaptability of negative ion reverse floatation to ore characteristic fluctuation is improved.
Owner:SINOSTEEL MAANSHAN INST OF MINING RES

Beneficiation process of maghemite

The invention relates to a beneficiation process of maghemite. Raw ores are the maghemite. The iron grade is 41%-43%. The content of ferruginous clay is over 30%. The beneficiation process of the maghemite is characterized in that crushed products with the grain size being 12-0 mm are processed according to the following technological flow comprising that (1) pre-grading and closed-loop ore grinding are conducted during ore grinding, (2) weak intensity magnetic separation-medium intensity magnetic separation-high intensity magnetic separation-elutriation magnetic separation are conducted during magnetic separation, and (3) spiral chute roughing separation, concentration and scavenging are conducted during gravity separation; and the comprehensive concentrates composed of magnetic separation concentrates and gravity separation concentrates are obtained, wherein the grade of the comprehensive concentrates is 62% or over, and the recovery rate is 62.00-63.00%. The beneficiation process ofthe maghemite has the advantages that the crushed products are graded in advance, only one-stage closed loop ore grinding is adopted, and therefore investment and energy consumption are reduced; (2)magnetic separation concentrates are directly obtained from the products of the one-stage ore grinding through an elutriation magnetic separator; and (3) tailing discarding is conducted on coarse andfine classification overflow of cyclone to remove the ferruginous clay before gravity separation, so that the influence of the ferruginous clay on the quality of the gravity separation concentrates islowered.
Owner:中冶北方(大连)工程技术有限公司

Magnetically separable and recyclable iron oxide SCR denitration catalyst and application method thereof

The invention discloses a magnetically separable and recyclable iron oxide SCR denitration catalyst and an application method thereof. The catalyst is prepared through the following steps: with a limonite ore as a raw material, crushing and screening to form particles, calcining the particles in an atmosphere of hydrogen or carbon monoxide, so as to reduce goethite in the particles to be magnetite to obtain the catalyst, or further calcining in an air atmosphere, so that the magnetite is oxidized to be maghemite to obtain the catalyst, wherein the goethite content of the limonite ore is not less than 60%, the limonite ore has a nano-micro hierarchical porous structure, and the specific surface area of the limonite ore is not less than 10m<2>/g. When in use, the catalyst and ammonia are simultaneously fed into a flue gas flow at the temperature of 300-450 DEG C, and the catalyst and dust are together adsorbed onto the electrode plate of an electric dust collector or the surface of a filter bag and then are collected into a dust hopper through a dust cleaning method; the SCR denitration catalyst in the material discharged from the dust hopper is separated and recycled through a magnetic separation method; if inactivated, the SCR denitration catalyst can be washed and regenerated with water or weak aqua ammonia.
Owner:HEFEI UNIV OF TECH

Manganese-doped maghemite catalyst used for thermal catalytic oxidation of formaldehyde, and preparation method thereof

The invention discloses a manganese-doped maghemite catalyst used for thermal catalytic oxidation of formaldehyde, and a preparation method thereof. According to the preparation method, a ferric salt and a manganese salt are taken as the main raw materials; a manganese-doped maghemite precursor is synthesized via sodium hydroxide coprecipitation; and the manganese-doped maghemite precursor is subjected to washing, freeze drying, screening, and roasting oxidation so as to obtain the manganese-doped maghemite catalyst used for thermal catalytic oxidation of formaldehyde. The manganese-doped maghemite catalyst is granular, possesses spinel structures, and weak magnetism. The manganese-doped maghemite catalyst can be used for effective thermal catalytic oxidation of high-concentration formaldehyde, and can be used for removing high-concentration formaldehyde (>1000mL/m3) at 300 DEG C; formaldehyde removing rate is 90% or higher; catalytic activity is high; initiation temperature is low; thermal stability is excellent; separation and recovery are convenient; no secondary pollution is caused; cost is low; and the manganese-doped maghemite catalyst is suitable for purifying treatment of high concentration formaldehyde in industrial exhaust gas.
Owner:GUANGZHOU INST OF GEOCHEMISTRY - CHINESE ACAD OF SCI

Ore grinding weak-magnetic strong-magnetic gravity separation reverse flotation process for magnetic hematite ore

InactiveCN112588431AShorten the beneficiation processGood beneficiation indexFlotationMagnetic separationIronstoneMaghemite
The invention relates to an ore grinding weak-magnetic strong-magnetic gravity separation reverse flotation process for a magnetic hematite ore. The ore grinding weak-magnetic strong-magnetic gravityseparation reverse flotation process for the magnetic hematite ore is characterized by comprising the following steps that the magnetic hematite ore with the grade of 25%-45% and the magnetite distribution rate of more than or equal to 60% is subjected to grinding and weak and strong magnet separation tailing discarding, coarse-fine classification is carried out on weak and strong magnetic concentrate, coarse-fine spiral chute gravity separation is carried out on a coarse fraction to obtain gravity concentrate, and tailings in gravity separation are re-ground and then returned to the weak andstrong magnetic separation; reverse flotation of rough flotation-fine flotation-three scavenging is carried out on the fine fraction to obtain floating concentrate, and floating tailings are discarded; and the gravity concentrate and the floating concentrate are combined to form the final concentrate with the iron grade larger than or equal to 65% and the total recovery rate larger than or equal to 80%. The ore grinding weak-magnetic strong-magnetic gravity separation reverse flotation process for the magnetic hematite ore has the advantages that (1), the method is suitable for all iron ores with high magnetic iron content, and fine-grained embedded iron ores are included; (2), the existing process is remarkably shortened, the concentrate grade is high, and the recovery rate is high; and (3), the ore treatment amount of the magnetic gravity separation process is a main body part, equipment operation is stable, operation and control are simple, meanwhile, the flotation pressure is reduced, investment is low, energy is saved, and environment friendliness is achieved.
Owner:ANSTEEL GRP MINING CO LTD

Magnetic renewable adsorbent for adsorbing gaseous zero-valent mercury and preparation method of magnetic renewable adsorbent

ActiveCN110801805AExcellent gaseous zero-valent mercury adsorption performanceStrong magneticGas treatmentOther chemical processesPhosphomolybdic acidSorbent
The invention discloses a magnetic renewable adsorbent for adsorbing gaseous zero-valent mercury and a preparation method of the magnetic renewable adsorbent, and belongs to the technical field of mercury adsorption. The adsorbent is formed by performing phosphomolybdic acid (HPMo) grafting on magnetite (Fe3O4) in a preparation process to form HPMo@Fe3O4, then performing high-temperature calcination to obtain MoO3@gamma-Fe2O3, and finally performing vulcanization modification. The phase change of maghemite is inhibited by a means of phosphomolybdic acid grafting, so as to improve the thermal stability of maghemite, and the magnetic property of maghemite is improved; meanwhile, the zero-valent mercury adsorption capacity of the phosphomolybdic acid grafted maghemite is improved by controlling the vulcanization effect of the surface of the phosphomolybdic acid grafted maghemite, the magnetic adsorbent which has excellent low-temperature zero-valent mercury adsorption capacity and can berecycled is prepared, and the magnetic adsorbent can be suitable for being combined with a wet-type electric precipitator to control mercury pollution of a coal-fired power plant in a centralized mode.
Owner:JIANGNAN UNIV

High-yield two-product mixed maghemite beneficiation process

The invention relates to a high-yield two-product mixed maghemite beneficiation process. The high-yield two-product mixed maghemite beneficiation process comprises three-section breakage including coarse breaking, medium breaking and fine breaking on mixed maghemite, and is characterized by further comprising the following steps: sieving operation, a one-section closed circuit grinding operation implemented by a one-section ball-milling-cyclone, primary beneficiation operation, coarse and fine classification operation, reselection operation, secondary magnetic separation operation and centrifuging operation; a primary magnetic separation operation sieve treats overflow products of one-section closed circuit grinding operation, sieving operation and undersizes, the coarse and fine classification operation treats bulk concentrate obtained by primary beneficiation, the reselection operation treats coarse grain products of the coarse and fine classification operation, the secondary beneficiation operation treats coarse particle products of the coarse and fine classification operation, and the centrifuging operation treats bulk concentrates of secondary weak magnetic separation. The high-yield two-product mixed maghemite beneficiation process has the advantages that iron ore concentrates I with grade being 62% for pelletizing raw materials and iron ore concentrates II with grade being 58% for sintered raw materials can be selected out.
Owner:MCC NORTH (DALIAN) ENG TECH CO LTD

Chinese chestnut shaped ferric oxide shell structure magnetic absorbent particle and preparation method thereof

The invention relates to a Chinese chestnut shaped ferric oxide shell structure magnetic absorbent particle as a water treatment agent for absorbing high-toxicity heavy metal ions and a preparation method thereof. The Chinese chestnut shaped ferric oxide shell structure magnetic absorbent particle is characterized in that the inside is of a porous structure formed by amorphous ferric oxide nano particles, and a shell is formed in a manner that a plurality of crystallized maghemite nano bars vertical grow on the amorphous ferric oxide nano particles. The preparation method comprises the steps of: mixing chloride, Fe(CO)5 and N,N-dimethylformamide according to the proportion of (0.01-1.6)mmol:0.50mL:(10-160)mL, and stirring to obtain a solution; and transferring the solution to an agitated reactor, heating at a temperature of 160-220 DEG C for 1-32h, and cooling to room temperature; collecting a brown settlement, cleaning and drying in vacuum to obtain the Chinese chestnut shaped ferric oxide shell structure magnetic absorbent particle. The invention has the advantages of simple synthesis method and mild reaction condition. The Chinese chestnut shaped ferric oxide shell structure magnetic absorbent particle has stronger absorbing capacity to heavy metal ions in water.
Owner:WUHAN UNIV OF TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products