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124results about How to "High reaction safety" patented technology

Preparation method of silica aerogel under atmospheric pressure

The invention discloses a method for preparing super-hydrophobic silica aerogel by atmospheric pressure drying. The method comprises the following steps: 1) preparing sol; 2) gelatinizing the sol; 3)aging gel; 4) exchanging a gel solvent; 5) carrying out surface hydrophobic modification; and 6) carrying out drying under atmospheric pressure. According to the preparation method of the silica aerogel, provided by the invention, tetraethoxysilane is used as a silicon source, ethanol is used as a solvent, acid and alkali are used as catalysts, and trimethylchlorosilane is used as a surface modifier, so that super-hydrophobic silica aerogel is prepared by atmospheric pressure drying. The prepared SiO2 aerogel with a super-hydrophobic three-dimensional network structure is tested to have a highspecific surface area, low density and good hydrophobicity at a room temperature. Therefore, the silica aerogel prepared through the method provided by the invention has excellent adsorption performance and has a good application prospect in the field of energy conservation. The preparation method of the silica aerogel under atmospheric pressure, provided by the invention, is simple in procedureand low in equipment requirements, can also shorten the process flow and reduce the cost, and is easy to industrialize.
Owner:ZHEJIANG UNIV OF TECH

Catalyst with ruthenium-loaded titanium dioxide hollow spheres embedded with silicon dioxide nanoparticles and preparation method and application of catalyst

The invention discloses a catalyst with ruthenium-loaded titanium dioxide hollow spheres embedded with silicon dioxide nanoparticles and a preparation method and application of the catalyst. The preparation method includes: using tetraethyl silicate as the raw material to prepare silicon dioxide microspheres; using titanium tetraisopropanolate to wrap the silicon dioxide microspheres with a layerof titanium dioxide and surfactant hexadecylamine, processing the product in an ammonia water solution through a hydrothermal method to partially etch the silicon dioxide microspheres inside so as toform cavities between the shell titanium dioxide and the inside silicon dioxide, and calcining under certain temperature and removing the surfactant to form crystal-form titanium dioxide; using a deposition-precipitation method to load precious metal ruthenium of different content. The catalyst has a special mesoporous spherical structure and large specific surface area and has high conversion rate and selectivity to guaiacol and other biomass phenol hydrogenation. The preparation method is easy to operate, simple in production process, low in equipment requirement and promising in industrialapplication prospect.
Owner:ZHEJIANG UNIV OF TECH

Industrial method for realizing direct ECH (epichlorohydrin) continuous production by phase transfer catalyst

The invention relates to the field of ECH (epichlorohydrin) production, in particular to an industrial method for realizing direct ECH continuous production by a phase transfer catalyst. The industrial method comprises the following steps: chloropropene and the catalyst are mixed in a mixing tank, and the mixture is mixed with another strand of raw material hydrogen peroxide for reaction in multistage tubular reactors. A mixer is arranged in the front of each tubular reactor, a buffer tank is arranged at the back of each tubular reactor, nitrogen is introduced in the buffer tanks, a gas phaseof the buffer tanks is condensed by a condenser, a liquid phase flows back, the gas phase enters a washing tower, one liquid phase of the buffer tank flows back and the other enters the next buffer tank to repeat the reaction process; part of the liquid phase flowing out of the last buffer tank flows back and the other part enters a separation system for separation. The design is ingenious, the multistage tubular reactors substitute for an agitator type reactor, reaction materials form turbulent flow and are mixed uniformly by a reflux pump instead of stirring by the agitator type reactor, sothat the reaction is safe and stable, and the operation cost is saved. The method has potential market value.
Owner:山东凯泰科技股份有限公司

Device and method for synthesizing bi(trichloromethyl) carbonic ester

The invention discloses a device for synthesizing bi(trichloromethyl) carbonic ester. The device comprises a liquid chlorine gasifier, a dimethyl carbonate gasifier, a heat exchanger, a tubular reactor, a gas storage tank, a stirring kettle, a flaker and the like. The invention further discloses a method for synthesizing the bi(trichloromethyl) carbonic ester. The method comprises the following steps: mixing chlorine with gasified dimethyl carbonate in a mole ratio of (5-7):1, performing heat exchange so as to obtain mixed gas phase, feeding the mixed gas phase into the tubular reactor filled with a solid catalyst, keeping reaction temperature to be 90-100 DEG C and the pressure to be 0.1-0.15Mpa, and performing reaction for 5-10 minutes; recycling unreacted chlorine for circulation use; performing flash evaporation, and performing flaking molding, so as to obtain the bi(trichloromethyl) carbonic ester. By adopting the method for synthesizing the bi(trichloromethyl) carbonic ester, the use amount of the chlorine can be reduced, the reaction time can be shortened, the equipment security can be improved, the reaction efficiency is high, continuous reaction can be achieved, the product yield can be greatly increased, and the dimethyl carbonate conversion rate can be greatly increased.
Owner:SHANDONG DEPU CHEM IND SCI & TECH

Method for continuous production of propylene oxide by direct oxidation of propylene with hydrogen peroxide through tubular reactors

The invention relates to the field of petrochemical industry, in particular to a method for continuous production of propylene oxide by direct oxidation of propylene with hydrogen peroxide through tubular reactors. The method comprises the steps: a catalyst, namely phosphotungstic acid quaternary ammonium salt is mixed with the hydrogen peroxide and an organic solvent, and the mixture is subjectedto azeotropic dehydration and then sequentially reacts through the multi-stage tubular reactors which are connected in series; and a raw material, namely the liquid propylene is divided into multiplestrands to be parallelly added into all the stages of tubular reactors, reacting mixed liquid flowing out from the tubular reactor of the last stage enters a tower reactor, and after reacting of thereacting mixed liquid in the tower reactor is completed, the reacting mixed liquid enters a separating system. The design is ingenious, through combination of the tubular reactors and the tower reactor and reasonable control over the reacting temperature and the reacting pressure, the atmosphere needing to be protected by N2 in the reactors in a laboratory process is omitted, and condensation filter tower devices which are additionally arranged in the reactors because of protection of the N2 and control over the oxygen content are omitted; the equipment investment and the tail gas treatment cost are saved greatly, tail gas emission of the reactors is less, and thus pollution to the environment is less; and the method has potential market value.
Owner:山东凯泰科技股份有限公司

Method for preparing diisobutylphosphine from liquid hydrogen phosphide

The invention relates to a method for preparing diisobutylphosphine from liquid phosphine, which comprises the following steps: adding low-temperature liquid phosphine and liquid isobutene into a reaction kettle in sequence, uniformly mixing, heating to a target reaction temperature, slowly dropwise adding an initiator solution into the reaction kettle through a diaphragm metering pump, and initiating free radical addition reaction; and after the reaction is finished, carrying out rectification separation on the obtained reaction product to obtain the target product diisobutylphosphine. The method not only improves the purity of the sodium hypophosphite byproduct phosphine as a raw material, but also creates conditions for low-pressure feeding of liquid phosphine and isobutene; purified liquid phosphine is used as a raw material, liquid-phase uniform mixing reaction of phosphine and isobutene is achieved, large-amount use of organic reaction solvents such as methylbenzene is avoided, and reaction efficiency is improved; meanwhile, compared with a hydrogen phosphide gas compression method, the reaction pressure of the system is reduced, and the reaction safety is improved. In addition, an addition reaction byproduct is selected as the initiator solvent, no new solvent substance is introduced into the system, and separation and recovery of the initiator solvent are avoided.
Owner:HUBEI XINGFA CHEM GRP CO LTD

Compound stabilizer for epoxidation reaction of unsaturated compound and application method thereof

The invention discloses a compound stabilizer for the epoxidation reaction of an unsaturated compound and an application method of the compound stabilizer. The compound stabilizer comprises carbamide, ethylene diamine tetraacetic acid, potassium sodium tartrate and sodium silicate. Peroxide and a peroxoic acid stabilizer including the ethylene diamine tetraacetic acid, the potassium sodium tartrate, concentrated sulfuric acid and 732 resin are uniformly mixed; the addition of the peroxoic acid stabilizer is 0.1 to 5 wt% of that of the peroxide; organic acid is dropwise added to the peroxide and the peroxoic acid stabilizer at 25 to 35 DEG C, so that peroxoic acid mixed solution is obtained after reaction; an epoxidation stabilizer including the carbamide, the ethylene diamine tetraacetic acid, and the potassium sodium tartrate and the sodium silicate is added into the unsaturated compound, and then the peroxoic acid mixed solution is added into the epoxidation stabilizer at 65 to 95 DEG C, so that an epoxidation compound is obtained after epoxidation reaction. The compound stabilizer has the advantages that the coordination of various stabilizers improves the stability of hydrogen peroxide and peroxoic acid in reaction solution, the frequency of the occurrence of secondary reaction is reduced, the reaction time is shortened, and the production cost is reduced.
Owner:甄曰菊
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