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53 results about "Azoxymethane" patented technology

Azoxymethane (AOM) is a carcinogenic and neurotoxic chemical compound used in biological research. It is the oxide of azomethane and is particularly effective for the induction of a colon carcinoma.

Method for preparing diethoxymethane by using active carbon supported solid acid catalyst

The invention relates to a method for preparing diethoxymethane by using an active carbon supported solid acid catalyst. The method is characterized in that formaldehyde and ethanol are used as raw materials and reacted under normal pressure under the action of a solid acid catalyst at the temperature of 70 to 100 DEG C, the reflux ratio is controlled to be 1:1-4:1, distillate of 74 to 76 DEG C is collected on the top of a tower, and the diethoxymethane product is obtained; after the aqueous solution in a tower kettle is filtered, the solid acid catalyst is recycled in the kettle; the molar ratio of the formaldehyde to the ethanol is 1:2-1:5, the formaldehyde raw material is a formaldehyde solution at the concentration of over 37 weight percent, and the ethanol raw material is absolute ethanol or an ethanol solution at the concentration of 75-95 weight percent; the solid acid catalyst is the active carbon supported solid acid catalyst, the active acid ingredient is sulfuric acid, and the acid solid capacity is 15 to 25 mass percent; and the consumption of the solid acid catalyst is 0.3 to 10 percent of the total mass of the reactants. The method has the advantages that the catalyst is economic in preparation, easy to separate from the product and low in equipment corrosion, and the waste catalyst is easy and convenient to reclaim and treat.
Owner:NANJING FORESTRY UNIV +1

Continuous catalysis and rectification technology for synthesizing diethoxymethane

The invention discloses a continuous catalysis and rectification technology for synthesizing diethoxymethane. According to the invention, formaldehyde and ethanol are adopted as raw materials, and a two-stage linkage catalysis rectifying tower composed of a first-stage reaction rectifying tower and a second-stage reaction rectifying tower is employed. Solid acid catalysts are loaded in both the first-stage and the second-stage reaction rectifying towers. The technology comprises the steps that: (A) formaldehyde is delivered to the first-stage reaction rectifying tower, while ethanol is delivered to the second-stage reaction rectifying tower; (B) formaldehyde discharged from the bottom of the first-stage reaction rectifying tower is delivered to the second-stage reaction rectifying tower, where formaldehyde is subject to a reaction with ethanol; and waste water is discharged from the bottom of the second-stage reaction rectifying tower; (C) material obtained from the top of the second-stage reaction rectifying tower is delivered to the first-stage reaction rectifying tower, where the obtained material is subject to a reaction with formaldehyde; and diethoxymethane, which is a target product, is obtained from the top of the first-stage reaction rectifying tower; (D) the steps from (A) to (C) are repeatedly circulated. The technology has advantages of short processing period, high selectivity, high yield, high product purity, and simple operation. Therefore, the technology is suitable for continuous industrial production.
Owner:石家庄一科发化工科技有限公司

Method for separating diethoxymethane and ethanol by glycerol and water multi-stage countercurrent liquid-liquid extraction

The invention relates to a method for liquid-liquid extracting and separating diethoxymethane (DEM) and ethanol by adopting glycerin and water in a way of multi-stage counter current, comprising the steps: polylol and the water are taken as extracting agent for liquid-liquid extracting the DEM and the ethanol solution; after extraction and hierarchical separation, extract phase is processed by rectifying, and then solvent can be recycled; the faffinate contains over 99.7% of DEM. The method has the prioritization scheme that liquid-liquid extraction with multi-stage counter current is adopted; the raw material DEM and the ethanol solution are sent to an extracting tower and contacted with extracting agent propanetriol and water which flow into the extracting tower along the reverse direction, the faffinate passes through a static hierarchical section 2 (the liquid stops at the section for more than 10min), and the faffinate contains more than 99.7% of DEM; the mixed liquid of extracting agent at the bottom of the extracting tower is separated by a rectifying tower, and ethanol water solution can be obtained on the top of the rectifying tower. The method can effectively separate the DEM and the ethanol solution, and the purity and one-time yield of the DEM respectively reaches over 99.7% and 98% after separation.
Owner:NANJING NORMAL UNIVERSITY

Production method of dibutoxymethane, diethoxymethane, dipropoxymethane or dipentyloxymethane

The invention provides a production method of dibutoxymethane, diethoxymethane, dipropoxymethane or dipentyloxymethane. The production method comprises the following steps of 1, taking formaldehyde or a formaldehyde derivative, mixing the formaldehyde or formaldehyde derivative and an alcohol raw material, and pre-heating the mixture to a temperature of 70-160 DEG C, 2, feeding the pre-heated mixture into a reactor, adding an acid catalyst into the reactor, carrying out heating until an alcohol-acid condensation reaction occurs and the materials in the reactor vaporize, and 3, releasing the produced gas from the reactor, directly feeding the gas into a rectifying tower communicated with the reactor, carrying out rectification, and taking out the product on the bottom of the rectifying tower, wherein the internal pressure of the rectifying tower is less than zero. The production method only adopts a rectifying tower-based treatment process, does not additionally use a dehydrating agent, and can produce a dibutoxymethane equimolecular quantity conditioning agent having water content less than 100ppm and purity more than 95%. The production method has simple processes and short production time, obviously reduces energy consumption and is suitable for industrial production.
Owner:李云勇 +2

Method for preparing diethoxymethane by supported heteropolyacid catalyst

The invention relates to a method for preparing diethoxymethane, in particular to a method for for preparing diethoxymethane by a supported heteropolyacid catalyst. According to the method, dimethoxymethane and ethanol are taken as raw materials, liquid acid and supported liquid acid are taken as catalysts, the preparation method of the supported heteropolyacid catalyst, for example 33% of H3PW12O40/SiO2, comprises the following steps that a phosphotungstic acid aqueous solution with the concentration of 33% by mass is used, SiO2 is taken as a carrier, the impregnation liquid volume is the approximate to the pore volume, a catalyst sample is obtained after the phosphotungstic acid aqueous solution and the SiO2 are mixed uniformly and stood at the normal temperature by 10h, the sample is dried at the temperature of 120 DEG C, and calcination is performed at the temperature of 350 DEG C to obtain the 33% of H3PW12O40/SiO2 catalyst by the mass is prepared. According to the method, the product is relatively simple, the selectivity is high, and the method has an excellent application prospect. The raw materials required by the method are easy to obtain, the whole process operation is simple, at the same time, the method doesn't produce any chemical substances polluting the environment, and the method belongs to the environment-friendly technology route.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Device for recycling industrial grade diethoxymethane and method for recycling industrial grade diethoxymethane

The invention discloses a device for recycling industrial grade diethoxymethane and a method for recycling the industrial grade diethoxymethane, the device comprises an extraction conversion tower anda side line regeneration tower connected with the extraction conversion tower, and the extraction conversion tower comprises a liquid-liquid extraction device and a catalytic conversion device whichare integrally arranged up and down. The method is as follows: the industrial grade diethoxymethane and an extractant are added into the liquid-liquid extraction device for reaction, and then a mixedsolution containing the extractant is sent to the side line regeneration tower for reaction; the mixed solution containing the extractant obtained at the bottom of the side line regeneration tower iscirculated to the liquid-liquid extraction device, an ethanol mixed solution obtained at the top of the tower is circulated to the catalytic conversion device, and a mixture of a formaldehyde solutionand a catalyst is added to the catalytic conversion device for catalytic conversion reaction. The significant advantage of the device is that the device can not only effectively recycle the industrial grade diethoxymethane, but also realize catalytic conversion of ethanol; the process is simple and the environment is protected.
Owner:NANJING NORMAL UNIVERSITY
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