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105 results about "Methyl lactate" patented technology

Methyl lactate, also known as lactic acid methyl ester, is a monobasic ester formed from lactic acid and methanol, commonly used as a solvent. Methyl lactate belongs to the lactate ester group of compounds that are considered nontoxic and highly and readily biodegradable.

Method for fine purification of lactic acid

The invention relates to a method for refining lactic acid by cation resin column bed catalysis and reactive rectification technology. The method solves the problems that the traditional esterification-hydrolysis technology uses concentrated sulfuric acid as a catalyst, thereby causing the environmental pollution, and high energy consumption, etc. Crude lactic acid after the pretreatment and concentration is subjected to the esterification reaction with methanol or ethanol by a cation resin column; then a mixture after the esterification reaction is subjected to reduced pressure distillation to obtain a mixture A of methyl lactate or ethyl ester, the methanol or the ethanol, water and the like and a distillation residue B; and B is mixed with the methanol or the ethanol and introduced into the cation resin column to take the esterification reaction. Subsequently, A is mixed with deionized water and introduced into the other cation resin column to be hydrolyzed to obtain a hydrolysis mixture C. The hydrolysis mixture C is introduced into a reaction rectifying tower to continue hydrolysis, the methanol or the ethanol is eluted from the top of the tower, lactic acid aqueous solution is obtained from a reboiler, and a high purity lactic acid product is obtained after concentration and can reach (Chinese and American) pharmacopoeia grade standard.
Owner:HEFEI UNIV OF TECH

Method for preparing ester by catalytic oxidization of 1,3-propanediol

The invention discloses a method for preparing an ester by catalytic oxidization of 1,3-propanediol. The catalyst adopted is a supported noble metal catalyst (gold or palladium); a carrier is made from metal oxides of different shapes and sizes or mixed oxides (such as CeO2, gamma-Al2O3, CuO, MgO, ZnO, ZSM-5, MoO3, V2O5 and the like), or a silicon dioxide-containing material or a carbon material; after the catalyst is treated by different preparation and treatment methods, the selective oxidization reaction of the 1,3-propanediol for preparing 3-methyl lactate, dimethyl malenate, 3-methoxypropionate and methyl acrylate is performed under a mild liquid-phase or liquid- and gas-phase reaction condition. The highest yield of the produced 3-methyl lactate is 81.5 percent (the conversion rate is 97.0 percent and the selectivity is 84.0 percent); the highest yield of the produced dimethyl malenate is 58.2 percent ( the conversion rate is 99.6 percent and the selectivity is 58.4 percent); and the highest yield of produced 3-methoxypropionate is 53.0 percent (the conversion rate is 97.0 percent and the selectivity is 58.4 percent) and the highest yield of produced methyl acrylate is 38.4 percent (the conversion rate is 92.2 percent and the selectivity is 41.6 percent).
Owner:QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI

Second-stage reaction process for preparing propenoic acid or ester from lactic acid or ester

The invention relates to a two-section reaction method for preparing acrylic acid or propylene ester by lactic acid or lactic ester, belonging to the biological matrix chemical product field. A two-stage vertical type fixed bed reactor is adopted; a front part of an upper-section reactor is connected with a material carburetor; a lower-section reactor is connected with a gas-liquid separator; catalyzers A,B,C and D are adopted, wherein, the catalyzer A is an X-type molecular sieve; a NaY-type molecular sieve is roasted, subject to ion exchange by a potassium nitrate solution to prepare the catalyzer B; a nitrate solution and sodium phosphate are used to prepare phosphate as the catalyzer C; and a mixture of CaSO4 and CuSO4 and phosphate are mixed to prepare the catalyzer D; the catalyzer A or B is positioned in the upper-section reactor; the catalyzer C or D is positioned in the lower-section reactor; air in the reactors is exhausted by nitrogen; the nitrogen flow speed is between 5 and 100 ml / min; the temperature of the carburetor is 235 DEG C; the upper-section reaction temperature is between 275 and 350 DEG C; the lower-section reaction temperature is between 350 and 450 DEG C; and a condensed liquid of the gas-liquid separator is kept at a temperature of 2 DEG C; after the temperature is stabilized, raw material is pumped to the carburetor; the raw material is an aqueous solution of the ethyl lactate and the methyl lactate or a lactic acid aqueous solution added with a polymerization inhibitor of 0.5 percent of the raw material mass; and the sampling speed of the raw material is between 0.5 and 2 ml / h. The method develops the advantages of different catalyzers and improves the selectivity of a target product.
Owner:BEIJING UNIV OF CHEM TECH

Synthesis method of high-purity D-2-chloropropionyl chloride

The invention provides a synthesis method of high-purity D-2-chloropropionyl chloride. A process path of chlorination, hydrolysis and chloroacylation of L-methyl lactate is adopted. Specifically, the synthesis method sequentially comprises the following steps: (1) the synthesis of D-methyl-2-chloropropionate: dropwise adding thionyl chloride into the mixed solution of the L-methyl lactate and pyridine, carrying out vacuum stirring, increasing the temperature to 55-90 DEG C, reacting for 1-5h, reducing the temperature to 25-35 DEG C, exhausting air, washing and separating, wherein the L-methyl lactate and the thionyl chloride are used as raw materials and the pyridine is used as a catalyst; (2) the synthesis of D-2-chloropropionic acid: hydrolyzing methyl-2-chloropropionate under the action of a sodium hydroxide solution, and carrying out chloroform extraction; and (3) the synthesis of D-2-chloropropionyl chloride: dropwise adding the thionyl chloride into the mixed solution of D-2-chloropropionic acid and the catalyst, increasing the temperature to 70-80 DEG C, reacting for 3-5 hours, and carrying out vacuum rectification to obtain a target product. The process path has the advantages that raw materials are easily available; synthesis steps are simple, safe and reliable; the waste gas generated in the production can be easily disposed; therefore, the process path is suitable for industrial production.
Owner:SHANDONG JINCHENG PHARMACEUTICAL GROUP CO LTD

Method for preparing methyl lactate through supported nickel oxide catalyzed monosaccharide conversion in near critical methanol medium

The invention discloses a method for preparing methyl lactate through supported nickel oxide catalyzed monosaccharide conversion in a near critical methanol medium. The method comprises the following steps: 1, adding monosaccharide, methanol and a supported nickel oxide catalyst to a high-temperature and high-pressure reaction kettle with a stirring function, wherein the monosaccharide is five-membered sugar, six-membered sugar or a five-membered sugar and six-membered sugar mixture; 2, starting stirring, heating above added materials to 140-240DEG C, and reacting the materials for 1-12h; and 3, cooling a material obtained after the reaction ends to room temperature, filtering the cooled material, rectifying the obtained filtrate to obtain a methyl lactate product and methanol for reuse, washing filter residues containing the catalyst with methanol, and drying the catalyst for reuse. The method for preparing methyl lactate through monosaccharide conversion has the advantages of high raw material utilization rate, high methyl lactate yield, and great reduction of the separation cost, low price and good reusability of the catalyst supported nickel oxide, good mass transfer performance of the near critical methanol used as a solvent and a reactant, greenness and good industrial application prospect.
Owner:ZHEJIANG UNIV

Process for preparing L- (+) -lactic acid

The present invention provides a commercially viable process for the preparation of highly pure and optically active L-(+)-lactic acid and S-(−)-methyl lactate, in high yield, obtained from esterification of aqueous crude lactic acid solution produced by sugar cane juice fermentation broth and methanol in continuous counter current trickle phase approach or in continuous counter current bubble column manner, using stabilizers and the methyl lactate so obtained is recovered and followed by purification of reasonably pure methyl lactate using reagent mixture such as sodium bi-carbonate, mono-ethanolamine or di-ethanolamine, urea or sodium-bicarbonate, mono-ethanolamine or di-ethanolamine, thiourea to reduce the impurity of dimethyl ester of dicarboxylic such as dimethyl oxalate or di-methyl succinate or methyl ester of mono-carboxylic acid such as methyl pyruvate present as an impurity, so as to get highly pure S-(−)-methyl lactate followed by hydrolyzing highly pure S-(−)-methyl lactate using highly pure lactic acid as a catalyst, using highly pure water as the hydrolysis media and by using pre-treated activated carbon with dilute L-(+)-lactic acid, in batch or continuous mode. This very high pure S-(−)-methyl lactate constitutes an important product having interesting possibilities of application at an industrial level, in pharmaceuticals. Highly pure L-(+)-lactic acid thus obtained is used as an acidulant, as a food additive, for pharmaceutical applications, a monomer for making poly-lactic acid, as a monomer to prepare biodegradable polymer which are useful for manufacturing bags, application films, in the field of sanitary field, and has medical applications.
Owner:COUNCIL OF SCI & IND RES
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