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68 results about "Isopropenyl acetate" patented technology

Isopropenyl acetate is an organic compound, which is the acetate ester of the enol tautomer of acetone. This colorless liquid is significant commercially as the principal precursor to acetylacetone. In organic synthesis, it is used to prepare enol acetates of ketones and acetonides from diols.

Synthesis process of vecuronium bromide

The invention discloses a synthesis process of vecuronium bromide. The synthesis process comprises the following steps: generating epiandrosterone sulfonyl ester (III) by carrying out esterification reaction between epiandrosterone (II) and paratoluensulfonylchloride; generating 5Alpha-androst-2-alkene-17-ketone (IV) by carrying out elimination and dehydration reaction between the (III) and 2,6-lutidines; generating 17-acetoxyl-5Alpha-androstane-2,16-diene (V) by carrying out enolization and esterification reaction between the (IV) and isopropenyl acetate; generating (2Alpha, 3Alpha, 16Alpha,17Alpha)-diepoxy-17Beta-acetyl-5Alpha-androstane (VI) by epoxy reaction of the (V) under the effect of hydrogen peroxide; generating 2Beta, 16Beta-di(1-piperidyl)-5Alpha-androstane-3Alpha-hydroxyl-17-ketone (VII) by ring-opening and addition reaction of the (VI) under the effect of hexahydropyridine; generating 2Beta, 16Beta-di(1-piperidyl)-5Alpha-androstane-3Alpha,17Beta-diol (VIII) by the (VII)under the reduction of potassium borohydride; generating 2Beta, 16Beta-di(1-piperidyl)-3Alpha, 17Beta- acetoxyl-5Alpha-androstane (IX) by carrying out esterification reaction of the (VIII) under the acetylation of acetic anhydride; and generating vecuronium bromide (I) by carrying out quaternary ammonium salt reaction between the (IX) and bromomethane. The invention has the advantages of low cost,less pollution and high yield.
Owner:XUZHOU NORMAL UNIVERSITY

Liquid glue stopper for handling borehole wall collapsing

The invention relates to a liquid glue stopper for handling borehole wall collapsing. The liquid glue stopper comprises, by weight, 200 parts of main agent A, 1-10 parts of activating agent B and 750 parts of water, and preferably, the liquid glue stopper comprises, by weight, 200 parts of main agent A, 5 parts of activating agent B and 750 parts of water. The main agent A is composed of, by weight, 8 parts of acrylamide, 1 part of n-butyl acetate and 1 part of isopropenyl acetate. The activating agent B is composed of, by weight, 7 parts of methanal and 3 parts of phenolic resin. The liquid glue stopper is prepared through the cross-linking reaction of the main agent A and the activating agent B, and the cross-linking time is 5-90 minutes. The liquid glue stopper further comprises a gel breaker C of ammonium persulfate, and the liquid glue stopper comprises, by weight, 200 parts of main agent A, 1-10 parts of activating agent B, 0.4-1.2 parts of gel breaker C and 750 parts of water. The liquid glue stopper is large in hardness and capable of bearing construction with the 40 MPa pressure difference and withstanding the temperature of 150 DEG C. Permanent leaking stoppage can be achieved without adding the gel breaker in the liquid glue stopper, self-gel breaking can be achieved when the gel breaker is added, flowback of the liquid glue stopper is promoted, and pollution to stratums is avoided.
Owner:CHINA PETROLEUM & CHEM CORP

High-efficiency energy-saving preparation method and preparation device of acetylacetone

ActiveCN103333063AImproved Absorption Esterification Production MethodIncrease productivityOrganic compound preparationChemical industryIsomerizationDistillation
The invention relates to a preparation method of a chemical or medical intermediate, and in particular relates to a high-efficiency energy-saving preparation method and preparation device of acetylacetone. The method sequentially comprises the steps of: adding acetone and introducing ketene simultaneously, proceeding with the reaction through continuously introducing isopropenyl acetate esterification liquid, continuously discharging the isopropenyl acetate esterification liquid to a simple distillation still, continuously distilling off mixed vapor containing the acetone and isopropenyl acetate, enabling the simply distilled mixed gas to enter an acetone recycling tower, carrying out rectification, recycling the acetone, enabling tower bottoms of the acetone recycling tower to enter an isopropenyl acetate rectifying tower, carrying out rectification, enabling the isopropenyl acetate gas from the tower top to enter into a transposition process after passing through a heat exchanger, carry out an isomerization reaction, enabling the produced transposition mixed gas to enter an end product rectifying tower after exchanging heat with the isopropenyl acetate gas, carrying out rectification and obtaining end products of the acetylacetone. The method has the advantages of realizing the continuous production, greatly reducing the energy consumption, reducing the production cost and achieving the effects of energy conservation and emission reduction.
Owner:JILIN BEISHA PHARMA

Process for preparing acetylacetone by conversion of isopropenyl acetate and special-purpose equipment thereof

The invention discloses a process for preparing acetylacetone by transforming acetic acid propylene and comprises the following steps of: steaming the acetic acid propylene into gas by a vaporizer; then, putting the gas to a first-way carrier gas and/or using a self heat interchanger, then leading the gas come into a reformer to get reforming gas, and finally cooling down the reforming gas. The invention also discloses a special device for the process. In the process for preparing acetylacetone by transforming acetic acidpropylene, the flow quantity of carrier gas can be adjusted according to the different inventory ratings, thereby reaching to the optimal residence time, greatly reducing carbon deposition and prolonging carbon blowing period, realizing optimal conversion rate and selectivity, and having large work condition operation window. The self heat interchanger can save energy, realize precise temperature raising in section, and raising the selectivity and yield of the transformation reaction. The combination of using the first-way carrier gas and the self heat interchanger, which are cooperated to work, can raise reaction selectivity and yield, and increase the operation flexibility in the best working conditions.
Owner:SHANGHAI WUJING CHEM

Preparation method of DHEA (dehydroepiandrosterone) intermediate 3 beta- acetoxyl- androstane-3, 5- diene-17-ketone

ActiveCN103694296AReduce manufacturing costFacilitate the implementation of large-scale industrial productionSteroidsPtru catalystIsopropenyl acetate
The invention discloses a preparation method of DHEA (dehydroepiandrosterone) intermediate 3 beta-acetoxyl-androstane-3,5-diene-17-ketone. The preparation method is characterized in that esterification reaction reagent is isopropenyl acetate. The preparation method comprise the following steps of dissolving 1W of 4AD (4-androstenediol) into 3-8V of organic solvent, wherein W is weight g, and V is volume ml; adding 1-5w% strong acidic catalyst, stirring and heating up to the reaction temperature of 40-80 DEG C; dripping 0.5-1.2 V of isopropenyl acetate, preserving heat and reacting for 1-2 hours after dripping, until displaying completion of reaction of raw materials by TLC (Thin Layer Chromatography); adding 2-6% V triethylamine for neutralization after reaction, and concentrating the solvent to dry; adding 1V of methyl alcohol, dissolving while stirring, cooling to crystallize for 2-3 hours, filtering, performing solvent washing, and baking to dry below 70 DEG C, thereby obtaining the DHEA intermediate 3 beta- acetoxyl- androstane-3, 5- diene-17-ketone. The DHEA intermediate prepared by the invention has high yield, high purity and steady mass, and can be baked under normal pressure; more importantly, solvent recovery rate is high, and the preparation method almost produces no wastewater, is economic and environmental friendly, and is very beneficial to industrial production.
Owner:HUNAN KEREY BIOTECH

Method for refining acetylacetone

A method for refining high-purity acetylacetone comprises procedures of devolatiligation, deacidification and deanhydride to coarse acetylacetone which later on enters a refining tower T1. The method is characterized in that the refining tower T1 is a pressure relief refining tower, the high-purity acetylacetone is extracted from the upper side line of the rectification section in liquid phase, acetone generated by the decomposition of acetylacetone and low-boiling mixed components, such as isopropenyl acetate, which are not completely removed due to instability of the initial stage of the process, are collected at the top of the tower, returned to a coarse acetylacetone groove V1, placed in the refining tower T1 after the procedures of devolatiligation, deacidification and deanhydride, and the tower kettle uses high-boiling components. The invention has the advantages that the refining tower T1 has the function of removing a small mount of low-boiling components because of liquid phase side line discharge way thereof, meanwhile, the acetone and isopropenyl acetate obtained from the top of the tower can be recycled, and the tower kettle uses high-boiling components, so that the whole rectification section is easy to control, flexible in operation, high in purity of the finished products, and stable in mass content of 99.9%.
Owner:SHANGHAI WUJING CHEM +1
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