Abstract: Ethylene glycol and a carbonate ester are simultaneously produced by reacting ethylene oxide and carbon dioxide to form ethylene carbonate, hydrolyzing of the solution containing the ethylene carbonate to obtain ethylene glycol, purifying ethylene glycol, transesterifying ethylene carbonate and a hydroxyl group-containing compound to form the corresponding carbonate ester and ethylene glycol, separating the carbonate ester and separating ethylene carbonate.

Abstract: Ethylene glycol and a carbonate ester are simultaneously produced by reacting ethylene oxide and carbon dioxide to form ethylene carbonate, hydrolyzing of the solution containing the ethylene carbonate to obtain ethylene glycol, purifying ethylene glycol, transesterifying ethylene carbonate and a hydroxyl group-containing compound to form the corresponding carbonate ester and ethylene glycol, separating the carbonate ester and separating ethylene carbonate.

Abstract: A process for producing an alkylene glycol, which is a continuous process for producing an alkylene glycol comprising the following steps (1) to (4), wherein the hydrolysis step (2) is divided into a plurality of stages, and the hydrolysis is carried out so that the water concentration in a reaction stage wherein the conversion of the alkylene carbonate is at least 60%, is from 15 to 30 wt %: (1) a carbonating step of reacting an alkylene oxide with carbon dioxide gas in the presence of a carbonating catalyst to form a reaction solution containing an alkylene carbonate, (2) a hydrolysis step of hydrolyzing the reaction solution obtained in step (1) while releasing carbon dioxide gas, to form an aqueous alkylene glycol solution, (3) a distillation step of distilling the aqueous alkylene glycol solution to obtain at least a dehydrated alkylene glycol and a solution containing the carbonating catalyst, and (4) a recycling step of supplying the solution containing the carbonating catalyst to the carbonating s

Abstract: Disclosed is a method for producing monoethylene glycol, which is a method for producing ethylene glycol that comprises a carbonation step in which ethylene oxide is allowed to react with carbon dioxide in the presence of a carbonation catalyst thereby effecting formation of a reaction solution containing ethylene carbonate, a hydrolysis step in which the reaction solution is converted into an ethylene glycol aqueous solution by hydrolyzing ethylene carbonate in the reaction solution and a distillation step in which purified ethylene glycol and a catalyst solution containing the carbonation catalyst are obtained from the ethylene glycol aqueous solution by distillation, wherein the improvement resides in that the reaction is carried out in the presence of a carbonation catalyst using a bubble column reactor by supplying ethylene oxide, carbon dioxide and water into the reactor.

Abstract: The present invention relates to a process for producing ethylene glycol from ethylene oxide wherein ethylene oxide in a gas resulting from oxidation of ethylene is absorbed in a specific absorbing solution, is allowed to react with carbon dioxide, converted into ethylene carbonate, and then subjected to hydrolysis to produce ethylene glycol.According to the present invention, a large energy consuming step such as stripping of ethylene oxide and separation of excess amounts of water during the ethylene glycol production becomes unnecessary and the process can be greatly simplified by combining the ethylene oxide absorption step and the carbonation step.

Abstract: The present invention relates to a method of recovering ethylene oxide comprising the steps of:bringing a mixed gas containing ethylene oxide into contact with an absorbent so as to cause the absorbent to absorb the ethylene oxide; andstripping and separating said ethylene oxide to recover it from the absorbent, where the absorbent contains propylene carbonate. By employing the present invention, it is possible to reduce the heat recovery loss resulting from cooling the absorbent at the time of transfer from the stripping step to the absorption step, to about one-third that compared with a conventional system using water, without producing the by-product ethylene glycol.