Process for the preparation of alkylene glycol
View Patent ↗The invention provides a process and a reactor for the preparation of an alkylene glycol from an alkylene oxide. Alkylene oxide, water, a homogeneous carboxylation catalyst and a homogenous hydrolysis catalyst are supplied to a reactor comprising a carboxylation zone and a hydrolysis zone. One or more ejectors are used to mix carbon dioxide and the liquid reagents in the carboxylation zone so that alkylene oxide reacts with carbon dioxide in the presence of water in the carboxylation zone to form a reaction solution comprising alkylene carbonate, water, the homogeneous carboxylation catalyst and the homogeneous hydrolysis catalyst. The reaction solution is supplied from the carboxylation zone to a hydrolysis zone, wherein alkylene carbonate and water react to form a product solution comprising alkylene glycol, the homogeneous carboxylation catalyst and the homogeneous hydrolysis catalyst. Carbon dioxide released by the reaction of alkylene carbonate and water in the hydrolysis zone is supplied to the carboxylation zone. Product solution is withdrawn from the hydrolysis zone.
1. A process for the preparation of an alkylene glycol from an alkylene oxide, comprising steps of
(a) supplying alkylene oxide, water, a homogeneous carboxylation catalyst and a homogeneous hydrolysis catalyst as liquid reagents to a carboxylation zone of a reactor,
(b) using one or more ejectors to mix carbon dioxide and the liquid reagents in the carboxylation zone so that alkylene oxide reacts with carbon dioxide in the presence of water to form a reaction solution comprising alkylene carbonate, water, the homogeneous carboxylation catalyst and the homogeneous hydrolysis catalyst;
(c) supplying the reaction solution from the carboxylation zone to a hydrolysis zone of a reactor, wherein alkylene carbonate and water react to form a product solution comprising alkylene glycol, the homogeneous carboxylation catalyst and the homogeneous hydrolysis catalyst;
(d) supplying carbon dioxide released by the reaction of alkylene carbonate and water in the hydrolysis zone to the carboxylation zone; and
(e) withdrawing the product solution from the hydrolysis zone.
2. A process according to claim 1 , wherein the carboxylation zone and the hydrolysis zone are contained within one reactor vessel.
3. A process according to claim 2 , wherein the single reactor vessel is divided into at least four compartments by internal baffles.
4. A process according to claim 1 , wherein the reactor comprises at least one recycle loop whereby liquid reagents are withdrawn from the carboxylation zone and subsequently returned to the carboxylation zone.
5. A process according to claim 1 , wherein carbon dioxide is supplied from the hydrolysis zone to the carboxylation zone without passing through a gas compressor.
6. A process according to claim 1 , wherein the hydrolysis zone comprises one or more inlets whereby steam is supplied to the hydrolysis zone, and the hydrolysis zone comprises one or more inlets whereby carboxylation catalyst and hydrolysis catalyst (in addition to the catalysts supplied in the reaction solution) are supplied to the hydrolysis zone.
7. A process according to claim 1 , wherein either the carboxylation zone or the hydrolysis zone has an inerts vent whereby gases are withdrawn.
8. A process according to claim 1 , wherein carbon dioxide is supplied from the hydrolysis zone to the carboxylation zone via an opening in a baffle separating the gas phase of the carboxylation zone from the gas phase of the hydrolysis zone, or wherein carbon dioxide is supplied from the hydrolysis zone to the carboxylation zone via external piping connecting the hydrolysis zone and the carboxylation zone.
9. A process according to claim 1 , wherein the carboxylation and hydrolysis catalysts are separated from the product stream by subjecting the product stream to a flash step in a flash vessel and a solution of the carboxylation and hydrolysis catalysts is recycled and supplied to the carboxylation zone.