FIELD: ethylene glycol production.
SUBSTANCE: present invention relates to a process for improving the production of an existing ethylene glycol production process. The process includes the following steps: (a) feeding the feed stream of the catalytic hydration tube reactor containing ethylene oxide and water to the non-catalytic glycol reactor; (b) interacting ethylene oxide and water in the non-catalytic glycol tube reactor to produce a product stream; (c) modifying the feed stream of the tube reactor as follows: producing a catalytic hydration feed stream, containing ethylene oxide and water; combining the catalytic hydration feed stream with the recycled split stream to form a first reactor inlet stream; feeding the inlet stream of the first reactor to the inlet of the first adiabatic reactor, where the inlet of the first adiabatic reactor has a first inlet temperature; reacting ethylene oxide and water in the presence of a first ion exchange resin catalyst in a first adiabatic reactor to produce an effluent containing water, ethylene glycol and unreacted ethylene oxide; further combining the effluent stream with the recirculated feed stream to form a combined stream containing water, ethylene glycol and unreacted ethylene oxide; feeding the combined stream to the inlet of the second adiabatic reactor, where the inlet of the second adiabatic reactor has a second inlet temperature; reacting ethylene oxide and water in the presence of a second ion exchange resin catalyst in a second adiabatic reactor to produce a second reactor effluent containing water, ethylene glycol and unreacted ethylene oxide; compressing the second effluent from the reactor; dividing the second reactor effluent into a recycle stream and a front stream; dividing the recirculated stream into a recirculated split stream and a feeding recirculated stream; feeding the front stream in the form of a tubular reactor feed stream to a non-catalytic tubular reactor to obtain a product stream in which the total concentration of diethylene glycol (DEG), triethylene glycol (TEG) and higher glycols in the product stream is higher than the total concentration of DEG, TEG and higher glycols in the front stream.
EFFECT: proposed method allows you to effectively and selectively obtain the target product.
13 cl, 1 dwg
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Authors
Dates
2023-05-22—Published
2019-04-30—Filed