Recovery and purification of ethylene
AssigneeIneos USA LLC
InventorsRian Reyneke, Michael Foral, Guang-Chung Lee, Wayne Eng, Iain Sinclair, Jeffery Logsdon
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Abstract
A process for the recovery and purification of ethylene and optionally propylene from a stream containing lighter and heavier components that employs an ethylene distributor column and a partially thermally coupled distributed distillation system.
Claims37
a process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, and optionally components heavier than ethane, comprising:
- a. directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen and methane and a first bottoms stream comprising components heavier than ethane;
- b. removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;
- c. directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor vapor overhead stream comprising ethylene, methane and hydrogen and substantially free of ethane, and an ethylene distributor bottoms stream comprising ethylene and ethane;
- d. separating the ethylene distributor overhead vapor stream into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethylene distributor overhead vapor stream;
- e. directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;
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- f. recovering a purified ethylene product from the ethylene distributor bottoms stream.
The process of claim I wherein at least a portion of the stripping vapor for the first distillation column, the ethylene distributor distillation column, and the demethanizer distillation column is provided by the vaporization of at least a part of the respective column bottoms liquid streams in a reboiler exchanger.
A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:
- a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;
- b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;
- c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;
- d) separating the ethane-free vapor stream of step (c) into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c);
- e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;
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- f) recovering a second purified ethylene product from the first and second liquid streams of step (c).
Dependencies are inferred from the claim text.