Processes for purifying acetic anhydride
AssigneeCelanese International Corporation
InventorsR. Jay Warner, Melchoir Meilchen, Nathan Kirk Powell
Life of this patent
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Abstract
In one embodiment, the invention is to a process for purifying acetic anhydride. The process includes the steps of feeding a liquid crude acetic anhydride stream directly to a distillation column and separating the liquid crude acetic anhydride stream to produce a light ends stream, a sidedraw and a residue stream. The sidedraw comprises substantially pure acetic anhydride product. The distillation column is operated at a pressure less than 101 kPa. The substantially pure acetic anhydride product comprises greater than 98 wt. % acetic anhydride, has a permanganate time of greater than 10 minutes, and has an APHA color of less than 10.
Claims28
A process for purifying acetic anhydride comprising the steps of:
- feeding a liquid crude acetic anhydride stream directly to a distillation column;
- and
- separating the liquid crude acetic anhydride stream to produce a light ends stream, a sidedraw comprising substantially pure acetic anhydride product, and a residue stream,
- wherein the distillation column operates at a pressure less than 101 kPa,
- wherein the substantially pure acetic anhydride product comprises greater than 98 wt. % acetic anhydride, has a permanganate time of greater than 10 minutes, and has an APHA color of less than 10.
A process for producing acetic anhydride comprising the steps of:
- contacting ketene gas with acetic acid in an absorber column to produce a liquid crude acetic anhydride stream and a residual ketene stream;
- feeding the liquid crude acetic anhydride stream directly to a distillation column;
- and
- purifying the liquid crude acetic anhydride stream to produce a light ends stream, a substantially pure acetic anhydride product stream, and a residue stream,
- wherein the substantially pure acetic anhydride product stream is withdrawn from the distillation column as a sidedraw,
- wherein the distillation column is operated at a pressure ranging from 20 kPa to 101 kPa,
- wherein the substantially pure acetic anhydride product stream comprises greater than 98 wt. % acetic anhydride, has a permanganate time greater than 10 minutes, and has an APHA color number of less than 10.
A process for purifying acetic anhydride comprising the steps of:
- feeding a liquid crude acetic anhydride stream directly to a distillation column;
- and
- separating the liquid crude acetic anhydride stream to produce a light ends stream, a sidedraw comprising substantially pure acetic anhydride product, and a residue stream,
- wherein the distillation column operates at a pressure less than 101 kPa and at a temperature less than 150° C.,
- wherein the substantially pure acetic anhydride product comprises greater than 98 wt. % acetic anhydride and has an APHA color of less than 10.
Dependencies are inferred from the claim text.