Calcium oxide or magnesium oxide production with alkali and sulfur dioxide intermediates
US-12017985-B2 · Jun 25, 2024 · US
US2017190650A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017190650-A1 |
| Application number | US-201615394365-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 29, 2016 |
| Priority date | Dec 31, 2015 |
| Publication date | Jul 6, 2017 |
| Grant date | — |
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A process for removing acetic acid from an aqueous stream containing yellow oil. According to the process, yellow oil is removed from the aqueous stream prior to the removal of acetic acid by a reverse osmosis membrane.
Opening claim text (preview).
1 . A process for recovering acetic acid from an aqueous stream, the process comprising: removing oily contaminants from the aqueous stream to form an effluent with a reduced concentration of oily contaminants; and removing acetic acid from the effluent by passing the effluent through a membrane separation zone. 2 . The process of claim 1 , wherein the membrane separation zone comprises at least one reverse osmosis membrane. 3 . The process of claim 1 , wherein the oily contaminants comprises polycyclic aromatic hydrocarbons and derivatives thereof. 4 . The process of claim 1 , wherein removing the oil contaminants comprises passing the aqueous stream through at least one oil absorbing material. 5 . The process of claim 1 , wherein removing the oily contaminants comprises passing the aqueous stream through at least two oil absorbing materials. 6 . The process of claim 4 , wherein the oil absorbing material comprises a curable polymeric surfactant. 7 . The process of claim 4 , wherein the oil absorbing material comprises activated charcoal. 8 . The process of claim 4 , wherein the oil absorbing material comprises walnut shells. 9 . The process of claim 4 , wherein the oil absorbing material comprises clay beds. 10 . The process of claim 1 , wherein removing the oily contaminants comprises removing at least 99 wt % of the oily contaminants in the aqueous stream. 11 . The process of claim 1 , the aqueous stream comprises terephthalic acid. 12 . The process of claim 1 , wherein the aqueous stream comprises paraxylene. 13 . The process of claim 1 , wherein the aqueous stream comprises methyl acetate. 14 . The process of claim 1 , wherein the aqueous stream comprises methyl hydroxide. 15 . The process of claim 1 , further comprising removing particulates from the water-containing stream prior to removing the oily contaminants. 16 . The process of claim 1 , further comprising: reacting a feed material comprising paraxylene with gaseous oxygen in a liquid phase oxidation reaction mixture comprising acetic acid solvent and water and in the presence of a catalyst composition comprising at least one heavy metal component in a reaction zone at temperature and pressure effective to maintain a liquid phase oxidation reaction mixture and form terephthalic acid, impurities comprising oxidation by-products, and a high pressure vapor phase comprising acetic acid, water and minor amounts of the paraxylene, terephthalic acid and by-products; separating the high pressure vapor phase to form an acetic acid-rich, water lean liquid and a high pressure gas comprising water vapor; and condensing the high pressure gas to form said aqueous stream.
having alkyl side chains which are oxidised to carboxyl groups · CPC title
Hydrocarbons, e.g. oil · CPC title
Reverse osmosis; Hyperfiltration · CPC title
by solid-liquid treatment; by chemisorption · CPC title
by reverse osmosis · CPC title
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