Removal of hydrocarbons from an aqueous stream
View Patent ↗The present application concerns a process for the removal of hydrocarbons from an aqueous stream, which process may include conducting a phenol-containing water stream into a separation column, separating the phenol-containing water in the column using heat to form an overhead portion and a bottoms portion, and collecting the overhead portion as well as the bottoms portion. Further, the process may include adding an eluent to an aqueous stream, thereby forming an aqueous mixture, subsequently conducting the aqueous mixture into a separation vessel, wherein it is allowed to settle into two phases, which form a hydrocarbon stream and a phenol-containing water stream, subsequently collecting the hydrocarbon stream, and conducting the phenol-containing water stream to the separation column for further separation.
1. A process for the removal of hydrocarbons from an aqueous stream, which process comprises:
adding 0.5 to 5 wt % cumene as an eluent to an aqueous stream comprising 2 to 15 wt % of hydrocarbons comprising phenol and at least one alpha methyl styrene or mesityl oxide to thereby form an aqueous mixture,
allowing the aqueous mixture to settle into two phases, which form a hydrocarbon stream containing said at least one alpha methyl styrene or mesityl oxide and a water stream comprising the majority of the phenol,
subsequently collecting the hydrocarbon stream and passing the collected hydrocarbon stream to distillation for recovery,
conducting the phenol-containing water stream into a separation column,
separating the phenol-containing water in the column using heat into an overhead portion and a bottoms portion, and
collecting the overhead portion as well as the bottoms portion, and
transferring the bottoms portion to a bio waste water treatment reactor and recycling the overhead portion for phenol recovery.
2. A process as claimed in claim 1 , which process comprises:
conducting the aqueous mixture formed by adding the eluent to the aqueous stream into a separation vessel, wherein it is allowed to settle into the hydrocarbon stream and the phenol-containing water stream.
3. The process of claim 2 , wherein the temperature in the separation vessel is 30-50° C. and the pressure is 110-200 kPa.
4. The process of claim 2 , wherein the separation column is operated with reflux using recycled steam at a temperature of 100-200° C.
5. The process of claim 2 , wherein the temperature in the separation vessel is at about 40° C. and the pressure is about 110-200 kPa.
6. The process of claim 2 , wherein the separation column is operated with reflux using recycled steam at a temperature of about 150° C.
7. The process of claim 1 , wherein the pH of the aqueous stream during the process is maintained at 4.5-6.
8. The process of claim 1 , wherein a concentration of salt in the aqueous stream is below 1000 ppm.
9. The process of claim 1 , wherein the amount of added eluent is sufficient to give an eluent concentration of 0.5 to 5 wt % before separation.
10. The process of claim 1 , wherein the pressure of the separation vessel is about 110-2001 kPa.
11. The process of claim 1 , wherein the pH of the aqueous stream during the process is maintained using sulphuric acid.