Process for producing ethanol by hydrogenation with carbon monoxide controls
A process for produce ethanol by hydrogenation acetic acid and/or esters thereof is disclosed. The process involves reacting hydrogen feed stream with an acetic acid feed stream in a reactor operated in the presence of a catalyst to form an ethanol mixture and monitoring carbon monoxide concentration of the fresh hydrogen feed stream and adjusting temperature in the reactor in response to the carbon monoxide concentration of the fresh hydrogen feed stream.
1. A process for producing ethanol comprising:
reacting hydrogen feed stream with an acetic acid feed stream in a reactor operated in the presence of a catalyst to form an ethanol mixture;
separating a vapor stream from the ethanol mixture and a liquid stream from the ethanol mixture, wherein the vapor stream has a steady state concentration of carbon monoxide;
recovering ethanol from the liquid stream;
combining a fresh hydrogen stream and the vapor stream to form the hydrogen feed stream; and
monitoring carbon monoxide concentration of the fresh hydrogen feed stream and adjusting temperature in the reactor in response to the carbon monoxide concentration of the fresh hydrogen feed stream.
2. The process of claim 1 , wherein the fresh hydrogen stream comprises from 0.03 to 1.5 mol. % carbon monoxide.
3. The process of claim 1 , wherein the fresh hydrogen stream comprises from 0.5 to 1 mol. % carbon monoxide.
4. The process of claim 1 , wherein the hydrogen feed stream is substantially free of carbon dioxide, nitrogen, methane, and ethane.
5. The process of claim 1 , further comprising combining a sufficient amount of the fresh hydrogen stream to maintain a molar ratio of hydrogen in the hydrogen feed stream to acetic acid in the acetic acid feed stream in the reactor of greater than 4:1.
6. The process of claim 1 , wherein the steady state concentration of carbon monoxide in the vapor stream is less than 2 mol. %.
7. The process of claim 1 , wherein the vapor stream further comprises carbon dioxide, nitrogen, methane, ethane, or mixtures thereof.
8. The process of claim 1 , wherein the reactor has a concentration of carbon monoxide that is greater than the steady state concentration of carbon monoxide in the vapor stream.
9. The process of claim 1 , wherein carbon monoxide in excess of the steady state concentration of carbon monoxide in the vapor stream is dissolved in the liquid stream.
10. The process of claim 1 , wherein the adjusted temperature is greater than 270° C. when the carbon monoxide concentration of the fresh hydrogen stream exceeds 0.03 mol. %.
11. The process of claim 1 , wherein the adjusted temperature is from 270° C. to 305° C. when the carbon monoxide concentration of the fresh hydrogen stream is from 0.03 mol. % to 1.5 mol. %.
12. The process of claim 1 , wherein the adjusted temperature is from 290° C. to 305° C. when the carbon monoxide concentration of the fresh hydrogen stream is from 1 mol. % to 1.5 mol. %.
13. The process of claim 1 , further comprising purging less than 15% of the vapor stream.
14. The process of claim 1 , wherein the ethanol mixture comprises less than 10 wt. % acetic acid.
15. The process of claim 1 , further comprising combining a secondary purified hydrogen stream with the fresh hydrogen stream and the vapor stream to form the hydrogen feed stream, wherein the secondary purified hydrogen stream contains at least 99.99 mol. % hydrogen.
16. A process for producing ethanol comprising:
reacting hydrogen feed stream with an acetic acid feed stream in a reactor operated in the presence of a catalyst to form an ethanol mixture;
separating a vapor stream from the ethanol mixture and a liquid stream from the ethanol mixture, wherein the vapor stream has a steady state concentration of carbon monoxide;
recovering ethanol from the liquid stream;
combining a fresh hydrogen stream that contains carbon monoxide and is less than 99.99% and the vapor stream to form the hydrogen feed stream; and
monitoring carbon monoxide concentration of the fresh hydrogen feed stream and adjusting the reactor to a temperature that is greater than 270° C. when the carbon monoxide concentration of the fresh hydrogen feed stream exceeds 0.03 mol. %.
17. The process of claim 16 , further comprising combining a sufficient amount of the fresh hydrogen stream to maintain a molar ratio of hydrogen in the hydrogen feed stream to acetic acid in the acetic acid feed stream in the reactor of greater than 4:1.
18. The process of claim 16 , wherein the steady state concentration of carbon monoxide in the vapor stream is less than 2 mol. %.
19. The process of claim 16 , further comprising purging less than 15% of the vapor stream.
20. The process of claim 16 , further comprising combining a secondary purified hydrogen stream with the fresh hydrogen stream and the vapor stream to form the hydrogen feed stream, wherein the secondary purified hydrogen stream contains at least 99.99 mol. % hydrogen.