Oxygenate separation using a metal salt

Patent metadata

Field	Value
Publication number	US-11447704-B2
Application number	US-201916597080-A
Country	US
Kind code	B2
Filing date	Oct 9, 2019
Priority date	Oct 11, 2018
Publication date	Sep 20, 2022
Grant date	Sep 20, 2022

Abstract

A process, a system, and an apparatus for separation of an oxygenate from a stream is provided. More specifically, a stream comprising the oxygenate is introduced to a quench tower along with a caustic outlet stream comprising a metal salt. Contact between the oxygenate and the metal salt results in conversion of a portion of the oxygenate into a derivative salt. The derivative salt and unconverted oxygenate are condensed by quenching and substantially removed from the quench tower as an oxygenate outlet stream. The gaseous components of the stream, minus a substantial portion of the oxygenate, are removed from the quench tower as a quench outlet stream.

First claim

What is claimed is:

1. A method comprising:
introducing an input stream comprising a lower alkane and oxygen to an oxidative dehydrogenation (ODH) reactor;
converting the lower alkane to an alkene in the ODH reactor and producing an ODH outlet stream comprising the alkene, unconverted lower alkane, an oxygenate, and a carbon-based oxide, wherein the oxygenate is a co-product of an ODH reaction in the ODH reactor;
introducing the ODH outlet stream comprising the oxygenate and a caustic outlet stream comprising a metal salt to a quench tower;
contacting the oxygenate with the metal salt in the quench tower to convert a portion of the oxygenate to a derivative salt comprising at least one of an acetate, an acrylate, or a malonate, wherein the derivative salt is formed from the metal salt and the oxygenate; and
removing from the quench tower:
a quench outlet stream; and
an oxygenate outlet stream comprising at least a substantial portion of the unconverted oxygenate and at least a substantial portion of the derivative salt.

2. The method of claim 1 , wherein the caustic outlet stream is produced from a caustic wash tower, wherein the ODH outlet stream and the caustic outlet stream are introduced separately to the quench tower, wherein the lower alkane comprises at least one of ethane or propane, wherein the alkene comprises at least one of ethylene or propylene, and wherein the metal salt comprises a carbonate.

3. The method of claim 2 , wherein the caustic wash tower processes the quench outlet stream, wherein introducing the ODH outlet stream to the quench tower occurs concomitantly with introducing the caustic outlet stream to the quench tower, wherein the lower alkane comprises ethane, wherein the alkene comprises ethylene, wherein the carbonate comprises at least one of sodium bicarbonate, potassium carbonate, or ammonium bicarbonate, and wherein the derivative salt comprises the acetate.

4. The method of claim 1 further comprising:
introducing the oxygenate outlet stream to a separation vessel and separating the unconverted oxygenate from the derivative salt via the separation vessel to produce:
a second oxygenate outlet stream from the separation vessel and comprising a substantial portion of the oxygenate from the oxygenate outlet stream; and
a separation outlet stream from the separation vessel and comprising a substantial portion of the derivative salt from the oxygenate outlet stream.

5. The method of claim 4 , further comprising recycling a portion of the separation outlet stream to the separation vessel.

6. The method of claim 4 , further comprising introducing ethyl acetate to the separation vessel.

7. The method of claim 5 , wherein the quench outlet stream comprises at least a substantial portion of the carbon-based oxide, the unreacted alkane, and the alkene that are present in the ODH outlet stream, and wherein the recycling comprises recycling the portion of the separation outlet stream as a recycle stream to the separation vessel via a recycle line coupled to a recycle inlet of the separation vessel and coupled to an outlet line from the separation vessel conveying the separation outlet stream.

8. The method of claim 4 , wherein the carbon-based oxide comprises at least one of carbon monoxide or carbon dioxide, and wherein the separation vessel comprises a liquid-liquid extraction tower.

9. The method of claim 1 , wherein the carbon-based oxide comprises carbon dioxide, and the method further comprises introducing the quench outlet stream to an amine wash tower and removing a substantial portion of the carbon-based oxide from the quench outlet stream.

10. The method of claim 1 , further comprising introducing the ODH outlet stream to an oxygen remover and removing oxygen, if present, from the stream in the oxygen remover prior to introducing the ODH outlet stream to the quench tower.

11. The method of claim 1 , further comprising maintaining the pH of the quench tower in a range of the pKa of the oxygenate to the pKa of the metal salt.

12. The method of claim 11 , wherein the oxygenate comprises acetic acid having a pKa of 4.7 and the metal salt comprises sodium bicarbonate having a pKa of 10.3.

13. The method of claim 1 , further comprising removing a portion of the oxygenate from the ODH outlet stream prior to introducing the ODH outlet stream to the quench tower.

14. The method of claim 7 , further comprising:
introducing into a caustic wash tower:
the quench outlet stream; and
a caustic agent selected from at least one of sodium hydroxide, potassium hydroxide, or ammonium hydroxide, wherein the carbon-based oxide present in the quench outlet stream contacts the caustic agent in the caustic wash tower to form the metal salt; and

removing the metal salt from the caustic wash tower via the caustic outlet stream and introducing the metal salt to the quench tower as part of the caustic outlet stream.

15. The method of claim 1 , comprising processing the quench outlet stream in a caustic wash tower to give the caustic outlet stream from the caustic wash tower and comprising the metal salt, wherein the metal salt comprises at least one of sodium hydrogen sulfide, sodium bicarbonate, potassium carbonate, or ammonium bicarbonate.

16. The method of claim 1 , wherein the oxygenate comprises at least one of acetic acid, acrylic acid, maleic acid, or maleic anhydride.

17. The method of claim 1 , wherein the derivative salt comprises at least one of sodium acetate, potassium acetate, ammonium acetate, sodium acrylate, potassium acrylate, ammonium acrylate, sodium malonate, potassium malonate, or ammonium malonate.

18. The method of claim 1 , further comprising producing the caustic outlet stream by at least one process selected from an oxidative dehydrogenation process, a cracking process, a refinery process, a paper manufacturing process, a soap manufacturing process, a detergent manufacturing process, or a food manufacturing processing.

19. The method of claim 1 , wherein the lower alkane comprises ethane, propane, or a mixture thereof, wherein the alkene comprises ethylene, propylene, or a mixture thereof, and the wherein the oxygenate comprises acetic acid.

20. The method of claim 19 , further comprising producing olefin derivatives from the alkene, wherein the metal salt comprises a carbonate.

21. The method of claim 20 , wherein the olefin derivatives comprise at least one of a polyethylene, a polypropylene, an ethylene oxide, a propylene oxide, a polyethylene oxide, a polypropylene oxide, a thermoplastic elastomer, or a thermoplastic olefin.

22. The method of claim 21 , wherein the polyethylene comprises at least one of a homopolymer of ethylene, a copolymer of ethylene and an α-olefin, a high density polyethylene (HDPE), a medium density polyethylene (MDPE), a low density polyethylene (LDPE), a linear low density polyethylene (LLDPE), or a very low density polyethylene (VLDPE).

23. A method comprising:
converting a lower alkane to an alkene in an oxidative dehydrogenation (ODH) reactor and producing from the ODH reactor an ODH outlet stream comprising the alkene, unconverted lower alkane, an oxygenate, and a carbon-based oxide;
introducing the ODH outlet stream and a caustic outlet stream having a metal salt to a quench tower and converting the oxygenate in the quench tower to a derivative salt formed from the oxygenate and the metal salt, wherein the derivative salt comprises at least one of an acetate, an acrylate, or a malonate;

Assignees

• Nova Chem Int Sa

Inventors

• Olayiwola Bolaji
• Simanzhenkov Vasily
• Goodarznia Shahin
• Koselek Michael
• Serhal Kamal

Classifications

• C10G2300/1092

  C2-C4 olefins · CPC title

• C07C7/17

  with acids or sulfur oxides · CPC title

• C07C7/1485

  oxides; hydroxides; salts (C07C7/156 takes precedence) · CPC title

• C10G2300/207

  Acid gases, e.g. H2S, COS, SO2, HCN · CPC title

• C10G2400/20

  C2-C4 olefins · CPC title