Oxygen stripping in etherification, ethers decomposition and isooctene production

Patent metadata

Field	Value
Publication number	US-11623906-B2
Application number	US-202117400318-A
Country	US
Kind code	B2
Filing date	Aug 12, 2021
Priority date	Aug 17, 2020
Publication date	Apr 11, 2023
Grant date	Apr 11, 2023

Abstract

A process for supplying deaerated water to a chemical plant that includes a distillation column for separating a reaction effluent comprising water and a product. The process includes inventorying the distillation column with aerated water (water having an oxygen content of greater than 50 ppbw, such as greater than 1 ppmw). The aerated water in the distillation column may then be distilled to produce an oxygen-containing overheads and a bottoms fraction comprising deaerated water. The deaerated water in the bottoms fraction ma be transported to an upstream or a downstream unit operation, and utilizing the deaerated water in the upstream or downstream unit operation. The reaction effluent is fed to the distillation column, transitioning the distillation column from separating oxygen from water to operations for separating the product from the water.

First claim

What is claimed as new and desired to be protected by Letters Patent is:

1. A process for supplying deaerated water to a chemical plant, wherein the chemical plant includes a distillation column for separating a reaction effluent comprising water and a product, the process comprising:
inventorying the distillation column with aerated water having an oxygen content of greater than 50 ppbw;
distilling the aerated water in the distillation column to produce an oxygen-containing overheads and a bottoms fraction comprising deaerated water;
transporting the deaerated water in the bottoms fraction to an upstream or a downstream unit operation;
utilizing the deaerated water in the upstream or downstream unit operation; and
feeding the reaction effluent to the distillation column, transitioning the distillation column from separating oxygen from water to operations for separating the product from the water.

2. The process of claim 1 , wherein the deaerated water comprises less than 15 ppbw oxygen.

3. The process of claim 1 , wherein the deaerated water comprises from less than 1 ppbw to no more than 10 ppbw oxygen.

4. The process of claim 1 , wherein the distillation column comprises an overheads condensation system, the process further comprising:
recovering an overheads fraction from the distillation column, the overheads fraction comprising water vapor and oxygen;
cooling the overheads fraction to condense at least a portion of the water, forming a cooled overhead fraction;
feeding the cooled overhead fraction to an overhead drum, accumulating a liquid water fraction and a vapor fraction comprising the oxygen;
withdrawing the vapor fraction from the overhead drum; and
feeding the liquid water fraction to the distillation column as a reflux.

5. The process of claim 1 , further comprising feeding nitrogen to the overhead drum, wherein the vapor fraction comprises nitrogen and oxygen.

6. The process of claim 1 , further comprising measuring an oxygen content of the bottoms fraction.

7. A method for starting up a system for producing methyl tert-butyl ether (MTBE), wherein the system comprises:
flow lines and a reactor, the flow lines configured for feeding methanol and a mixed C4 stream, comprising isobutylene and other olefinic and/or paraffinic C4s, and the reactor configured for reacting the isobutylene and methanol to produce a crude MTBE effluent comprising MTBE, unreacted isobutylene, unreacted methanol, and the other olefinic and/or paraffinic C4s;
a catalytic distillation reactor for concurrently (i) reacting the unreacted isobutylene and methanol to form additional MTBE, and (ii) separating the crude MTBE to recover a bottoms fraction comprising the MTBE and an overheads fraction comprising methanol and the other olefinic and/or paraffinic C4s;
an extraction column for extracting the unreacted methanol with water, producing a C4 raffinate fraction comprising the other olefinic and/or paraffinic C4s, and an extract fraction comprising water and methanol;
a distillation column for separating the extract fraction to recover an overheads fraction comprising methanol and a bottoms fraction comprising water;
the method comprising:
inventorying the distillation column with aerated water, having an oxygen content of greater than 50 ppbw;
distilling the aerated water in the distillation column to produce an oxygen-containing overheads and a bottoms fraction comprising deaerated water having less than 15 ppbw oxygen;
transporting the deaerated water in the bottoms fraction to the extraction column;
repeating the inventorying, distilling, and transporting until the extraction column and distillation column are fully inventoried with deaerated water; and
starting up the reactor and the catalytic distillation reactor;
feeding the overheads fraction comprising the methanol and the other olefinic and/or paraffinic C4s to the extraction column, transitioning the extraction column to producing the C4 raffinate fraction and the extract fraction comprising water and methanol;
feeding the extract fraction to the distillation column, transitioning the distillation column to separating the methanol from the water.

8. The method of claim 7 , wherein the repeating comprises conducting the inventorying, distilling, and transporting continuously, recirculating water from the extraction column to the distillation column until the water is deaerated.

9. The method of claim 7 , wherein the repeating comprises conducting the inventorying, distilling, and transporting batchwise in the distillation column, transporting batches of deaerated water to inventory the extraction column.

10. The method of claim 9 , further comprising accumulating a volume of deaerated water in a sump of the distillation column.

11. The method of claim 7 , wherein the distillation column comprises an overheads condensation system, the method further comprising:
recovering an overheads fraction from the distillation column, the overheads fraction comprising water vapor and oxygen;
cooling the overheads fraction to condense at least a portion of the water, forming a cooled overhead fraction;
feeding the cooled overhead fraction to an overhead drum, accumulating a liquid water fraction and a vapor fraction comprising the oxygen;
withdrawing the vapor fraction from the overhead drum; and
feeding the liquid water fraction to the distillation column as a reflux.

12. The method of claim 11 , comprising feeding the liquid water fraction to the distillation column as a total reflux.

13. The method of claim 11 , further comprising feeding nitrogen to the overhead drum, wherein the vapor fraction comprises nitrogen and oxygen.

14. The method of claim 11 , further comprising measuring an oxygen content of the bottoms fraction.

Assignees

• Lummus Technology Inc

Inventors

• Barias Rosette
• Korpelshoek Maurice
• Scott Michael Jon
• Schwarz Eric Arthur
• Jamal Shahid

Classifications

• Y02P20/10

  Process efficiency · CPC title

• C07C43/046

  Alkyl tert-alkyl ether, e.g. CH3OC(CH3)3 · CPC title

• C07C41/42

  by distillation · CPC title

• C07C41/38 Primary

  by liquid-liquid treatment · CPC title

• C07C41/06 Primary

  by addition of organic compounds only · CPC title