Method and apparatus for producing acetic acid

Patent metadata

Field	Value
Publication number	US-10894759-B2
Application number	US-201916542858-A
Country	US
Kind code	B2
Filing date	Aug 16, 2019
Priority date	Sep 30, 2015
Publication date	Jan 19, 2021
Grant date	Jan 19, 2021

Abstract

A process for stably and safely producing acetic acid without increasing an internal pressure of a distillation column is provided. The process comprises ( 1 ) a carbonylation reaction step for allowing methanol to react with carbon monoxide; ( 2 ) a flash step for separating the reaction mixture into a volatile phase and a less-volatile phase; ( 3 ) a first distillation step for separating the volatile phase into a first overhead and a crude acetic acid stream rich in acetic acid; and ( 4 ) a separation step for separating at least acetaldehyde from the first overhead. The separation step ( 4 ) comprises ( 6 ) a second distillation step for distilling the first overhead while controlling an internal pressure of a distillation column provided with a pressure control unit 68 to form a second overhead rich in acetaldehyde and methyl iodide and a bottom or lower stream, and ( 7 ) an extraction step for extracting acetaldehyde from the second overhead to form an extract rich in acetaldehyde and a raffinate rich in methyl iodide.

First claim

The invention claimed is:

1. A process for producing acetic acid, comprising:
carbonylating methanol with carbon monoxide in the presence of a catalyst system, acetic acid, methyl acetate, and water, wherein the catalyst system comprises a metal catalyst, an ionic metal iodide, and methyl iodide, to obtain a reaction mixture;
flash-evaporating the reaction mixture to separate the reaction mixture into a volatile phase and a less-volatile phase;
first-distilling the volatile phase to separate the volatile phase into a first overhead, a side-cut acetic acid stream and a bottom stream, wherein the first overhead contains at least one permanganate reducing compound (PRC) and methyl iodide, and the PRC contains at least acetaldehyde; and the side-cut acetic acid stream mainly contains acetic acid; and
separating at least acetaldehyde from the first overhead,
wherein the separation comprises:
second-distilling the first overhead to separate the first overhead into a second overhead rich in acetaldehyde and methyl iodide and a bottom or lower stream, the second distillation comprising at least one distillation column, while controlling an internal pressure of the distillation column in the second distillation by the following method (1) and/or (2):
(1) introducing at least one gas selected from the group consisting of a nitrogen gas, an off-gas, and an inert gas constantly to the feeding line communicating with the column top of the distillation column, with remaining a control valve on the feeding line open at a predetermined degree of opening,
(2) discharging or withdrawing a non-condensable gas, and
extracting acetaldehyde from the second overhead to form an extract rich in acetaldehyde and a raffinate rich in methyl iodide.

2. The process according to claim 1 , wherein the separation further comprises:
condensing the first overhead to form a two-phase first condensate, wherein at least a portion of an upper phase, a lower phase, or both is distilled in the second distillation while controlling the internal pressure of the distillation column.

3. The process according to claim 2 , wherein at least a portion of at least the lower phase is distilled in the second distillation while controlling the internal pressure of the distillation column.

4. The process according to claim 1 , wherein the first overhead is distilled in the second distillation while controlling the internal pressure of the distillation column to 0.1 to 0.7 MPa.

5. The process according to claim 1 , wherein the control of the internal pressure of the distillation column comprises:
detecting the internal pressure of the distillation column by a pressure sensor to obtain a detected value,
producing a controlling signal based on the detected value and a standard value, and
providing or sending the control signal from a pressure control unit disposed at a top of the distillation column to a pressure control valve to regulate or control an opening degree of the pressure control valve for regulating an outflow rate of the first overhead.

6. The process according to claim 1 , wherein the second distillation comprises a plurality of distillation steps, and the first overhead is distilled while controlling an internal pressure of the distillation column in at least a downstream distillation step.

7. The process according to claim 1 , which further comprises:
condensing the second overhead to form a second condensate and an off-gas, wherein the second condensate is subjected to the extraction and
directly or indirectly recycling a useful component in the off-gas to at least one selected form the group consisting of the carbonylation reaction, the first distillation, and the second distillation.

8. The process according to claim 7 , wherein the off-gas is condensed to form a third condensate, and the third condensate is recycled to at least one selected from the group consisting of the carbonylation reaction, the first distillation, and the second distillation.

9. The process according to claim 1 , wherein an off-gas produced from the process is recycled to at least one selected from the group consisting of the carbonylation reaction, the first distillation, and the second distillation.

10. The process according to claim 7 , wherein the off-gas is adsorbed to an absorption solvent under an applied pressure, and at least one component selected from the group consisting of methyl iodide, methyl acetate, dimethyl ether, water, and carbon monoxide is diffused from the resulting absorption solvent and is recycled to at least one selected from the group consisting of the carbonylation reaction, the first distillation, and the second distillation.

11. The process according to claim 1 , wherein at least a portion of the raffinate is recycled to at least one selected from the group consisting of the carbonylation reaction, the first distillation, and the second distillation.

12. The process according to claim 1 , wherein the second overhead is subjected to water extraction stepwise or continuously with a plurality of theoretical stages.

13. The process according to claim 1 , which further comprises:
fourth-distilling the extract to form a fourth overhead containing an aldehyde and a bottom or lower aqueous stream,
wherein the aqueous stream is used for extraction in the extraction.

14. The process according to claim 1 , wherein an acetaldehyde concentration in a reaction medium in a reactor of the carbonylation reaction is maintained at not more than 400 ppm by weight, and
the process further comprises distilling the side-cut acetic acid stream and separating the side-cut acetic acid stream into a purified acetic acid and at least one component selected from the group consisting of a lower boiling point component and a higher boiling point component, wherein at least one of the following (i) to (iii) is satisfied: (i) a potassium permanganate test value of the purified acetic acid is maintained at not less than 120 minutes, (ii) a propionic acid concentration of the purified acetic acid is maintained at not more than 200 ppm by weight, and (iii) an iodide concentration of the purified acetic acid is maintained at not more than 100 ppb.

15. The process according to claim 1 , wherein in the method (1), the internal pressure of the distillation column is controlled by introducing at least one gas selected from the group consisting of a nitrogen gas, an off-gas, and an inert gas with a flow rate of not more than 1% relative to a flow rate of the first overhead being fed to the distillation column in the second distillation.

16. The process according to claim 1 , wherein in the method (2), the internal pressure of the distillation column is controlled by regulating or controlling the temperature and/or the flow rate of a cooling water for a condenser, which cools and condenses an overhead from the distillation column in the second distillation, to form a condensate and a noncondensable gas, and by regulating or controlling a discharging amount of the noncondensable gas from a discharging line.

17. The process according to claim 1 , wherein in the method (2), the inner pressure of the distillation column is controlled by detecting a pressure and/or a flow rate at a withdrawing port communicating with a gaseous phase in a hold tank, which is disposed downstream of a condenser for cooling and condensing an overhead from the distillation column in the second distillation to form a condensate and a noncondensable gas, and regulating or controlling a discharge amount of the noncondensable off-gas.

Assignees

• Daicel Corp

Inventors

• Miura Hiroyuki
• Mizutani Yoshihisa

Classifications

• C07C53/08

  Acetic acid (pyroligneous acid C10C; preparation of vinegar C12J) · CPC title

• C07C51/48

  by liquid-liquid treatment · CPC title

• C07C51/44

  by distillation · CPC title

• C07C51/12 Primary

  on an oxygen-containing group in organic compounds, e.g. alcohols · CPC title

• B01D5/006

  with evaporation or distillation · CPC title