Calcium oxide or magnesium oxide production with alkali and sulfur dioxide intermediates
US-12017985-B2 · Jun 25, 2024 · US
US2020140366A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020140366-A1 |
| Application number | US-201816466977-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 2, 2018 |
| Priority date | Jul 2, 2018 |
| Publication date | May 7, 2020 |
| Grant date | — |
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Provided is an acetic acid production method that enables, in a scrubbing system, efficient separation and obtaining of methyl iodide and an absorbing solvent; restrainment of corrosion of the interior of a distillation column; efficient separation between and recovery of hydrogen iodide and methyl iodide; or sufficient recovery of hydrogen iodide. The acetic acid production method according to the present invention includes a first absorption step and a second absorption step. In the first absorption step, an offgas is brought into contact with a first absorbent to allow the first absorbent to absorb an iodine compound from the offgas, to give a first gas, where the first absorbent includes at least one of C2 or higher alcohols, esters of C3 or higher carboxylic acids, esters between carboxylic acids and C2 or higher alcohols, ethers, ketones, water, and basic aqueous solutions. In the second absorption step, the first gas is brought into contact with a second absorbent to allow the second absorbent to absorb an iodine compound from the first gas, where the second absorbent includes at least one of C2 or higher alcohols, esters of C3 or higher carboxylic acids, ethers, esters between carboxylic acids and C2 or higher alcohols, ketones, water, basic aqueous solutions, and acetic acid and differs in composition from the first absorbent.
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1 . A method for producing acetic acid, the method comprising: a first absorption step of: feeding, to an absorption column, at least a portion of offgases formed in an acetic acid production process; bringing the fed offgas into contact with a first absorbent in the absorption column to allow the first absorbent to absorb an iodine compound from the offgas, the first absorbent including at least one liquid selected from the group consisting of: C2 or higher alcohols; esters of C3 or higher carboxylic acids; esters between carboxylic acids and C2 or higher alcohols; ethers; ketones; water; and basic aqueous solutions; and whereby separating into: a first gas having a lower iodine compound concentration as compared with the offgas; and a first solution containing the iodine compound and the first absorbent; and a second absorption step of: bringing the first gas into contact with a second absorbent in the absorption column or in another absorption column to allow the second absorbent to absorb an iodine compound from the first gas, the second absorbent differing in composition from the first absorbent and including at least one liquid selected from the group consisting of: C2 or higher alcohols; esters of C3 or higher carboxylic acids; esters between carboxylic acids and C2 or higher alcohols; ethers; ketones; water; basic aqueous solutions; and acetic acid; and whereby separating into: a second gas having a lower iodine compound concentration as compared with the first gas; and a second solution containing the iodine compound and the second absorbent. 2 . A method for producing acetic acid, the method comprising: a carbonylation step of reacting methanol with carbon monoxide in the presence of a catalytic system, acetic acid, methyl acetate, and water in a reactor to form acetic acid, the catalytic system including a metal catalyst and methyl iodide; and a separation step of separating, using at least one selected from evaporators and distillation columns, a reaction mixture from the carbonylation step into: a stream including the metal catalyst; an acetic acid stream rich in acetic acid; and a stream richer in light ends than the acetic acid stream, the method optionally further comprising an acetaldehyde-removing system of separating, using a distillation column or columns, acetaldehyde from at least a portion of a condensate resulting from condensation of the stream richer in light ends, the method comprising: a first absorption step of: feeding, to an absorption column, at least one offgas selected from the group consisting of: an offgas from the reactor; an offgas from the evaporator or evaporators, an offgas from the distillation column or columns in the separation step; and an offgas from the distillation column or columns in the acetaldehyde-removing system; bringing the fed at least one offgas into contact with a first absorbent in the absorption column to allow the first absorbent to absorb an iodine compound from the offgas, the first absorbent including at least one liquid selected from the group consisting of: C2 or higher alcohols; esters of C3 or higher carboxylic acids; esters between carboxylic acids and C2 or higher alcohols; ethers; ketones; water; and basic aqueous solutions; and whereby separating into: a first gas having a lower iodine compound concentration as compared with the offgas; and a first solution containing the iodine compound and the first absorbent; and a second absorption step of: bringing the first gas into contact with a second absorbent in the absorption column or in another absorption column to allow the second absorbent to absorb an iodine compound from the first gas, the second absorbent differing in composition from the first absorbent and including at least one liquid selected from the group consisting of: C2 or higher alcohols; esters of C3 or higher carboxylic acids; esters between carboxylic acids and C2 or higher alcohols; ethers; ketones; water; basic aqueous solutions; and acetic acid; and whereby separating into: a second gas having a lower iodine compound concentration as compared with the first gas; and a second solution containing the iodine compound and the second absorbent. 3 . The method for producing acetic acid according to claim 1 , wherein the first absorbent includes water. 4 . The method for producing acetic acid according to claim 1 , wherein the second absorbent includes acetic acid. 5 . The method for producing acetic acid according to claim 1 , wherein one of the first absorbent and the second absorbent has a water concentration of 10 ppm by mass or more. 6 . The method for producing acetic acid according to claim 1 , wherein, of the first absorbent and the second absorbent, one has a water concentration of 10 ppm by mass or more, and the other has an acetic acid concentration of 10 ppm by mass or more. 7 . The method for producing acetic acid according to claim 1 , wherein the method comprises: a stripping step of separating, by distillation, the second solution into: an overhead stream rich in methyl iodide; and a bottom stream rich in acetic acid. 8 . The method for producing acetic acid according to claim 7 , wherein the overhead stream rich in methyl iodide is recycled to a reaction step. 9 . The method for producing acetic acid according to claim 7 , wherein a charge liquid to a distillation column in the stripping step has a methyl iodide concentration of 100 ppm by mass or more. 10 . The method for producing acetic acid according to claim 7 , wherein a charge liquid to a distillation column in the stripping step has a hydrogen iodide concentration of less than 100 ppm by mass. 11 . A method for producing acetic acid, the method comprising: a carbonylation step of reacting methanol with carbon monoxide in the presence of a catalytic system, acetic acid, methyl acetate, and water in a reactor to form acetic acid, the catalytic system including a metal catalyst and methyl iodide; an evaporation step of separating, using an evaporator, a reaction mixture from the carbonylation step into: a vapor stream; and a residue stream; a light ends-removing step of separating, by distillation, the vapor stream into: an overhead stream rich in light ends; and a first acetic acid stream rich in acetic acid; and a dehydration step of separating, by distillation, the first acetic acid stream into: an overhead stream rich in water; and a second acetic acid stream richer in acetic acid than the first acetic acid stream, the method optionally further comprising at least one of: a heavy ends-removing step of separating, by distillation, the second acetic acid stream into: a bottom stream rich in heavy ends; and a third acetic acid stream richer in acetic acid than the acetic acid stream before being subjected to the distillation; and an acetaldehyde-removing system of separating, using a distillation column or columns, acetaldehyde from at least a portion of a condensate resulting from condensation of the overhead stream rich in light ends, the method comprising: a first absorption step of: feeding, to an absorption column, at least one offgas selected from the group consisting of: an offgas from the reactor; an offgas from the evaporator; an offgas from a distillation column in the light ends-removing step; an offgas from a distillation column in the dehydration step; an offgas from a distillation column in the heavy ends-removing step; and an offgas from the distillation column or columns in the acetaldehyde-removing system; bringing the fed at least
by distillation · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
on an oxygen-containing group in organic compounds, e.g. alcohols · CPC title
by steam distillation · CPC title
Hydrogen iodide · CPC title
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