System for producing phenol and bisphenol A including removal unit for removing methanol and acetone

Patent metadata

Field	Value
Publication number	US-10457620-B2
Application number	US-201716329087-A
Country	US
Kind code	B2
Filing date	Nov 28, 2017
Priority date	Nov 28, 2016
Publication date	Oct 29, 2019
Grant date	Oct 29, 2019

Abstract

A system for producing phenol and bisphenol A comprising: a first production unit for producing phenol comprising a decomposition reaction unit and a purification unit; a second production unit for producing bisphenol A comprising a reaction unit and a concentration unit; and a removal unit for removing methanol and acetone during the production of phenol and bisphenol A. The removal unit includes a removal column comprising an overhead purge part, a bottom recirculation part and a supply part. The supply part comprises a purification unit discharge part to supply methanol, acetone, and water discharged from the purification unit to the removal column and a concentration unit discharge part to supply phenol, acetone, and water discharged from the concentration unit to the removal column, and is provided to the midsection of the removal column.

First claim

The invention claimed is:

1. A system for producing phenol and bisphenol A comprising:
a first production unit for producing phenol comprising a decomposition reaction unit and a purification unit;
a second production unit for producing bisphenol A comprising a reaction unit and a concentration unit; and
a removal unit for removing methanol and acetone during the production of phenol and bisphenol A the removal unit comprising:
a removal column comprising an overhead purge part, a bottom recirculation part and a supply part;
wherein the supply part comprises a purification unit discharge part to supply methanol, acetone, and water discharged from the purification unit to the removal column and a concentration unit discharge part to supply phenol, acetone, and water discharged from the concentration unit to the removal column,

wherein the supply part is provided to the midsection of the removal column;
wherein the overhead purge part removes methanol and acetone from the removal column; and
wherein the bottom recirculation part recirculates phenol, water, and trace amounts of methanol and acetone to the purification unit.

2. The system for producing phenol and bisphenol A according to claim 1 ,
wherein the purification unit comprises:
a first column for separating a reaction product discharged from the decomposition reaction unit into an acetone-rich fraction and a phenol-rich fraction;
a second column connected to an acetone-rich discharge line for purifying the acetone-rich fraction discharged from a top of the first column; and
a separator connected to the acetone removal discharge line for separating an acetone removal fraction discharged from the bottom of the second column into an aqueous layer fraction comprising methanol, acetone and water, and an organic layer fraction, and
wherein the purification unit discharge part comprises an aqueous layer discharge line through which the aqueous layer fraction is discharged from the separator.

3. The system for producing phenol and bisphenol A according to claim 1 ,
wherein the concentration unit comprises:
a dehydration column for removing unreacted acetone and water from a reaction product discharged from the reaction unit; and
an acetone recovery column connected to an unreacted acetone discharge line discharged from an upper end of the dehydration column for recovering acetone by removing acetone from the water-rich fraction, and
wherein the concentration unit discharge part comprises a water-rich discharge line through which a water-rich fraction comprising phenol, acetone, and water is discharged from the acetone recovery column.

4. The system for producing phenol and bisphenol A according to claim 1 , wherein the bottom recirculation part recirculated to the purification unit comprises methanol in an amount of 100 ppm or less based on a total weight of flow.

5. The system for producing phenol and bisphenol A according to claim 1 , wherein a reaction in which phenol and acetone are produced from cumene oxide and an acid solution is performed in the decomposition reaction unit.

6. The system for producing phenol and bisphenol A according to claim 2 , wherein the purification unit further comprises a neutralizer at a front end part of the first column, and the neutralizer neutralizes the reaction product discharged from the decomposition reaction unit.

7. The system for producing phenol and bisphenol A according to claim 1 , wherein a reaction in which bisphenol A and water are produced is performed in the reaction unit.

Assignees

• Lg Chemical Ltd

Inventors

• Lee Sang Beom
• Lee Sung Kyu
• Shin Joon Ho
• Lee Sung Ho
• Park Sa Eun
• Jeong In Yong

Classifications

• C07C45/53

  of hydroperoxides · CPC title

• C07C37/86

  by treatment giving rise to a chemical modification (chemisorption C07C37/82) · CPC title

• C07C37/70

  by physical treatment · CPC title

• C07C37/68

  Purification; separation; Use of additives, e.g. for stabilisation {(C07C37/004 and C07C37/005 take precedence)} · CPC title

• C07C37/08

  by decomposition of hydroperoxides, e.g. cumene hydroperoxide · CPC title