CN107793296A - The method that bisphenol-A is prepared using the group technology of suspension crystallization and film-falling crystallization - Google Patents
The method that bisphenol-A is prepared using the group technology of suspension crystallization and film-falling crystallization Download PDFInfo
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- CN107793296A CN107793296A CN201710990086.0A CN201710990086A CN107793296A CN 107793296 A CN107793296 A CN 107793296A CN 201710990086 A CN201710990086 A CN 201710990086A CN 107793296 A CN107793296 A CN 107793296A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/68—Purification; separation; Use of additives, e.g. for stabilisation
- C07C37/70—Purification; separation; Use of additives, e.g. for stabilisation by physical treatment
- C07C37/84—Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by crystallisation
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/68—Purification; separation; Use of additives, e.g. for stabilisation
- C07C37/685—Processes comprising at least two steps in series
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- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention discloses a kind of method that group technology using suspension crystallization and film-falling crystallization prepares bisphenol-A, including multistage suspension to crystallize multistage fusion-crystallization.The present invention can prepare the bisphenol-A with higher than 99.9% purity, more economical with recrystallization/distilation compared to suspension crystallization.
Description
Technical field
The present invention relates to a kind of method for preparing bisphenol-A.
Background technology
The known method for preparing bisphenol-A (2,2- double (4 '-hydroxy phenyl) propane) includes making acetone and excessive phenol
Reacted in the presence of strong acid catalyst such as sulphonic acids cationic ion-exchange resin.Reaction form a kind of product mixtures, except containing
Outside unreacted phenol and a small amount of acetone, BPA and water are mainly contained, in addition, also generating the typical by-product of a small amount of condensation reaction
Thing, such as 2- (4- hydroxy phenyls) -2- (2- hydroxy phenyls) propane (adjacent, p- BPA), the indane class of substitution, hydroxyphenyl indanol
There are three or more in the full class of class, hydroxyphenyl chroman class, spirobindene, the indenols class of substitution, the xanthene class of substitution and molecular skeleton
The advanced condensed compounds of individual phenyl ring.
Generally product is cooled down to form bisphenol a/phenol substantially equimolar crystalline adduct, by BPA and phenol from reaction
Separated in mixture.The operation is carried out by following steps, cools down reactant mixture, leads to bisphenol a-phenol adduct
Suspension crystallization mode is crossed to crystallize.Then by the suitable equipment for solid- liquid separation by bisphenol a-phenol adduct crystal from liquid
Separated in phase, these suitable equipments such as rotary filter or centrifuge.Washed by using suitable solvent, can remove and add
The impurity of solvate crystal surface attachment, these solvents usually contain one or more and are selected from following component：Acetone, water, phenol,
BPA and accessory constituent.The BPA/ phenol complex crystal that solid/liquid separation obtains is typically passed through further purification step
Suddenly, it includes, for example, distillation, desorption or extraction method, can remove phenol and may reduce secondary in BPA in this step
The concentration of component.
Such as want to obtain bisphenol A with high purity, it usually needs crystallize using n ＞ 1 n levels cascaded suspension, carry out knot again repeatedly
Crystalline substance operation, it is necessary to increase the separator of crystalline adduct and the number of crystalline adduct dissolving tank, that just generates device
The problem of maximization, installation cost rise；Also have by from bisphenol-A melt distill make its purify method, it has been found that except
Go in the processing procedure of phenol, bisphenol-A can be decomposed thermally to form impurity, such as phenol, isopropenyl phenol, only distill bar by control
It is difficult that part, which avoids decomposition of the bisphenol-A in phenol step is removed,
The content of the invention
It is an object of the invention to provide a kind of convenience, effect are good using suspension crystallization and the group technology of film-falling crystallization
The method for preparing bisphenol-A.
The present invention technical solution be：
A kind of method that group technology using suspension crystallization and film-falling crystallization prepares bisphenol-A, it is characterized in that：Including following step
Suddenly：
（One）Suspension crystallization
(1) at a temperature of 65-75 DEG C, reaction solution is adjusted in phenol, makes p, p- content of bisphenol A is 25-35 weight %；
(2) reaction solution is filled with crystallization reactor number n ＞ 1 n level cascaded suspension crystallizers at this temperature, will reacted molten
Liquid circulates in each crystallizer, cycle rate >=2000m3/ hour；
(3) in series-connected crystallizers, thermograde arrangement be from first crystallizer, 60 DEG C, second 50 DEG C of crystallization reactor,
Final 40 DEG C of crystallization reactor
(4) cleaned and/or dissolved using phenol, obtain bisphenol a/phenol crystalline adduct；Used as cleaning and/or dissolving
Phenol at least a portion be using refined phenol.
（Two）Fusion-crystallization
(1) temperature at 150-175 DEG C, under 1-150 millibar vacuum, by bisphenol a/phenol crystalline adduct phenol remove,
The melting bisphenol-A liquid phase finally given is less than 1% containing phenol；
(2) bisphenol-A liquid will be melted to be filled with n ＞ 1 falling-film crystallizer of n levels series connection, carries out multi-step melt liquid film-falling crystallization behaviour
Make；Obtain product.
Step（Two）Successively by feeding, crystallizing, raffinate into crystallizer in every grade of falling-film crystallizer in fusion-crystallization
Discharge, all sweating, melting and refined product discharge step；In charging, crystallization, raffinate discharge stage, set from 160-
125 DEG C of temperature ramps gradually dropped, in sweating, all melting and refined product discharging phase, set what is edged up from 125-160 DEG C
Temperature ramp.
Step（Two）Before melting bisphenol-A liquid enters falling-film crystallizer, addition sodium acid carbonate 1-50ppm, control pH
5.05-5.10。
The present invention can make product purity, yield and synthesis using suspension crystallization and the group technology of film-falling crystallization
Device maximization of economic benefit, the bisphenol-A with higher than 99.9% purity can be prepared.Compared to recrystallization/distilation more
It is economical.The parallel operational mode of the crystallizer of first stage, during the fusion processes in crystallizer, crystallizer in addition continues
At the same temperature, what output of products amount and product quality can be synchronous is maintained at a high level, can so improve for operating
System availability, while product purity can also be improved；The series connection film-falling crystallization of second crystallization stage, the structure of multistage contrary operation
Think, preset material balance, heat balance with carefully controlling and be combined, the product of any required purity can be produced, by
In control setting can be changed easily to meet the change of product specification, considerable market potential can be won and reduction is manufactured into
This.
With reference to embodiment, the invention will be further described.
Embodiment
A kind of method that group technology using suspension crystallization and film-falling crystallization prepares bisphenol-A, comprises the following steps：
（One）Suspension crystallization
(1) at a temperature of 65-75 DEG C, reaction solution is adjusted in phenol, makes p, p- content of bisphenol A is 25-35 weight %；
(2) reaction solution is filled with crystallization reactor number n ＞ 1 n level cascaded suspension crystallizers at this temperature, will reacted molten
Liquid circulates in each crystallizer, cycle rate >=2000m3/ hour；
(3) in series-connected crystallizers, thermograde arrangement be from first crystallizer, 60 DEG C, second 50 DEG C of crystallization reactor,
Final 40 DEG C of crystallization reactor
(4) cleaned and/or dissolved using phenol, obtain bisphenol a/phenol crystalline adduct；Used as cleaning and/or dissolving
Phenol at least a portion be using refined phenol.
（Two）Fusion-crystallization
(1) temperature at 150-175 DEG C, under 1-150 millibar vacuum, by bisphenol a/phenol crystalline adduct phenol remove,
The melting bisphenol-A liquid phase finally given is less than 1% containing phenol；
(2) bisphenol-A liquid will be melted to be filled with n ＞ 1 falling-film crystallizer of n levels series connection, carries out multi-step melt liquid film-falling crystallization behaviour
Make；Obtain product.
Step（Two）Successively by feeding, crystallizing, raffinate into crystallizer in every grade of falling-film crystallizer in fusion-crystallization
Discharge, all sweating, melting and refined product discharge step；In charging, crystallization, raffinate discharge stage, set from 160-
125 DEG C of temperature ramps gradually dropped, in sweating, all melting and refined product discharging phase, set what is edged up from 125-160 DEG C
Temperature ramp.
Step（Two）Before melting bisphenol-A liquid enters falling-film crystallizer, addition sodium acid carbonate 1-50PPm, control pH5.05-
5.10 so that the decomposition loss of p, p- bisphenol-A is less than 0.5%, and product has good form and aspect.
Specific process parameter example is as follows：
（One）Suspension crystallization prevailing operating conditions are as follows：
(1) the composition composition of base feed
Bisphenol-A：25 weight %, phenol：65 weight %, other：10 weight %
(2) crystallization reactor number n=2；
Partial crystallization tower A：Temperature：60 DEG C, the residence time：120min
Partial crystallization tower B：Temperature：50 DEG C, the residence time：120min
（3）The composition composition of discharging solution
Bisphenol-A：47 weight %, phenol：52 weight %, other：1 weight %.Adjust purifying phenol and clean dosage, can effectively control
BPA relative to accessory substance composition.
（Two）Fusion-crystallization
（1）Multi-stage vacuum vapo(u)rization system removes phenol, and prevailing operating conditions are as follows：
Feeding temperature：120℃
One-level is evaporated：150 DEG C of pressure of temperature：10 supports
Dual evaporation：160 DEG C of pressure of temperature：5 supports
Three-level is evaporated：165 DEG C of pressure of temperature：1 support
Discharging melting bisphenol-A：Purity is 97.5%p, p-BPA, 1% phenol, (the assay method of other impurities 1.5%：Gas-chromatography
ASTM methods).
（2）Multi-stage falling-film crystallizes, and prevailing operating conditions are as follows：
Feeding temperature：170℃
Stage falling-film：170-125 DEG C of temperature, time 150min
Two level falling liquid film：170-125 DEG C of temperature, time 140min
Three-level falling liquid film：170-125 DEG C of temperature, time 120min
Product bisphenol-A：Purity is 99.92%p, p-BPA, 185ppm, o, p-BPA, other high-boiling-point impurities of 150ppm（Measure side
Method：Liquid chromatogram ASTM methods).
Claims (9)
1. a kind of method that group technology using suspension crystallization and film-falling crystallization prepares bisphenol-A, it is characterized in that：Including following step
Suddenly：
(1) suspension crystallization
(1) at a temperature of 65-75 DEG C, reaction solution is adjusted in phenol, makes p, p- content of bisphenol A is 25-35 weight %, excellent
It is 25 weight % to select content of bisphenol A；
(2) reaction solution is filled with crystallization reactor number n ＞ 1 n level cascaded suspension crystallizers at this temperature, will reacted molten
Liquid circulates in each crystallizer；
(3) in series-connected crystallizers, thermograde arrangement is second 50 DEG C of crystallization reactor from first 60 DEG C of crystallizer,
Final 40 DEG C of crystallization reactor；
(4) cleaned and/or dissolved using phenol, obtain bisphenol a/phenol crystalline adduct；
(2) fusion-crystallization
(1) temperature at 150-175 DEG C, under 1-150 millibar vacuum, by bisphenol a/phenol crystalline adduct phenol remove,
The melting bisphenol-A liquid phase finally given is less than 1% containing phenol；
(2) bisphenol-A liquid will be melted to be filled with n ＞ 1 falling-film crystallizer of n levels series connection, carries out multi-step melt liquid film-falling crystallization behaviour
Make, obtain product.
2. the method that the group technology according to claim 1 using suspension crystallization and film-falling crystallization prepares bisphenol-A, it is special
Sign is：N=2 in the n levels cascaded suspension crystallizer；In series-connected crystallizers, thermograde arrangement is first crystallizer
60 DEG C, second 50 DEG C of crystallization reactor.
3. the method that the group technology according to claim 1 or 2 using suspension crystallization and film-falling crystallization prepares bisphenol-A,
It is characterized in that：In step (1), cycle rate >=2000m that reaction solution is circulated in each crystallizer3/ hour.
4. the method that the group technology according to claim 1 or 2 using suspension crystallization and film-falling crystallization prepares bisphenol-A,
It is characterized in that：It is using refined phenol as at least a portion in the clean and/or phenol of dissolving in step (1).
5. the method that the group technology according to claim 1 or 2 using suspension crystallization and film-falling crystallization prepares bisphenol-A,
It is characterized in that：Successively by feeding, crystallizing, raffinate into crystallizer in every grade of falling-film crystallizer in step (2) fusion-crystallization
Discharge, all sweating, melting and refined product discharge step.
6. the method that the group technology according to claim 5 using suspension crystallization and film-falling crystallization prepares bisphenol-A, it is special
Sign is：In charging, crystallization, raffinate discharge stage, the temperature ramp gradually dropped from 170-125 DEG C is set.
7. the method that the group technology according to claim 5 using suspension crystallization and film-falling crystallization prepares bisphenol-A, it is special
Sign is：In sweating, all melting and refined product discharging phase, the temperature ramp to be edged up from 125-170 DEG C is set.
8. the method that the group technology according to claim 1 or 2 using suspension crystallization and film-falling crystallization prepares bisphenol-A,
It is characterized in that：Step (2) is before melting bisphenol-A liquid enters falling-film crystallizer, addition sodium acid carbonate 1-50ppm, control pH
5.05-5.10。
9. the method that the group technology according to claim 1 or 2 using suspension crystallization and film-falling crystallization prepares bisphenol-A,
It is characterized in that：The vacuum removal phenol step of step (2) uses multi-stage vacuum vapo(u)rization system.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710990086.0A CN107793296B (en) | 2015-08-12 | 2015-08-12 | Method for preparing bisphenol A by adopting combined process of suspension crystallization and falling film crystallization |
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| CN201510489640.8A CN105130758B (en) | 2015-08-12 | 2015-08-12 | The method that bisphenol-A is prepared using the group technology of suspension crystallization and film-falling crystallization |
| CN201710990086.0A CN107793296B (en) | 2015-08-12 | 2015-08-12 | Method for preparing bisphenol A by adopting combined process of suspension crystallization and falling film crystallization |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2090562A1 (en) * | 2008-02-06 | 2009-08-19 | Maciej Kiedik | A method to obtain polycarbonate-grade bisphenol A |
| CN101525274A (en) * | 2008-01-09 | 2009-09-09 | 拜尔材料科学股份公司 | Crystallization process for the preparation of bisphenols |
| CN101525276A (en) * | 2009-04-10 | 2009-09-09 | 南通星辰合成材料有限公司 | Process for synthesizing bisphenol A by utilizing cation resin |
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| PL210812B1 (en) * | 2007-02-14 | 2012-03-30 | Inst Ciężkiej Syntezy Organicznej Blachownia | The manner of obtaining of bisphenol A |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101525274A (en) * | 2008-01-09 | 2009-09-09 | 拜尔材料科学股份公司 | Crystallization process for the preparation of bisphenols |
| EP2090562A1 (en) * | 2008-02-06 | 2009-08-19 | Maciej Kiedik | A method to obtain polycarbonate-grade bisphenol A |
| CN101525276A (en) * | 2009-04-10 | 2009-09-09 | 南通星辰合成材料有限公司 | Process for synthesizing bisphenol A by utilizing cation resin |
Non-Patent Citations (1)
| Title |
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| 张勇: "双酚A生产过程中的化学工程问题", 《石油化工》 * |
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| CN105130758A (en) | 2015-12-09 |
| CN107793296B (en) | 2021-05-18 |
| CN105130758B (en) | 2017-12-08 |
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