EP1549597A1 - Procede de recuperation de phenol a partir de flux aqueux - Google Patents
Procede de recuperation de phenol a partir de flux aqueuxInfo
- Publication number
- EP1549597A1 EP1549597A1 EP03817460A EP03817460A EP1549597A1 EP 1549597 A1 EP1549597 A1 EP 1549597A1 EP 03817460 A EP03817460 A EP 03817460A EP 03817460 A EP03817460 A EP 03817460A EP 1549597 A1 EP1549597 A1 EP 1549597A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- phenol
- aqueous
- salt
- polar solvent
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 238000000034 method Methods 0.000 title claims abstract description 26
- 238000011084 recovery Methods 0.000 title abstract description 13
- 150000003839 salts Chemical class 0.000 claims abstract description 34
- 239000012454 non-polar solvent Substances 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 10
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 claims description 36
- 239000000203 mixture Substances 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 239000012044 organic layer Substances 0.000 claims description 10
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000010410 layer Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims 2
- 239000003495 polar organic solvent Substances 0.000 claims 1
- 239000003921 oil Substances 0.000 description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 238000006386 neutralization reaction Methods 0.000 description 3
- 239000012074 organic phase Substances 0.000 description 3
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical group COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003278 mimic effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- KSSNXJHPEFVKHY-UHFFFAOYSA-N phenol;hydrate Chemical compound O.OC1=CC=CC=C1 KSSNXJHPEFVKHY-UHFFFAOYSA-N 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- 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
- C07C37/72—Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by liquid-liquid treatment
Definitions
- the invention is drawn generally to the field of the manufacture of phenol. Specifically, the invention is drawn to a method for the recovery of phenol from an aqueous stream, wherein the phenol is partitioned from the aqueous stream in such a way as to minimize the water and salt content of the phenol.
- BACKGROUND OF THE INVENTION It is very common in the manufacture of phenol to generate aqueous streams containing significant amounts of phenol either as the free phenol or as a phenate salt. In order to maximize yield and minimize the environmental impact of waste water streams, manufacturers undertake to recover as much of this phenol as possible.
- Phenol containing aqueous streams are generated from a number of sources in a phenol manufacturing facility.
- a primary source of these streams is from the recovery of phenol from non-phenol organic streams such as cumene and alpha-methylstyrene.
- the phenol is removed from these organic streams by extraction with an aqueous base such as sodium hydroxide to form an aqueous phenate solution.
- the phenol is subsequently sprung from the aqueous solution by neutralization with an appropriate acid.
- the sprung phenol is then separated from the aqueous layer and recycled to crude phenol processing.
- a drawback of adding phenol recovered in this fashion to a process stream is that the recovered phenol generally contains a substantial amount of water and dissolved salts carried over from the aqueous streams. The salts may subsequently precipitate in process equipment, causing damage and lengthy shutdowns for cleaning and repairs. [0004] It would therefore be desirable to provide a method for recovering phenol from salt containing aqueous streams that minimizes the quantity of water and dissolved salts carried over into the recovered phenol.
- SUMMARY OF THE INVENTION [0005]
- the present invention provides a method for minimizing the content of salt in phenol recovered from salt containing aqueous streams.
- the method of the present invention makes use of relatively non-polar solvents to improve the separation between phenol and salt containing water solutions.
- Preferred non-polar solvents are organic streams comprising cumene, alpha-methylstyrene or mixtures thereof due to their ready availability in a phenol manufacturing environment.
- phenol with a low salt content is recovered from a salt containing aqueous stream.
- the low salt content in the recovered phenol is accomplished by addition of a relatively non-polar solvent to the phenol containing aqueous stream prior to separation.
- relatively non-polar as referred to herein is meant non- polar relative to phenol and water.
- the process according to the current invention is applicable to process streams comprising water and phenol.
- an aqueous process stream is generated by extraction of phenol from an organic stream with an aqueous base such as sodium hydroxide to form an aqueous phenate solution.
- the phenol is subsequently sprung from the phenate solution by neutralization with an appropriate acid.
- a relatively non-polar solvent is added to the phenol water mixture.
- the combined mixture is then agitated to effect mixing of the phenol and non-polar solvent.
- the combined mixture is then separated into a phenol containing organic layer and a waste aqueous layer.
- Preferred solvents are organic streams comprising cumene, alpha-methylstyrene or mixtures thereof due to their ready availability in a phenol manufacturing plant.
- the organic streams utilized will generally comprise crude streams of cumene, alpha-methylstyrene or mixtures thereof that have been previously isolated from the decomposition of cumene hydroperoxide in the production of phenol.
- the solvent composition used be as a whole non- polar relative to water and phenol.
- the relatively non-polar solvent is added in a ratio to phenol of about 0.4:1 to about 1.2:1. More preferably the ratio of non-polar solvent to phenol is about 0.5: 1 to about 1 : 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
L'invention concerne un procédé amélioré de récupération de phénol à partir de flux aqueux. Ledit procédé consiste à ajouter un solvant relativement non polaire à un flux aqueux contenant du phénol afin d'améliorer la séparation du phénol du flux aqueux. L'amélioration entraîne un flux de phénol présentant un niveau de sel réduit récupéré à partir du flux aqueux.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2003/019538 WO2005005359A1 (fr) | 2003-06-20 | 2003-06-20 | Procede de recuperation de phenol a partir de flux aqueux |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1549597A1 true EP1549597A1 (fr) | 2005-07-06 |
Family
ID=34061430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP03817460A Withdrawn EP1549597A1 (fr) | 2003-06-20 | 2003-06-20 | Procede de recuperation de phenol a partir de flux aqueux |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP1549597A1 (fr) |
| JP (1) | JP2006503923A (fr) |
| CN (1) | CN1675153A (fr) |
| AU (1) | AU2003247583A1 (fr) |
| WO (1) | WO2005005359A1 (fr) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7779625B2 (en) | 2006-05-11 | 2010-08-24 | Kalypto Medical, Inc. | Device and method for wound therapy |
| JP7771765B2 (ja) * | 2022-01-13 | 2025-11-18 | 三菱ケミカル株式会社 | フェノールの製造方法及びフェノール組成物 |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004046039A1 (fr) * | 2002-11-20 | 2004-06-03 | Abb Lummus Global Inc. | Extraction de phenol d'eaux residuaires |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1075119B (de) * | 1960-02-11 | Phenolchemie Gesellschaft mit bt. schrankter Haftung, Gladbeck (Westf) | Verfahren zum Entphenolen von Abwassern | |
| GB517618A (en) * | 1938-07-27 | 1940-02-05 | George William Johnson | Improvements in the recovery of phenols from oils and waste aqueous liquors |
| GB711656A (en) * | 1951-04-24 | 1954-07-07 | Bataafsche Petroleum | Improvements in or relating to the recovery of phenols |
| US4298765A (en) * | 1980-03-26 | 1981-11-03 | Allied Corporation | Purification of phenol with reduced energy consumption |
| US4504364A (en) * | 1982-06-28 | 1985-03-12 | The Lummus Company | Phenol purification |
| IT1271279B (it) * | 1994-12-15 | 1997-05-27 | Enichem Spa | Processo per il recupero di fenolo da un flusso acquoso contenente na2 so4 |
| DE19954141A1 (de) * | 1999-11-11 | 2001-06-13 | Phenolchemie Gmbh & Co Kg | Verfahren zur Verringerung des Salzgehaltes in Hochsieder aufweisenden Fraktionen, die bei der Herstellung von Phenol aus Cumol anfallen, durch Extraktion |
-
2003
- 2003-06-20 WO PCT/US2003/019538 patent/WO2005005359A1/fr not_active Ceased
- 2003-06-20 AU AU2003247583A patent/AU2003247583A1/en not_active Abandoned
- 2003-06-20 EP EP03817460A patent/EP1549597A1/fr not_active Withdrawn
- 2003-06-20 CN CN03819256.XA patent/CN1675153A/zh active Pending
- 2003-06-20 JP JP2005503937A patent/JP2006503923A/ja active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004046039A1 (fr) * | 2002-11-20 | 2004-06-03 | Abb Lummus Global Inc. | Extraction de phenol d'eaux residuaires |
Non-Patent Citations (1)
| Title |
|---|
| See also references of WO2005005359A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1675153A (zh) | 2005-09-28 |
| WO2005005359A1 (fr) | 2005-01-20 |
| JP2006503923A (ja) | 2006-02-02 |
| AU2003247583A1 (en) | 2005-01-28 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 20050112 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
| AX | Request for extension of the european patent |
Extension state: AL LT LV MK |
|
| DAX | Request for extension of the european patent (deleted) | ||
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 20071117 |