AR106813A1 - PROCESS FOR PURIFICATION OF PROPENE OXIDE - Google Patents
PROCESS FOR PURIFICATION OF PROPENE OXIDEInfo
- Publication number
- AR106813A1 AR106813A1 ARP160103608A ARP160103608A AR106813A1 AR 106813 A1 AR106813 A1 AR 106813A1 AR P160103608 A ARP160103608 A AR P160103608A AR P160103608 A ARP160103608 A AR P160103608A AR 106813 A1 AR106813 A1 AR 106813A1
- Authority
- AR
- Argentina
- Prior art keywords
- propene oxide
- feeding
- point
- extractive distillation
- feed point
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/32—Separation; Purification
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/04—Compounds containing oxirane rings containing only hydrogen and carbon atoms in addition to the ring oxygen atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Epoxy Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Se purifica óxido de propeno mediante destilación extractiva, alimentando óxido de propeno crudo que comprende entre 15 y 97% en peso de óxido de propeno, entre 2 y 84% en peso de metanol, y acetaldehído a un punto de alimentación A en la sección del medio de una columna de destilación extractiva; alimentando un solvente acuoso de extracción a un punto de alimentación B situado por encima del punto de alimentación A; y alimentando un compuesto reactivo de estructura R¹-Y-NH₂, donde Y es oxígeno o NR² y R¹ y R² son independientemente entre sí hidrógeno, un grupo alquilo o un grupo arilo, o una sal de dicho compuesto reactivo, al punto de alimentación B, punto de alimentación A o entre los puntos de alimentación A y B; retirando una corriente S1 de la parte superior de la columna de destilación extractiva para proporcionar un primer producto de óxido de propeno que contiene menos de 200 ppm de agua; y retirando una corriente S2 en un punto de remoción 5 a 25 etapas de separación teóricas por encima del punto de alimentación B para proporcionar un segundo producto de óxido de propeno que contiene entre 500 y 10000 ppm de agua.Propene oxide is purified by extractive distillation, feeding crude propene oxide comprising between 15 and 97% by weight of propene oxide, between 2 and 84% by weight of methanol, and acetaldehyde to a feed point A in the section of the medium of an extractive distillation column; feeding an aqueous solvent of extraction to a feeding point B located above the feeding point A; and by feeding a reactive compound of structure R¹-Y-NH₂, where Y is oxygen or NR² and R¹ and R² are independently from each other hydrogen, an alkyl group or an aryl group, or a salt of said reactive compound, at feed point B , feed point A or between feed points A and B; removing a stream S1 from the top of the extractive distillation column to provide a first propene oxide product containing less than 200 ppm of water; and removing a stream S2 at a removal point 5 to 25 theoretical separation stages above feed point B to provide a second propene oxide product containing between 500 and 10,000 ppm of water.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15196539 | 2015-11-26 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR106813A1 true AR106813A1 (en) | 2018-02-21 |
Family
ID=54705129
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP160103608A AR106813A1 (en) | 2015-11-26 | 2016-11-25 | PROCESS FOR PURIFICATION OF PROPENE OXIDE |
Country Status (4)
Country | Link |
---|---|
KR (1) | KR102022226B1 (en) |
AR (1) | AR106813A1 (en) |
TW (1) | TW201730170A (en) |
WO (1) | WO2017089080A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110003136B (en) * | 2019-04-26 | 2023-08-01 | 江苏扬农化工集团有限公司 | Method and device for removing aldehyde ketone impurities in HPPO process by using efficient auxiliary agent |
CN113512014B (en) * | 2021-08-06 | 2022-11-25 | 中触媒新材料股份有限公司 | Method for purifying epoxypropane containing aldehyde impurities |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2810662C3 (en) * | 1978-03-11 | 1982-03-25 | Bayer Ag, 5090 Leverkusen | Process for the purification of an epoxy or a mixture containing such |
IT1152299B (en) | 1982-07-28 | 1986-12-31 | Anic Spa | PROCEDURE FOR THE EXPOSSIDATION OF HYDRAULIC COMPOUNDS |
DE3780476T2 (en) | 1986-01-28 | 1992-12-17 | Enichem Sintesi | METHOD FOR EPOXYDING OLEFINIC COMPOUNDS. |
EP1247805A1 (en) | 2001-03-05 | 2002-10-09 | Degussa AG | Process for the epoxidation of olefins |
EP1424331A1 (en) | 2002-11-26 | 2004-06-02 | Degussa AG | Process for the epoxidation of olefins |
EP1424332A1 (en) | 2002-11-26 | 2004-06-02 | Degussa AG | Process for the purification of crude propene oxide |
US20040220433A1 (en) | 2003-03-28 | 2004-11-04 | Evert Van Der Heide | Process for the preparation of propylene glycol |
EP1489074A1 (en) | 2003-06-18 | 2004-12-22 | Degussa AG | Process for the epoxidation of propene |
-
2016
- 2016-11-02 WO PCT/EP2016/076321 patent/WO2017089080A1/en active Application Filing
- 2016-11-02 KR KR1020187012567A patent/KR102022226B1/en active IP Right Grant
- 2016-11-23 TW TW105138448A patent/TW201730170A/en unknown
- 2016-11-25 AR ARP160103608A patent/AR106813A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
WO2017089080A1 (en) | 2017-06-01 |
KR102022226B1 (en) | 2019-09-18 |
KR20180069835A (en) | 2018-06-25 |
TW201730170A (en) | 2017-09-01 |
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