MXPA02011890A - Proceso para producir isopropanol de pureza ultra-elevada. - Google Patents
Proceso para producir isopropanol de pureza ultra-elevada.Info
- Publication number
- MXPA02011890A MXPA02011890A MXPA02011890A MXPA02011890A MXPA02011890A MX PA02011890 A MXPA02011890 A MX PA02011890A MX PA02011890 A MXPA02011890 A MX PA02011890A MX PA02011890 A MXPA02011890 A MX PA02011890A MX PA02011890 A MXPA02011890 A MX PA02011890A
- Authority
- MX
- Mexico
- Prior art keywords
- high purity
- isopropyl alcohol
- separation column
- purity isopropyl
- stream
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
- C07C29/80—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/20—Power plant
Abstract
Un proceso para producir alcohol isopropilico de alta pureza. En una forma de realizacion, el proceso comprende los pasos de: (a) alimentar una corriente de alimentacio que comprende al menos alrededor de 99.9% en peso de alcohol isopropilico a una columna de separacion; (b) separar el alcohol isopropilico en una corriente de cabezal tomada en el cabezal de la columna de separacion y una corriente de colas tomada como colas de la columna de separacion; y (c) remover el alcohol isopropilico de alta pureza en un punto: (i) debajo de donde la corriente de alimentacion entra a la columna de separacion pero sobre la corriente de colas, o (ii) sobre donde la corriente de alimentacion entra a la columna de separacion pero por debajo de la corriente de cabezal, donde el alcohol isopropilico de alta pureza tiene un contenido de metales de menos de alrededor de 1 ppmm y un contenido de agua de menos de alrededor de 100 ppm. De manera opcional, el proceso incluye el paso de hacer pasar el alcohol isopropilico de alta pureza a traves de una resina de intercambio ionico despues de remover el alcohol isopropilico de alta pureza de la columna de separacion, con ello formando un alcohol isopropilico de pureza ultra-elevada que contiene menos de 100 ppb de cualquier impureza de metal.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/587,103 US6733637B1 (en) | 2000-06-02 | 2000-06-02 | Process for producing ultra-high purity isopropanol |
PCT/US2001/016675 WO2001094284A2 (en) | 2000-06-02 | 2001-05-23 | Process for producing ultra-high purity isopropanol |
Publications (1)
Publication Number | Publication Date |
---|---|
MXPA02011890A true MXPA02011890A (es) | 2003-06-19 |
Family
ID=24348359
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MXPA02011890A MXPA02011890A (es) | 2000-06-02 | 2001-05-23 | Proceso para producir isopropanol de pureza ultra-elevada. |
Country Status (15)
Country | Link |
---|---|
US (1) | US6733637B1 (es) |
EP (1) | EP1299333B1 (es) |
JP (1) | JP4801870B2 (es) |
KR (1) | KR100790413B1 (es) |
CN (1) | CN1189436C (es) |
AR (1) | AR028653A1 (es) |
AT (1) | ATE341529T1 (es) |
AU (1) | AU2001264857A1 (es) |
BR (1) | BR0110695B1 (es) |
CA (1) | CA2408645C (es) |
DE (1) | DE60123615T2 (es) |
MX (1) | MXPA02011890A (es) |
MY (1) | MY126661A (es) |
TW (1) | TWI239944B (es) |
WO (1) | WO2001094284A2 (es) |
Families Citing this family (43)
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KR20050042026A (ko) * | 2001-10-31 | 2005-05-04 | 허니웰 인터내셔널 인코포레이티드 | 유기 용매 정제 |
US20090284732A1 (en) * | 2005-08-12 | 2009-11-19 | Vitale Rodney P | Apparatus and method of using thermochromic and photochromic indicators |
CN1332918C (zh) * | 2006-04-24 | 2007-08-22 | 广东西陇化工有限公司 | 超高纯醇类化合物的制备方法 |
JP5308645B2 (ja) * | 2007-08-29 | 2013-10-09 | オルガノ株式会社 | 陽イオン性不純物を含むアルコールの精製方法 |
FR2941452B1 (fr) * | 2009-01-27 | 2011-02-11 | Arkema France | Procede de purification de la fraction azeotropique generee lors de la synthese de l'acrylate de n,n-dimethyl aminoethyle |
CN102060663A (zh) * | 2009-11-18 | 2011-05-18 | 天津市康科德科技有限公司 | 色谱纯异丙醇的制备方法 |
CN102398895B (zh) * | 2010-09-16 | 2014-09-24 | 上海化学试剂研究所 | 一种超纯电子级化学试剂的生产方法 |
CN102399140B (zh) * | 2010-09-17 | 2015-04-15 | 联仕(上海)电子化学材料有限公司 | 一种超纯电子级醋酸的生产方法 |
CN102452897A (zh) * | 2010-12-06 | 2012-05-16 | 江苏达诺尔半导体超纯科技有限公司 | 超高纯异丙醇的生产工艺 |
JP5762861B2 (ja) * | 2011-07-15 | 2015-08-12 | オルガノ株式会社 | アルコールの精製方法及び装置 |
JP5762863B2 (ja) * | 2011-07-15 | 2015-08-12 | オルガノ株式会社 | アルコールの精製方法及び装置 |
JP5762860B2 (ja) | 2011-07-15 | 2015-08-12 | オルガノ株式会社 | アルコールの精製方法及び装置 |
JP5762862B2 (ja) * | 2011-07-15 | 2015-08-12 | オルガノ株式会社 | アルコールの精製方法及び装置 |
WO2013165602A1 (en) * | 2012-05-01 | 2013-11-07 | Entegris, Inc. | Organic solvent purifier and method of using |
EP2894141B1 (en) * | 2012-09-06 | 2018-03-28 | LG Chem, Ltd. | Method and apparatus for preparing isopropyl alcohol |
JP5930921B2 (ja) * | 2012-09-13 | 2016-06-08 | オルガノ株式会社 | アルコールの精製方法及び装置 |
CN103848718B (zh) * | 2012-12-06 | 2016-09-14 | 华东理工大学 | 离子交换纤维与微孔膜耦合柱制备电子级异丙醇的方法 |
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US9758458B2 (en) | 2013-08-20 | 2017-09-12 | Lg Chem, Ltd. | Method for purifying isopropyl alcohol |
US20160200649A1 (en) * | 2013-08-20 | 2016-07-14 | Lg Chem, Ltd. | Method for purifying isopropyl alcohol |
WO2015026161A1 (ko) * | 2013-08-20 | 2015-02-26 | 주식회사 엘지화학 | 이소프로필 알코올의 정제 방법 |
WO2015026160A1 (ko) * | 2013-08-20 | 2015-02-26 | 주식회사 엘지화학 | 이소프로필 알코올의 정제 방법 |
KR101662896B1 (ko) * | 2013-08-20 | 2016-10-05 | 주식회사 엘지화학 | 이소프로필 알코올의 정제 방법 |
WO2015026162A1 (ko) * | 2013-08-20 | 2015-02-26 | 주식회사 엘지화학 | 이소프로필 알코올의 정제 방법 |
JP2017119233A (ja) | 2015-12-28 | 2017-07-06 | オルガノ株式会社 | 有機溶剤の精製方法 |
JP2017119234A (ja) * | 2015-12-28 | 2017-07-06 | ダウ グローバル テクノロジーズ エルエルシー | 親水性有機溶媒のための精製プロセス |
JP6935399B2 (ja) * | 2016-06-17 | 2021-09-15 | 株式会社トクヤマ | イソプロピルアルコールの製造方法 |
KR102223128B1 (ko) * | 2016-12-13 | 2021-03-04 | 오르가노 코포레이션 | 이온교환체 충전 카트리지 및 금속제거칼럼 |
CN106748652B (zh) * | 2016-12-30 | 2020-04-03 | 安徽时联特种溶剂股份有限公司 | 一种去除工业级异丙醇中痕量金属杂质的方法 |
JP7118898B2 (ja) * | 2017-01-23 | 2022-08-16 | 株式会社トクヤマ | イソプロピルアルコール組成物及びイソプロピルアルコールの製造方法 |
KR102326779B1 (ko) * | 2017-07-05 | 2021-11-16 | 후지필름 가부시키가이샤 | 약액, 약액 수용체 |
TWI803499B (zh) * | 2017-07-26 | 2023-06-01 | 日商富士軟片股份有限公司 | 過濾裝置、純化裝置、藥液的製造裝置、已過濾的被純化物、藥液及感光化射線性或感放射線性樹脂組成物 |
US11905499B2 (en) | 2018-10-03 | 2024-02-20 | Tokuyama Corporation | High-purity isopropyl alcohol and method for manufacturing same |
CN112771015B (zh) * | 2018-10-05 | 2023-07-04 | 株式会社德山 | 异丙醇的制造方法 |
KR102552042B1 (ko) * | 2018-11-30 | 2023-07-05 | 주식회사 엘지화학 | 이소프로필 알코올의 정제방법 |
JP6819713B2 (ja) | 2019-03-27 | 2021-01-27 | 栗田工業株式会社 | 有機溶媒の処理方法及び処理材 |
WO2020217911A1 (ja) | 2019-04-26 | 2020-10-29 | オルガノ株式会社 | 有機溶媒の精製方法及び有機溶媒の精製装置 |
JP7219174B2 (ja) * | 2019-06-20 | 2023-02-07 | オルガノ株式会社 | 非水溶媒の精製方法 |
TW202146365A (zh) * | 2020-03-27 | 2021-12-16 | 美商富士軟片電子材料美國股份有限公司 | 用於純化溶劑之系統及方法 |
WO2021200936A1 (ja) | 2020-04-02 | 2021-10-07 | 株式会社トクヤマ | 半導体処理液及びその製造方法 |
KR102629120B1 (ko) * | 2020-11-09 | 2024-01-24 | 주식회사 엘지화학 | 석유화학 제품 내 메탈 성분 제거방법 |
CN113999094A (zh) * | 2021-09-30 | 2022-02-01 | 西安吉利电子新材料股份有限公司 | 一种直接生产电子级过氧化氢和丙酮的方法 |
CN114748885A (zh) * | 2022-05-20 | 2022-07-15 | 北京化工大学 | 一种电子级异丙醇的生产装置及其生产工艺 |
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US4399000A (en) | 1981-10-07 | 1983-08-16 | Georgia Tech Research Institute | Process for producing absolute alcohol by solvent extraction and vacuum distillation |
US4788043A (en) * | 1985-04-17 | 1988-11-29 | Tokuyama Soda Kabushiki Kaisha | Process for washing semiconductor substrate with organic solvent |
US4762616A (en) * | 1986-12-19 | 1988-08-09 | Shell Oil Company | Isopropyl alcohol purification process |
EP0284052B1 (en) * | 1987-03-25 | 1993-09-29 | Hitachi, Ltd. | Process for producing ultra-pure water and process for using said ultra-pure water |
JPH0680594A (ja) * | 1992-09-03 | 1994-03-22 | Daiso Co Ltd | 重金属除去方法 |
DE69408517T2 (de) | 1993-11-29 | 1998-09-10 | Mitsubishi Chem Corp | Verfahren und Vorrichtung zur Trennung eines Flüssigkeitsgemisches |
US5571387A (en) | 1994-09-13 | 1996-11-05 | Uop | Continuous single vessel distillation and adsorption process |
US5585527A (en) | 1994-10-31 | 1996-12-17 | Uop | Continuous distillation and membrane process |
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JPH09299702A (ja) * | 1996-05-16 | 1997-11-25 | Kyowa Yuka Kk | 蒸留方法 |
JP3560422B2 (ja) * | 1996-08-13 | 2004-09-02 | 株式会社トクヤマ | イソプロピルアルコールの精製方法 |
US5897750A (en) | 1997-08-28 | 1999-04-27 | Berg; Lloyd | Separation of acetone from isopropanol-water mixtures by extractive distillation |
-
2000
- 2000-06-02 US US09/587,103 patent/US6733637B1/en not_active Expired - Fee Related
-
2001
- 2001-05-23 JP JP2002501802A patent/JP4801870B2/ja not_active Expired - Fee Related
- 2001-05-23 CN CNB018104894A patent/CN1189436C/zh not_active Expired - Fee Related
- 2001-05-23 WO PCT/US2001/016675 patent/WO2001094284A2/en active IP Right Grant
- 2001-05-23 KR KR1020027016415A patent/KR100790413B1/ko not_active IP Right Cessation
- 2001-05-23 AU AU2001264857A patent/AU2001264857A1/en not_active Abandoned
- 2001-05-23 AT AT01939327T patent/ATE341529T1/de not_active IP Right Cessation
- 2001-05-23 EP EP01939327A patent/EP1299333B1/en not_active Expired - Lifetime
- 2001-05-23 CA CA002408645A patent/CA2408645C/en not_active Expired - Fee Related
- 2001-05-23 MX MXPA02011890A patent/MXPA02011890A/es active IP Right Grant
- 2001-05-23 BR BRPI0110695-3A patent/BR0110695B1/pt not_active IP Right Cessation
- 2001-05-23 DE DE60123615T patent/DE60123615T2/de not_active Expired - Lifetime
- 2001-05-30 MY MYPI20012571 patent/MY126661A/en unknown
- 2001-05-30 AR ARP010102586A patent/AR028653A1/es unknown
- 2001-06-01 TW TW090113392A patent/TWI239944B/zh not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
CA2408645C (en) | 2009-11-03 |
DE60123615T2 (de) | 2007-08-30 |
CN1431984A (zh) | 2003-07-23 |
WO2001094284A3 (en) | 2002-05-02 |
AU2001264857A1 (en) | 2001-12-17 |
EP1299333A2 (en) | 2003-04-09 |
AR028653A1 (es) | 2003-05-21 |
WO2001094284A2 (en) | 2001-12-13 |
EP1299333B1 (en) | 2006-10-04 |
KR100790413B1 (ko) | 2008-01-02 |
JP4801870B2 (ja) | 2011-10-26 |
KR20030007838A (ko) | 2003-01-23 |
JP2003535836A (ja) | 2003-12-02 |
US6733637B1 (en) | 2004-05-11 |
CA2408645A1 (en) | 2001-12-13 |
CN1189436C (zh) | 2005-02-16 |
TWI239944B (en) | 2005-09-21 |
DE60123615D1 (de) | 2006-11-16 |
MY126661A (en) | 2006-10-31 |
BR0110695B1 (pt) | 2012-06-12 |
ATE341529T1 (de) | 2006-10-15 |
BR0110695A (pt) | 2003-03-18 |
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