MY112960A - Process for producing isopropyl alcohol - Google Patents
Process for producing isopropyl alcoholInfo
- Publication number
- MY112960A MY112960A MYPI96000652A MYPI19960652A MY112960A MY 112960 A MY112960 A MY 112960A MY PI96000652 A MYPI96000652 A MY PI96000652A MY PI19960652 A MYPI19960652 A MY PI19960652A MY 112960 A MY112960 A MY 112960A
- Authority
- MY
- Malaysia
- Prior art keywords
- ranging
- temperature
- isopropyl alcohol
- extraction agent
- pressure
- Prior art date
Links
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 title abstract 12
- 238000000034 method Methods 0.000 title abstract 3
- 239000003795 chemical substances by application Substances 0.000 abstract 4
- 238000000605 extraction Methods 0.000 abstract 4
- 239000007791 liquid phase Substances 0.000 abstract 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 239000002253 acid Substances 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 230000036571 hydration Effects 0.000 abstract 1
- 238000006703 hydration reaction Methods 0.000 abstract 1
- 238000011031 large-scale manufacturing process Methods 0.000 abstract 1
- 239000012071 phase Substances 0.000 abstract 1
- 229930195734 saturated hydrocarbon Natural products 0.000 abstract 1
- 239000011949 solid catalyst Substances 0.000 abstract 1
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
- C07C29/03—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
- C07C29/04—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/10—Monohydroxylic acyclic alcohols containing three carbon atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
IN A PROCESS FOR PRODUCING ISOPROPYL ALCOHOL BY DIRECT LIQUID PHASE HYDRATION OF PROPYLENE AND WATER IN THE PRESENCE OF A STRONG ACID SOLID CATALYST AT A HIGH TEMPERATURE AND A HIGH PRESSURE, THE REACTION IS CARRIED OUT AT A TEMPERATURE IN A RANGING BETWEEN 100? AND 250?C AND A PRESSURE IN A RANGING BETWEEN 60 AND 200 ATM IN AN EXCESS OF WATER. THEN, A LIQUID PHASE OF THE REACTION PRODUCT IS CONTACTED WITH AN EXTRACTION AGENT OF A SATURATED HYDROCARBON HAVING 3 OR 4 CARBON ATOMS AT A TEMPERATURE IN A RANGING BETWEEN THE CRITICAL TEMPERATURE OF THE EXTRACTION AGENT AND THE TEMPERATURE HIGHER THAN THE CRITICAL TEMPERATURE BY 40?C UNDER A PRESSURE RANGING BETWEEN THE CRITICAL PRESSURE OF THE EXTRACTION AGENT AND 200 ATM AT AN S/F RATIO RANGING BETWEEN 0.3 AND 3 WHICH IS CALCULATED FROM THE EQUATION OF THE AMOUNT OF THE EXTRACTION AGENT DIVIDED BY THE AMOUNT OF THE EXTRACT FEED. FINALLY, AFTER ISOPROPYL ALCOHOL IS EXTRACTED FROM THE LIQUID PHASE, IT IS SEPARATED FROM THE RESULTANT EXTRACT PHASE THUS OBTAINED. ACCORDING TO THIS PROCESS, THE ENERGY REQUIRED FOR CONCENTRATING ISOPROPYL ALCOHOL IS REDUCED, AND ALSO LARGE-SCALE PRODUCTION FACILITIES ARE NOT NECESSARY.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3713695 | 1995-02-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MY112960A true MY112960A (en) | 2001-10-31 |
Family
ID=12489207
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MYPI96000652A MY112960A (en) | 1995-02-24 | 1996-02-23 | Process for producing isopropyl alcohol |
Country Status (5)
| Country | Link |
|---|---|
| KR (1) | KR100219006B1 (en) |
| DE (1) | DE69605460T2 (en) |
| MY (1) | MY112960A (en) |
| SG (1) | SG50572A1 (en) |
| TW (1) | TW338031B (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101582001B1 (en) * | 2012-06-28 | 2015-12-31 | 주식회사 엘지화학 | Preparation method for isopropyl alcohol |
| JP7118898B2 (en) * | 2017-01-23 | 2022-08-16 | 株式会社トクヤマ | Isopropyl alcohol composition and method for producing isopropyl alcohol |
| KR102756239B1 (en) * | 2019-09-24 | 2025-01-17 | 주식회사 엘지화학 | Method for preraring isopropyl alcohol |
| KR102586512B1 (en) | 2020-06-23 | 2023-10-06 | 주식회사 엘지화학 | Method for preraring isopropyl alcohol |
| KR102792304B1 (en) * | 2021-05-06 | 2025-04-04 | 주식회사 엘지화학 | Method for preraring isopropyl alcohol |
| KR102673698B1 (en) * | 2021-05-31 | 2024-06-07 | 주식회사 엘지화학 | Method for preraring isopropyl alcohol |
| KR102673700B1 (en) * | 2021-05-31 | 2024-06-07 | 주식회사 엘지화학 | Method for preraring isopropyl alcohol |
| EP4488252A4 (en) * | 2022-08-22 | 2026-03-04 | Lg Chemical Ltd | PROCESS FOR THE PREPARATION OF ISOPROPYL ALCOHOL |
| KR20250037124A (en) * | 2023-09-08 | 2025-03-17 | 주식회사 엘지화학 | Method for preparing isopropyl alcohol |
| WO2025053403A1 (en) * | 2023-09-08 | 2025-03-13 | 주식회사 엘지화학 | Method of preparing isopropyl alcohol |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1249845B (en) * | 1965-07-24 | |||
| DE2429770C3 (en) * | 1974-06-21 | 1981-04-16 | Deutsche Texaco Ag, 2000 Hamburg | Process for the production of lower alcohols by direct catalytic hydration of lower olefins |
| US4469903A (en) * | 1983-09-21 | 1984-09-04 | Uop Inc. | Process for the production of isopropyl alcohol |
| JPS6225982A (en) * | 1985-07-29 | 1987-02-03 | Mitsubishi Heavy Ind Ltd | Method of concentrating and purifying alcohol |
| JPS6225983A (en) * | 1985-07-29 | 1987-02-03 | Mitsubishi Heavy Ind Ltd | Method of concentrating and purifying alcohol |
| DE3850772T2 (en) * | 1987-07-24 | 1994-11-03 | Japan As Represented By Minist | Experience in concentrating and cleaning alcohol. |
| FR2644453A1 (en) * | 1989-03-20 | 1990-09-21 | Centre Nat Rech Scient | PROCESS FOR THE PREPARATION OF MONOFUNCTIONALIZED CYCLIC TETRAMINES |
| JPH0327336A (en) * | 1989-06-26 | 1991-02-05 | Tsuushiyousangiyoushiyou Kiso Sangiyoukiyokuchiyou | Dehydration of alcohol |
-
1996
- 1996-02-17 TW TW085102041A patent/TW338031B/en not_active IP Right Cessation
- 1996-02-23 DE DE69605460T patent/DE69605460T2/en not_active Expired - Lifetime
- 1996-02-23 MY MYPI96000652A patent/MY112960A/en unknown
- 1996-02-23 SG SG9605309A patent/SG50572A1/en unknown
- 1996-02-24 KR KR1019960004512A patent/KR100219006B1/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| KR960031412A (en) | 1996-09-17 |
| SG50572A1 (en) | 2003-07-18 |
| KR100219006B1 (en) | 1999-09-01 |
| DE69605460D1 (en) | 2000-01-13 |
| DE69605460T2 (en) | 2000-07-20 |
| TW338031B (en) | 1998-08-11 |
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