YU101502A - Process control for acetic acid manufacture - Google Patents
Process control for acetic acid manufactureInfo
- Publication number
- YU101502A YU101502A YU101502A YUP101502A YU101502A YU 101502 A YU101502 A YU 101502A YU 101502 A YU101502 A YU 101502A YU P101502 A YUP101502 A YU P101502A YU 101502 A YU101502 A YU 101502A
- Authority
- YU
- Yugoslavia
- Prior art keywords
- process control
- concentration
- column
- acetic acid
- real time
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
- C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A method of real time process control in a reaction system for the procuction of acetic acid from the carbonylation of methanol. Raction system samples are collected from columns (30, 40, 50, 60, 70, 80) and/or transfer lines (120, 130, 140, 150, 160, 170, 180, 184, 186, 188, 190, 192, 194, 196, 197, 198, 199, 200, 210, 220) downstream of a reactor vessel (10), and the concentration of one or more components in the sample is measured by an infrared analyzer (90). The concentration measurements are then used to make adjustments in the concentration of components in the reaction system, directly or indirectly, such as by adjusting the temperature profile in a particular column (30, 40, 50, 60, 70, 80), the flow rate of solution in to or out of a column (30, 40, 50, 60, 70, 80), the vent gas rate out of the reactor (10) or a column (30, 40, 50, 60, 70, 80), or the addition or extraction of a component to or from the solution. For optimum process control, the measurements are transmitted to a control unit for real time analysis, and the adjustements are made substantially instantly after the infrared analysis.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/611,067 US6362366B1 (en) | 1998-12-18 | 2000-07-06 | Manufacturing and process control methods |
US09/672,893 US6552221B1 (en) | 1998-12-18 | 2000-09-29 | Process control for acetic acid manufacture |
Publications (1)
Publication Number | Publication Date |
---|---|
YU101502A true YU101502A (en) | 2006-05-25 |
Family
ID=47227300
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
YU101502A YU101502A (en) | 2000-07-06 | 2001-01-25 | Process control for acetic acid manufacture |
Country Status (3)
Country | Link |
---|---|
KR (1) | KR20030016370A (en) |
MY (1) | MY119549A (en) |
YU (1) | YU101502A (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3332594B2 (en) * | 1994-08-12 | 2002-10-07 | ダイセル化学工業株式会社 | Acetic acid purification method |
GB9625335D0 (en) * | 1996-12-05 | 1997-01-22 | Bp Chem Int Ltd | Process |
GB9626428D0 (en) * | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
GB9626429D0 (en) * | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
-
2001
- 2001-01-25 YU YU101502A patent/YU101502A/en unknown
- 2001-01-25 KR KR10-2003-7000128A patent/KR20030016370A/en not_active Application Discontinuation
- 2001-03-29 MY MYPI20011487A patent/MY119549A/en unknown
Also Published As
Publication number | Publication date |
---|---|
KR20030016370A (en) | 2003-02-26 |
MY119549A (en) | 2005-06-30 |
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