AR050721A1 - OXIDATION IN LIQUID PHASE WITH IMPROVED REAGENT DISTRIBUTION - Google Patents
OXIDATION IN LIQUID PHASE WITH IMPROVED REAGENT DISTRIBUTIONInfo
- Publication number
- AR050721A1 AR050721A1 ARP050103658A ARP050103658A AR050721A1 AR 050721 A1 AR050721 A1 AR 050721A1 AR P050103658 A ARP050103658 A AR P050103658A AR P050103658 A ARP050103658 A AR P050103658A AR 050721 A1 AR050721 A1 AR 050721A1
- Authority
- AR
- Argentina
- Prior art keywords
- oxidation
- oxidizable compound
- cta
- reaction
- reaction zone
- Prior art date
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Se describe un proceso y aparato optimizados para llevar a cabo de manera más eficiente y economica la oxidacion de un compuesto oxidable. Tal oxidacion en ase líquida se lleva a cabo en un reactor de columna de burbujas que provee una reaccion sumamente eficiente a temperaturas relativamente bajas. Cuando el compuesto oxidado es el paraxileno y el producto de la reaccion de oxidacion es ácido tereftálico bruto (CTA), tal producto CTA puede purificarse y separarse mediante técnica más economicas que las que se emplearían si el CTA se formara por un proceso de oxidacion convencional de alta temperatura. Reivindicacion 1: Un proceso que comprende: (a) introducir una corriente de oxidante que comprende oxígeno molecular en una zona de reaccion de un reactor de oxidacion inicial; (b) introducir una corriente de alimentacion que comprende un compuesto oxidable en dicha zona de reaccion, donde dicho compuesto oxidable tiene un punto de ebullicion de al menos aproximadamente 50 degree C, donde al menos aproximadamente 10 moles por ciento de dicho compuesto oxidable están en estado gaseoso cuando se introducen en dicha zona de reaccion; y (c) oxidar al menos una porcion de dicho compuesto oxidable en una fase líquida de un medio de reaccion multi-fásico.A process and apparatus optimized to carry out the oxidation of an oxidizable compound is described more efficiently and economically. Such oxidation in liquid ace is carried out in a bubble column reactor that provides an extremely efficient reaction at relatively low temperatures. When the oxidized compound is paraxylene and the oxidation reaction product is crude terephthalic acid (CTA), such CTA product can be purified and separated by more economical techniques than would be used if CTA were formed by a conventional oxidation process. high temperature Claim 1: A process comprising: (a) introducing an oxidant stream comprising molecular oxygen into a reaction zone of an initial oxidation reactor; (b) introducing a feed stream comprising an oxidizable compound in said reaction zone, wherein said oxidizable compound has a boiling point of at least about 50 degree C, where at least about 10 mole percent of said oxidizable compound are in gaseous state when they are introduced into said reaction zone; and (c) oxidizing at least a portion of said oxidizable compound in a liquid phase of a multi-phase reaction medium.
Applications Claiming Priority (27)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US60686604P | 2004-09-02 | 2004-09-02 | |
US60678504P | 2004-09-02 | 2004-09-02 | |
US60665304P | 2004-09-02 | 2004-09-02 | |
US60668904P | 2004-09-02 | 2004-09-02 | |
US60673004P | 2004-09-02 | 2004-09-02 | |
US60678704P | 2004-09-02 | 2004-09-02 | |
US60673704P | 2004-09-02 | 2004-09-02 | |
US60661904P | 2004-09-02 | 2004-09-02 | |
US60672504P | 2004-09-02 | 2004-09-02 | |
US63134504P | 2004-11-29 | 2004-11-29 | |
US63146404P | 2004-11-29 | 2004-11-29 | |
US63132704P | 2004-11-29 | 2004-11-29 | |
US63131504P | 2004-11-29 | 2004-11-29 | |
US63135604P | 2004-11-29 | 2004-11-29 | |
US63135204P | 2004-11-29 | 2004-11-29 | |
US63138304P | 2004-11-29 | 2004-11-29 | |
US63135104P | 2004-11-29 | 2004-11-29 | |
US63155904P | 2004-11-29 | 2004-11-29 | |
US11/154,139 US7371894B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,484 US7399882B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,482 US7390921B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/153,994 US7910769B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,221 US7586000B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,237 US7572932B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,201 US7741515B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,165 US7381836B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
US11/154,220 US7563926B2 (en) | 2004-09-02 | 2005-06-16 | Optimized liquid-phase oxidation |
Publications (1)
Publication Number | Publication Date |
---|---|
AR050721A1 true AR050721A1 (en) | 2006-11-15 |
Family
ID=37441641
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP050103658A AR050721A1 (en) | 2004-09-02 | 2005-09-01 | OXIDATION IN LIQUID PHASE WITH IMPROVED REAGENT DISTRIBUTION |
Country Status (3)
Country | Link |
---|---|
AR (1) | AR050721A1 (en) |
MY (1) | MY142452A (en) |
TW (1) | TW200624175A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114949889A (en) * | 2022-05-23 | 2022-08-30 | 中冶焦耐(大连)工程技术有限公司 | Pre-evaporator for coking crude benzene low-temperature hydrofining process |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116212776B (en) * | 2023-04-13 | 2024-09-10 | 江苏正丹化学工业股份有限公司 | Micro-nano gas-liquid reaction device for liquid phase air oxidation of pseudocumene |
-
2005
- 2005-09-01 MY MYPI20054096 patent/MY142452A/en unknown
- 2005-09-01 AR ARP050103658A patent/AR050721A1/en unknown
- 2005-09-02 TW TW094130029A patent/TW200624175A/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114949889A (en) * | 2022-05-23 | 2022-08-30 | 中冶焦耐(大连)工程技术有限公司 | Pre-evaporator for coking crude benzene low-temperature hydrofining process |
Also Published As
Publication number | Publication date |
---|---|
TW200624175A (en) | 2006-07-16 |
MY142452A (en) | 2010-11-30 |
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