Oxidation system with sidedraw secondary reactor
View Patent ↗Disclosed is an optimized process and apparatus for more efficiently and economically carrying out the liquid-phase oxidation of an oxidizable compound. Such liquid-phase oxidation is carried out in a bubble column reactor that provides for a highly efficient reaction at relatively low temperatures. When the oxidized compound is para-xylene and the product from the oxidation reaction is crude terephthalic acid (CTA), such CTA product can be purified and separated by more economical techniques than could be employed if the CTA were formed by a conventional high-temperature oxidation process.
1. A reactor system comprising:
a primary oxidation reactor defining a first liquid inlet, a first gas inlet, and a first outlet; and
a secondary oxidation reactor defining a second inlet and a second outlet, wherein said first outlet is coupled in fluid flow communication with said second inlet, wherein all fluid flow communication comprising a slurry between said first primary oxidation reactor and said secondary oxidation reactor is directed from said primary oxidation reactor to said secondary oxidation reactor, and wherein said secondary oxidation reactor is a bubble column reactor; wherein said first liquid inlet is not in fluid communication with said secondary oxidation reactor.
2. The reactor system of claim 1 wherein said primary oxidation reactor is a bubble column reactor.
3. The reactor system of claim 1 wherein said secondary oxidation reactor is located outside of said primary oxidation reactor.
4. The reactor system of claim 3 wherein at least a portion of said secondary oxidation reactor is located alongside said primary oxidation reactor.
5. The reactor system of claim 1 wherein said second reactor is not a piston flow reactor.
6. The reactor system of claim 1 wherein said primary oxidation reactor via defines a slurry outlet connected in fluid flow communication with said secondary oxidation reactor, wherein said slurry outlet is located between the top and bottom ends of said primary oxidation reactor.
7. The reactor system of claim 6 wherein said primary oxidation reactor defines therein a primary reaction zone, wherein said slurry outlet is space at least about 0.1 H i from the bottom and top ends of said primary reaction zone.
8. The reactor system of claim 7 , wherein said slurry outlet is spaced at least about 0.25 H i from the bottom and top ends of said primary reaction zone.
9. The reactor system of claim 1 wherein said primary oxidation reactor defines therein a primary reaction zone, wherein said secondary oxidation reactor defines therein a secondary reaction zone, wherein the ratio of the volume of said primary reaction zone to said secondary reaction zone is in the range of from about 4:1 to about 50:1.
10. The reactor system of claim 9 wherein said primary reaction zone has a ratio of maximum vertical height to maximum horizontal diameter in the range of from about 3:1 to about 30:1, wherein said secondary reaction zone has a ratio of maximum vertical height to maximum horizontal diameter in the range of from about 1:1 to about 50:1.
11. The reactor system of claim 9 wherein the ratio of the maximum horizontal diameter of said primary oxidation zone to the maximum horizontal diameter of said secondary oxidation zone is in the range of from about 0.1:1 to about 0.6:1, wherein the ratio of the maximum vertical height of said primary oxidation zone to the maximum vertical height of said secondary oxidation zone is in the range of from about 0.1:1 to about 0.9:1.
12. The reactor system of claim 9 wherein said primary reaction zone has a maximum diameter (D p ), wherein the volumetric centroid of said secondary reaction zone is horizontally spaced at least about 0.5 D p from the volumetric centroid of said primary reaction zone.
13. The reactor system of claim 12 wherein said primary reaction zone has a maximum height (H p ), wherein the volumetric centroid of said secondary reaction zone is vertically spaced less than 0.5 H p from the volumetric centroid of said primary reaction zone.
14. A reactor system comprising:
a primary oxidation reactor defining a first liquid inlet, a first gas inlet, and a first outlet;
a secondary oxidation reactor defining a second inlet and a lower slurry outlet, wherein said secondary oxidation reactor is a bubble column reactor, wherein said first outlet is coupled in fluid flow communication with said second inlet; and
a downstream flow conduit coupled in fluid flow communication with said lower slurry outlet, wherein all fluid flow communication comprising a slurry between said first primary oxidation reactor and said secondary oxidation reactor is directed from said primary oxidation reactor to said secondary oxidation reactor, and wherein said downstream flow conduit is not coupled in fluid flow communication with said primary oxidation reactor; wherein said first liquid inlet is not in fluid communication with said secondary oxidation reactor.
15. The reactor system of claim 14 further comprising a downstream liquor exchange vessel, wherein said downstream flow conduit is coupled in fluid flow communication with said downstream liquor exchange vessel.
16. The reactor system of claim 14 further comprising a downstream digestion reactor, wherein said lower slurry outlet is in fluid flow communication with said downstream digestion reactor.
17. The reactor system of claim 14 wherein said primary oxidation reactor is a bubble column reactor.
18. The reactor system of claim 14 wherein said secondary oxidation reactor is located outside of said primary oxidation reactor.
19. The reactor system of claim 18 wherein at least a portion of said secondary oxidation reactor is located alongside said primary oxidation reactor.
20. The reactor system of claim 14 wherein said primary oxidation reactor defines therein a primary reaction zone, wherein said secondary oxidation reactor defines therein a secondary reaction zone, wherein the ratio of the maximum horizontal diameter of said primary oxidation zone to the maximum horizontal diameter of said secondary oxidation zone is in the range of from about 0.2:1 to about 0.5:1, wherein the ratio of the maximum vertical height of said primary oxidation zone to the maximum vertical height of said secondary oxidation zone is in the range of from about 0.1:1 to about 0.9:1.