Micro-interface enhanced oxidation system and oxidation method for preparing hydrogen peroxide
US-12090458-B2 · Sep 17, 2024 · US
US9339778B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9339778-B2 |
| Application number | US-201113581946-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 23, 2011 |
| Priority date | Mar 1, 2010 |
| Publication date | May 17, 2016 |
| Grant date | May 17, 2016 |
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A column-type solid-liquid countercurrent contact apparatus, a washing apparatus for solid particles such as poly(arylene sulfide) (PAS) particles, a PAS manufacturing apparatus, a method of solid-liquid countercurrent contact, a method of washing solid particles such as PAS particles, and a method of manufacturing PAS, wherein a column top part, a column body part, and a column bottom part are included, the column body part is provided with a plurality of stirring chambers connected in the vertical direction and mutually divided by a ring-shaped partitioning plate, a paddle blade (a blade diameter/a diameter of the stirring chamber≧0.65 and the blade diameter/the diameter of the stirring chamber≦0.10) and a baffle are disposed at each of the plurality of stirring chambers, and a disc having a size covering at least a part of a communication opening positioned below the paddle blade is attached to a rotating shaft or to the paddle blade.
Opening claim text (preview).
The invention claimed is: 1. A column-type solid-liquid countercurrent contact apparatus comprising a column top part, a column body part, and a column bottom part, for causing solid particles and a liquid to be subjected to countercurrent contact, the column body part including: a plurality of stirring chambers connected in a vertical direction and mutually divided by each of ring-shaped partitioning plates having a communication opening in the center thereof, each of the plurality of stirring chambers including: a paddle blade fixed to a shared rotating shaft passing through the communication opening of each of the ring-shaped partitioning plates, and satisfying the following formulas (1) and (2): (a blade diameter of the paddle blade)/(a diameter of the stirring chamber)≧0.65 formula (1) (a blade width of the paddle blade)/(the diameter of the stirring chamber)≦0.10 formula (2); at least one baffle extending in the vertical direction along an inner wall surface of the column body part; and a disc having a size covering at least a part of the communication opening positioned below the paddle blade, and being attached to the paddle blade so as not to have a gap between a circumference of the rotating shaft and the disc. 2. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein (a) the column top part includes a solid particle inlet through which the solid particles or a slurry containing the solid particles are supplied, (b) the column top part includes, at an upper part than the solid particle inlet, a liquid outlet through which the liquid is discharged, (c) the column bottom part includes a liquid inlet through which a liquid for contact with the solid particles is supplied, and (d) the column bottom part includes, at a lower part than the liquid inlet, a processed product outlet through which a processed product is removed, the processed product resulting from the solid particles being subjected to contact process with the liquid for contact. 3. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the paddle blade is a flat paddle blade. 4. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the paddle blade is disposed at a lower half region of each of the stirring chambers. 5. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein a ratio of an area of the communication opening of each of the ring-shaped partitioning plates in a horizontal direction to a cross-sectional area of each of the stirring chambers in the horizontal direction is within a range of 4 to 25%. 6. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the communication opening has a circular shape. 7. The column-type solid-liquid countercurrent contact apparatus according to claim 6 , wherein the disc has a circular shape, and a diameter thereof is larger than that of the rotating shaft and has a ratio within a range of 0.3 to 1.2 times the diameter of the communication opening of each of the ring-shaped partitioning plates. 8. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein a ratio H/D between a height H and an inner diameter D of each of the stirring chambers is within a range of 0.2 to 3.0. 9. The column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the solid particles are poly(arylene sulfide) particles. 10. A solid particle washing apparatus comprising the column-type solid-liquid countercurrent contact apparatus according to claim 1 . 11. A poly(arylene sulfide) manufacturing apparatus comprising the column-type solid-liquid countercurrent contact apparatus according to claim 1 . 12. A method of solid-liquid countercurrent contact of solid particles using the column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the method comprises inputting the solid particles into the apparatus such that the particles move downward through the stirring chambers while liquid moves upward through the stirring chambers. 13. A method of washing solid particles using the washing apparatus according to claim 10 , wherein the method comprises inputting the solid particles into the apparatus such that the particles move downward through the stirring chambers while liquid moves upward through the stirring chambers. 14. A method of solid-liquid countercurrent contact of poly(arylene sulfide) particles using the column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the method comprises inputting the particles into the apparatus such that the particles move downward through the stirring chambers while liquid moves upward through the stirring chambers. 15. A method of manufacturing poly(arylene sulfide) using the column-type solid-liquid countercurrent contact apparatus according to claim 1 , wherein the method comprises inputting poly(arylene sulfide) particles into the apparatus such that the particles move downward through the stirring chambers while liquid moves upward through the stirring chambers. 16. A method of washing poly(arylene sulfide) particles using the washing apparatus according to claim 10 , wherein the method comprises inputting the particles into the apparatus such that the particles move downward through the stirring chambers while liquid moves upward through the stirring chambers.
Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction (B01J8/0285, B01J8/067, B01J8/087, B01J8/1836 take precedence) · CPC title
of sulfides · CPC title
Compositions of polyethers obtained by reactions forming an ether link in the main chain (of polyacetals C08L59/00; of epoxy resins C08L63/00; of polythioether-ethers C08L81/02; of polyether-sulfones C08L81/06); Compositions of derivatives of such polymers · CPC title
inside the bed, e.g. rotary mixer · CPC title
inside the bed, e.g. baffles · CPC title
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