IP Library Granted Patent US 11,639,314
Granted Patent B2
US 11,639,314 · App. 16/792,585 · Granted May 2, 2023

Porous fired granulated body and method for manufacturing the same

Inventors: Akira Takahashi (Seto, JP); Junya Shimosato (Seto, JP); Takahiko Nakamura (Seto, JP); Noriyuki Tamura (Seto, JP)
Assignee: Itochu Ceratech Corporation
C04B38/0051C04B35/111C04B35/62685C04B35/62695C04B35/634C04B38/009C04B38/067C04B2111/0081C04B2235/3217C04B2235/3218C04B2235/60
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Quick Facts
Patent No.
US 11,639,314
App. No.
16/792,585
Granted
May 2, 2023
Kind
B2
Abstract

A porous fired granulated body is formed by consolidating numerous alumina particles to each other while letting mainly interconnected pores remain in network form across an entire cross section of a granulated body particle. The pores have an inner diameter controlled by a droplet diameter of a pore forming agent and have numerous precipitated alumina crystals formed on inner surfaces thereof. Manufacture is performed by spraying the pore forming agent (emulsion) onto a raw material to form a coating layer of the pore forming agent on a surface of the raw material particle and controlling the inner diameter of the pores. A porous fired granulated body of alumina having a high specific surface area and having higher strength for the same specific surface area can thus be provided by a simple manufacturing method.

Claims (20)

1. A method for manufacturing a porous fired granulated body comprising alumina particles consolidated to each other while letting interconnected pores remain in network form across an entire cross section of a granulated body particle, wherein the pores have an inner diameter controlled by a droplet diameter of a pore forming agent and have precipitated alumina crystals formed on inner surfaces thereof, the method for manufacturing the porous fired granulated body comprising: a granulating process of using a tumbling disk granulator, including a rotating plate, to wet-granulate a raw material comprising an alumina powder, while spraying on liquid agents; and a firing process of firing a granulated body; and

wherein the granulating process includes respective sub-processes of:

1) a process of performing primary spraying of a crystal precipitating agent on the raw material undergoing primary tumbling circulation along an outer peripheral portion of the rotating plate,

2) a process of performing secondary spraying of a pore forming agent on the primary sprayed raw material undergoing secondary tumbling circulation at an inner side of the primary tumbling circulation,

3) a process of performing tertiary spraying of a binder on the secondary sprayed raw material undergoing tertiary tumbling circulation at an inner side of the secondary tumbling circulation, and

4) a process of making the tertiary sprayed raw material progress in granulation growth through further tumbling circulation and adjusting particle size of the granulated body particle to a required diameter, and

the primary, secondary, and tertiary spraying are respectively performed at tumbling side portions of the primary, secondary, and tertiary tumbling circulations.

2. The method for manufacturing the porous fired granulated body according to claim 1 , wherein the raw material is an alumina powder with an Na 2 O content of not more than 0.3%.

3. The method for manufacturing the porous fired granulated body according to claim 2 , wherein the alumina powder is a calcined alumina powder with an Na 2 O content of not more than 0.1% and a median particle diameter of 0.1 to 100 μm.

4. The method for manufacturing the porous fired granulated body according to claim 1 , wherein a lubricant is added simultaneously in loading the raw material into a loading portion of the rotating plate in a batch or continuously.

5. The method for manufacturing the porous fired granulated body according to claim 1 , wherein a content of a soda component, in terms of Na 2 O, is less than 0.03%.

6. The method for manufacturing the porous fired granulated body according to claim 1 , wherein a pore diameter of pores in the granulated body particle is adjusted to be in a range of 0.5 to 50 μm and a biaxial mean diameter (arithmetic mean of major diameters and minor diameters) of the precipitated alumina crystals is 0.1 to 5 μm.

7. The method for manufacturing the porous fired granulated body according to claim 6 , wherein a mean particle diameter (median diameter) of the granulated body particle is 0.1 to 5 mm and a specific surface area (BET method) is 0.1 to 20 m 2 /g.

8. A method for manufacturing a porous fired granulated body comprising ceramic particles consolidated to each other while letting interconnected pores remain in network form across an entire cross section of a granulated body particle, and wherein the pores have an inner diameter controlled by a droplet diameter of a pore forming agent and have precipitated alumina crystals formed on inner surfaces thereof, the method for manufacturing the porous fired granulated body comprising: a granulating process of using a tumbling disk granulator, including a rotating plate, to wet-granulate a raw material comprising a ceramic powder, while spraying on liquid agents; and a firing process of firing a granulated body; and

wherein the granulating process includes respective sub-processes of:

1) a process of performing primary spraying of a crystal precipitating agent on the raw material undergoing primary tumbling circulation along an outer peripheral portion of the rotating plate,

2) a process of performing secondary spraying of a pore forming agent on the primary sprayed raw material undergoing secondary tumbling circulation at an inner side of the primary tumbling circulation,

3) a process of performing tertiary spraying of a binder on the secondary sprayed raw material undergoing tertiary tumbling circulation at an inner side of the secondary tumbling circulation, and

4) a process of making the tertiary sprayed raw material progress in granulation growth through further tumbling circulation and adjusting particle-size of the granulated body particle to a required diameter, and

the primary, secondary, and tertiary spraying are respectively performed at tumbling side portions of the primary, secondary, and tertiary tumbling circulations.

Continuity (2)
Division 15546372
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