Calcination apparatus, process for producing oxide catalyst, and process for producing unsaturated acid or unsaturated nitrile

Patent metadata

Field	Value
Publication number	US-9643918-B2
Application number	US-201514874140-A
Country	US
Kind code	B2
Filing date	Oct 2, 2015
Priority date	Feb 18, 2011
Publication date	May 9, 2017
Grant date	May 9, 2017

Abstract

Disclosed is a calcination apparatus, including: a calcination tube having open ends at both terminals; a pair of hoods, each hood covering each open end of the calcination tube; and a pair of rings, each ring sealing a gap between the calcination tube and the hood, wherein the rings are directly or indirectly fixed on an outer surface of the calcination tube; a groove is provided along a circumferential direction of the ring at a contact surface side between the ring and the hood; a sealed chamber surrounded by the hood and the groove is formed; and both the calcination tube and the rings rotate in a circumferential direction of the calcination tube while keeping the hood in contact with both sides of the groove.

First claim

The invention claimed is:

1. A calcination apparatus, comprising:
a calcination tube having open ends at both terminals;
a pair of hoods, each hood covering each open end of the calcination tube; and
a pair of rings, each ring sealing a gap between the calcination tube and the hood,
wherein the rings are directly or indirectly fixed on an outer surface of the calcination tube;
a groove is provided along a circumferential direction of the ring at a contact surface side between the ring and the hood;
a sealed chamber surrounded by the hood and the groove is formed; a pair of flanges, each flange protruding from an inner surface of the hood toward an inside in a circumferential direction of the calcination tube,
wherein each of the plurality of annular members is in contact with each of the pair of flanges; and
both the calcination tube and the rings rotate in a circumferential direction of the calcination tube while keeping the hood in contact with both sides of the groove.

2. A calcination apparatus, comprising:
a calcination tube having open ends at both terminals;
a pair of hoods, each hood covering each open end of the calcination tube; and
a pair of rings, each ring sealing a gap between the calcination tube and the hood,
wherein the rings are directly or indirectly fixed on an outer surface of the calcination tube;
each of the rings comprises a plurality of annular members disposed in a width direction of the ring;
each of the plurality of annular members comes into contact with the hood;
a sealed chamber surrounded by at least the hood and the plurality of annular members is formed; a pair of flanges, each flange protruding from an inner surface of the hood toward an inside in a circumferential direction of the calcination tube, wherein each of the plurality of annular members is in contact with each of the pair of flanges and
both the calcination tube and the rings rotate in a circumferential direction of the calcination tube while keeping the hood in contact with the plurality of annular members.

3. The calcination apparatus according to claim 1 , wherein a space surrounded by at least the calcination tube, the rings, and the hood is maintained under an inert gas atmosphere; and the sealed chamber is filled with an inert gas.

4. The calcination apparatus according to claim 3 , wherein the hood comprises a supply port for supplying the inert gas to the sealed chamber.

5. The calcination apparatus according to claim 3 , wherein an atmospheric pressure within the space is higher than an atmospheric pressure outside the space.

6. The calcination apparatus according to claim 3 , wherein a pressure difference P1 represented by the following equation (1) is more than 0 mm H 2 O and 900 mm H 2 O or less:
P 1=(an atmospheric pressure within the space)−(an atmospheric pressure outside the space)  (1).

7. The calcination apparatus according to claim 3 , wherein a pressure difference P2 represented by the following equation (2) is more than 0 mm H 2 O and 500 mm H 2 O or less:
P 2=(a pressure of the sealed chamber)−(a pressure within the space)  (2).

8. The calcination apparatus according to claim 3 , wherein an oxygen concentration of the space is 1000 ppm or less.

9. The calcination apparatus according to claim 1 , further comprising a unit for imparting an impact to the calcination tube.

10. The calcination apparatus according to claim 2 , wherein a space surrounded by at least the calcination tube, the rings, and the hood is maintained under an inert gas atmosphere; and the sealed chamber is filled with an inert gas.

11. The calcination apparatus according to claim 10 , wherein the hood comprises a supply port for supplying the inert gas to the sealed chamber.

12. The calcination apparatus according to claim 10 , wherein an atmospheric pressure within the space is higher than an atmospheric pressure outside the space.

13. The calcination apparatus according to claim 10 , wherein a pressure difference P1 represented by the following equation (1) is more than 0 mm H 2 O and 900 mm H 2 O or less:
P 1=(an atmospheric pressure within the space)−(an atmospheric pressure outside the space)  (1).

14. The calcination apparatus according to claim 10 , wherein a pressure difference P2 represented by the following equation (2) is more than 0 mm H 2 O and 500 mm H 2 O or less:
P 2=(a pressure of the sealed chamber)−(a pressure within the space)  (2).

15. The calcination apparatus according to claim 10 , wherein an oxygen concentration of the space is 1000 ppm or less.

16. The calcination apparatus according to claim 10 , further comprising a unit for imparting an impact to the calcination tube.

Assignees

• Asahi Kasei Chemicals Corp

Inventors

• Tateno Eri
• Kaneta Masatoshi
• Fukuzono Toshihiko
• Watanabe Haruhiko

Classifications

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title

• F27D99/0073

  Seals · CPC title

• B01J6/004

  using hot gas streams in which the material is moved · CPC title

• B01J23/28

  Molybdenum · CPC title

• C07C253/24 Primary

  by ammoxidation of hydrocarbons or substituted hydrocarbons · CPC title