Method for controlling circulation rate of solids in an interconnected fluidized bed

Patent metadata

Field	Value
Publication number	US-9895647-B2
Application number	US-201514731598-A
Country	US
Kind code	B2
Filing date	Jun 5, 2015
Priority date	Dec 12, 2014
Publication date	Feb 20, 2018
Grant date	Feb 20, 2018

Abstract

The present invention provides a method for dynamically controlling the circulation rate of solids in an interconnected fluidized bed. When an interconnected fluidized bed is operating, it is available to control the circulation rate of solids by adopting the steps of adjusting the height difference between the orifice on the weir and the bottom surface of the bed region, adjusting the cross-sectional area of the above orifice, or adjusting the height of the above weir. By using multiple ways, the circulation rate of solids can be improved substantially. In addition, the curve of circulation rate of solids can be converged to the maximum circulation rate of solids effectively.

First claim

The invention claimed is:

1. A method for dynamically controlling the circulation rate of solids in an interconnected fluidized bed, said interconnected fluidized bed comprising a plurality of bed regions respectively separated by a weir, a portion of said weirs having at least an orifice for passing a plurality of fluid-like particles, and for dynamically controlling the circulation rate of said fluid-like particles in said interconnected fluidized bed, said method comprising at least one step selected from the group consisting of:
adjusting the height difference between said orifice and a bottom surface of said bed region;
adjusting the cross-sectional area of said orifice; and
adjusting the height of said weir.

2. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 1 , wherein a fluid inlet module is disposed at the lower part of said bed regions for transporting fluid upwards.

3. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 2 , and further comprising a step of adjusting the fluid entering rate of said fluid inlet module for dynamically controlling the circulation rate of solids of said fluid-like particles in said interconnected fluidized bed.

4. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 1 , wherein said interconnected fluidized bed is connected with at least a solid feed module.

5. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 4 , and further comprising a step of adjusting the solid quantity of said fluid-like particles in said interconnected fluidized bed using said feed module for dynamically controlling the circulation rate of solids of said fluid-like particles in said interconnected fluidized bed.

6. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 4 , and further comprising a step of adjusting the solid type of said fluid-like particles in said interconnected fluidized bed using said feed module for dynamically controlling the circulation rate of said fluid-like particles in said interconnected fluidized bed.

7. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 1 , wherein said weir connects with a lifting module in said step of adjusting the height difference between said orifice and said bottom surface of said bed region.

8. The method for dynamically controlling the circulation rate of solids in the interconnected fluidized bed of claim 1 , wherein a gate is disposed and adjusted at said orifice in said step of adjusting the cross-sectional area of said orifice.

Assignees

• Institute Of Nuclear Energy Res Atomic Energy Council Exec Yuan R O C
• Iner Aec Executive Yuan

Inventors

• Chyou Yau Pin
• Chen Po Chuang
• Hsu Hung Te
• Wu Keng Tung

Classifications

• B01D53/346 Primary

  Controlling the process · CPC title

• B01J8/36

  with fluidised bed through which there is an essentially horizontal flow of particles · CPC title

• B01D53/62

  Carbon oxides · CPC title

• B01D53/83

  with moving reactants · CPC title

• B01D2257/504

  Carbon dioxide · CPC title