Fluidized bed solid circulation system using pressure and density difference, fluidized bed reaction system having the same and solid circulation method

Abstract

Disclosed is provided to overcome problems of conventional methods using each of a solid discharge nozzle and a screw conveyer. According to one exemplary embodiment of the present invention, a fluidized bed system is provided to circulate solids using pressure and density difference. More particularly, a fluidized solid circulation system using pressure and density difference is characterized by comprising: a first fluidized bed reactor; a second fluidized bed reactor; a first cyclone; a second cyclone; a first pressure control valve; a second pressure control valve; a lower loop seal; an upper loop seal; and a control part, thereby circulating the solids between the first fluidized bed reactor and the second fluidized bed reactor.

Claims

1. A system for circulating solids being inside the fluidized bed reactors therebetween using pressure and density difference in a fluidized bed reaction system having a plurality of fluidized bed reactors each of which is injected with a fluidizing gas, and a plurality of cyclones which separate gases and entrained solids discharged from each of the plurality of fluidized bed reactors, wherein the fluidized bed circulation system using pressure difference comprises: a plurality of pressure control valves which are formed in each gas vent of a plurality of cyclones and control the internal pressure of each the plurality of fluidized bed reactor; a lower loop seal which interconnects lower portions of the two fluidized bed reactors and is injected with a fluidizing gas; an upper loop seal which interconnects sides of the two fluidized bed reactors and is injected with a fluidizing gas; and a control part which controls each the pressure control valves and makes a pressure difference, that is, a difference between the internal pressure of the two fluidized bed reactors to be over a predetermined pressure difference, thereby circulating solids between the two fluidized bed reactors.

2. The fluidized bed solid circulation system using pressure difference of the claim 1, wherein the lower loop seal comprises: a plenum which is equipped with a partition and is injected with a fluidizing gas from opposite sides; a distributor which is positioned at an upper portion of the plenum and has a plurality of pores, thereby permitting the fluidizing gas to move up to the upper portion; and a connection pipe which is positioned at an upper end of the distributor and each end portion of which is connected between the two fluidized bed reactors, thereby conveying the fluidizing gas to each the two fluidized bed reactors.

3. The fluidized bed solid circulation system using pressure difference of the claim 2, wherein the upper loop seal comprises: a solid inlet pipe which flows in solids from one of the two fluidized bed reactor; a solid outlet pipe which flows out solids to the other; and a U shaped pipe which is positioned between the solid inlet pipe and the solid outlet pipe, and there is a height difference between a solid inlet height of the solid inlet pipe and a solid outlet height of the solid outlet pipe.

4. A fluidized bed reaction system having a solid circulation system using pressure difference comprising: a first fluidized bed reactor which has a first fluidizing gas injection part to be injected with a fluidizing gas; a second fluidized bed reactor which has a second fluidizing gas injected part to be injected with a fluidizing gas; a first cyclone to which solids and gases are conveyed from the first fluidized bed reactor and which separates the conveyed solids and gases; a second cyclone to which solids and gases are conveyed from the second fluidized bed reactor and which separates the conveyed solids and gases; a first pressure control valve which is formed on a gas vent of the first cyclone and controls the internal pressure of the first fluidized bed reactor; a second pressure control valve which is formed on a gas vent of the second cyclone and controls the internal pressure of the second fluidized bed reactor; a lower loop seal which interconnects lower portions of the first fluidized bed reactor and the second fluidized bed reactor and is injected with a fluidizing gas; an upper loop seal which interconnects sides of the first fluidized bed reactor and the second fluidized bed reactor and is injected with a fluidizing gas; and a control part which controls each of the first pressure control valve and the second pressure control valve to make an internal pressure difference, that is, a difference between the internal pressure of the first fluidized bed reactor and the second fluidized bed reactor to be over a predetermined pressure difference, thereby circulating the solids between the first fluidized bed reactor and the second fluidized bed reactor.

5. The fluidized reaction bed system having a solid circulation system using pressure difference of the claim 4, wherein the predetermined pressure difference is P.sub.2 represented by Formula 1 as below: $\begin{array}{cc}{P}_2=P_1=H_4\left(1-{\mathrm{.Math.}}_{\mathrm{mf}}\right)\left({}_s-{}_g\right)\frac{g}{g_c},& \left[\mathrm{Formula}1\right]\end{array}$ where H.sub.4 is a difference between a solid bed height (H.sub.2) of the second fluidized bed reactor and a solid bed height (H.sub.1) of the first fluidized bed reactor, P.sub.1 is a pressure drop (pressure difference) [Pa] by the solid bed, corresponding to a height (H.sub.2) of the second fluidized bed reactor, .sub.mf is a voidage [] of the solid bed in the minimum fluidized bed condition, .sub.s is a solid density [kg/m.sup.3], .sub.g is a gas density [kg/m.sup.3], g.sub.c is a constant of gravitational acceleration, 1[(kgm)/(Ns.sup.2)], and g is gravitational acceleration, 9.8 [m/s.sup.2].

6. The fluidized bed reaction system having a solid circulation system using pressure difference of the claim 5, wherein the lower loop seal comprises: a plenum which is equipped with a partition and is injected with a fluidizing gas from opposite sides; a distributor which is positioned at an upper portion of the plenum and has a plurality of pores, thereby permitting the fluidizing gas to move up to the upper portion; and a connection pipe which is positioned at an upper end of the distributor and each end portion of which is connected between the first fluidized bed reactor and the second fluidized bed reactor, thereby conveying the fluidizing gas to each of the first fluidized bed reactor and the second fluidized bed reactor.

7. The fluidized bed reaction system having a solid circulation system using pressure difference of the claim 6, wherein the upper loop seal comprises: a solid inlet pipe which flows in solids from the second fluidized bed reactor; a solid outlet pipe which flows out solids to the first fluidized bed reactor; and a U shaped pipe which is positioned between the solid inlet pipe and the solid outlet pipe, and there is a height difference between a solid inlet height of the solid inlet pipe and a solid outlet height of the solid outlet pipe.

8. The fluidized bed reaction system having a solid circulation system using pressure difference of the claim 7, the solids are circulated from the first fluidized bed reactor to the second fluidized bed reactor through the lower loop seal, and recirculated from the second fluidized bed reactor to the first fluidized bed reactor through the upper loop seal.

9. The fluidized bed reaction system having a solid circulation system using pressure difference of the claim 8, the particle density of solids inside the first fluidized bed reactor is greater than that of solids inside the second fluidized bed reactor.

10. The fluidized bed reaction system having a solid circulation system using pressure difference of the claim 9, the first fluidized bed reactor is configured to be an oxidation reactor, and the second fluidized bed reactor is configured to be a reduction reactor.

11. A fluidized bed solid circulation method using pressure difference between a fluidized bed reaction system comprising: first and second fluidized bed reactors into which a fluidizing gas is flown respectively; first and second cyclones which separate gases and entrained solids discharged from each the first and second fluidized bed reactors; first and second pressure control valves which are formed on gas vents of each the first and second cyclones and control the internal pressure of each the first and second fluidized bed reactors; a lower loop seal which interconnects lower portions of the first and second fluidized bed reactors and is injected with a fluidizing gas; and an upper loop seal which interconnects sides of the first fluidized bed reactor and the second fluidized bed reactor and is injected with a fluidizing gas, wherein the solid circulation method circulates solids inside the first and second fluidized bed reactors by using pressure differences and comprises the steps of: inserting solid particles into the first and second fluidized bed reactors and the lower and upper loop seals on the same internal pressure condition in the first fluidized bed reactor and the second fluidized bed reactor; injecting a fluidizing gas into the first and second fluidized bed reactors and the lower and upper loop seals; controlling the internal pressure of the first fluidized bed reactor to be greater than that of the second fluidized reactor by that a control part controls the first pressure control valve and the second pressure control valve; rendering a pressure difference of the first fluidized bed reactor and the second fluidized bed reactor to reach a predetermined pressure difference; and circulating the solids between the first fluidized bed reactor and the second fluidized bed reactor.

12. The fluidized bed solid circulation method using pressure difference of the claim 11, wherein in the step of reaching a predetermined pressure difference, a height of a solid bed in the second fluidized bed reactor reaches a height of a solid inlet pipe (H.sub.UL), and a difference (H.sub.4) between a solid bed height of the first fluidized bed reactor and a solid bed height of the second fluidized bed reactor reaches a difference between a height of a connection portion where a solid inlet pipe of an upper loop seal is connected to the second fluidized bed reactor, and a height of a connection portion where a solid outlet pipe of the upper loop seal is connected to the first fluidized bed reactor.

13. The fluidized bed solid circulation method using pressure difference of the claim 12, wherein the predetermined pressure difference is P.sub.2 represented by Formula 1 as below: $\begin{array}{cc}{P}_2=P_1=H_4\left(1-{\mathrm{.Math.}}_{\mathrm{mf}}\right)\left({}_s-{}_g\right)\frac{g}{g_c},& \left[\mathrm{Formula}1\right]\end{array}$ where H.sub.4 is a difference between a solid bed height of the first fluidized bed reactor and a solid bed height of the second fluidized bed reactor, P.sub.1 is a pressure drop (pressure difference) [Pa] by the solid bed, corresponding to a height (H.sub.2) of the second fluidized bed reactor, .sub.mf is a voidage [] of the solid bed in the minimum fluidized bed condition, .sub.s is a solid density [kg/m.sup.3], .sub.g is a gas density [kg/m.sup.3], g.sub.c is a constant of gravitational acceleration, 1[(kgm)/(Ns.sup.2)], and g is gravitational acceleration, 9.8 [m/s.sup.2].

14. The fluidized bed solid circulation method using pressure difference of the claim 13, wherein in the step of circulating the solids, the solids are circulated from the first fluidized bed reactor to the second fluidized bed reactor through the lower loop seal, and recirculated from the second fluidized bed reactor to the first fluidized bed reactor through the upper loop seal.

15. The fluidized bed solid circulation method using pressure difference of the claim 14, wherein a reaction for increasing the density of the solid particles occurs in the first fluidized bed reactor, while a reaction for decreasing the density of the solid particles occurs in the second fluidized bed reactor.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The following drawings depict only preferable embodiments of the present invention and render the technical idea of the present invention to be understood more clearly with reference to the following detailed description. Therefore, the present invention is not limited to these drawings, in which:

(2) FIG. 1A is a schematic view of a multi fluidized beds reaction system to illustrate conventional solid circulation between a fast fluidized bed and a bubble fluidized bed.

(3) FIG. 1B is a schematic view of a multi fluidized beds reaction system to illustrate conventional solid circulation between a fast fluidized bed, a bubbling fluidized bed and a bubbling fluidized bed.

(4) FIG. 2 is a schematic view of a fluidized bed reaction system having a fluidized bed solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention.

(5) FIG. 3 is a flowchart of a fluidized bed solid circulation method using pressure and density difference according to the exemplary embodiment of the present invention.

(6) FIG. 4 is a block diagram showing a signal flow in a control part according to the exemplary embodiment of the present invention.

(7) FIG. 5 is a schematic view of a fluidized bed reaction system having a fluidized solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention when P.sub.1=P.sub.2.

(8) FIG. 6 is a schematic view of a fluidized bed reaction system having a fluidized solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention when P.sub.1>P.sub.2 and P.sub.2<P.sub.1.

(9) FIG. 7 is a schematic view of a fluidized bed reaction system having a fluidized bed solid circulation system using pressure and density difference according to the exemplary embodiment to illustrate a solid flow direction when P.sub.2P.sub.1.

DETAILED DESCRIPTION OF THE EMBODIMENTS

(10) Exemplary embodiments will now be described with reference to the accompanying drawings to understand objects, other objects, features and advantages of the present invention. However, the present invention is not limited to the exemplary embodiments described herein and may be embodied in different forms. Rather, the exemplary embodiments are provided so that this disclosure will be through and complete, and will fully convey the idea of the present invention to those of ordinary skilled in the art.

(11) In the description, when an element is referred to as being on the other element, it means that the element can be directly formed on the other element or interpose another element between them. Also, in the drawings, thickness of elements is exaggerated for easy understanding of technical features.

(12) In the description, exemplary embodiments will be described with reference to a top plan view and/or an end view as an ideal exemplary view of the present invention. In the drawings, thickness of membranes and areas is exaggerated for easy understanding of technical features. Thus, a form of exemplary views may be changed according to manufacture technologies and/or permissible errors. Therefore, exemplary embodiments of the present invention are not limited to the particular form illustrated but include changes in forms generated by manufacture processes. For instance, an area illustrated as a right angle may have a form of being rounded or having a predetermined curvature. Thus, areas as illustrated in the drawing have properties and the shape thereof is intended to illustrate a particular form but do not limit the scope of the invention. In many different exemplary embodiments, the terms such as first, second and etc., are used for the description of many different elements, these elements, however, should be not limited by such terms. These terms are merely used for the purpose of distinguishing one element from the others only. The exemplary embodiments described and embodied herein include their complementary embodiments.

(13) The terms used in the description are for the purpose of describing exemplary embodiments only and are not intended to limit the present invention. As used in the description, the singular forms are intended to include the plural forms as well, unless the context clearly indicates otherwise. The terms comprise and/or comprising used in the description do not the presence or addition of one or more other components.

(14) In describing exemplary embodiments hereinafter, many specific matters are provided to assist in more detailed explanation and comprehensive understanding of the present invention. However, it is apparent that the exemplary embodiments can be used by those of ordinary skilled in the art without those specific matters. In the description of the present invention, certain explanations which are commonly known but hardly related thereto are omitted in order to prevent unnecessary obscurity in explanation of the present invention.

(15) Hereinafter, according to the exemplary embodiment of the present invention, explained are configurations and functions of a fluidized bed reaction system 100 having a fluidized bed solid circulation system using pressure and density difference, and a solid circulation method. Firstly, FIG. 2 is a schematic view to illustrate a fluidized bed reaction system 100 having a fluidized bed solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention. And FIG. 3 is a flowchart to illustrate a fluidized bed solid circulation method using pressure and density difference according to the exemplary embodiment of the present invention. Also, FIG. 4 is a block diagram showing a signal flow in a control part according to the exemplary embodiment of the present invention.

(16) As illustrated in FIG. 2, the fluidized bed reaction system 100 having a fluidized bed solid circulation system using pressure and density difference according to the exemplary embodiment may be configured to include a first fluidized bed reactor 10, a second fluidized bed reactor 30, a first cyclone 20, a second cyclone 40, a first pressure control valve 25, a second pressure control valve 45, a lower loop seal 50, an upper loop seal 60 and etc.

(17) As illustrated in FIG. 2, the first fluidized bed reactor 10 and the second fluidized bed reactor 30 are bubbling fluidized beds capable of being performed on the condition of a low flow velocity, respectively. Gases and some of entrained solids discharged from the first fluidized bed reactor 10 are separated in the first cyclone 20, thereby recirculating the solids to the first fluidized bed reactor 10 and discharging the gases through a first vent 24. Similarly, gases and some of entrained solids discharged from the second fluidized bed reactor 30 are separated in the second cyclone 40, thereby recirculating the solids to the second fluidized bed reactor 30 and discharging the gases through a second vent 44.

(18) A first pressure control valve 25 is formed on one side of the first gas vent 24 and a second pressure control valve 45 is formed on the second vent 44, thereby controlling the pressure of each the first fluidized bed reactor 10 and the second fluidized bed reactor 30.

(19) The first fluidized bed reactor 10 and the second fluidized bed reactor 30 are interconnected to each other with the upper loop seal 60 and the lower loop seal 50, and a fluidizing gas is injected into the upper loop seal 60 and the lower loop seal 50 to fluidize solid particles being in the upper loop seal 60 and the lower loop seal 50, thereby rendering the behavior thereof similar to that of a fluidized phase. A gas required for the reaction may be used as a fluidizing gas to be injected into the upper loop seal 60 and the lower loop seal 50, a steam may be used for fluidization and separated by condensation after discharge, or an inert gas may be used therefor.

(20) Hereinafter, each configuration of the present invention will be described. As illustrated in FIG. 2, the first fluidized bed reactor 10 may be inserted with solids, have a built-in distributor 18 and include a first fluidizing gas injection part 11 into which a first fluidizing gas is injected, a first discharge part 12 through which gases and entrained solids are discharged, a first solid inlet 14 which flows in the solids discharged through a solid discharge part of the first cyclone, a solid inlet pipe 15 which is connected with the upper loop seal 60, a first pressure measurement part 16 which measures an internal pressure of the first fluidized bed reactor 10, and a solid discharge pipe 17 through which solids in a first solid bed 13 are discharged to the lower loop seal 50.

(21) Further, the first cyclone 20 flows in gases and entrained solids discharged from the first discharge part 12 of the first fluidized bed reactor 10, separates the flown solids and gases and circulates the solids to the first fluidized bed reactor 10 through a first circulation pipe 22 which is interposed between a first solid discharge part 21 and the first solid inlet 14, wherein a first gas discharge part 23 is connected with the first vent 24.

(22) Further, as illustrated in FIG. 2, the second fluidized bed reactor 30 may be inserted with solids, have a built-in distributor 38 and include a second fluidizing gas injection part 31 into which a second fluidizing gas is injected, a second discharge part 32 from which gases and entrained solids are discharged, a second solid inlet 34 which flows in the solids discharged through a solid discharge part of the second cyclone 40, a solid outlet pipe 35 which is connected with the upper loop seal 60, a second pressure measurement part 36 which measures an internal pressure of the second fluidized bed reactor 30, and a solid supply pipe 37 which flows in the solids from the lower loop seal 50.

(23) Further, the second cyclone 40 flows in gases and entrained solids discharged from the second discharge part 32 of the second fluidized bed reactor 30, separates the flown solids and gases and circulates the solids to the second fluidized bed reactor 30 through a second circulation pipe 42 which is interposed between a second solid discharge part 41 and the first solid inlet 34, wherein a first gas discharge part 43 is connected with the second vent 44.

(24) The first pressure control valve 25 equipped with the first gas vent 24 controls an internal pressure of the first fluidized bed reactor 10, while the second pressure control valve 45 equipped with the second gas vent 44 controls an internal pressure of the second fluidized bed reactor 30.

(25) And the lower loop seal 50 interconnects lower portions of the first fluidized bed reactor 10 and the second fluidized bed reactor 30 and is injected with a fluidizing gas through a third fluidizing gas injection part 51. The lower loop seal 50 is configured to include a plenum 52 which is equipped with a partition 53 and is injected with a fluidizing gas from opposite sides; a distributor 54 which is positioned at an upper portion of the plenum 52 and has a plurality of pores, thereby permitting the fluidizing gas to move up to the upper portion; and a connection pipe 55 which is positioned at an upper end of the distributor and each end portion of which is connected between the two fluidized bed reactors, thereby conveying the fluidizing gas to each of the first fluidized bed reactor 10 and the second fluidized bed reactor 30.

(26) The upper loop seal 60 interconnects sides of the first fluidized bed reactor 10 and the second fluidized bed reactor 30 and is injected with a fluidizing gas through a fourth fluidizing gas injection part 61. In particular, the upper loop seal 60 is configured to include a solid inlet pipe 62 which flows in solids from the second fluidized bed reactor 30, a solid outlet pipe 63 which flows out the solids to the first fluidized bed reactor 10, and a U shaped pipe which is positioned between the solid inlet pipe and the solid outlet pipe.

(27) The solid inlet pipe 62 is connected with the solid outlet 35 of the second fluidized bed reactor 30, and the solid outlet pipe 63 is connected with the solid inlet column 15 of the first fluidized reactor 10. Further, the solid outlet column 35 and the solid inlet column 15 are connected to have a height difference.

(28) As illustrated in FIG. 4, the control part controls the first pressure control valve 25 and the second pressure control valve 45 based on values measured in the first pressure measurement part 16 and the second pressure measurement part 36 to make an internal pressure difference in the first fluidized bed reactor 10 and the second fluidized bed reactor 30 to be over a predetermined pressure difference, thereby circulating solids between the first fluidized bed reactor 10 and the second fluidized bed reactor 30.

(29) Hereinafter, a solid circulation method will be described according to the configurations mentioned above. Firstly, solid particles are inserted into the first fluidized bed reactor 10 and the second fluidized bed reactor 30 and the lower loop seal 60 and the upper loop seal 50 on the same internal pressure condition in the first fluidized bed reactor and the second fluidized bed reactor (S10). And a fluidizing gas is injected into the first fluidized bed reactor 10 and the second fluidized bed reactor 30 and the lower loop seal 50 and the upper loop seal 60 (S20). FIG. 5 is a schematic view of a fluidized bed reaction system 100 having a fluidized solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention when P.sub.1=P.sub.2.

(30) In other words, on the same pressure condition in the first fluidized reactor 10 and the second fluidized reactor 30 (a pressure difference between the two fluidized beds is 0, that is, P.sub.2=0), solid particles are inserted into the first fluidized reactor 10 and the second fluidized reactor 30 and the solids inside the first and second fluidized bed reactor 10 and 30 are fluidized to convey the solids through the lower loop seal 50, thereby rendering a height (H.sub.1) of the first solid bed 13 inside the first fluidized bed reactor 10 to be equal to a height (H.sub.2) of the second solid bed 33 inside the second fluidized bed reactor 30. On this condition, the solids cannot be circulated and solid particles reside in the first fluidized bed reactor 10, the second fluidized reactor 30, the upper loop seal 60 and the lower loop seal 50.

(31) And the control part controls the first pressure control valve 25 and the second pressure control valve 45, thereby controlling an internal pressure of the first fluidized bed reactor 10 to be greater than that of the second fluidized reactor 30 (S30). FIG. 6 is a schematic view of the fluidized bed reaction system 100 having a fluidized solid circulation system using pressure and density difference according to the exemplary embodiment of the present invention when P.sub.1>P.sub.2 and P.sub.2<P.sub.1.

(32) In other words, when a pressure (P.sub.1) of the first fluidized bed reactor 10 becomes higher than a pressure (P.sub.2) of the second fluidized bed reactor (30) by controlling the first pressure control valve 25 which controls an internal pressure of the first fluidized bed reactor 10 and the second pressure control valve 45 which controls an internal pressure of the second fluidized bed reactor 30, as illustrated in FIG. 6, a height (H.sub.1) of the solid bed 13 in the first fluidized bed reactor 10 becomes lower and a height (H.sub.2) of the solid bed 33 in the second fluidized bed reactor 30 becomes higher, while conveying solids through the lower loop seal 50. In this case, since the height (H2) of the second solid bed 33 in the second fluidized bed reactor 30 is lower than a height (H.sub.UL) of the upper end of the solid inlet pipe 62 of the upper loop seal 60, the solids would not be circulated.

(33) In addition, a pressure between the first fluidized bed reactor 10 and the second fluidized bed reactor 30 reaches a predetermined pressure (S40). FIG. 7 is a schematic view of a fluidized bed reaction system 100 having a fluidized bed solid circulation system using pressure and density difference according to the exemplary embodiment to illustrate a solid flow direction when P.sub.2P.sub.1.

(34) That is, when a pressure difference between the first fluidized bed reactor 10 and the second fluidized bed reactor 30 (P.sub.2=P.sub.1P.sub.2) becomes increased more, as illustrated in FIG. 2, a height (H.sub.1) of the first solid bed 13 is decreased more while a height (H.sub.2) of the second solid bed 33 is increased more. Thus, when the height (H.sub.2) of the second solid bed 33 inside the second fluidized bed reactor 30 reaches a height (H.sub.UL) of a solid inlet in the upper loop seal 60, solid particles of the second fluidized bed reactor 30 are conveyed to the first fluidized bed reactor 10 through the upper loop seal 60. At this time, a height of the second solid bed 33 of the second fluidized bed reactor 30 is increased by H.sub.4 from a height of the first solid bed 13 of the first fluidized bed reactor 10, and a pressure (P.sub.1) added downwardly by solids corresponding to H.sub.4 becomes equal to a pressure difference (P.sub.2) between the two fluidized beds. Accordingly, the minimum pressure difference (P.sub.2) between the two reactors required for the solid circulation can be determined based on the formula 1 as bellow.

(35) $\begin{array}{cc}{P}_2=P_1=H_4\left(1-{\mathrm{.Math.}}_{\mathrm{mf}}\right)\left({}_s-{}_g\right)\frac{g}{g_c}& \left[\mathrm{Formula}1\right]\end{array}$

(36) wherein, H.sub.4 is a height difference between the first solid bed and the second solid bed

(37) P.sub.1 is a pressure drop (pressure difference) [Pa] by the solid bed corresponding to a height of H.sub.4

(38) P.sub.2 is the minimum pressure difference [Pa] required for solid circulation

(39) .sub.mf is a voidage [] of the solid bed in the minimum fluidized bed condition

(40) .sub.s is a solid density [kg/m.sup.3]

(41) .sub.g is a gas density [kg/m.sup.3]

(42) g.sub.c is a constant of gravitational acceleration, 1[(kgm)/(Ns.sup.2)]

(43) g is gravitational acceleration, 9.8 [m/s.sup.2]

(44) As a result, the first pressure control valve 25 and the second pressure control valve 45 controls the first fluidized bed reactor 10 and the second fluidized bed reactor 30 respectively to generate a pressure difference (P.sub.2) between the two fluidized beds. Such a pressure difference changes heights of solid beds being inside the first fluidized bed reactor 10 and the second fluidized bed reactor 30 to circulate the solids from the first fluidized bed reactor 10 to the second fluidized bed reactor 30 through the lower loop seal 50 and to complete a system for recirculating the solid from the second fluidized bed reactor 30 to the first fluidized bed reactor 10 through the upper loop seal 60 (S50).

(45) Meanwhile, as shown in the formula 1, since the minimum pressure difference (P.sub.2) between the first and second fluidized bed reactors 10, 30 required for the solid circulation is proportional to the density of particles, in order to make solid circulation between the first and second fluidized bed reactors 10, 30 smooth (that is, being capable of solid circulation at the lower pressure difference and increasing the amount thereof), it is advantageous that a particle density of solids inside the second fluidized bed reactor 30 is lower than a particle density of solids inside the first fluidized bed reactor 10.

(46) In other word, it is advantageous to proceed a reaction for increasing the density of solid particles in the first fluidized bed reactor 10 and a reaction for decreasing the density of solid particles in the second fluidized bed reactor 30.

(47) For instance, in the case of chemical-looping combustion reaction as below, in a view of solid particles, oxidation reaction is a reaction in which oxygen in the air is bound to Ni. In contrast, reduction reaction is a reaction in which NiO is changed into Ni by separating oxygen included in the solid particle. Accordingly, as reactions are proceeded, the density of solid particles is increased in an oxidation reactor while being decreased in a reduction reactor.

(48) Oxidation reaction of chemical-looping combustion: 4Ni+2O.sub.2.fwdarw.4NiO

(49) Reduction reaction of chemical-looping combustion: 4NiO+CH.sub.4.fwdarw.4Ni+CO.sub.2+2H.sub.2O

(50) Therefore, in the case of chemical-looping combustion, the first fluidized bed reactor 10 in FIG. 2 is used as an oxidation reactor in which the density of particles is increased and the second fluidized bed reactor 30 is used as a reduction reactor in which the density of particles is decreased, thereby being capable of solid circulation at the lower pressure difference and increasing the amount thereof at the same pressure difference.

(51) In addition, the system and method described above are not limited to the configurations and methods of the exemplary embodiments of the present invention but various alterations may be made thereto by selectively combing each the embodiments.

DESCRIPTION OF SYMBOL

(52) 10: a first fluidized bed reactor 11: a first fluidizing gas injection part 12: a first discharge part 13: a first solid bed 14: a first solid inlet 15: a solid inlet pipe 16: a first pressure measurement part 17: a solid discharge pipe 18: a first fluidized bed distributor 20: a first cyclone 21: a first solid discharge part 22: a first circulation pipe 23: a first gas discharge pipe 24: a first gas vent 25: a first pressure control valve 30: a second fluidized bed reactor 31: a second fluidizing gas injection part 32: a second discharge part 33: a second solid bed 34: a second solid inlet 35: a solid outlet pipe 36: a second pressure measurement part 37: a solid supply pipe 38: a second fluidized bed distributor 40: a second cyclone 41: a second solid discharge part 42: a second circulation pipe 43: a second gas discharge part 44: a second gas vent 45: a second pressure control valve 50: a lower loop seal 51: a third fluidizing gas injection part 52: a plenum 53: a partition 54: a distributor 55: a connection pipe 60: an upper loop seal 61: a forth fluidizing gas injection part 62: a solid inlet pipe 63: a solid outlet pipe 64: a U-shaped pipe 70: a control part 100: a fluidized bed reaction system having a solid circulation system using pressure and density differences