CIRCULATING FLUIDIZED BED GASIFICATION OR COMBUSTION SYSTEM

Abstract

The present invention is related to a circulating fluidized bed gasification or combustion system (1) using coal or biomass as raw material and comprising a combustion/gasification reactor (2); a cyclone (3) which is in connection with the reactor (2) in order that solid particles are separated from gas flow; a downcomer (4) which is in connection with the reactor (2) and the cyclone (3), extends along the reactor (2), and enables solid particles captured by the cyclone (3) to be sent to the combustion/gasification reactor (2) again; a distributing plate (5) which is in connection with the reactor (2) and performs primary gas supply to the system (1) homogeneously; at least one conduit which is positioned parallel to the downcomer (4); an ejector (7) which is positioned on the downcomer (4) vertically, comprises at least one nozzle (6) spraying pressurized gas towards the reactor (2).

Claims

1. A circulating fluidized bed gasification or combustion system using coal or biomass as raw material, comprising: a combustion/gasification reactor; a cyclone which is in connection with the combustion/gasification reactor in order that solid particles are separated from a gas flow; a downcomer which is in connection with the combustion/gasification reactor and the cyclone, extends along the combustion/gasification reactor, and enables the solid particles captured in the cyclone to be sent to the combustion/gasification reactor again; a distributing plate which is in connection with the combustion/gasification reactor and performs primary gas supply to the system homogeneously; wherein a ejector which is positioned on the downcomer vertically; comprises a nozzle suitable for spraying pressurized gas towards the combustion/gasification reactor and suitable for creating a solid column between the combustion/gasification reactor and the cyclone by creating vortexes on account of the fact that the pressurized gas sprayed by means of the nozzle spreads to the environment from the nozzle located on the downcomer in order to prevent counter flow of the solid particles and gas that may occur towards the downcomer and the cyclone from inside the combustion/gasification reactor.

2. The system according to claim 1, wherein an output pressurized gas can be air, superheated steam, nitrogen, carbon dioxide gas or any inert gases.

3. The system according to claim 1, further comprising a solid level meter/switch which measures a level of the solid column accumulating on an upper part of the ejector by means of the vortexes created by the ejector.

4. The system according to claim 1, wherein the ejector adjusts intensity of the vortexes, that is a resistance against a solid flow, by a flow-rate of the sprayed gas in order to control a flow-rate of the solid particles from the downcomer towards the combustion/gasification reactor.

5. (canceled)

6. The system according, to claim 2, further comprising a solid level meter/switch which measures a level of the solid column accumulating on an upper part of the ejector by means of the vortexes created by the ejector.

7. The system according to claim 2, wherein the ejector adjusts intensity of the vortexes, that is a resistance against a solid flow, by a flow-rate of the sprayed gas in order to control a flow-rate of the solid particles from the downcomer towards the combustion/gasification reactor.

8. The system according to claim 3, wherein the ejector adjusts intensity of the vortexes, that is a resistance against a solid flow, by a flow-rate of the sprayed gas in order to control a flow-rate of the solid particles from the downcomer towards the combustion gasification reactor.

9. The system according to claim 6, wherein the ejector adjusts intensity of the vortexes, that is a resistance against a solid flow, by a flow-rate of the sprayed gas in order to control a flow-rate of the solid particles from the downcomer towards the combustion/gasification reactor.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0019] FIG. 1 is a front view of the inventive system.

[0020] FIG. 2 is a view of the ejector included by the inventive system.

[0021] The components illustrated in the figures are individually numbered, where the numbers refer to the following:

[0022] 1. L System

[0023] 2. Reactor

[0024] 3. Cyclone

[0025] 4. Downcomer

[0026] 5. Distributing. plate

[0027] 6. Nozzle

[0028] 7. Ejector

[0029] 8. Solid Level Meter

[0030] a. Vortex

[0031] b. Solid Column.

DETAILED DESCRIPTION OF THE INVENTION

[0032] Circulating fluidized bed gasification or combustion system realized to fulfill the objectives of the present invention is shown in the figures attached, in which

[0033] The inventive circulating fluidized beef gasification or combustion system (1) comprises: at least one combustion/gasification reactor (2); at least one cyclone (3) which is in connection with the reactor (2) in order that solid particles such as coal biomass are separated from gas flow; at least one downcomer (4) which is in connection with the reactor (2) and the cyclone (3), extends along the reactor (2), and enables solid particles captured in the cyclone (3) to be sent to the combustion/gasification reactor (2) again; at least one distributing plate (5) which is in connection with the reactor and performs primary gas supply to the reactor (2) homogeneously; at lust one conduit (not shown in the figures) which is positioned parallel to the downcomer (4); at least one ejector (7) which is positioned on the downcomer(4) vertically, has at least one nozzle (6) spraying pressurized gas towards the reactor (2), and creates a solid column (b) between the reactor (2) and the cyclone (3) by creating, vortexes (a) on account of the fact that the pressurized gas sprayed by means of the said nozzle (6) spreads to the environment from the nozzle located on the downcomer (4) in order to prevent counter flow of particle and gas that may occur towards the downcomer (4) and the cyclone (3) from inside the reactor (2).

[0034] In the inventive system (1), as supply is performed into the reactor (2) homogeneously by means of the distributing plate (5) which is in connection with the reactor (2). Solid circulation is provided in the system (1) by the ejector (7) which is vertically positioned to the downcomer (4). The ejector (7) is used to create vortexes (a) on the upper part of the ejector (7) by enabling the pressurized gas flow towards the reactor (2) at high speeds from the nozzle which is positioned parallel to the downcomer (4). Flow-rate of solid flow which is downwards, in other words towards to the reactor (2), is controlled by means of the vortexes (a) created by the ejector (7). When the flow-rate of the gas exiting the ejector (7) is increased, intensity of the vortex (a) increases and thus resistance against solid flow increases, whereas resistance against solid flow reduces by decrease of intensity of the vortex (a) when the flow-rate of the gas is reduced. Therefore, control of solid flow-rate is ensured by increasing/decreasing flow-rate of the gas sprayed from the ejector (7). Resistance increases as the intensity of the vortex (a) created is increased and the solid column (b) occurs on the upper pact of the ejector (7) when a certain resistance level is reached. Discharge of the solid column (b) downwards is prevented by the vortexes (a) created by the high-speed gas sprayed from the ejector (7), Thus, solid flow is provided towards the reactor (2) at desired level. By this means, the solid flow-rate received from the cyclone (3) and the solid flow-rate sent downwards from the vortex (a) region become equal and thus the height of the solid column (.sub.h) remains fixed at the same height by

[0035] In the inventive system (1), pressurized gas, air, superheated steam, nitrogen, carbon dioxide gas or any inert gas can he used as propellant fluid.

[0036] The system (1) disclosed in an embodiment of the invention comprises at least one solid level meter switch (8) which measures the level of the solid column (b) accumulating on the upper part of the ejector (7) by means of the vortexes (a) created by the ejector (7). Thus, differences of solid flow-rate resulting from fluctuations that may occur during the process are compensated.

[0037] In the system (1) developed by the present invention, solid particles sent to the reactor (2) piss through a severe turbulence due to the Vortexes (a) created through the ejector (7) and agglomeration problem, which is frequently experienced in fluidized bed systems, is reduced by means of this severe turbulence. in addition to this, gas flow towards the cyclone (3) is stopped by means of the solid column (b) generated on the upper part of the ejector (7) by means of the vortexes (a) and the high-speed gas sprayed towards the reactor (2) from the ejector (7). Therefore, efficiency of the cyclone (3) is enhanced. By means of the system (1) developed by the present invention, a pressure barrier is generated without using systems with static (L valve, etc.) or fluidized bed (loop seal, etc) which are used to provide circulation loop of solid material in system with circulating fluidized bed.

[0038] Within these basic concepts, it is possible to develop various embodiments of the inventive Circulating Fluidized Bed Gasification or Combustion System, it cannot be limited to the examples disclosed herein and it is essentially according to the claims.