Title: Fluidized bed furnace for burning partly dehydrated sludge and method of burning sludge in a fluidized bed furnace

Description: BRIEF DESCRIPTION OF THE DRAWING

In the Drawing:

FIG. 1 is a horizontal sectional view of a dehydrated sludge furnace constructed in accordance with the invention; and

FIG. 2 is a vertical sectional view of another embodiment of sludge furnace constructed in accordance with the invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

Referring to the drawing in particular, the invention embodied therein in FIG. 1 comprises a fluid bed furnace which, as shown in plan view, includes two semi-circular end walls 1 and 2 which join respective ends of an intermediate rectangular portion 6. The termination of the ends of the rectangular central section 6 is indicated by dotted lines 3 and 4. In this construction of furnace, in accordance with the invention, there is provided a post combustion chamber 5 which connects downwardly into the top or roof 50 of the combustion chamber which is located below the roof 50. The combustion chamber has the area of the entire roof 50, including the central rectangular section 6 and the two end cylindrical sections 6a and 6b. Air supply conduits 10 and 11 are connected tangentially into the post combustion chamber 5 for supplying sufficient after combustion air thereto. The sludge is advantageously charged through the roof 50 through an opening 7 provided for that purpose. A further opening 8 is provided for a burner which is directed downwardly through the roof 50 into the combustion chamber.

In the embodiment of the invention shown in FIG. 2, the fluidized bed furnace shown in vertical cross-section includes a bottom wall 52 over which a fluidized bed 12 is maintained. The fluidized bed includes refractory particles and it is maintained in a fluidized condition by directing heating gases upwardly through the bottom 52 through an inlet connection 54 leading to a plurality of upwardly directed nozzles 16. The heating gases are directed in the direction of the arrow 14 through the connection 54 and the nozzle 16 and they provide combustion air for the maintenance of combustion in the fluidized bed 12. In a preferred form, guide walls 56 immediately adjacent the bottom 52 flare upwardly and outwardly in order to increase the area of the fluidized bed immediately above the bottom 52.

In addition to the combustion which is maintained by the heated gases directed through the conduit 54, it is sometimes also necessary, usually periodically, to direct a combustible fuel into the furnace by means of burners 9 which are oriented at oblique sections 58 adjacent the top of the furnace side walls 60. Immediately above the fluidized bed 12, the furnace defines a combustion chamber 13 which is covered at the top by a substantially horizontal roof 50'.

After the gases are burned in the combustion space 13, they are passed upwardly through a post combustion chamber 19 which is of much smaller diameter or cross-section than the main combustion chamber 13. Advantageously, combustion air, which may be supplied through the conduit 14, is first passed into association with the post combustion chamber 19 which is designed as a recuperator, so that the air is preheated, before it is passed through the fluidized bed 12.

In accordance with a further feature of the invention, openings 7 are provided in furnace roof 50 for the direct feeding of the sludge which has been previously dehydrated. In the preferred form, the sludge is dehydrated preferably by centrifuge means 17 which are located directly above the openings 7.

The gases produced during the burning of the sludge in fluidized bed 12 burn out in the combustion chamber under supply of combustion air introduced laterally into the combustion chamber through nozzles 18 located on each side wall 60. Advantageously, this combustion air is also preheated in the recuperator so that a temperature of 800.degree. to 900.degree.C is maintained in combustion chamber 13. Should it not be possible to obtain this temperature by the sludge combustion, the heating burners 9 are put into operation by means of control means (not shown) until the conditions for the maintenance of the temperature of the sludge combustion are re-established. The combustion gases which leave the combustion chamber 13 and pass into the post combustion chamber are not completely burned. For this reason, secondary air is directed tangentially into the post combustion chamber 19 through two diametrically oppositely arranged inlet nozzles 10' and 11'. The post combustion chamber 19 is designed as a recuperator so that it is possible to simultaneously recuperate heat for heating up the combustion air. Preferably, the device comprises a radiation recuperator so as to permit the heat transfer by radiation of the dust containing flue gases.

The furnace includes an outlet connection 20 so that useless material may be discharged from the lower end of the bed 12.

The combustion chamber is advantageously provided with the oblique walls 58 at each side so that the burners 9 may be directed downwardly into the combustion chamber 13 and be in an orientation such that they will not be subject to the accumulation of dust and debris thereon and will be free from a risk of clogging. This is very important since the burners are not permanently in operation and frequently, they will be out of service for long periods. In addition to the fact that the oblique arrangement prevents the clogging of the burners, the position also ensures that the spacing between the burner walls and the refractory brickwork will not become clogged either due to their inclined disposition.

In order to ensure a satisfactory motion of the fluidized bed 12, particularly in the marginal zones at each end, the side walls 60 are enlarged outwardly and upwardly, preferably, by an angle .alpha. of from 15.degree. to 20.degree. relative to the vertical. The construction ensures that the entire surface of the fluidized bed can be kept in motion.

The post-combustion chamber advantageously has either a circular cross-section or an angular cross-section. an angular cross-section would be advantageous for the support of the post combustion chamber on the furnace roof because a formation of the post combustion chamber with two rectangular sides, for example, arranged opposite to each other, can be mounted directly on the upper edges of the longitudinal walls of the furnace roof 50', while the other two rectangular sides can project from the substantially plane furnace roof 50' vertically upwardly. In some instances, the furnace is constructed as a waste heat boiler, and in such instances, it is desirable to have the furnace of substantially rectangular cross-section. Post combustion chamber recuperator 19 would also advantageously be of rectangular cross-section which would continuously change with increasing height into a circular cross-section.

While specific embodiments of the invention have been shown and described in detail to illustrate the application of the principles of the invention, it will be understood that the invention may be embodied otherwise without departing from such principles.
Other info:


Inventors: Albrecht, Erhard (Essen, DT)

Application Number: 520208
Filing Date: 1974-11-01
Publication_date: 1976-03-02
Assignee: Rheinstahl AG (DT)
Primary Class(es): 110/243 110/252, 110/254
Other Classes:
US Patent Ref:

3515381	Jun, 1970	Foch	110/8.
3702595	Nov, 1972	Muirhead et al.	110/28.
3772998	Nov, 1973	Menigat	110/8.
3776150	Dec, 1973	Evans et al.	110/28.
3848549	Nov, 1974	Pryor et al.	110/8.
3863577	Feb, 1975	Steever et al.	432/58.

Other Refs:
Primary Examiner: Sprague, Kenneth W.
Assistant Examiner:
Attorney: McGlew and Tuttle