The sealings of the ends of rotary drum driers are usually either so called labyrinth sealings or mechanical sealings having a seal ring that slides against the end of the kiln, hereinafter called mechanical sealings. The former are non-contacting sealings, the parts of which are formed in such a way that the flow resistance through the sealing is as great as possible. They are not totally tight, and thus gases and dust most often escape to the surroundings to some extent. In general, they are used when the pressure lower than the pressure of the surroundings prevails in the drum and when the conditions in the drum allow a small leakage from the surroundings into the kiln.

Better tightness is pursued by means of mechanical sealings, which are used in more demanding conditions, for example when reducing conditions prevail in the kiln and an air leakage through the sealing into the inside of the kiln would cause undesirable combustion reactions in the proximity of the leakage point.

Although having a simple structure, a labyrinth sealing is not applicable to all objects. A mechanical sealing, in turn, is more expensive and needs to be maintained significantly more often, as the slide surface needs to be lubricated in order to prevent or delay the wearing thereof. In the applications in which the dust in the kiln causes wearing, the sporadic access of dust onto the slide surfaces increases the wearing of the surfaces despite the lubrication, causing thus even a significant increase in the need of maintenance.

In causticizing plants of sulphate pulp mills, the lime is regenarated in rotary drum kilns. The recent development of the regeneration process has, however, led to situations where the area of the feed end of the kiln operates at a very high degree of feeding. Consequently, dry feed material (so called lime sludge) often gets out through the sealing and causes significant damage in the surroundings of the kiln due to excessive dusting. This happens despite the fact that in the area of the feed end of the drum at the point of the sealing there is a lower pressure inside the drum than in the surroundings. The dust leakage takes place because the particle size of lime sludge is very small, on average 10 - 20 jim. Hereby, when being in movement, the lime sludge flows like water, penetrating the sealing.

During the operation of a rotary drum, for example a rotary drum kiln, the end of the drum does not stay in position but moves in the direction of the axis of the drum to the extent of the longitudinal thermal expansion of the drum shell. The bend of the end of the drum depends upon the load it carries, which load varies according to the degree of feeding of the drum. It also has a radial displacemnet, the size of which is usually, depending upon the accuracy of manufacture, a few or a

few tens of millimeters. All these factors have to be taken into account in a sealing arrangement.

An object of the present invention is to create a sealing arrangement between the rotary drum and the stationary end chamber thereof arranged in a material flow relation with each other, which arrangement would be better than the known ones. The need of maintenance of such an arrangement is smaller than with sealings generally in use, such as with mechanical sealings, in which the moving and stationary parts of the sealing rub together.

By means of the arrangement, the leaking of gas and solid matter (dust) is also prevented.

The invention relates to a method of preventing leakages of gas and solid matter dust by using pressurized gas, such as air, at the connecting point of a rotary drum and a stationary end chamber, such as a feed chamber, at the end of which drum there are a vertical end surface and an opening through which the drum is connected to the stationary chamber. What is essential for the method is that pressurized gas is fed on the end surface of a rotary drum toward the center axis of the drum in such a way that the angle (a) between the feeding direction of the gas and the plane substantially perpendicular to the center axis of the rotary drum is 900 or less, and in such a way that, due to the effect of the gas flow, the end surface of the drum is located at a distance from the stationary surface, whereby they do not substantially rub together in a wearing way.

The present invention also relates to a sealing arrangement defined in the appended claims.

The present invention is based on the use of pressurized gas, such as air, which is guided to the sealing in such a way that it prevents the leaking of the gas and solid

matter dust from the connection point of a rotary drum kiln, and a stationary chamber, such as a feed chamber of a rotary drum kiln, and that as little air as possible is directed from the sealing out to the surroundings.

Furthermore, due to the effect of the gas flow, the pressure of the gas pushes the countersurfaces of the rotary drum and the end chamber away from each other.

Thanks to the air-floating brought about in this way, the countersurfaces of the rotary drum and the stationary system (feed chamber, sealing rings) do not rub together, at least not in wearing way. The advantageous aspect of the method according to the invention is that the sealing air flow required can be generated at an overall efficiency of a few kilowatts by means of a simple blower.

The sealing according to the invention operates well when said angle is 900, but thus the required amount of sealing gas is larger than with smaller angles. The sealing gas flow typically divides in two directions, i.e. to a blow inward into the sealing and to a leakage away from the sealing. When said angle is a right angle, the sealing gas flow is divided in such a way that about half of it flows out. Not even in a case like this is a large total amount of gas required, and thus this can be regarded as a completely satisfactory arrangement. It is advantageous that the sealing does leak outward to some extent, because thereby it can be ensured that there is no excessive leakage of ambient air to the process.

The energy of the gas can be most effectively guided to prevent the penetration of the solid matter dust through the sealing of the connection point by directing the sealing air or other sealing gas obliquely, i.e. in such a way that said angle is below 90". The oblique direction also prevents the air from passing outward from the sealing and becoming wasted air which does not contribute

to the sealing process. The smaller the angle between the radius of the drum and the direction of air on the plane passing through the radius and the center axis of the drum is, the better the direction of air. The angle is below 900, preferably about 50 to about 600, most preferably about 100 to about 300. However, the smaller the angle oi is, the higher the sealing structure becomes in the direction of the radius, and also the bigger the weight and the higher the price. Hence, the size of the angle has to be optimized in each case separately. The sealing arrangement in which a significant part of the gas, for example 30 W or more, flows outward from the sealing, may be quite satisfactory, in particular if it is cost-effective.

The present invention may also be applied to various apparatus comprising a rotary drum and a stationary end chamber arranged in a material flow relation with each other. A conventional apparatus included in this group is a horizontal rotary kiln which is used for calcination for example in chemical pulp and cement industry and in which the dust leakages to the surroundings of the kiln are a significant problem. These kinds of kilns are also used in other combustion processes. Drum applications are in general used in the following operations: heating/cooling of material, phase transition (e.g.

evaporation of liquid), and chemical reaction (e.g.

reduction and calcination) . This group includes rotary driers, rotary coolers for hot material, reduction kilns, calcinators etc.

The invention is illustrated in more detail with reference to the appended figures, in which Fig. 1 schematically illustrates a longitudinal cross- section of one end of a rotary drum kiln and a stationary feed end, to the connecting point of which the present invention is applied;

Fig. 2 illustrates an apparatus in accordance with Fig. 1 viewed from the end; Fig. 3 illustrates a cross-section of a sealing arrangement in accordance with the present invention, said sealing arrangement being used in Fig. 1; Fig. 4 illustrates a partial blow-up of Fig. 3; and Fig. 5 illustrates the connection of a sealing air line.

Fig. 1 shows the end on the side of the feed apparatus of the material in a rotary drum kiln 1. A kiln like this is used in the lime calcination and the manufacture of cement, for example. The rotary kiln comprises a horizontal, elongated rotary drum having a cylindric shell 11, which rotates in relation to a stationary feed chamber 12 of the material and to the discharge end (not shown) of the material at the opposite end of the drum.

The drum is horizontal or positioned gently inclined in a manner known as such. The material is fed into the chamber 12 through a channel 13. The flue gases flow in the opposite direction relative to the material to be treated and are discharged through the upper part 14 of the feed chamber.

A sealing as gas- and dust-tight as possible has to be arranged on the stationary surfaces of the feed chamber in connection with the rotary countersurfaces of the rotary drum. A sealing arrangement in accordance with the invention is generally denoted by reference numeral 15 in Fig. 1.

One sealing arrangement in accordance with the invention has been disclosed in more detail in Figs 3 and 4. The end 16 of the drum 11 is machined vertical, whereby the axial displacement thereof can be eliminated. A ring 17 made of wear-resisting material has been attached to the end of the drum, the countersurface of which is machined, if needed, in the corresponding way, toward the drum. In

other words, the ring 17 rotates along with the drum.

Reference numeral 29 denotes the kiln neck connected to the opening at the end of the kiln shell. The extension of the feed chamber extends as far as to the kiln neck.

By means of a counterweight system 21 (Figs. 1 and 2), a stationary sealing ring 18 (Fig. 3, Fig. 4) is pressed against the ring 17 and thus also against the end 16 of the drum, which sealing ring comprises a blow hole 22.

The hole is shaped as a circle or a polygon. It is directed obliquely in the direction of the radius R of the drum toward the center axis C of the drum 11 and gas is blown through it toward the inside of the kiln. In the plane passing through the radius and the longitudinal axis of the drum, an angle ot is formed between the blow hole 22 (and also the feeding direction S of the air) and the vertical plane being perpendicular to the center axis and passing through the radius R of the drum.

One essential feature of a preferred embodiment of the invention, namely the oblique direction of the blow hole, brings about many advantages. In this way, the energy can be guided in the best possible way to prevent the penetration of gas and dust out of the sealing. The oblique direction also decreases or prevents the passing of air through the sealing back outward, where it would become wasted air not contributing to the sealing process. The smaller the angle a is, the better the direction of air from the point of view of the functioning of the sealing. In the arrangement according to the figures, the angle a is about 150 (Fig. 4). In practice, the technical factors of manufacture determine how small the size of the angle is preferably adjusted.

In any case, the angle a has to be below 90". Preferably, it is about 50 to about 600, most preferably about 100 to about 300.

The angle of the blow hole is typically 25 - 450. The object of the bevelling is to decrease the inflow loss of the sealing gas out of the air distribution box into the hole, in other words to decrease the energy consumption of the sealing gas.

The sealing ring 18 is attached gas-tightly into an annular air distribution box 19, into which the sealing air or other gas is directed from an air blower 23 or other source of pressurized gas. The air distribution box, for its part, is attached by means of a flexible sealing bellows 20 or other sealing and flexible structural arrangement to the stationary feed end 12. The sealing bellows is made of material resistant to high temperature and dampness.

The sealing ring 18 is detached from the countersurface of the rotary drum, i.e. from the ring 17, by the pressure of the sealing air. The excessive growing of the distance or spacing formed hereby is prevented by means of the counterweight system 21 in such a way that by adding weights 24 the sealing ring 18 is pressed substantially against the countersurface, using, however, so little force that virtually no wearing of the surfaces results. The sealing ring 18 and the distribution chamber 19 of sealing air are supported against the feed end 12 by means of the structures of the counterweight system 21 in such a way that the sealing bellows 20 does not have to carry their weight.

Dust leakages through the sealing usually take place in the area of the lower part of the sealing. Hereby, there is a risk that sealing air escapes through the upper part of the sealing, where the additional flow resistance caused by the dust bed is absent or is significantly smaller than in the lower part. Escaping of sealing air in this way can be prevented or at least decreased by

dividing the annular air distribution box 19 into two halves. Fig. 5 illustrates such an arrangement. The air distribution box is divided into two halves 19a and 19b, into which the sealing air is guided through separate supply pipes 26 comprising valves 27 and pressure indicators 28 for controlling the air flow. The air that is directed to the upper part 19a is at a lower pressure than the air directed to the lower part l9b. If it is desirable to adjust the conditions at different points of the sealing ring in more detail, the chamber 19 may be divided by partition walls into even more parts.

The sealing arrangement may also be arranged on the cylindric part of the rotary cylinder end. This arrangement may, however, be less advantageous, while the rotary countersurface (ring 17) and the sealing ring 18 would rub together to a greater extent as a result of the radial displacement of the cylinder. In addition, the sealing bellows has to compensate not only the axial movement of the cylinder but also the radial displacement, and moreover, the supply of air into the distribution chamber 19 has to be arranged by means of flexible elements.

The present invention provides a method more reliable than the former ones of preventing the gas and dust leakages from the connecting point of a stationary member and a rotary member, such as a drum. By directing the gas flow in a particular way (angle a) it is possible to make the sealing gas flow in the desired direction. By directing the sealing gas at an overpressure preferably obliquely to the sealing of the connecting point, the possibility of such flows is significantly decreased. The sealing arrangements applying the principle of the invention also require very little maintenance compared with for example mechanical sealings usually used in this connection. In the sealing arrangement according to the invention, the stationary surface and the rotary surface do not rub together in a manner that would be substantially wearing (the countersurfaces do not actually come into contact with each other, at most they only touch each other very lightly from time to time).

The spacings between the countersurfaces are adjustable.

Also, the delivery, use and maintenance costs of the sealing arrangement are low.