The invention relates to a pulp washing method used to re¬ move chemicals dissolved in IDquids, for example in con- nection with chemical or mechanical pulp washing or bleaching processes, or to replace the chemicals contained in a liquid. The invention also relates to a pulp washing machine for carrying out. this method.

The known washing methods belong to the categories of dif¬ fusion washjng, displacement washing, and pressing. Diffu¬ sion washers often are drum filters, boosted either by- vacuum or pressure. A displacement step using showers is often added to them. Displacement washers are either drums, wire machines or towers. In all washers the washing liquid ' generally moves in the counter-current direction in relation to the pulp to be washed. The desired washing water con¬ sumption is 2 to 2.5 cubic metres of water per one dry pulp ton. In order to reach a sufficiently good washing result, for example, four washing filters in series, or a multiphase drum displacement washer are often used. In principle, washing presses operate like pressure filters, that is to say, they remove liquid from pulp by pressure. Usually, these washing presses are either of a screw or a double roll type, but also drum presses have been tried.

Modern displacement towers and displacement drums are very efficient washing machines and they can cope with the total washing needs of the production line, even alone, but, on the other hand, they also are very expensive and large units.

Due to their high prices and big sizes, displacement towers

and displacement drums are not well suited for improving the efficiencies of existing washing lines. Washing filters can always be added in series to the line, but even this is re ^¬ latively expensive and it also requires the installing of diluting devices and, in addition to this, the configuration as a whole will then form a relatively large unit.

Washing presses are often used to enhance the existing washing lines. However, the most efficient of the known presses suitable for this purpose, the screw presses, cut so much of the fibers when kneading them under pressure against the perforated housing and the screw flange that they cannot in general be used in the production of high qualify chemi¬ cal pulp. Double ro l presses again are expensive but, on the other hand, very efficient devices by which an approxi¬ mately 1 per cent pulp can be dried to an about 40 per cent dry matter content.

The one-phase drum presses used to press pulp do not break the fibers and they would be suitable, also as far as their prices are concerned, to enhance the existing washing lines but they have not appeared efficient even when improved by a displacement step brought about by pumping. Pumping washing liquid evenly through a pressed pulp layer has turned out to be difficult and unefficient, and most often the displace¬ ment step has been omitted.

The object of the invention is to eliminate these diffi¬ culties, that, is to say, to create a simple, very reliably operating and sufficiently efficient washing device that will not. break fibers and, despite of that, is so cheap that it can be used to enhance existing washing lines. Further, the aim of the invention is the possibility to use the washing device in special situations as a press to dry pulp, for example, for provisional storage.

In order to achieve this aim the method according to this invention is characterized bv the facts disclosed in claim

1. The characterist cs of the machine according to the in¬ vention will be apparent, respectively, in claim "7•

The idea of the invention is to use the press for drying wood wastes, known as such, so that a detergent is fed to the pulp once or several times as it is running through the rotating drum, between the drum and the pressing ro inside it.

The basic machine can, for instance, be a press according to Patent. FI 62330, said patent being attached herewith as a reference. According to the invention, washing liquid feeding means will be added to the machine in suitable positions along the pulp feeding track. The detergent is advantageously fed to the pulp after every pressing step, whereafter washing liquid and all solid materials diluted in it will be removed by the next pressing step. Feeding the liquid to that side of the pulp layer that is farther away from the perforation results in a displacement effect, enhancing the washing procedure as such.

As the pulp under pressure, in the method according to the invention, does not move in relation to the pressing sur¬ faces, the pressing operation will not break the fibers in the way a screw press does.

In the following, the invention will be described in more detail, with references to the attached drawings illustra¬ ting one washing device structure, in connection of which a method according to the invention has been applied.

Fig. 1 shows a perspective of the washing device according to the invention, a d in a partly cut form.

Fig. 2 shows a side view of the device, and in a partly cut form.

Fig. 3 shows a cross section of the device.

The washing device comprises a rotatable, perforated drying drum 1, a rotatable pressing roll 2, a solid liquid feeding means 3, integral with the machine body, and a solid guiding plate assembly 4 consisting of pieces of screw threads. In practice, the guiding plate assembly 4 is easiest, to fix in the liquid feeding means 3, whereby they will form one in ^¬ tegrated entity. It is adv sab e to make the guiding plate assembly 4 such that the perimeter of the plates runs so near the drum surface that it wi l at the same time remove all pulp possibly attached to it. The drum 1 and the pressing roll 2 rotate in the direction shown by arrows. The pressing roll 2 is pressed downwards towards the drum sur¬ face so that the liquid will be pressed out from the pulp through the perforation of the drum 1. If so desired, also the roll 2 may be perforated. For other components than the feeding means 3, reference is made to said patent FI 62330.

The operation of the device has been illustrated by showing the incoming dirty pulp 10 by black and the outgoing washed pulp 11 by white and the intermediate phases in respective grey tones. The dirtyness of the liquid coming through the drum 1 is shown respectively.

The pulp to be washed 10 is fed to the washing device at the point 5. It. is advantageous to feed the pulp coming from the preceding washing step without diluting, at least in 12 per ^¬ cent consistency, in order not to increase the length of the drying drum excessively, or by using any suitable predrying method. The liquid is leaving pulp, and with it also some of the solid state matter, when it for the first time passes the pressing point between the roll 2 and the drum 1. If needed, the pulp can also be dried further by directing it several times through the pressing point, but in practice this is seldom necessary. Next, washing liquid 7 is added to the pulp by liquid feeding means 3. This liquid 7 flows to the pulp through the openings or holes in the trailing edge of the means 3 after every pressing movement., except, the last pressing. Thus, it is advantageous to feed the liquid

as near as possible to the surface of the pressing roll when it. most likely will come to contact with the whole layer of pulp and, in addition to this, also drive the dirtier liquid, by displacing it, in forward direction and out from the pulp.

Pulp is moved in longitudinal direction in relation to the drum (see the arrows in Fig. 2) by guiding plates 4 and, additionally, possibly by tilting the drum downwards in machine direction. After pressing, washing liquid is again added to the pulp and the operation will continue, as described above, as many times as determined by the drum 1 length and the pulp guiding plates 4. The last guiding plate 4 will at the same time push the pulp out from the machine. In practice, it is advantageous to close one end of the drum 1 by a non-rotatable cover plate 9, through the opening 5 of which the pulp is fed into the drum. If necessary, the out¬ flow of pulp from the drum 1 can be limited by a solid or an adjustable output end cover plate 8, to maintain the drum uniformly filled by pulp.

The washing liquid 6 can be recovered at every pressing phase and pumped to the preceding phase by the counter- current principle. Alternatively, it is possible to use the crossflow principle, i.e. to use in the phase the same, equally fresh washing liquid, without recovering and re¬ circulating it, as the washing is carried out at a fairly high consistency, depending on the conditions, between 15 to 30 per cent, whereby the consumption of washing liquid will diminish, anyway.

The washing liquid can, of course, also be fed to the pulp through the drum 1 or through the perforations of the pressing roll 2. Then the liquid feeding means 3 will, respectively, be outside the drum 1 or inside the pressing roll 2. In Fig. 3 there is a liquid feeding means con¬ structed parallell to the drum 1 or to the axle of the roll 2, as an open elongated box 12 against the perforation of

the roll, wherein the washing liquid pressure will be effective, and the periphery of which is sealed against the perforation of the roll like a suction box.

The advantages obtained by the present invention are signi¬ ficant:

As the washing itself is carried out at a fairly high con¬ sistency, the consumption of washing liquid will be very reasonable as compared with the washing result. The washing device can be constructed mechanically very resisting, as the liquid flows will be very small, compared with the fil¬ ter and drum displacement devices operating with low densi¬ ties, whereby no delicate wire surfaces are required, and, instead, thick steel pressing surfaces with bored or punched holes can be used. This kind of pressed pieces will never break unexpectedly and they will last long. Sealing between moving and solid elements is easy, as the pulp at high con¬ sistency will not leak through the sealings so easily as the aqueous, low consistency pulp, whereby, for example, a ^■ simple and reliable labyrinth packing can be used. In special situations, pulp can be dried, after stopping the washing liquid feed, by simply pressing it, e.g., for provisional storage. In case other arrangements in the mill allow it, the whole washing line is possible to be con¬ structed based on this kind of equipment, whereby there is no need at any of the steps to dilute the pulp more than for its boiling consistency, whereby also the amount of the liquid to be fed to the evaporation plant will diminish and contribute to savings.