The present invention concerns an intermittently operating pressurized filter for concentrating a solid matter suspension, comprising a filter tank and on this tank an inlet conduit provided with a supply pump, for introducing under pressure the suspension to be filtered, and an outlet conduit provided with a valve, for removing the concentrated sludge, and a plurality of filtering elements suspended from the roof, the filtrate flowing through these elements and the interior of these elements communicating with a filtrate collecting tank located thereabove and thereby collecting sludge on their external surface, and this sludge being arranged to be intermittently detached by voiding the pressure within the filtering tank by opening for the suspension residing therein an exit flow through a drain conduit, whereby the filtrate in the collecting tank will pass in countercurrent fashion through the filtering elements, and in said pressurized filter the filtrate being arranged during the filtering step to be removed through a filtrate draining conduit departing from the collecting tank, under effect of the pressure produced by the supply pump in the suspension inlet conduit.
A pressurized filter of this type is eminently suitable for use in filtering white liquor from lime milk in the digesting liquor regenerating process in sulphate pulp mills, but it is also well applicable in other filtering operations.
The problem in connection with pressurized filters of this type known in the art is the removal of the sludge from the surface of the filtering elements. As taught by the present invention, this problem is solved in a simple manner. The invention is characterized in that the collecting tank is of enclosed construction, and that the sludge has been arranged to be removed from the surface of the filtering elements with the aid of the hydrostatic pressure of the filtrate residing in the collecting tank, by applying atmospheric pressure to the draining conduit of the collecting tank. The filtrate will then flow in countercurrent fashion through the filtering elements and it will detach the sludge from the filtering elements.
The draining conduit of the filtering tank is usually connected to a washing tank. One advantageous embodiment of the invention is then characterized in that the filtrate draining conduit departing from the collecting tank is connected by a falling pipe, provided with a valve, to the washing tank and that the draining conduit of the collecting tank has been arranged so that it can be placed under atmospheric pressure by opening the valve in the falling pipe.
One advantageous embodiment of the invention is characterized in that the collecting tank has been subdivided by means of partitions into sections, a specific branch conduit provided with a valve departing from each such section, and that these branch conduits have been joined to constitute a common draining conduit. Thanks to this arrangement, any one section can be shut off to be inoperable. This is necessary in the case that it is observed that the filtrate coming into the particular section is impure, this constituting a sign indicating that one of the filtering elements, or filtering mantles, supplying filtrate into this section is damaged.
The invention shall be described in the following, making reference to the attached drawing, wherein:
FIG. 1 displays a pressurized filter, according to an embodiment of the invention, sectioned and incorporated in a diagram of operation.
FIG. 2 presents the pressurized filter according to another embodiment, sectioned.
FIG. 3 shows the section carried along the line III--III in FIG. 2.
The suspension which one wishes to filter, or in this case the lime milk, enters the filtering tank 2 by the inlet conduit 1, driven by the feed pump 5. From the roof 3 of the tank 2, cylindrical filtering elements 4 are suspended. These elements may be, for instance, 200 in number, though in the drawing only one such element has been depicted in considerably enlarged size.
The white liquor contained in the lime milk is filtered by effect of the pressure prevailing in the filtering tank 2, through the mantle on the filtering element, and the solid matter of the lime milk, or the lime sludge, is deposited on the surface of the filter mantle. The filtrate, that is the white liquor, is carried into the collecting tank 6 located above, whence it goes, driven by the feed pump 5, to the filtrate draining conduit 7 and further to the digesting plant or into a storage tank. Removal of the lime sludge which has accumulated on the filtering element 4, or upon the mantle, is accomplished as follows. The feed pump 5 is stopped and the valves 8 and 9 are closed. Valves 10 and 11 are opened. The pure liquor in the collecting tank 6 will now flow through the filtering elements 4 into the filtering tank 2 and it will thereby detach the lime milk layer from the surfaces of the mantles. The lime sludge and liquor flow through the draining conduit 13 into the washing tank 12, whence the mixture is pumped either to a suction filter or to a clarifier. During this washing step, the filter draws air through the valve 11.
After the filter has been emptied, the valve 10 is closed and valve 8 is opened, and the feed pump 5 is started. After the filter thus has been refilled, valve 11 is closed and valve 9 opened, whereby another filtering period will commence. All these operations may naturally be automated.
It is thus understood that the filter operates intermittently, its operation being divided into a filtering period and a washing period. The length of the filtering period is determined by the lime sludge content of the lime milk, as follows:
The duration of the washing period is between 1 and 5 min., and thereby the filtering period will be more than 99% of the total time of operation. The purity of the white liquor after filtering is less than 10 mg/l, and the degree of purity of the input liquor has no substantial effect on the end result. The pressurized filter depicted in FIGS. 2 and 3 differs from that just presented in that the collecting tank 6 has been subdivided by means of vertical partitions 14 into sections 15. From each section departs a specific branch conduit 16, which has been provided with a shut-off valve 17. After the valves 17, the branch conduits have been combined to form a common draining conduit 7. In this embodiment one is enabled to shut out of operation any one section in case impure filtrate should flow into this section, which on the other hand indicates that one of the mantles is faulty.
It is obvious to a person skilled in the art that different embodiments of the invention may vary within the scope of the claims presented hereinbelow. For instance, the pressurized filter of the invention may be used to other purposes as well, not only for filtering lime sludge out of lime milk.