The invention relates to a method for removing gas from wood chips according to the preamble of the appended claim 1. The invention also relates to a device for implementing the aforementioned method in accordance with the preamble of the appended claim 12.
When manufacturing cellulose and paper pulp, the ligno-cellulose-containing wood chips used as raw material are cooked in an alkaline solution in order to separate the fibres and lignin contained in them from each other. The manufacture comprises several stages, both before and after the cooking. Before cooking, the wood chips are directed to the gas removal phase, where gases, primarily air, are removed from both inside the wood chips and the spaces between them by directing hot steam to the wood chips. Removing gas from the spaces between the wood chips decreases the amount of gases disturbing the operation of the digester. In addition, when the gases are removed from inside the wood chips, the chips absorb cooking chemicals better, which improves the yield of the cooking and the quality of the pulp it provides.
Vertical bins or vessels or horizontal screws are generally used for removing gas from wood chips. The screws being used are generally wood chip conveyor screws, which convey wood chips, for example, from chipping to the digester. Generally, this type of screws are installed horizontally or only in a small angle with the horizontal level. The steam needed for removing gas is generally fed from nozzles installed on the lower surface of the shell forming the bottom of the screw. However, the loading of the screws varies in relation to time, i.e. in relation to the length of the screw, the amount of wood chips moving inside varies, resulting in slow warming of individual wood chips to the maximum temperature and varying their delay in the screw. Consequently, the processing of the wood chips is not uniform. In addition, the delay of the wood chips in the screw is not long enough in order for the gas removal to be complete.
When using vertical bins or vessels in removing gas, the wood chips are generally fed to the bin from its upper end and the steamed wood chips are removed from the lower end of the bin. The steam is generally fed to the lower part of the bin and it flows upwards against the direction of motion of the wood chip material. This kind of a solution for steaming wood chips is disclosed, for example, in the U.S. Pat. No. 4,867,845, where wood chips are fed to a bin with an downward-increasing diameter from the upper end of the bin and the steamed wood chips are removed from the lower end of the bin, by means of a rotating discharger installed at the bottom of the bin. Steam is fed vertically to the centre of the bin, via a steam pipe installed parallel to the vertical central axis of the bin. The end of the steam pipe extending close to the bottom of the bin, from where the steam is discharged to the bin, is formed as an expanding taper. Steam flows upwards from the steam pipe, through the wood chip column packed in the bin.
The publication U.S. Pat. No. 6,199,299 also discloses a chip bin, where steam is fed to wood chips flowing downwards in the bin from the middle of the height of the bin, via steam nozzles installed in the shell of the bin.
US-publication 5,628,873 discloses a downwards-tapered steam bin, where steam is fed to the wood chip flow flowing downward in the chip bin from above the conical narrowing part. Steam feeding takes place both via the shell of the bin and the steam feeding pipes installed within the bin.
The problem with the above-mentioned bins is that the gas removal in them is not even throughout the entire wood chip flow. The steam fed via the bin shell cannot penetrate to the middle of the wood chip flow in such a manner that all the wood chips would receive an identical steam processing. The steam fed to the middle of the bin, to its lower part, does not penetrate into the wood chips next to the walls of the bin or into the chips on the wood chip surface of the bin efficiently enough to attain an even gas removal result. In addition, in the solutions presented above, the warming of the wood chips is slow in the bin, in which case a part of the wood chips do not receive a proper gas removal processing.
The purpose of the present invention is therefore to provide a method for removing gas from wood chips, which avoids the above-mentioned problems and in which the gas removal from wood chips takes place in such a manner that all the wood chips receive an identical steam processing. Thus, the pulp resulting from the cooking following the gas removal is homogenous.
To attain this purpose, the method according to the invention is primarily characterized in what will be presented in the characterizing part of the independent claim 1.
The device according to the invention, in turn, is primarily characterized in what will be presented in the characterizing part of the independent claim 12.
The other, dependent claims present some preferred embodiments of the invention.
The invention is based on the idea that gas removal from wood chips is preformed in a vertical, elongated gas removal vessel, to which the wood chips are fed from the upper part of the vessel and the wood chips are removed from its lower part. Steam is fed to the wood chips to the wood chip flow travelling downwards in the vessel from the middle and edges of the flow, in cross-direction in relation to the wood chip flow. The feed rate of wood chips to the vessel and the discharge rate from it are maintained on a level that the wood chip flow is moving as a so-called plug flow, in which case the wood chips move evenly in relation to the entire cross-section area of the vessel. Therefore, steam is fed into these wood chips in the plug flow. The level of the surface of wood chips in the vessel is controlled by means of the feed rate and discharge rate of the wood chips. The surface of the wood chips is maintained on such a level that the steam fed to the wood chips does not escape directly to the steam space in the upper part of the vessel. The steam feeding means are thus arranged to feed steam to a distance from the surface of the wood chips, inside the wood chip flow. The height of the gas removal vessel and the placement of the steam feeding means in relation to the height of the vessel is arranged in such a manner that the delay time of wood chips in the vessel is long enough for the gas removal to be as efficient as possible.
The majority of the steam required in the gas removal from wood chips is fed via the steam feeding pipe arranged in the middle of the wood chip flow and the rest of the steam is fed from around the wood chip flow, via steam feeding means arranged in the shell of the vessel. In order for the gas removal to be efficient enough, the temperature of the wood chips in the vessel is raised quickly to approx. 100° C. and maintained there substantially over the entire time the wood chips remain in the vessel. The amount of the steam being fed is controlled by means of the temperature and pressure measurements of the steam gathering in the upper part of the vessel. The steam forming in the gas removal is removed from the upper part of the vessel, from above the surface of the wood chips and the condensate is removed from the lower part of the vessel.
An advantage of the gas removal method according to the invention is that as a result of both the design of the gas removal vessel and the transverse steam flow, which does not prevent the flow of the wood chips, an even, downward plug flow of wood chips is created, resulting in each wood chip receiving an equally long and identical steam processing. Consequently, the gas removal within individual wood chips is efficient and fast. The transverse steam flow does not prevent the downward flow of the wood chips either. Further, the quick raising of the temperature of the wood chips to the processing temperature with a transverse steam flow ensures enough delay time for the wood chips in the processing temperature, which improves gas removal significantly. Also, the dimensions of the gas removal vessel and the placement of the steam feeding means in relation to the height of the vessel improve gas removal. The gas removal device used in implementing the method, i.e. the gas removal vessel is simple to manufacture and easy to install in its place and it takes little room in the cramped device environments of pulp and paper mills.
The invention can also be applied in renewing equipment in factories, which manufacture pulp. Thus, acquiring a completely new gas removal device can be avoided and economical savings can be created.
In the following, the invention will be described in more detail with reference to the appended drawings, in which
In
The wood chips that have gone through the gas removal process are removed from the bin 2 by the discharge means 5 that are connected to the bottom of the bin. The discharge means comprises several pushing means 6, which move the wood chips to a discharge opening 7 that is centralized with the midpoint of the bottom of the bin 2. The pushing means 6 are placed substantially evenly over the periphery of the entire shell of the bin 2 defining the bottom of the bin. The power transmission of the discharge means is implemented, for example, hydraulically. The discharge opening is connected to a discharge means arranged under it, i.e. to a screw 8, by means of which the gas-free wood chips are transferred forward.
The wood chips fed to the bin fill the bin 2 substantially evenly to the level of the surface 9 of the wood chips. The surface of the wood chips settles within a distance from the roof 19 of the bin. A free space, i.e. a gas space 13 remains between the surface 9 of the wood chips and the roof of the bin. The level of the surface 9 of the wood chips in the bin is controlled by controlling the feed rate of the wood chip feeding device 3 and/or the discharge rate of the wood chip discharge means 5 and the screw 8 discharging the wood chips from the bin. The discharge rate is controlled according to the production of the digester. For the purpose of controlling, one or more sensors 10 measuring the level of the surface of the wood chips are arranged in the bin 2. On the basis of the data provided by the surface level sensor 10, the controller 21 controls the rate of the feeding device 3 and/or the discharge means 5 and the screw 8 and at the same time the delay time of the wood chips in the delay zone 25 between the steam feeding means 11 and 12 as well as the discharge means 5. The surface level of the wood chips is to be the wood chips must be controlled onto such level that the wood chip surface extends all the time above the steam feeding openings of the steam feeding means 11 and 12 feeding steam to the bin. Thus, the steam is prevented from directly escaping to the steam space 13 above the surface of the wood chips.
As can be understood from what is described above, the wood chips move downward in the bin 2 by forming a downward moving wood chip flow, which is described with the arrow A in the figure. The downward movement and the effect of the steam fed to the wood chip flow causes the wood chip flow to become dense, thus forming a so-called plug flow. Thus, the downward expanding design of the bin promotes the even movement of the flow in such a manner that no blockages or other obstacles blocking the even flow form in it. The wood chip flow is guided by means of the flow controller 14 arranged in the lower part of the bin, which flow controller evens the chip flow in the bin. In addition, the flow controller 14 prevents the wood chips from directly discharging to the discharge opening 7 and thus the blockage of the discharge opening 7.
Steam is fed to the wood chip flow in cross direction in relation to the wood chip flow with first steam feeding means 11 and second steam feeding means 12. The first steam feeding means 11, i.e. the steam feeding pipe 11 is arranged in the middle of the bin 2. The steam feeding pipe 11 thus directs steam to the middle of the bin 2 in such a manner that at least a part of its length combines with the vertical mid-axis of the bin. The end of the steam feeding pipe 11 that extends inside the bin is closed, preventing the steam from flowing into the chip flow directly, in the same direction with it. In the lower end of the steam feeding pipe 11 there is an around the steam feeding pipe extending steam distribution means 15, which can be a perforation extending around the feeding pipe, or some suitable means attached to the feeding pipe, such as, for example, a screen, which distributes steam from the steam feeding pipe 11 evenly to the wood chips horizontally on every side of the pipe. In the embodiment of
The gases that the steam has displaced from the wood chips and the spaces between them, gathers in the gas space 13 between the surface 9 of the wood chips and the roof 19 of the bin, from where it is advantageously directed out via a unit 16. It is also possible to remove gases from the bin 2 by sucking them via the steam feeding pipe 11 or the distribution chamber 12. Thus, the steam flow can be effectively directed in a cross-direction through the wood chip flow. In addition, this way the channelling of the steam in the wood chip flow can be prevented. The steam gases can be sucked from only one of the steam feeding means at a time, because feeding enough steam to the wood chip flow and maintaining a high enough temperature in it must be guaranteed throughout the entire gas removal process. In other words, if the steam gases are sucked via the distribution chamber 12, enough steam must be fed from the steam feeding pipe 11. Further, if the sucking of steam gases takes place via the steam feeding pipe 11, enough steam must be fed via the distribution chamber 12 and the steam feeding units 17.
By means of the temperature sensor 22 arranged in the gas space 13 above the wood chip surface 9, the temperature of the gas space 13 above the wood chip surface is monitored. If the temperature rises too high, it is a sign of a malfunction of the bin, in which case an alarm is given. The temperature prevailing in the gas space 13 above the wood chip surface is lower than the processing temperature of the wood chips. This is because a part of the steam fed to the wood chips flows upstream in the upper part of the wood chip column towards the surface 9 of the wood chips and displaces the colder gas in the wood chips, which flows upwards to the gas space 13.
The condensate formed in connection with the wood chip gas removal flows to the bottom of the discharge means 5 connected to the lower part of the bin and are removed from there via the condensate removal units 18. The condensate can also be removed from the screw 8 (not shown in the figure).
The flow of the wood chips in the bin 2 can, if desired, be directed by means of the design of the steam feeding means 11.
The invention is not intended to be limited to the embodiments presented as examples above, but the invention is intended to be applied widely within the scope of the inventive idea as defined in the appended claims. The gas removal vessel can thus also be of the same diameter in relation to its entire height, a vessel that is round in its cross section. Further, as the steam used in gas removal can be used either fresh steam or expansion steam received from another process of the pulp or paper mill. Also, the steam gas received from the gas removal device can be compressed and recycled back as heating steam to the device.
Number | Date | Country | Kind |
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20040637 | May 2004 | FI | national |
20055098 | Feb 2005 | FI | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/FI05/50133 | 4/26/2005 | WO | 1/3/2007 |