DEVICE AND METHOD FOR DILUTION OF CELLULOSE PULP
A device and a method for dilution of cellulose pulp of a consistency of between 20% and 45%. The cellulose pulp is arranged to fall down in a pulp chute during an addition of dilution liquid. The dilution is performed to a consistency in the range of 6-18%, above a level of established diluted pulp in a bottom of a pulp chute. A central distribution device with nozzles for addition of dilution liquid to the falling pulp above the level of established diluted pulp in the bottom of the pulp chute is arranged in the center of the pulp chute. The nozzles of the distribution device are fed with dilution liquid via a pipe that is arranged at least partly through the pulp chute.
The present invention relates to an improved device for dilution of cellulose pulp in the form of flocs and to a related method. The dilution is intended to be performed in order to dilute HC-cellulose pulp of an original consistency of about 20 to 45% (HC=High Consistency), the dilution being withheld until the formation of a MC-pulp, i.e. until the pulp reaches a consistency in the range of 6-18% (MC=Medium consistency).
BACKGROUNDIn connection to the dilution of decomposed cellulose pulp of a high dryness, typically a consistency of above 20%, it is normal procedure to add dilution liquid whilst agitating by means of a dilution screw. This has also been the starting point in the Swedish patent SE 526292, which represents the prior art. Within this prior art dilution to the desired consistency is achieved by the addition of dilution liquid via a ring shaped supply chamber around a pulp chute.
A ring shaped supply chamber for the addition of dilution liquid has been used in the business for a long time and has for instance been utilized for the dilution of cellulose pulp after HC-Ozon reactors, i.e. bleaching reactors in which cellulose pulp of high consistency, i.e. above approximately 20%, is bleached with Ozon. A HC-Ozon reactor is conventionally a horizontal reactor with an interior transport and mixing screw, which normally is arranged directly after a shredding screw from a wash press, and in which the pulp falls down into a pulp chute after having been treated in the HC-Ozon reactor. In e.g. U.S. Pat. No. 5,174,861, the fundamentals of a horizontal. Ozon reactor is disclosed, in which the HC-pulp falls freely down into a dilution tank after the reactor.
It has been noticed that the use of a ring shaped supply chamber around a pulp chute that periferally injects dilution liquid towards the falling floes of pulp, only achieves a certain degree of penetration into the flow and that the maximum quantity of dilution liquid that may be added is limited.
In a plant with a capacity of 3000 ADT (Absolutely Dry Tons) of pulp a day, a pulp chute of a diameter in the range of 1.5 metre is utilized and conventionally no pulp chute for MC-pulp (Medium Consistency) with a diameter of less than 0.80 metres has been utilized. This means that a very good agitation of the pulp is required in order to achieve a satisfactory dilution by means of a ring shaped supply chamber.
SHORT DESCRIPTION OF THE INVENTIONThe present invention relates to an improvement of the dilution with respect to a ring shaped supply chamber. An object of the invention is to overcome the problems of the prior art and to evenly distribute the dilution such that substantially the whole pulp volume will have the same consistency. This is achieved by means of a device according to claim 1.
According to a first aspect, the invention relates to a device for dilution of cellulose pulp of a consistency of between 20 and 45%, which device comprises a pulp chute through which cellulose pulp is arranged to fall down under the addition of dilution liquid, wherein the dilution is performed to a consistency in the range of 6-18%, and wherein the addition of dilution liquid is performed on the falling pulp above a level of established diluted pulp in the bottom of the pulp chute. Further, a central distribution device with a nozzle arranged in the centre of the pulp chute for the addition of dilution liquid to the falling pulp in the centre of the pulp chute and above the level of established diluted pulp in the bottom of the pulp chute, wherein the nozzle is fed with dilution liquid via a pipe that is arranged at least partly through the pulp chute.
According to a second aspect, the invention relates to a method of dilution of cellulose pulp with a consistency of between 20 and 45%, where dilution liquid is added to the cellulose pulp in a pulp chute, which dilution is performed to a consistency in the range of 6-18% as the cellulose pulp is in free fall above an established level of diluted cellulose pulp at the bottom of the pulp chute. The dilution liquid is added in the centre of the pulp chute.
In the device and the method according to the invention flocs of pulp are wetted throughout essentially the whole cross section of the pulp chute before the flocs hit the established pulp level in the chute. Thus, not only the flocs of pulp falling along the walls of the pulp chute will be wet, in which case the degree of wetting decreases with increasing distance from the walls of the pulp chute and is close to zero in the centre of the pulp chute. Instead, an even dilution, which is especially important with increasing capacity of the plants, and with the invention it is possible to reach a capacity of 4-5000 ADT pulp per day and plant.
With the invention it is possible to obtain a higher degree of homogen dilution of cellulose pulp in free fall, since more dilution liquid may be added, which furthermore may be more evenly distributed in the pulp. Also, it is possible to obtain a high degree of homogenously diluted cellulose pulp already in the free fall, i.e. without agitating the liquid. Another advantage is that it is possible to divide the dilution liquids such that a less aggressive dilution liquid may be added in the periphery as a complement to treat the walls of the pulp chute leniently, wherein a less costly material may be used for these, while more aggressive pH adjusting chemicals, such as acids or bleaching chemicals, are added in the centre of the chute and surrounded by a protecting curtain of less aggressive cellulose pulp, closer to the inner walls of the chute.
Below, an embodiment of the invention will be described in detail with reference to the accompanying figures, of which:
In the upper part of the pulp chute 3 a dilution device 10 is arranged, which adds dilution liquid to the flow of flocs that falls freely down towards an established level of pulp 6 in the pulp chute 3. The dilution device 10 comprises a line 15 that is drawn to a central distribution device with nozzles 11 arranged in the centre of the pulp chute 3 in order to distribute dilution liquid to the cellulose pulp, as it falls freely in the centre of the pulp chute. Additionally, in the shown embodiment there is also a supply chamber 16, which is arranged for adding dilution liquid concentrically around the pulp chute, and which is provided with a plurality of nozzles 14 on the inner wall 3A of the chute 3 (see
The diluted pulp, which by the addition of dilution liquid has obtained a relatively homogenous concentration, forms an established level 6 of diluted pulp in the bottom of the chute 3. In connection to the bottom of the chute a MC-pump 4 is arranged, which in a conventional manner is provided with a fluidizer 5 in front of the pump wheel of the pump. The fluidizer 5 is at least partly arranged inside the chute 3 and provides a hefty agitation of the cellulose pulp in the bottom of the pulp chute, which is indicated with rotational arrows, and accomplishes the homogenisation of the concentration of the cellulose pulp. Normally, the fluidizer is integrated with the pump wheel of the pump, but it may also be separated from the pump wheel and be provided with an own driving means, and placed in immediate connection of the inlet to the pump wheel.
In
As is apparent from the figures, the central distribution device comprises at least one pipe 15 extending from the wall 3A of the pulp chute 3 inwards, towards the centre of the pulp chute. At the end of this pipe 15, at least one nozzle 11 is arranged, for the addition of at least a part of the dilution liquid. The nozzles 11 may have several outlets and may distribute the dilution liquid in form of a downwardly directed shower stream 11A with a substantially conical jet (see
An alternative or complement to such a distribution of the nozzles 11 in the centre of the pulp chute 3 is to, as in the shown embodiment, also arrange peripheral outlets 14. In
In one embodiment of the invention the feeding pipe 15 is provided with a separate feeding, wherein the outlets or nozzles 11 of the central distribution devices may be fed with a different dilution liquid from another source than the one that is being fed to the peripheral nozzles 14. Thus, it is possible to add a pH-regulating agent, bleaching chemicals or other additives centrally in the pulp chute, whereby the falling flocs of pulp that has been totally or partly diluted with a less aggressive dilution liquid shields off the centrally added dilution liquid such that it does not reach the inner wall 3A of the pulp chute. The design of the supply chamber 16 and the upper parts of the pulp chute 3 may hence be designed in a simpler and cheaper material, where only the pipe 15 and nozzle 11 of the central distribution device requires materials that are resistant to a concentrated dilution liquid.
Large quantities of dilution liquid are added to the flow of freely falling pulp flocs and may be followed by air or gas in the flow, wherein an active deaeration may be needed in order to vent redundant volumes accompanying the flow. The pulp chute may therefore be designed with a deaeration canal 13 that is connected to the pulp chute above the supply chamber 10. The deaerated gases may either be released to the surrounding atmosphere or to a decomposition system depending on whether the gases are environmental harmful or not.
Claims
1. A device for dilution of cellulose pulp of a consistency of between 20% and 45%, comprising:
- a pulp chute through which cellulose pulp is arranged to fall down,
- means for adding the dilution liquid on the falling pulp above a level of established diluted pulp at a bottom of the pulp chute to dilute the consistency to a range of 6-18%,
- a central distribution device with a nozzle arranged in a center of the pulp chute adapted to add dilution liquid to the falling pulp in the center of the pulp chute and above the level of established diluted pulp at the bottom of the pulp chute, and
- means for feeding the nozzle with dilution liquid via a pipe that is arranged at least partly through the pulp chute.
2. The device according to claim 1, wherein the central distribution device has several nozzles that are evenly distributed over a width of the pulp chute.
3. Device The device according to claim 1 wherein a peripheral distribution device with peripheral nozzles is arranged for adding dilution liquid from an inner wall of the pulp chute.
4. The device according to claim 3, wherein the central distribution device is arranged below the peripheral nozzles of the peripheral distribution device.
5. The device according to claim 4 wherein the device further comprises means for separating the feeding to the nozzles of the central distribution device from the feeding to the peripheral nozzles of the peripheral distribution device, and means for feeding dilution liquid from different sources to the peripheral nozzles of the peripheral device and the nozzle of the central distribution device.
6. The device according to claim 5 wherein a deaeration canal is arranged in connection to the pulp chute above the nozzle of the central distribution device and the peripheral nozzles of the peripheral device.
7. A method for dilution of cellulose pulp having a consistency of between 20% and 45%, comprising:
- adding a dilution liquid to the cellulose pulp in a pulp chute, which dilution is performed to a consistency in a range of 6-18% as the cellulose pulp is in free fall above an established level of diluted cellulose pulp at a bottom of the pulp chute, and
- adding dilution liquid in a center of the pulp chute.
8. The method of claim 7 wherein the dilution liquid is added from several nozzles that are substantially evenly distributed over a width of the pulp chute.
9. The method of claim 7 wherein dilution liquid also is added from an inner wall of the pulp chute.
10. The method of claim 9 wherein different dilution liquids are added in the center and a periphery of the pulp chute, wherein the dilution liquid added in the center of the pulp chute is more concentrated than the dilution liquid added in the periphery of the pulp chute.
11. The method of claim 7 wherein at least 25% of the dilution liquid is added in the center of the pulp chute.
Type: Application
Filed: Mar 20, 2009
Publication Date: Jan 13, 2011
Inventors: Magnus Danielsson (Matfors), Johan Bylander (Sundsvall), Marten Dahl (Ankarsvik)
Application Number: 12/920,112
International Classification: D21C 3/00 (20060101); D21F 1/00 (20060101);