1. Field of the Invention
The present invention relates to a separation pump as claimed in the preamble of independent claim 1.
The present invention relates also to the use of a separation pump.
Gas removal in various process steps such as in various steps of pulping is often inhibited due to foam, which is created in the various process steps, because gas is trapped in the foam or because the foam is so viscous that it prevents free gas flow.
On the other hand, foam can be used for separating components from a mixture, in other words, for separating the components of the foam from the liquid or (liquid) suspension. In addition, foam is an excellent carrier for gas, in other words, for separation of gas from a mixture containing gas and liquid or liquid suspension, since gas is a component of foam. For example in pulp mill processes, foam is a result of air mixing with the soap/tall oil coming from the raw materials. In pulp mill processes foam is utilized to separate soap/tall oil from a filtrate for example by flotation and skimming. In this way can for example in flotation processes gas and various components be separated from the rest of a mixture in the form of foam containing gas and the component(s) to be separated.
2. Prior Art
Publication WO 94/17242 discloses an apparatus for separating fibers from fibre-containing water. The apparatus comprises means for feeding fibre-containing water into said apparatus, means for feeding gas into said water for forming fibre-enriched foam, and means for discharging fibre-depleted water and fibre-enriched foam from said apparatus. The apparatus comprises a mantle shaped essentially as a body of revolution and means for causing said fibre-containing water to rotate in a vortex on the inner surface on said mantle. The means for feeding gas into said water comprise a gas distribution part of said mantle for feeding finely distributed gas into the vortical water. The means for discharging fibre-enriched foam extend into the area of a foam column generated in the center of said stationary mantle. The discharging means are preferably connected to a foam extinguishing apparatus. This apparatus does not provide for gas separation from the fibre-containing water i.e. the liquid.
Publication WO 95/17235 discloses an apparatus for pumping and separating a mixture of gas and liquid according to the preamble of independent claim 1. In this publication foam is considered as being an obstacle for gas separation and it is in this publication suggested to collapse foam inside the rotatable drum means by spraying the foam. This arrangement does not allow separating the components of the foam from the liquid or liquid suspension in the separation pump, because when the foam collapses, the components of the foam will mix up with the liquid or liquid suspension.
In the past, as for example in a separation pump as disclosed in WO 95/17235, foam was considered as a problem in separation pumps and as a problem for the proper function of separation pumps. On the other hand, because foam is used as a carrier for removing gas and other components from a mixture for example in flotation and skimming, it would be desirable if foam could be removed in the form of foam from the inner space of a rotatable drum means of a separation pump without collapsing the foam inside the inner space of the rotatable drum means. This would allow separating components of the foam from the mixture in a separation pump and/or separation of components capable of foaming from the mixture in a separation pump. This would in addition allow separation of foam in general from the mixture in a separation pump.
The purpose of the invention is to provide a separation pump, which is capable of separating in addition to gas from a mixture of gas and liquid or suspension also such components of the mixture capable of foaming (i.e. such components which may be a part of foam) and/or such components which are components of a foam present in the mixture of gas and liquid or suspension fed into the separation pump.
A separation pump according to the invention is characterized by the features defined in independent claim 1.
Preferred embodiments are presented in the independent claims of the invention.
In a separation pump according to the present invention, the separation pump comprises foam discharging means for discharging foam from the inner space of the rotatable drum of the separation pump. The foam discharging means of a separation pump according to the invention also comprises a second outlet for preferably leading out foam and/or components of the foam from the inner space of the separation pump so that the foam and/or components of the foam does not mix up with the essentially gas-free liquid or the essentially gas-free liquid suspension in the inner space of the separation pump, which essentially gas-free liquid or suspension is lead out from the inner space of the separation pump via a first outlet.
The gas, which is separated from the mixture of gas and liquid or suspension in the separation pump can be completely a part of the foam in other words be completely trapped in the foam. It is also possible that a part of the gas which is separated from the mixture of gas and liquid and suspension in the separation pump is free in other words not a part of the foam. If the mixture of gas and liquid or suspension fed to the separation pump contains no such components, which can produce foam with gas and/or no foam, all of the gas which is separated from the mixture of gas and liquid and suspension in the separation pump is free i.e. not a part of any foam.
The separation pump of the invention can for example be used in pulp mill processes. Also other uses are possible, where gas and a component capable of foaming are to be removed from liquid or suspension. The separation pump according to the invention can also be used for removing foam from a mixture of gas and liquid or suspension in a process.
The foam discharging means are preferably, but not necessarily, provided at the axis of rotation of the rotatable drum means, because foam tends to migrate towards the axis of rotation of the rotatable drum means rotates, because foam is less dense than liquid or suspension.
In a preferred embodiment of the invention, the foam discharging means are provided at the axis of rotation of the rotatable drum means, at the outlet end of the separation pump. In such embodiment the foam is discharged from the same end of the inner space of the rotatable drum means as the essentially gas-free liquid or essentially gas-free suspension. This means that the foam to be discharged from the inner space of the rotatable drum means does not have to be moved or to flow in a direction against the flow of the mixture of gas and liquid or suspension or against the flow of gas-free liquid or gas-free suspension in the inner space of the rotatable drum means.
In a preferred embodiment of the invention, the separation pump comprises foam breaking means for at least partly breaking down the foam. These may be mechanical means for breaking down the foam and/or may use some additive for example a chemical for breaking down the foam. Alternative or in addition, the foam may for example be sprayed with a fluid in order to break down the form. Alternatively, the foam may be discharged from the separation pump in the form of foam and broken down later, outside the separation pump.
In a preferred embodiment of the invention, the foam discharging means of the separation pump comprises a foam extraction chamber for receiving foam from the inner space of the rotatable drum means. The foam extraction chamber may form an extension of the inner space of the rotatable drum means at the outlet end of the separation pump. An advantage of such a foam extraction chamber is that it forms a space for the foam, which prevents foam and/or components of the foam inside the separation pump from mixing up with the essentially gas-free liquid or essentially gas-free suspension leaving the separation pump at the first outlet.
In a preferred embodiment of the invention, the separation pump comprises foam moving means for causing a flow of foam from the inner space of the rotatable drum means towards the foam discharging means, preferably into a foam extraction chamber if the separation pump is provided with such a foam extraction chamber.
In a preferred embodiment of the invention, the separation pump is provided with a pressure increasing means for creating a pressure inside the inner space of the rotatable drum means for pressing foam towards the foam discharging means.
In a preferred embodiment of the invention, the separation pump is provided with a pressure decreasing means for creating a pressure inside the inner space of the rotatable drum means for sucking foam towards the foam discharging means.
In a preferred embodiment of the invention, the separation pump comprises a set of blades for rotating the fluid mixture at the inlet end of the rotatable drum means. Additional rotating (mixing) of the fluid mixture in addition to rotating the fluid mixture with the rotating drum means promotes the formation of foam and therefore promotes separation of foaming components from the fluid mixture.
In a preferred embodiment of the invention, the separation pump is provided with a third inlet for feeding an additive i.e. foaming agent into the mixture of gas and suspension or liquid to enhance foaming (forming of foam).
The separation pump of the invention is particularly suitable for removing soap from a mixture in a pulp mill process. The invention relates also to the use of a separation pump according to the invention for removing soap from a mixture in a pulp mill process. All wood species contain extractive substances. Some of these substances are dissolved into liquor in the pulping process. For example resin and fatty acids are dissolved into pulping liquor and form sodium salts, which are surface active compounds (less dense than surrounding liquor) and have a potential for “washing” other components out of wood by micelle formation. These Na-salts are typically called soap in the pulp and paper industry. Soap is primarily related to softwoods although there are also some soap in hardwoods also, but not in the same extent as with softwoods.
The present invention, together with additional objects and advantages of preferred embodiments of the invention will best be understood from the following description, when read in connection with the accompanying drawings, of which:
It is to be noted that the present separation pump operates largely in the same manner as the apparatus described in WO 95/17235 except for the features relating to handling foam. Reference is made to the detailed description in said publication, it being clear to those skilled in the art that the many variations in the general construction and operation of the prior art pump are applicable to large extent also to the separation pump according to the present invention.
An example of a suspension is filtrate or filtration water.
The separation pump 1 shown in
The separation pump 1 shown in
The rotatable drum means 10 shown in the figures has an essentially circular cross-section. The rotatable drum means 10 has an inner wall 11. Because the rotatable drum means 10 is hollow, the inner walls 11 of the rotatable drum means 10 forms an inner space 12.
The rotatable drum means 10 are rotatable around an axis of rotation 13 for causing liquid or suspension 4 of fluid mixture 2 fed into the rotatable drum means 10 via the fluid mixture inlet 6 to form a layer of liquid or suspension 14 on the inner wall 11 and for causing gas 3 of fluid mixture 2 fed into the rotatable drum means 10 via the fluid mixture inlet 6 to migrate towards the axis of rotation 13 of the rotatable drum means 10.
The separation pump 1 comprises in addition a foam discharging means 15 for removing foam 16 from the inner space 12 of the rotatable drum means 10. The foam discharging means 15 comprises a second outlet 17 for discharging foam 16 or at least partly broken down foam 16 and gas 3 from the foam discharging means 15.
The foam discharging means 15 are preferably, but not necessarily, provided at the outlet end 7 of the separation pump 1.
The foam discharging means 15 are preferably, but not necessarily, provided at the axis of rotation 13 of the rotatable drum means 10, and in addition preferable at the outlet end 7 of the separation pump 1.
The foam discharging means 15 are in
Alternatively, or in addition to the mechanical foam breaking means, the second pump means may be provided with chemical foam breaking means (not shown in the figures) for breaking down the foam using chemicals (not shown in the figures).
In
In
In
In the fifth embodiment shown in
In
In
If the foam extraction chamber 21 rotates, the foam extraction chamber 21 is preferably, but not necessarily, adapted to rotate together with the rotatable drum means 10. Alternatively, the foam extraction chamber 21 may be provided with rotating means for rotating the foam extraction chamber 21.
The separation pump 1 shown in
The foam moving means 23 are preferably, but not necessarily, arranged at the outlet end 7 of the separation pump 1. In the separation pump shown in
The separation pump 1 can preferably, but not necessarily, comprise pressure increasing means (not shown in the figures) for increasing the pressure in the inner space 12 of the rotatable drum means 10 for pressing foam to the foam discharging means 15, in
The separation pump 1 can preferably, but not necessarily, comprise pressure decreasing means (not shown in the figures) for decreasing pressure in the inner space 12 of the rotatable drum means 10 for sucking foam to the foam discharging means 15, in
The rotatable drum means 10 has preferably, but not necessarily, a generally cylindrical configuration or at least a part of the rotatable drum means 10 has preferably, but not necessarily, a generally cylindrical configuration. The generally cylindrical configuration of the rotatable drum means 10 has preferably, but not necessarily a diameter to length ratio of 1:1 to 1:20.
The rotatable drum means 10 extends preferably, but not necessarily, into the pump housing 8 at the outlet end 7. If the rotatable drum means 10 extends into the pump housing 8 at the outlet end 7, the diameter of the portion of the rotatable drum means 10 located in the pump housing 8 is preferably, but not necessarily, larger than the diameter of the rest of the rotatable drum means 10.
The rotatable drum means 10 may alternatively end at the pump housing 8 at the outlet end 7.
The rotatable drum means 10 comprises preferably, but not necessarily, a blade wheel 26 extending into the stationary pump housing 8.
In
The foam discharging means 15 are preferably, but not necessarily, located in the direction of the axis of rotation 13 of the rotatable drum means 10 after the outlet end 7 of the rotatable drum means 10. In
The separation pump 1 shown in
The inlet end 5 of the separation pump is preferably, but not necessarily, provided with a third inlet 30 for feeding air/gas or chemical(s) or foaming agents for forming foam into the fluid mixture 2. It is also possible to feed air/gas or chemical(s) or foaming agents into the separation pump via the second inlet 25.
The invention also relates to the use of a separation pump in a pulp mill process for separating soap from a mixture.
It is apparent to a person skilled in the art that as technology advanced, the basic idea of the invention can be implemented in various ways. The invention and its embodiments are therefore not restricted to the above examples, but they may vary within the scope of the claims.
Number | Date | Country | Kind |
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20075558 | Jul 2007 | FI | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/FI08/50399 | 7/1/2008 | WO | 00 | 6/28/2010 |