DEVICE FOR REMOVING GASEOUS COMPONENTS AND/OR SOLID IMPURITIES PRESENT IN A GASEOUS FLUID FLOW

Abstract: The invention concerns a means for removing gas­ eous components and/or solid impurities present in a gaseous fluid flow. The means (10) comprises a frame structure (11, 12), a fluid flow inlet connector (13), dis­ posed within the frame structure (11, 12) a scrubber means (15), an exit connector (14) for carrying off the purified fluid flow, and a connector (20) for introducing scrubbing liquid into the means (10) and contacting it with the fluid flow. The scrubbing liquid exit flow has been disposed to pass through the fluid flow inlet con­ nector (13) in opposite direction with reference to the fluid flow. The end region (21) adjacent to the scrubber means (15) of the fluid flow inlet connector (13) has a diminishing cross sectional diameter to the purpose of accelerating the flowing fluid flow before the fluid flow enters the scrubber means (15). The inlet connector (13) has been provided with holes (22) which have been adap­ ted to receive into the inlet connector (13) the return flow of the scrubbing liquid. The holes (22) have been disposed in that region of the inlet connector (13) where the flow of the fluid flow is not accelerated, whereby the scrubbing liquid return flow within the inlet con­ nector (13) is prevented from being entrained with the fluid flow and produces pre-purification of the fluid flow.

Description: Means for removing gaseous components and/or solid impurities present in a gaseous fluid flow The present invention concerns a means serving the removal of gaseous components and/or solid impurities present in a gaseous fluid flow, said means comprising a frame structure, an inlet connector for the fluid flow, accommodatd within the frame structure a scrubber means, an exit connector for carrying off the purified fluid flow, and a connector for conducting a scrubbing liquid into the means and for contacting this liquid with the fluid flow, and in said means the exit flow of the scrubbing liquid having been disposed to pass through the fluid flow inlet connector in a direction opposite to the fluid flow. Gaseous fluid flows frequently contain impurities both in the form of gaseous components and of solid particles, which have to be removed prior to blowing out or reusing the fluid flow. In practice that situation is also frequently encountered in which the gas flow contains solid components in such abundance that their separation is indicated before the flow enters the scrubber. It is common in usual circumstances to use towards purification of the gaseous fluid flow a wet scrubber, in which the gaseous fluid flow is conducted into the frame portion of a separator, in other words, into a fluid tank or reaction portion, where it is tried to bring the scrubbing liquid and the gaseous fluid flow into the most complete contact possible with each other. At this scrubbing phase at least part of the coarser fraction of the solid matter separates and remains in the separating tank. However, endeavours are mostly to achieve that the greater part of the solid matter is separated in dry state already, before the scrubber, either in a settling chamber or in a cyclone separator. By this design the advantage is gained that the quantity of impurities carried into the scrubbing liquid is minimized, whence the amount of sludge that has to be carried off will also remain minimal. After the scrubber part usually a blower is provided because then the wear suffered by the blower will be less. After the blower follows furthermore a droplet separator; depending on the application this may consist of a grille, a set of gratings, droplet separators resembling a cyclone separator, various rotating and round towers, etc. In scrubber designs of prior art, the blower is usually similar to a conventional centrifugal blower. A blower design of the so-called disintegrator type is also known in the art, in which the fluid flow is directed with its impurities, as is also the scrubbing liquid. A design of this kind requires high power input from the drive, and the wear of the blower is also high. In scrubbers of the venturi type, the gaseous fluid flow is accelerated with its impurities in the venturi section to gain a high velocity, and at the same time the scrubbing liquid is inducted into the accelerated fluid flow. After the venturi section, whereat the velocity of the gaseous fluid flow is reduced, there is a droplet separator, where in the first place the impurities serve as crystallisation nuclei for the drops. One has also towards purification of a gaseous fluid flow employed the so-called S-wave scrubber, where the gaseous fluid flow, after flowing together with the scrubbing liquid through an S-wave shaped slit ends up in free space and thence further in a blower. There is no actual separate droplet separator: separation of droplets takes place in the free space after the S wave before the blower. In this design, too, the risk is present that supercondensing moisture may be entrained with the gaseous fluid flow and therefore droplets are flung out and into the surroundings. The object of the invention is to accomplsih an improvement of scrubber designs known in the art. It is a detailed object of the invention: to provide a scrubber design by which a high scrubbing efficiency is attained without scrubbers requiring a high energy input. The other objects of the invention, and the advantages gainable with its aid, will become apparent from the disclosure of the invention. The object of the invention is accomplished with a means mainly characterized in that the end region adjacent to the scrubber means of the fluid flow inlet connector has a diminishing cross sectional diameter to the purpose of accelerating the fluid flow passing through said inlet connector before it enters said scrubber means, and that said inlet connector has been provided with holes adapted to receive the return flow of the scrubbing liquid into said inlet connector, said holes having been disposed in that region of said inlet connector where the fluid flow is not being accelerated, whereby the return flow of the scrubbing liquid within the inlet connector is prevented from being entrained with the fluid flow and effects pre-purification of the fluid flow. The rest of the characteristic features of the means of the invention are stated in claims 2-4. By the means of the invention numerous significant advantages are gained. By the means of the invention a problem solution is achieved wherein only the gas which has already been nearly purified is carried to the final scrubbing together with a minimal scrubbing liquid quantity, with the consequence that the solid matter loading of the gas is minimal. It is then possible to manage in the driving of the blower means employed as scrubber means with low motor outputs, without any major amounts of energy, and at the same time the most efficent venturi action possible is still attained; in other words, one achieves high scrubbing efficiency and high velocities of the gaseous fluid flow, up to 60-100 m/s for instance. I. the subsequent droplet separation the velocity of the gaseous fluid flow is reduced enough to make the liquid droplets separate and to enable them to run along the walls of the frame structure and down to the bottom, and further through apertures in the inlet connector into the inlet connector for pre-purification of the gaseous fluid flow. In the design of the invention in fact 3 an energy consumption figure as low as 1 HP per 1000 m /hr of gaseous fluid flow to be washed is achieved. The external disposable subatmospheric pressure will be about 2000 Pa, that is, the efficiency of the blower means is about 74%. The invention is now described in detail with reference being made to a preferred embodiment of the invention, depicted in the figure of the attached drawing, but to whichtbe invention is not meant to be exclusively confined. The figure of the drawing presents, in schematical elevational view, an advantageous embodiment of the means of the invention. In the figure of the drawing, the means of the invention in general is indicated by the reference numeral 10. The means 10 comprises a frame structure 11,12, a fluid flow inlet connector 13, a scrubber means 15 disposed within the frame structure 11,12, an exit connector 14 for carrying off the purified fluid flow, and a connector 20 for introducing scrubbing liquid into the means 10 and for contacting it with the fluid flow. In this embodiment, the gaseous fluid flow has been disposed to flow through a pretreatment section 19 into the inlet connector 13, whereby when flowing into the means 10 the gaseous fluid flow is already pre-purified. The pretreatment section 19 may consist e.g. of a cyclone separator or a scrubbing tube or another equivalent construction known in itself in the art, from which the gaseous fluid flow together with its non-abrasive impurities is conducted in a rotary motion about a vertical axis into the inlet connector 13. In this embodiment a blower means is used as scrubber means 15, this blower means having been arranged to be driven by a motor 16. The impeller of the blower means 15 may be closed or open. In the present emb-iiment, the impeller has been provided with baffles 17 for directing the gaseous fluid flow along the vane of the blower means 15. The motor 16 rotating the impeller has in this embodiment been carried on the wall 11 of the frame structure by mediation of rods 18. Between the rods 18 and the wall 11 ample free space is left, so that the gaseous fluid flow can pass upwardly towards the exit connector 14. In accordance with the fundamental idea of the invention, the end region 21 adjacent to the scrubber means 15 of the fluid flow inlet connector 13 has a diminishing cross sectional diameter to the put pose of accelerating the incoming fluid flow before the fluid flow enters the scrubber means 15. According to another important char acteristic feature, the inlet connector 13 has been provided with holes 22 adapted to receive the return flow of the scrubbing liquid and to admit it into the inlet connector 13. It should be particularly noted that the holes 22 have been disposed to lie in that area of the inlet connector 13 where no acceleration is applied to the fluid flow. In this embodiment, the scrubbing liquid inlet connector 20 has been disposed to pass through the wall of the fluid flow inlet connector 13 and to be directed within the inlet connector 13 towards its flow orifice pointing to the scrubber means 15. The mode of operation of the means 10 of the invention is as follows. The gaseous fluid flow pre-purified in the pretreatment section 19 passes through the inlet connector 13 in a flow motion rotating about a vertical axis and it is accelerated in the conical section 21 from an initial velocity at point A about 7-12 m/s to 20-25 m/s at the point B. At this point, the scrubbing liquid is introduced through the connector 20 into the gaseous fluid flow, whereafter the blower means 15 accelerates the gaseous fluid flow and the scrubbing liquid from velocity 20-25 m/s at B to 60-100 m/s at C. By this design an extremely high scrubbing efficiency is achieved without need to employ a blower means 15 that would require high motor power. In the droplet separation following after the acceleration, the velocity of the gaseous fluid flow drops so much in the owl section 11 that the droplets will separate and are enabled to run down along the wall 11 to the bottom 12 and further through the apertures 22 into the inlet connector 13. The holes 22 in the inlet connector 13 have been shaped so that they are adapted to direct the scrubbing fluid return flow to rotate within the inlet connector 13 in a rotary motion with the same sense of rotation as the gaseous fluid flow progressing in opposite direction, whereby the scrubbing fluid return flow as it flows downward in the inlet connector 13 passes perpendicularly to the upwardly flowing gaseous fluid flow and thus effects the most efficient possible prescrubbing of the gaseous fluid flow within the inlet connector 13. The downwardly flowing scrubbing liquid flows in this embodiment into a preseparatror, which possibly also incorporates a liquid collection tank. In the design according to the invention, the blower means 15 has been advantageously carried out so that the blower means 15 as it accelerates the fluid flow directs part of the purified fluid flow as a recycling flow back through the holes 22 in the inlet connector 13 into the inlet connector 13,whereby such a rotating fluid flow drives the liquid droplets flung out by the blower means 15 ahead of itself towards the holes 22 and causes the scrubbing liquid to be put in a rotary motion within the inlet connector 13. In the embodiment depcited in the figure of the drawing, the end portion 21 adjacent to the scrubber means 15 of the inlet connector 13 is conically tapering. The means of the invention is not critical as regards the design selected for the scrubber means 15. Rotary power to the impeller may naturally be provided with an externally placed motor or by belt transmission, or using a hydraulic motor. The motor 16 may also be completely isolated from the gaseous fluid flow by covering it with appropriate protective shields. It is then for instance possible to cool the motor by an external air current. The exit connector 14 may equally be of another kind, and it may if required be provided e.g. with an additional droplet separator in order to ensure the best possible droplet separation. Moreover, the conical portion 21 If the inlet connector 13 may be replaced merely with a constricted aperture, through which the gaseous fluid flow is admitted to flow to the impeller of the blower means 15.

Claims: Claims 1. Means for removing gaseous components and/or solid impurities present in a gaseous fluid flow, said means (10) comprising a frame structure (11,12), a fluid flow inlet connector (13), a scrubber means (15) disposed within the frame structure (11,12), an exit connector for carrying off the purified fluid flow, and a connector (20) for conducting scrubbing liquid into the means (10) and contacting it with the fluid flow, and in said means (10) the scrubbing fluid exit flow having been disposed to pass through the fluid flow inlet connector (13) in opposite direction with reference to the fluid flow, characterized in that the end region (21) adjacent to the scrubber means (15) of the fluid flow inlet connector (13) has a cross sectional diameter diminishing to the purpose of accelerating the fluid flow passing through said inlet connector (13) before the entrance of the fluid flow into said scrubber means (15), and that said inlet connector (13) has been provided with holes (22) which have been adapted to receive and admit into said inlet connector (13) the return flow of the scrubbing liquid, said holes being disposed in that region of said inlet connector (13) where the flow of the fluid flow is not being accelerated, whereby the scrubbing liquid return flow within the inlet connector (13) is prevented from being entrained with the fluid flow and effects pre-purification of the fluid flow. 2. Means according to claim 1, characterized in that the scrubbing liquid inlet connector (20) has been disposed to pass through the wall of the fluid flow inlet connector (13) and to be directed within the fluid flow inlet connector (13) towards the latter s flow orifice pointing to the scrubber means (15). 3. Means according to claim 1 or 2, characterized in that the scrubbing means is a blower means disposed to accelerate the fluid flow already accelerated in the fluid flow inlet connector (13) to even higher velocity and to operate as droplet separator in that said blower means directs part of the purified fluid flow as a recirculating flow back through holes (22) in said inlet connector (13) into said inlet connector (13), whereby the circulating fluid flow drives before itself droplets flung out by the blower means towards said holes and effects better setting into rotation in said inlet connector (13) of the scrubbing liquid, the scrubbing liquid in rotary motion within said inlet connector (13) having been disposed to produce in the fluid flow progressing in the opposite direction the most efficient possible pre-purifying effect. 4. Means according to any one of claims 1-3, characterized in that the fluid flow inlet connector (13) is conically tapering at its end (21) adjacent to the scrubber means (15).

Inventors: JARVENPAA, VILJO JUHANA, Järvenpää, Viljo Juhana
Applicants: JARVENPAA, VILJO JUHANA
Application year: 1982
Main classification: B01D47
IPC codes: B01D50, B01D47, B01D53