A METHOD FOR CLEANSING GAS AND APPARATUS HEREFOR

Abstract: Method for cleansing gas from solid, liquid and/or gaseous contaminants, by bubbling the gas through a liquid bath (32), and by introducing the incoming gas into a distribution means (14) and causing the gas to pass in part-streams through a multiple of inlet orifices (64) located at progressively increasing depths beneath the surface (34) of the liquid (32). With increasing inlet pressure an increasing number of inlet orifices (64) are utilized for an increasing number of part-streams. The gas flow is passed from respective inlet orifices (64) through connecting means (24, 26, 28) to outlet orifices (31) located at a considerably higher height level (h) than corresponding inlet orifices (64). The gas flow is caused to flow out through venturi nozzles (28) and/or to strike against impinger or striking surfaces (39) with a minimum pressure drop corresponding to said height differential (h). In this way full operational pressure is immediately achieved, as soon as gas is passed out through any of the inlet orifices (64), and an intense mixing of gas and liquid as well as a high cleansing efficiency are guaranteed.

Description: A method for cleansing gas and apparatus herefor The present invention relates to a method for cleansing gases from solid, liquid and/or gaseous impurities of the kind more clearly shown in the preamble of claim 1. The invention also relates to an arrangement of apparatus for carrying out the method, in accordance with the preamble of the main apparatus claim. The invention is particularly intended for use as a passive emergency system capable of being activated in the event of an accident or in the event of interruptions in operations in, for example, nuclear power plants, chemical industries or other industries where such circumstances may result in the release of airborne contaminants dangerous to the health. The invention, however, can also be applied under normal operating conditions, for instance, in a plant or manufactur¬ ing process. The invention, both with regard to function and construction, has been developed in response to the very special require¬ ments placed on an emergency safety system. Such a system shall be capable of standing in permanent readiness for a period of at least ten years, and must be capable of instant activation to full effect in the event of an emergency. It is highly beneficial if the emergency system is able to function automatically and independently, in the absence of operating personnel and power input. Very specific requirements are placed on emergency systems for nuclear power stations and intended for extracting radio¬ active particles and gases from substances that are released as a result of a breakdown in operation. The following condi¬ tions are examples of those conditions which can be required of such an emergency system: - no electric power supply - no active control and monitoring by operating personnel - long endurance in the absence of power input - total endurance for several days - capable of absorbing gas and extracting dust particles - high degree of efficiency within widely varying rates of flow. These requirements are fulfilled with a safety system that comprises a very large stone-bed filter. In this case, dust is extracted through physical phenomenon, sedimentation and diffusion, wherewith particles but have a size in the order of 0.5-10 μm are only slightly affected.. Such a filter is consequently relatively large and considerably expensive. Despite this, such filtershave poor extraction efficiency with regard to the very finest particles, particularly in regard of particles beneath 0.5 micron. The filter also has poor efficiency with regard to gas separation, the gas in this case being adsorbed on the stone material. Distinct from such known filters, the present invention propo¬ ses the use of wet cleansing apparatus, using a liquid into which the contaminated gas is guided to a location beneath the surface of said liquid. The separator or filter will then, function as a water seal which when no overpressure prevails in the space or chamber connected to the gas cleanser, holds said space isolated from the surrounding atmosphere. In order for wet cleansing apparatus to be efficient, it is necessary for the liquid and gas to be thoroughly mixed to¬ gether in the apparatus. Thus, the cleansing liquid must be dispersed throughout the gas in the form of fine liquid drop- lets and/or the gas must be passed through the liquid in the form of small gas bubbles. Furthermore, the cleansing efficien¬ cy of wet cleansing apparatus into which the gas is introduced beneath the surface of the liquid bath is highly dependent on the rate of flow, and a good cleansing effect is only obtained within a relatively narrow flow range. This presents parti¬ cular problems in some cases, since an emergency system must be capable of dealing with flow rates of varying magnitudes, without needing to be monitored or controlled actively. There is proposed in DE-PS- 228 733 a cleansing system in which the incoming gas flow is divided into a plurality of part flows which are directed in fine jets against impinge- ■ ment or striking surfaces. This system, however, has the aforesaid drawback of having low efficiency at small rates of flow, since in this latter case the gas .. bubbles through the liquid in relatively large bubbles and is relatively unaffected. US-A-3 216 181 (c.f.Fig. 4), US-A 3 520 113 (c.f. Fig. 7) and US-A 4 182 617 (c.f. Fig. 2) teach wet cleansing systems in which the gas is introduced beneath the surface of a liquid bath through a plurality of apertures located at progressively deeper depths. In use, the incoming gas forces down the level of liquid in the inlet conduit with increasing gas flow rates and inlet pressures, until the first outlet aperture is exposed and the gas is able to flow up through the liquid. As the gas flow rate and inlet pressure increase, the liquid 'surface is pressed down progressively still further, so as to expose .more and more of the outlet apertures, such that gas is able to flow therefrom in the form of part gas-flows. In this way at least substantially all flow will pass through the outlet apertures utilized, irrespective of the inlet pressure and the total flow through the gas cleansing system. One drawback with such known gas cleansing systems is that when the surface of the liquid in the inlet conduit is pressed down beneath an inlet aperture, the gas will be for¬ ced out into the cleansing bath at a low energy level and in the absence of pressure drop. The gas will therefore stream out and up through the liquid in the form of relatively large bubbles, resulting in relatively poor separation of fine particles and gaseous contaminants. Such known cleansing systems are therefore not totally satisfactory as passive emergency systems intended for separating highly toxic partic¬ les from contaminated gas flows in, e.g., the event of an accident in a nuclear power plant. Consequently an object of the present invention is to alle¬ viate the drawbacks of the prior art techniques and to pro¬ vide a method for cleansinq gases of the aforesaid kind which will enable particulate contaminants, and particularly the finest particles thereof, to be extracted efficiently, which will also enable gaseous contaminants to be extracted, and which can be applied without requiring the supply of power from external power sources. The extent to which contaminant separation is achieved shall be substantially independent of the rate of gas flow. A further object of the invention is to provide for the purpose of carrying out the method appara¬ tus of simple construction, apparatus which can be produced at low manufacturing costs, and apparatus which will operate without requiring the provision of active mechanical compo- nents and without the active assistance of personnel. It shall also be possible to decontaminate the apparatus after use. Accordingly, the method according to the invention is charac- terized primarily by the characterizing features set forth in the preamble of Claim 1 , and the apparatus according to the invention is characterized primarily by the characterizing features set forth in the characterizing clause of the main apparatus claim. When practising the method according to the invention and using the inventive apparatus, high cleansing efficiency is constantly achieved irrespective of the magnitude of the total gas flow. Because the contaminated gas is caused to pass through first inlet orifices located at progressively increas¬ ing depths beneath the surface of the liquid and then through outlet orifices located at considerable heights above corres¬ ponding inlet orifices, it is guaranteed that the contaminated gas will constantly pass through the outlet nozzle at a considerable drop in pressure corresponding to the difference in the height between inlet orifice and outlet orifice. In this way the gas passing through the last of the outlet orifices utilized will also be subjected to a considerable drop in pressure and will therewith be cleansed effectively. Since the distributor means opens freely towards the liquid bath beneath its lowermost inlet orifice, the liquid is able to rise up into the distributor means at decreased inlet pressure (=ceasing emergency conditions), such that the liquid again will rise above some or all of the previously open inlet orir 5 fices and close off these openings. According to one particularly advantageous embodiment of the invention the outlet nozzles are in the form of venturi nozzles having walls which present suction openings to the surrounding liquid bath. This obviates the need of providing separate 0 cleansing liquid inlet pipes and guarantees a constant and positive supply of liquid to the venturi nozzles. By means of the present invention it is possible to separate 5 particles and liquid droplets by absorption with high efficien¬ cy over a wide range of magnitudes . Gaseous contaminants are separated by being dissolved in the washing liquid and/or by reaction with substances incorporated in the liquid. Q In accordance with the invention, the pressure of the gas in * a containment or containing structure subsequent to a break¬ down in operation is utilized effectively to propel the gas through the gas cleansing apparatus. This enables the appara¬ tus to operate fully independently of external power sources. 5 The inventive cleansing apparatus can also be used as a separa¬ tor means in process industry. In this respect the cleansing apparatus may be combined with an upstream fan or correspon¬ ding device when the overpressure of the contaminated gas is 0 excessively low. This combination can also be applied when the cleansing apparatus according to the invention is intended for use in such breakdown situations as those in which no overpressure is found or occurs. In order to enable the outer wall of the gas cleansing appa¬ ratus to withstand the pressures generated, the wall is conveniently constructed as a pressure vessel. Guiding partition walls conveniently ensure that there is formed a reflow channel from the proximity of the surface of the liquid to a location beneath the outlet orifices for contaminated gas. The rising bubbles therewith act as an airlift, and cause the liquid to circulate. This counteracts local depletion or consumption of cleansing additives in the washing liquid and also provides a cooling effect, since the bottom liquid also communicates with non-activated parts of the separator. The invention will now be described in more detail with reference to a non-limiting exemplifying embodiment thereof and with reference to the accompanying drawings. In the drawings, which are schematic and, in part, partial views, Figure 1 is a vertical sectional view of a first gas cleansing apparatus according to the invention; Figure 2 is a horizontal sectional view taken on the line II-II in Figure 1 ; Figure 3 is a detailview of Figure 1 , illustrating an outlet orifice in co-action with an opposing impingement or striking surface; Figure 4 is a vertical sectional view of a second embodiment- of a gas cleansing apparatus according to the inven¬ tion; Figure 5 is a horizontal sectional view taken on the line V-V in Figure ; Figure 6 is a detail view of a partition wall provided with inclined lamellae sedimentation plates for separating gas bubbles and particles from recirculating washing liquid; Figures 7-9 are mutually different views of a third embodi- merit of the invention; and Figure 10 is a sectional view in larger scale of a preferred venturi nozzle intended for use in cleansing appara¬ tus according to the invention. Figures 1-3 illustrate highly schematically a gas cleansing apparatus which comprises a pressure vessel 1 , consisting of an outer wall 10, a bottom 11 and a cover or lid 13; and further comprising an inlet 12, a distributor means 14 and an outlet 16. The distributor means comprises a plurality of radially and obliquely downwardly extending distribution pipes 18, the illustrated embodiment having six such pipes. The distri¬ bution pipes have an outer vertically and downwardly extend- 5ing pipe section 20 having a downwardly facing, free opening 22. The distribution pipes 18 have arranged on their respec¬ tive obliquely extending parts riser pipes 24 which are connected to transversely extending distribution pipes 26. As will best be seen from Figure 3, the distribution pipes 026 have provided thereon contaminated-gas outlet nozzles 28 provided with outlet orifices 31. The outlet nozzles, of which only two are shown in Figure 2, may conveniently have the form of venturi nozzles, which are preferably provi¬ ded with suction orifices 29 intended for washing or cleansing 15 liquid and facing the surrounding liquid bath 32. Arranged above the outlet nozzles are respective dispersing devices in the form of impingement or striking surfaces comprising angle iron 30 carried by a supporting structure not shown. 20 The distributing means 14 is lowered into a liquid bath 32 to a given depth beneath the surface 34 of the bath, and in accordance with one preferred embodiment the outlet nozzle 28 has the form of a venturi nozzle. The majority of the outlet orifices 31 of the venturi nozzles 28 are preferably 25 all located on the same level, preferably at a distance of at least approximately 0.5 m, from the surface of the liquid, preferably 2 m. The inlet orifices 64 for contaminated gas for respective venturi nozzles 28 are, in turn, located approximately 1 m or further beneath the outlet orifices 3031. As a result of this height differential there is constant¬ ly achieved a satisfactory cleansing effect with each venturi nozzle, as soon as contaminated gas enters through the down¬ wardly located inlet orifice 64 of said nozzle. The conta¬ minants are isolated during passage through the venturi tube 5 with the aid of liquid drawn by suction through the suction openings 29, this liquid being entrained in droplet form by the gas. These contaminant-laden liquid droplets are, in turn, separated from the gas, partly in the form of a liquid film on the inner surface of the pipe 49 and partly during passage between the outlet orifices 31 and the liquid surface 34. With regard to droplet separation during passage through liquid, a given smallest height differential is required in order to provide satisfactory separation. The invention is not restricted, however, to outlet nozzles in the form of venturi nozzles, but also includes the use of preferably fine outlet pipes directed towards the respec- tive impingement or striking surfaces, so as to atomize the gas into fine bubbles which pass up through the liquid bath. The height of the bath above the outlet orifices 31 should be such as to expose the bubbles to the liquid for a suffi- cient length of time. This applies particularly in this latter embodiment. A substantially horizontal intermediate bottom 36 is arranged between the surface 34 of the liquid and the outlet 16. 'The intermediate bottom 36 has provided therein a plurality of through-passing openings 38 with separating means 40 for separating fine liquid droplets and possibly particles, said means being shown purely schematically. These separating means may, in principle, be of any desired kind. Cyclone devices, however, are particularly preferred. As illustrated in Figure 4, separated liquid can therewith be brought down beneath the liquid surface 34, via an extension pipe 42. The extension pipe 42 may be shielded against direct ingress of gas bubbles by means, e.g., of a hood (not shown) . Further separating means for separating particles and liquid droplets may be arranged in a manner known per se in the space 44, above the intermediate wall 36 and upstream of the outlet 16. The outlet 16 may, in turn, be connected to a further cleansing arrangement or may pass directly to a smoke stack or some other discharge device. The gas cleansing apparatus operates in the following manner. In an unloaded state, washing liquid enters through the orifi¬ ces 29,31 of the outlet nozzles 28 and the lower openings 22, such that an inner liquid surface 46 in the distributing means 14 and the inlet pipe 12 adopt the same position as the surface 34 of the surrounding liquid bath. The gas cleanser now has a water seal function. In the event of a breakdown or accident in which gas is released, the pressure increases and the inner liquid surface 46 is pressed down until it reaches beneath a threshold 65 at the level of the highestmost inlet orifice or orifices 64 of respective out¬ let nozzles 28. Gas will now exit through these outlet nozzle and will draw finely divided liquid droplets into the gas stream during its passage past the suction openings 29. Solid and liquid contaminants together with contaminated gases are absorbed by the liquid droplets sucked into the nozzles. The exiting gas impinges on the impinger or striking surface 30, and is therewith broken down into fine gas bubbles, which rise up through the washing liquid 32. The gas is cleansed further through a washing-bottle effect, the now contaminant- laden liquid droplets, dust particles and gaseous contami¬ nants being taken up by the washing liquid. A certain- propor tion of the droplets are separated in the upper part 49 of the nozzle 28 and settle as a film on the inner surface of said upper part. Thus, the separation or extraction of contaminants takes place in two stages. In a first stage dust extraction and the absorption of gases and ions takes place through a venturi and/or impinger effect through inertia forces in and adjacent the outlet nozzles 28 and the impinger or striking surfaces 30. In a second separation stage, the extraction of dust and absorption of gases takes place through a washing- bottle effect, i.e. absorption, sedimentation and/or diffu¬ sion during passage of the gas bubbles through the washing liquid up to the surface 34 of the liquid bath. Separation of gaseous contaminants can be greatly enhanced by incorporating in the washing liquid substances which cause chemical reactions to rapidly consume, i.e. react with, ions dissolved in the liquid(so-called chemical amplification) . For instance, the separation of acid gaseous components can be improved by dissolving alkaline components in the liquid. Absorption of gaseous iodine can be facilitated by mixing sodium thiosulphate with the washing liquid. As will be understood from the aforegoing and seen from Figures 1-3, all nozzles 28 on one and the same riser pipe 24 of this embodiment will begin to operate substantially simultaneously. The riser pipes 24 on different main pipes 18 may be located on mutually displaced levels, so that not all riser pipes incorporated in one and the same pipe ring will begin to operate at one and the same time. Figures 7-9 illustrate various examples of alternative embodi- ments of the distributing means 14, in which each inlet orifice 64 is connected with asingle outlet orifice 31. Figure 7 illustrates in section part of a distributing means having a main distributing pipe 18. The pipe 18 is provided with downwardly extending connecting pipes 23, each having two obliquely and downwardly, approximately transversely extending distribution or side pipes 26. The side pipes 26 are provided at their free ends with a downwardly extending, vertical pipe section 20 having a free opening 22. Similar - to the preceding embodiment, any condensation formed is able to pass out through the openings 22, while washing or cleansing liquid is able to pass up into the distributing means 14 when the rate of gas flow decreases. Arranged in approximately uniform spaced relationship on the distribution pipes 26 are a plurality of vertically and upwardly e tend- ing venturi nozzles 28 having inlet orifices 64 which face the distribution pipes. The venturi nozzles 28 are provided at their lower ends with suction openings 29 for washing liquid, and at the top thereof with outlet orifices 31 for processed gas. In order to obtain smooth starting conditions in the absence of shock loads at the initial stage of gas release through the gas cleansing^apparatus, each section has two highly located, short side pipes 26' which discharge at loca¬ tions above the remaining nozzles. The downwardly depending pipe sections 20' of the side pipes 26', however, extend down to the same level as remaining pipe sections 20. The distributors are also constructed such that the orifices 64 of the venturi arrangements 28 lie at progressively increasing 5 depths on an increasing number of distribution or side pipes 26, so that the number of active separators increases continu¬ ously with accelerating speeds with increasing gas flow and inlet pressure. 10 Figure 8 illustrates an embodiment which differs slightly from the embodiment of Figure 7 and in which side pipes 26 pass directly from the main distributing pipes 18, in the absence of intermediate, vertical connecting pipes 23. 15 Figure 9 is a sectional view in larger scale of a side pipe 26 having in its upwardly facing surface inlet orifices 64 and vertically upstanding connecting pipes 55 for accommodating venturi nozzles 28. In the Figure 9 embodiment a further outlet nozzle becomes operative or active when the internal 20 water surface 46 moves to the level referenced 46 ' . A preferred embodiment of a venturi nozzle for use with cleansing apparatus according to the invention is illustra¬ ted in Figure 10. The venturi nozzle comprises an inlet part 25 41, a narrowing constriction 43, a cylindrical throat 45, a conically widened part 47 and a cover 51. Located oeneath the cover 51 are laterally directed outlet openings 31. The venturi nozzle has at its lower end a screwthread connection 53 for fitting the nozzle to an upstanding connection pipe 3055 on respective side pipes 26. Located between the constric¬ tion 43 and the throat is an annular groove 57 which has a sharp- edge 59 facing the throat 45. The suction openings 29 discharge into said groove 57, wherewith the liquid entering the groove is able to distribute circumferentially therearound. 35 The groove 57 suitably has an axial extension of 2-4 mm, and the groove edge 63 facing the constriction 43 has a radius which is 0.5-1 mm greater than the radius of the groove edge 59. The tangent to the wall of the constriction adjacent the groove edge 63 therewith passes externally of the groove edge S9-. When gas passes through the venturi nozzle, liquid is sucked into the groove 57 and is torn loose upstream of or adjacent the sharp edge 59, in the form of fine liquid drop- 5 lets. The contaminants in the gas are taken-up by these liquid droplets, during passage through the throat 45, the conically widened section 47 and the upper part 49. The device is thus a self-suction venturi separator. According to the invention, a : least 0.5 kg, preferably 2-3 kg liquid, e.g. water, per 10.of. gas processed shall be drawn by suction through suction openings 29 and into the venturi nozzles 30. Consequently, the suction openings 29 and the grooves 57 are dimensioned such that the desired quantity of liquid will be sucked in at the given drop in pressure. The pressure drop is therewith deter- 15 mined by the difference in levels between the lower orifices 64 and the outlet orifices 31. A pressure drop of 1 m water- column or more is required in the majority of the cases in order to obtain satisfactory cleansing of the gas. It can be mentioned by way.of example that 99% cleansing efficiency 20 can be obtained in a venturi nozzle at a pressure drop of 4 10 Pa, corresponding to 1 m water-column. In the illustrated embodiment, the troat has a diameter of 10 mm and the upper part 49 a diameter of 26 mm. It has been 25 found that in order to achieve a high degree of cleansing, the throat diameter should not exceed about 30 mm. The embodiment illustrated in Figures 4 and 5 includes a modified distributing means 14' having a centrally located, 0 cylindrical distribution chamber 52 and a plurality of distri¬ bution pipes 54 which extend obliquely upwards from the chamber 52 at mutually different levels. The distribution pipes 54 are provided with radially and inwardly directed parts 56 having horizontally and outwardly projecting distri- 35 bution pipes 58. These distribution pipes 58 are provided with outlet nozzles 28, solely shown in one enlarged detail view, and may have located thereabove impinger or striking surfaces 30, as illustrated in Figures 1-3. In this case, 13 the outlet nozzles 28 may have a shorter length, since the inlets64 are located somewhat lower in the distribution chamber 52. The venturi nozzles, however, require a minimum length in order to provide an effective cleansing effect. The gas cleansing apparatus illustrated in Figures 4 and 5 is divided into sections by means of radially extending parti¬ tion walls 60, which are delimited upwardly by the inter¬ mediate bottom 36 and which extend down beneath the level of the outlet nozzles 28. The partition walls extend inwardly to the proximity of the inlet pipe 12, and outwardly to the proximity of the outer wall 10 of the apparatus. Arranged adjacent the outer wall is a circumferential guiding inter¬ mediate wall 48, the upper part of which extends above the surface 34 of the liquid bath when the bath is at rest, and the bottom part of which terminates adjacent the bottom 11 of the apparatus. The partition walls 60 may extend down into the slot-like space 50 and serve to steady the guiding inter¬ mediate wall 48. T «his, arrangement,however, is not necessary for the function of " the cleansing apparatus, and the inter¬ mediate wall 48 may instead be supported by stays connected to the outer wall 10. The distributions pipes 54 present inlet orifices or gas intakes 64 in the wall of the distribution chamber 52 at mutually different height levels. This enables the various cleansing sections to be brought into operation stepwise with increasing inlet pressures. Subsequent to exposure of a gas intake 64, due to the interior liquid surface 46 being pressed down to a lower level, the contaminated gas is able to flow up through the distribution pipe 54, 46 and out through the distribution pipes 58 and their respective outlet nozzles 28. Due to the height differential h between the liquid surface 46 and the distribution pipes 58, there will prevail an overpressure corresponding to the height differen¬ ce in the outlet nozzles 2b. The contaminated gas is thereby able to flow out with a pronounced pressure drop through the outlet nozzles 28, which guarantees a good cleansing effect and fine automization of the air into small bubbles. Because the gas intakes6 are arranged at mutually different heights, it is possible, in this way, to activate automatically one section after another at part loads, with full cleansing effect. This is particularly important for achieving effective extraction of the dust present. The inertia effects are greatly dependent on gas speed, and a low gas speed will result in poor separation. Because of the density reducing effect created by the gas bubbles, the actively working gas cleansing sections 66 will present a higher liquid level 34'. This liquid level 34' lies above the upper edge 68 of the guiding intermediate wall 48. This enables washing liquid to be recirculated from precisely those sections 66 which are actively working and to which contaminated gas is supplied. This prevents local concentra¬ tion of contaminants and depletion of additives in the upper parts of the actively working sections, particularly at part loads. Figure 6 is a detail view of the slot-like space 50 having arranged therein inclined lamellae sedimentation plates 74. These plates 74 define a multiple of inclined spaces or chambers 72 which are defined upwardly and downwardly by said lamellae sedimentation plates 74. Gas bubbles 76 present in a volume of liquid introduced into such an inclined space will rise towards the upper defining plates, whereas particu¬ lars material will sink towards the bottom defining plate. The gas bubbles 76 then rise along the undersurface of the overlying plate, up to the liquid surface 34 or 34' respec¬ tively. The settling particles 78 slide down along the sur¬ face of the underlying plate, and finally fall to the bottom 11 of the vessel, from the bottom edge 80 of respective plates. The use of lamellae sedimentation plates results in lateral displacement of recirculated liquid. This prevents liquid from being recirculated to the same cell or section at part loads, therewith counteracting depletion of the additive sub¬ stances. A heat exchange coil (not shown) may be arranged in the vessel for cooling or, on special occasions, for heating the liquid in the gas cleansing apparatus. The volumetric capacity of the vessel should be sufficiently large to accommodate the condensation formed and the solid particles extracted during active working of the apparatus during a breakdown in operations. When the apparatus is used for cleansing process gases, condensation and solid, extracted particles can be removed through the normally-closed bottom outlet 84 of the vessel, for instance through an arrangement of valves in which two valves are arranged one behind the other. The impinger or striking surfaces may have any desired con¬ figuration. For example, they may comprise perforated plates arranged above the outlet orifices 31. Such a plate will also be effective in distributing the gas bubbles formed across the whole surface, thereby utilizing the available volume to a greater extent. In the case of certain applications the vessel 1 may be freely open at the top. In this case., the side walls 10 must be sufficiently high to prevent the escape of liquid through splashing. Such a vessel may be provided with further separa¬ tor means, such as grids or filters for separating liquid droplets and/or static or fluidised particle beds located above or beneath the surface of the liquid bath. The guiding intermediate walls 48 may be placed at any desired location in the vessel 1 for isolation the slot¬ like spaces 50, for example adjacent the radial partition walls 60, or in pairs with interconnecting short walls. Conveniently, although not necessarily, the intermediate walls 48 are placed between different sections 66 or between parts served by different distribution pipes 18, 54. The vessel 1 need not be circular, but may have any desired configuration, depending, for instance, on local conditions, and may be of rectangular or irregular configuration. Further¬ more, the inlet pipe 12 may be connected to the vessel at any desired location thereon, for instance asymmetrically in the cover lid 13, or may pass through the side wall 10 of the vessel or through the bottom 11 thereof. It is important, however, that the inlet is connected to the distribution means 14 and 14' at a location above the highest gas intake 64. The outlet openings 28 may be connected to respective associa¬ ted gas intakes in the distribution means 14, 1 ' in any desired manner. In the majority of cases an arrangement which comprises horizontal or, for self-drainage purposes, slightly inclined distribution pipes 26, 58 and distribution pipes 18, 54, 56 affords the most suitable solution. The outlet nozzles 28 can be made higher than illustrated in Figure 4, in order to ensure that the liquid droplet sucked in through the suction openings 29 have sufficient distance to pass in order to be effective. It will be understood, however, that cleansing with the aid of a venturi effect can be dispensed " with and solely the impinger action and washinq-bottle effect relied upon. A gas cleansing apparatus according to the invention may have any desired size and may include a multiple of mutually sepa¬ rate and mutually independent distribution means 14 and/or 14'. Furthermore, a gas cleansing plant may comprise a plurality of separate gas cleansing apparatus arranged in groups or at a distance from one another. This latter arrange- ment facilitates maintenance work, e.g. pipe work, and enables individual units to be placed out of action while retaining- a state of readiness. The gas cleansing apparatus according to the invention can thus be given very large dimensions. For example, in the case of an emergency system intended for nuclear power stations, 2 the area may be as great as 50-100 m and the diameter of the apparatus may be 10 m or larger. The initial liquid volume must also be chosen to allow for liquid losses. In the case of a gas release of the order of 10 kg/sec. at a temperature of 150°C, the water boiled-off is liable to be in the order of 3 1.0-3.5 m /h. Additional liquid losses occur as a result of mist formations. The invention is not restricted to the illustrated embodiments, and modifications can be made within the scope of the follow¬ ing claims. For example, the various part solutions illustra- ted in the drawings and/or described in the description can be combined in any desired manner when constructing a gas cleansing apparatus according to the invention.

Claims: CLAIMS 1. A method for cleansing gas from solid,liquid and/or gaseous contaminants, by bubbling the gas through a liquid bath (32) , and by introducing the incoming gas into a distri¬ bution means (14,14') and causing the gas to pass in part- streams through a multiple of inlet orifices (64) located at progressively increasing depths beneath the surface (34, 34') of the liquid (32), the gas flow at increasing inlet pressures being caused to pass through an increasing number of inlet orifices (64) located at depths beneath the liquid surface (34, 34') which increase with corresponding inlet pressure, such that with increasing inlet pressure an increasing number of inlet orifices (64) are utilized for an increasing number of part-streams, such that at least substan¬ tially the same flow passes through the inlet orifices utili- zed irrespective of the inlet pressure and the total flow through the gas cleansing apparatus, characterized by passing the gas flow from respective inlet orifices (64) through connecting means (24,26,28; 54,56-,28) to outlet orifices (31) located at a higher height level (h) than corresponding inlet orifices (64) , and causing the gas flow to pass out into the liquid bath (32) at a pressure drop corresponding to the height differential (h) between respective outlet orifices (31) and an internal liquid surface (46) in said distributions means (14,14') . 2. A method according to Claim 1, characterized by constrict¬ ing the gas flow during its passage through said connecting means, so as to generate high speed gradients, for example in the venturi nozzles (the outlet nozzles 28) , liquid, preferably washing liquid, being sucked into the nozzles through openings (29) provided in the walls of the said nozzles and facing the surrounding liquid bath (3 : 2) . 3. A method according to Claim 1 or 2, characterized by causing the gas part-streams upon exit into the liquid bath ( 32 ) to strike against means (impinger or striking surfaces 30) operative in splitting respective gas streams into fine bubbles, which are permitted to pass out through the liquid while delivering contaminants to said liquid. 4. Apparatus for carrying out the method according to Claim 1, 2 or 3, comprising a vessel (1) which is partially filled with a washing or cleansing liquid (32), an inlet (12) for contaminated gas, a distribution means (14,14') which presents a multiple of inlet orifices (64) for the incoming contamina- ted gas at progressively increasing depths beneath the liquid surface (34,34'), and an outlet (16) for cleansed gas, the liquid surface or surfaces (46) in the interior of the distri¬ bution means (14,14') being pressed down with increasing inlet pressure such as to expose inlet orifices (64) progressively at increasing depths and permit gas to flow therethrough, characterized in that connecting means (24,26,28; 54,56,58, 28) extend from respective inlet orifices (64) to outlet orifices (31) for part-streams of contaminated gas at higher height level (h) than corresponding inlet orifices (64) and beneath the surface (34,34') of the liquid. 5. Apparatus according to claim 4, characterized in that the distributor pipes (18) and/or distributor chamber (52) of distributor means (14, 14') exhibits openings (22) towards the liquid bath (32) situated under the lowermost inlet ori¬ fice (64) intended for gas flow. 6. Apparatus according to Claim 4 ' or 5, characterized in that a large number of outlet orifices (31) are arranged beneath preferably substantially the whole of the liquid surface (34,34'), and/or that the height differential (h) beween the outlet orifices (31) and respective corresponding inlet orifices (64) is approximately 1 m or more, and/or that the outlet orifices (31) are located at a distance from the liquid surface (34) of at least 0.5 m, preferably about 2.0 m, and/or that the major part of the outlet orifices (31) are located on one and the same level. 20 7. Apparatus according to Claim 4, 5 or , characterized in that the outlet orifices have the form of nozzles which ex¬ hibit particle separating properties, for example venturi nozzles (the outlet nozzles 28) which preferably present openings (29) in the nozzle wall, which face the surround ¬ ing liquid bath (32). 8. Apparatus according to at least one of Claims 4-7, characterized in that the vessel (1) is divided into sections by means of radially extending partition walls (60) which extend from a region beneath the outlet orifices (31) to a location above the gas-laden surface (34) of the liquid bath and preferably to a location above the intermediate bottom (36) . 9. Apparatus according to any of Claims 4-8, characterized in that one or more guiding intermediate walls (48) are arranged, for example, adjacent the outer wall (10) ' of the vessel (1) , adjacent the radial partition wall (60) or in pairs opposite one another and define one or more preferably slot-like spaces (50) through which liquid lifted by through- flowing gas can re-circulate down to the lower part of the vessel (1) , and in that said one or more guiding intermediate wall (48) preferably extends to a location above the liquid surface (34) during conditions of rest, but not to the surface (34') of the gas-laden liquid, and/or in that the lower edge of the guiding intermediate wall (48) is preferably located beneath the inlet orifices (28) ; and/or in that obliquely positioned lamellae sedimentation plates (74) are arranged in t least some of said one or more slot-like spaces (50) . 10. Apparatus according to at least one of Claims 4-9, characterized in that separator means for separating liquid droplets and any residual contaminants is arranged above the liquid surface (34,34')/ in that the vessel is preferably a closed vessel (1) and includes a cover or lid (13) having at least one outlet (16) , in that an intermediate bottom (36) is arranged above the highest liquid surface (34') and isolates a chamber (44) upstream of the outlet (16) , and in that the intermediate bottom (36) is provided with openings (38) provided with separation means (40), for instance cyclones, intended for separating fine liquid droplets and particles, the bottom outlet of the cyclones extending down to beneath the liquid surface (34) , preferably through an extension pipe (42) .

Inventors: GUSTAVSSON LENNART, JOHANSSON LARS-ERIK, LINDAU LEIF, GUSTAVSSON, LENNART, JOHANSSON, LARS-ERIK, LINDAU, LEIF
Applicants: FLAEKT AB
Application year: 1987
Main classification: B01D47
IPC codes: B01D47, B01D53, G21C9, G21F9