METHOD AND DEVICE FOR REMOVING FLOATING LIQUID IMPURITIES,PARTICULARLY OIL,FROM A FLOWING WATER SURFACE

Abstract: Separation of impure surface water layer, separation of mixture of impurities and water and method for implementation of discharging impurities separated, according to which local water level lowering required for flowing impure surface water layer through overflow spillway is performed in conformity with the Bernouilli formula by suction effect produced and maintained by increasing flow rate, while separation taking place in the same step is carried out by the transient decrease of flow rate, then by change of direction. By turbulent-free inflow without decrease of rate really excellent scraping efficiency can be achieved. The device for carrying out said method comprises a submersion body of submersion depth first increasing downstream then decreasing, provided with opening serving as hopper to produce suction effect, on bottom in range of greatest submersion cross-section or behind latter, with adjustable spillway on front end on side of inflow, whereas with baffle plate controlling direction of flow and defining cross-section in inner space of submersion body, and with a flow-free zone for collecting the impurities separated.

Description: Method and device for removing floating liquid impurities, particularly oil, from a flowing water surface Technical field The invention relates to a method for removing floating liquid impurities, particularly oil, from a flowing (or forced flowing) water surface by creating locally water surface range of lowered level, by inlet of surface layer of water contaminated (by oil) in the range of water of lowered level through spillway, by separating the mixture of liquid impurities and water, and by removing the separated, collected impurities. Furthermore, the invention relates to a device for removing liquid impurities, particularly oil, floating on the water surface, from flowing or forced- lowing water surface, executed as structural units submerged in water, provided with wall elements as well as overflow spillway encircling a range of lowered water level. Background art Due to the ever increasing industrialization impurities dange- rous to the purity and living substance of natural water sources occur more and more frequently and great efforts are made all over the world to prevent and eliminate them. Among the impu¬ rities, petroleum products are reckoned with as the most dan¬ gerous ones. Different methods and equipment have been deveiop- ed in order to remove them. They can practically be divided in two groups, considering the operational principles. One of the groups contains the (oil) scrapers operating on the basis of the so called adhesion principle in such a way that while oil adheres to certain structural matters submerged in i pured water - which are afterwards taken out -, water does not adhere to them. Thus the oil can be recovered by scraping, wiping, extraction from means of generally large surface (rotary discs, elevators, bundles of fibres, tussels) made of such structural materials (steel, plastics, etc.). The other group involves the oil and impurity scraping πethos for separating the impured surface layer of water. Their common feature is that the space inside the spillway or overflow ring - 2 - of α tank floating on water is sucked by a pump suitable for sucking the mixture of impurities and water creating by this level difference between two parts of the spillway. The surface lcyer-of water and the impurities, such as oil, floating to- gather with, same on the surface runs slowly, i.e. overflows through the spillway i.e. overflow ring. The pump sucks the mixture of oil and water flowing in and continuously maintains the level difference. The mixture sucked is seo 1 σrated so that * oil would o.g. gravitationally be separated. Thc-re are also equipment known with their scrcping unit servicing G± ike same time as separator. A common disadvantage of ail known equipment is that they can be used with full efficiency for still water only as a fundamental condition of their efficient operation is that there can be only at least a slight speed difference bet- ween the equipment and the impured water. Therefore, such equip¬ ment are operated in such a way that the impurities in the vi¬ cinity of the scraper are locally stepped by damπiing, air blast etc. Scraping, however, is in such case of very low efficiency, considerable losses incur, i.e. depending on the water rate uπ- der the effect of the sucking swirls producing, one part of the impurities floating on the surface (such as oil) iecves the scraper, bypassing the equipment and the damming elements mostly from below. Disclosure of Invention The subject of the invention is to separate the impure surface layer of water, to separate the mixture of impurities and water, and to develop method and device - realizing the principle of discharging impurities - suitable for the removal, at a high rate of scraping efficiency, the liquid impurities, particularly e.g. petroleum products floating on the surface in flowing or forced flowing water. According to the present invention the separation of impure surface water layer, separation in the same step and collec¬ tion of the separate impurities, can be realized in the clean- ing cross-section by producing and maintaining expedient speed σ of flow influenced Loth in its .'irccticn and rate. Accordingly, this aim can be achieved by applying the method referred to above in the course of which, cccording to the invention, local water level lowering in flowing cr forced flowing water is effected by creating i.e. maintaining a flow range of increased speed, while the separation of the mixture by the trcnsient reduction of speed and changing the direction of flow subsequent to the inflow of surface water layer let in said range without any speed reduction. Tπ_ scraping efficiency can be considerably increased by turbulent-free inflow of the surface water lover in the range of lowered water level. In a preferably and advantageous per ormance of the method accord¬ ing to the invention, the impurities, ~ articuiσrly oil, obtained from the mixture, are separated in a practically flow-free zone inside the range of lowered water level, then from here same is discharged either continuously or intermittently in the- known way e.g. by pumping, gravitationally, by mechanical, adhesion means, etc. The device for carrying out the method according to the invention comprising a tcnk-Iike submersion body provided ' ith spillway on its open front side facing the water flow, while on the other parts v/ith closed walls overhanging the water surface of a sub¬ mersion depth first increasing downstream from the front side provided with spillway then gradually decreasing, v/ith at least one opening of adjustable croεs-εεcticπ in the bottom, in the bo¬ dy cross_section of the greatest submersion depth, with a baffle plate in its inner space from the front side provided v/ith spill¬ way, overhanging the range above the bottom hole, dividing the inner sr.ace of the body in oarts separated from each other. Such embodiments of the device according to the invention that are provided with spillway of adjustable position (of adjustable height) and/or baffle plate of adjustable angle position proved to be suitable, furthermore, it is advantageous to provide - on the bottom of the submersion body - also a deflection hopper covering the opening from outside, being practically perpendi¬ cular to the direction of water flow, provided with an outlet opening of adjustable cross-section. For the sake of undisturbed outlet - to be effected in inter ¬ mittent mode of operation too in given cases - of the separated impurities it is advantageous to form even an impurity collect ¬ ing zone in the submersion body separated by a barrier starting from the bottom and ending under the lowered water level in the front side part opposite to the spillway. For the sake of the possible best turbulent-free inflow of the surface water layer and of ensuring the minimum level of scraping losses, the pre ¬ ferable embodiments of the device according to the invention are provided also with swirl-diffusion grid arranged in the sur ¬ face water layer, before the spillway. The method and device cccording to the invention enable, by us¬ ing the energy of flow, in one step and one equipment, the col¬ lection of liquid impurities e.g. petroleum products floating on the water surface, the separation of impure surface water layer, the separation of the mixture of impurities and water and the discharging of separr ed and collected impurities. The impure surface water layer is separated without speed reduction (with¬ out damming) and together with the swirl-diffusion grid being on the inlet side of the device it r-.kos possible to eliminate swirls, taking away the lcyer of impurities, causing in uch way loss in discharging. Local lowering of the water level ana continuous flowing through of the mixture of impurities and water along the separating forced path are effected by the suction effect pro- duced by the increase of the flow rate, based on the Bernoulli formula, without the utilization of an external power source (e.g. pumping). The separating forced path ensuring undisturbed flow- through, by its increasing cross-section adjustable by selecting the proper angle position of the baffle plate performs gradual deceleration of the mixture of impurities and water in the first . section subsequent to the inflow, then behind the baffle plate end the flow is performing horizontal rotation, meanwhile, the upper layer of impurities, particularly oil-phase, stops and the lower water layer leaves the inner space of the submersion body, accelerating towards the opening forming the sink of sucking action. - 5 - The method end device described above in details can be widely applied, as according to the invention, portable oil scrapers, fluvial impurity separators - as engineering structures (e.g. in hydro-electric power stations) -, preventive oil traps on a fixed plate for the outlet pipeline of impurity sources (e.g. oil refineries, heating plants, etc.) as well as impurity-, particularly oil-contamination traps, collecting basins estab¬ lished by bed setting and earthwork, serving for prevention purposes can be made. Furthermore, the characteristics of the method according to the invention can be made use of when de¬ signing moving oil scraper ships i.e. the portable preventive devices according to the invention can be applied also as moving impurity-, especially oil-scrapers in case they are moved (e.g. pushed or hauled; by a water craft on still water. Brief Description of Drawings The essential steps of the method according to the invention • and the device according to the invention will now be further described in details by way of example with reference to the accompanying drawings in which: Fig. 1 is a schematic top view of an oil removing device ac¬ cording to the invention and Fig. 2 is a sectional diagram taken along II-II plane of the same device shown in Fig. 1. Best Mode of Carrying out the Invention The device taken as example, illustrated on the drawings con¬ tains practically a tank-like submersion body 2 v/ith rectan¬ gular top view, provided with spillway 4 of adjustable heigh by turning along an axis on the open front end 21 facing the direction of water flow, encircling a rectangular water sur- face range by side walls 22, 23 and front end 24. The down¬ stream section of its bottom 25 is executed with submersion depth of first increcsing from front end 21 provided with spillway 4 then gradually decreasing. On bottom 25 of submer¬ sion body 2, approximately in the middle, in the greatest submersion depth, there is a hole 26 whose clear opening is adjustable by the angle position of a closing element. A further essential feature of submersion body 2 is that in its inner space there is a baffle plcte 27 dividing the inner space of submersion body 2 in parts separated from each other, starting from front end 21 provided with spillway 4 overhanging the range above open ¬ ing 26 being in bottom 25. There is also a deflection hopper 3 in bottom 25 of submersion body 2, covering opening 26 from out¬ side, practically perpendicular to direction of water flow, pro¬ vided with outlet orifice of adjustable cross section. In sub- εrsicn body 2 in the front end range, opposite to spillway 4. there is an impurity collecting zone separated by barrier 2S starting from bottom 25 ending under the water surface and in case of impurity, e.g. oil removal by pumping, the end of the suction conduit joined to the suction stud is butting into it. Other mechanical, adhesion etc. impurity discharging ecns can be connected .v/ith said device according to the invention also in said zone. Submersion body 2 is kept floating by float 1 placed on its two sides. The device according to the invention operates as follows: The flowing water, while bypassing from below float -2 kept floa¬ ting end anchored by float 1 , locally accelerates along contracted streamlines. By this way, one important feature of the method according to the invention can be achieved, namely in a flowing or forced flowing water cross section a cross-sectional range of increased flow rate is produced and maintained.As a result, ac¬ cording to the Bernoulli formula the increase of speed produces local suction ef ect through opening 26 formed on bottom 25 in " the inner space of submersion body 2 and this results in perma¬ nent water level decrease in the water surface range provided with spillway 4, encircled by side walls 22, 23 and front wall 24. The rate of the suction effect can be set by means of the execution of the longitudinal section of submersion body 2, i.e. in case a given means is applied for various flow rates, by changing the throttle defining cross section of opening 2 and that of adjustable deflection hopper 3. The impurities particularly oil floating on the surface flow together with the surface layer of water through spillway 4, by the help of the water level difference, without speed re ¬ duction, in the rcπge of lowered water level of submersion bo ¬ dy 2. Cy avoiding damming, as wall as by help, of grid 5 arran ¬ ged in fro'-.t of spillway turbulent-free inflow of the impure surface water can be ensured thus there will be no swirls caus¬ ing losses in discharging. As structural material, rubber can preferably be used for i.ckinπ grid 5 due to its favourable damping end self-clccning ability. Referring to a further characteristic feature of the method according to the invention, separation of impurities and water can be performed by reducing the rate of surface water layer flow in the range of lowered water level and by changing the direction of flow. For this purpose baffle plate 27 placed in the inner space of submersion body 2 takes the liquid flow flow¬ ing in through spillway 4, leaving submersion body 2 throuth opening 26 onto a forced path of gradually increasing cross section bringing about accordingly the reduction of the flow rate, then making it perform a horizontal, approximately 180 turn too. It has been experienced that in the course of this, gravitational separation of impurities, particularly oil, and water flowing on the surface takes place, the impurities (oil) get collected in a practically low-free zone provided with barrier 2ό starting rc:.. bottom 25, ending under the lowered water surface, In a front end part opposite to spillway 4 of submersion body 2, v.hii the excess water leaves the inner Space of submersion body 2 throuth opening 26 and deflection hopper 3 making repeated change of direction. Thereafter, the oil can be discharged in any of the ways already known. It can be easilv understood that it is no matter in the cours of carrying out the method according to the invention and in the device suitable for said purpose, how trie relative speed difference between the device and the wa er to be purified is produced. Therefore, the device for carrying out the method according to the invention can bo made cs equipment anchored _ o - properly in flowing surface water or as equipment to be moved in still water by vessels or otherwise. The scope of protection is not limited to the embodiment described above only by way of example with reference to the drawings, within the scope of protection defined by the attached claims other devices of dif¬ fering embodiment can also be realized.

Claims: AMENDED CLAIMS (received by the International Bureau on 18 May 1981 (18.05.81)) 1. (cancelled) 2. (cancelled) 3. (cancelled) 4. (cancelled) 5. (cancelled) 6. (cancelled) 7. (cancelled) 8. (cancelled) 9. (cancelled) 10. (cancelled) 11. (cancelled) 12. (new) lie od for removing floating liquid impu¬ rities- pa ticularly oil, from a flowing or forced flo/ing water surface by separating of impure water surface layer through a spillway or a spillover, by separating the πimture of liquid impurities and water while continuous forced flowing of water through a created locally water surface range of lowered level in relation to the flowing water surface, and by removing the separated collected impurities, characterised in that the local water surface range of constant lowered level is performed by a suction- -effect established and continuously maintained by way of increasing the flow rate in flowing or forced fleeing water for securing the άeceleration-fre.e inflow of the water layer containing the separated impurities and that the separation of the mixture is carried out by turbulent-free decelerating the forced flowing water surface layer containing the separated impurities in the water surface range of lowered water level and by changing the direction of flow bv the aid of this changing in direction a locally flow-free zone inside thewater surface range of lowered level is created, where the separated impurities are colle ed gravitationally, due to the kinetic energy of the drift and from where the impurities can be removed continuously or ciscontinuously, in a known manner e.g. by pumping. 13. (new) Device for removing floating liquid impuri ties, particularly oil, from a flowing or forced flo 0 ing .a 1 comoπsing a s.ruc.i ' unit part sufcmerged in water, provided with an opening at the bottom and with wall elements encircling the range of lowered water level i.e. with spillway, wherein means e.g. a pump - for removing the collected impur 5 ties- can be connected to said structural unit, chara terised in that said device comprises a tank-like su mersion body (2) with bottom (25) of a submersion depth first increasing downstream then gradually decreasing from the front end (21) provided with an 0 adjustable spillway (4) of vertically positi as compared eo submersion body (2) connected to them, wherein said submersion bcdy (2) has on its open fro end (21) facing the direction of water flow, a swirl diffusion grid (5) preferably made of rubber or of 5 another elastic material, running essentially paralle with the direction of water flow, positioned in or u the dividing level between the surface water layer t be separated and wherein εt the deepest point of the submersion body (2) an opening (26) of adjustable cr C -section is located above the zone of greatest cuter streaming rate and of smallest pressure, outwardly surrounded by a deflection hopper (3) of adjustable mc: :ence _cr _.. '...1 -, v- - .. = ; r_e oues_.ee 1 - ~ — OMPI 14. (new) Device as claimed in claim 13, -_ __. ϋ u ii e_ _ ij . in that in the submersion body (2) there is a baffle plate (27) for increasing the efficiency of the separation and the collection of impurities, start¬ ing from front end (21) provided with a spillway (4), overlapping the range above opening (2c) and being located at an angle suitable for ensuring the turbu¬ lent-free deceleration, of the surface water layer flowing through spillway (4) and containing the impu¬ rities. 15. (new) Device as claimed in claim 13 or 14, characterised in that in the submersion body (2) in its area at the front end part opposite the spill¬ way (4) there is a barrier (28) starting frcm the bot.om. (25) and ending under the lowered water level in order to increase the efficiencj * of the separated impurities collecting zone.

Inventors: SZEREDAY P
Applicants: NOVEX FOREIGN TRADE CO LTD, SZEREDAY P
Application year: 1980
Main classification: E02B15
IPC codes: C02F1, E02B15