METHOD AND PLANT FOR THE ANAEROBIC PURIFICATION OF WASTE WATER

Abstract: For the anaerobic purification of waste water it is difficult to maintain good operative contact between sludge particles with bac­ teria and water to be purified, i.e. sufficiently freely floating sludge particles, which means avoiding the formation of a dense settled layer of active sludge and avoiding easy washing away of sludge with the water in the usual upward flow thereof. The inven­ tion proposes the generation of a downward flow of the water to be purified in a reaction chamber (2) and the introduction of an oxygen-free gas to contact the active sludge particles so that gas bubbles adhere thereto and keep them floating as much as possible notwithstanding said downward flow. Any sludge moving downwards with the water too much enters a flotation device (6) near the top of the reaction chamber (2), from which it overflows (7) to be returned wholly or partially to the reaction chamber. Preferably, the reaction chamber has a central riser pipe (3) leading water with some sludge from the bottom of the reaction chamber (2) upwardly to the flotation device (6).

Description: The invention relates to a method and a plant for the anaerobic purification of waste water. Known anaerobic purification systems have an in­ let for the waste water near the bottom end of a reactor compartment in which active sludge purifies the waste water through the action of anaerobic bacteria with the evolution of fermentation gas, mainly methane and carbon dioxide. The upward flow of liquid counteracts the set­ tling of the sludge and increases the chance of sludge particles also being carried upwards which have then to be separated from the purified waste water and fermenta­ tion gas produced in a so-called three-phase separator. Problems with the operation of a three-phase separator often make it necessary to use an additional post settler from which the sludge is returned to the reactor chamber again. All kinds of measures have been proposed to ob­ tain sludge particles which continue to float in such a rising current of waste water as steadily as possible in order in this way to act as intensively as possible on the waste water so that not too much sludge is carried upwards and not too much sludge settles and forms, at the bottom of the reactor chamber, an excessively compact layer which keeps too small a part of the surface of the sludge intensively in contact with the waste water. How­ ever, this requires complicated measures, with which, however, it is often difficult to maintain a good equili­ brium. A considerable problem in this connection is that if the sludge blanket is not too easy to carry upwards, the waste water switches over to channel formation through the sludge blanket. These short-circuiting cur­ rents result in a deteriorating operation of the plant. A sludge blanket on the bottom of the reactor compart­ ment often blocks up the waste water inlet points. The object of the invention is to provide an im­ provement in this respect and for this purpose a method according to the invention is primarily characterized in that in a reactor compartment a downward flow of the waste water is produced and that an oxygen-free gas is brought into contact with the active sludge in a manner such that gas bubbles adhere to the sludge particles, as a result of which the conglomerate of sludge particles and small gas bubbles experiences an upward force which causes it to remain essentially within the reactor compartment despite the downward flow of the waste water therein. For this purpose a plant according to the inven­ tion is primarily characterized in that it has a waste water inlet at the top end of the reactor compartment thereof, and an outlet thereof near the bottom end of the said compartment, with the result that a downward flow of the waste water can be maintained therein, and that means are provided for distributing an oxygen-free gas in the waste water so that gas bubbles adhere to the sludge par­ ticles, as a result of which the sludge particles exper­ ience an upward force which causes them to remain essen­ tially in the reactor compartment despite the downward flow of the waste water therein. The gas used must not of course be oxygen-con­ taining in order not to disturb the action of the anaero­ bic bacteria. Nitrogen appears to give good results. Carbon dioxide gas might also be considered. It has emerged that application of the invention may lead to very good results. With a good design of method and plant the fermentation gas developed by the fermentation will form itself as and into larger bubbles which are easily able to rise in the downward waste cur­ rent in the reactor compartment and which can be collec­ ted and removed independently of purified waste water and sludge. In a manner known per se purified waste water and entrained sludge particles can be separated in a flota­ tion device. Preferably the flotation device is placed at the top of the reactor compartment. Since in the case of downward flow in the reactor compartment the waste water is removed from the bottom of said chamber, virtu­ ally only such sludge is carried along with the waste water through said outlet which is not (no longer) firmly attached to a gas bubble. By introducing said oxygen-free gas into this outlet current of purified waste water con­ taining sludge in this manner, said sludge particles in particular are reloaded with gas, with the result that they can again perform good service in the reactor com­ partment. The small gas bubbles are preferably attached to the sludge in the flotation device, and in particular with the aid of a flotation generator. The proposed flo­ tation generator operates on the dissolved-air principle, an oxygen-free gas being dissolved in a pressure tank at high pressure (approx. 5 bar) in a recirculating current of purified waste water. The recirculating water, satu­ rated with an oxygen-free gas at high pressure, is intro­ duced into the flotation device at atmospheric pressure, as a result of which the small gas bubbles emerge from the supersaturated solution and adhere to the sludge. In the flotation device the conglomerate forms a floating layer which is returned again to the reactor compartment. All kinds of preferred characteristics of method and plant according to the invention are based on the said idea of the adherence of gas bubbles to sludge. The invention lends itself particularly well to being embodied in a manner such that the reactor compart­ ment is located essentially below the ground level and has a length (height) which is a multiple of the horizon­ tal diameter or comparable transverse dimension. In this case only a small amount of pumped energy is required as supply of the waste water at the top of the reactor com­ partment and removal thereof from the bottom via a riser pipe which, for example, runs centrally upwards through the reactor compartment and debouches near the ground level or at least at the top of the reactor compartment can take place through a system of communicating vessels, it being possible to supply the waste water virtually at atmospheric pressure above the liquid level in the reac­ tor compartment and the same quantity of purified waste water flowing away automatically through the riser pipe. The considerable length (height) of the reactor compart­ ment provides a long action path for the sludge and the relatively small horizontal diameter of said compartment provides a uniform downward waste water current over the whole surface. The invention will now be explained in more de­ tail with reference to the accompanying drawing which shows a plant according to the invention in vertical sec­ tion somewhat diagrammatically. Below the ground level 1 a circularly cylindrical reactor compartment 2 is installed in the ground and pro­ vided with a central riser pipe 3 which is in communica­ tion with the reactor compartment at the bottom through an opening 4. Through an opening 5 the riser pipe 3 is in liquid communication at the top with a flotation device 6 in which the current velocities are low as a result of the spacious dimensions and sludge lighter than purified waste water can easily rise to the surface where it can flow away along with some water over an overflow rim 7, helped in this process by a lightweight scraper 8 which is caused to rotate slowly by a central motor 9 which op­ tionally has a suitable transmission system. Said sludge flows away through a pipe 10 to a sludge return chamber 11 which may be situated wholly or partially under the ground level 1. From there said sludge is returned through a pipe 12 to the reactor compartment 2, which pipe 12 may debouch into the gas collection space 13 above the liquid surface therein. The waste water to be purified is also introduced into said reactor compartment 2 at the top through a pipe 14. Gas collected in the space 13 is removed through a pipe 15. Purified waste water is removed from the flota­ tion compartment 6 by passing under the lower rim 16 of an immersed partition, in which process it rises and, via an overflow rim 17, ends up in a duct 18 which has an outlet 19. At the bottom of the flotation compartment 6 around the opening 5 where the riser pipe 3 debouches therein there is an upright screen 20 around which on the bottom of the compartment 6 there is an annular tube 21 which has openings. Purified waste water freed of sludge enters therein and flows from this point through a pipe 22 via a pump 23 to a flotation generator 24 into which a gas inlet 25 debouches. From this point said water flows via pipe 26 to a debouchment 27 directly above opening 5. The pump 23 draws in said waste water and pressurizes it, with the result that, in compartment 24, it can absorb a considerable quantity of oxygen-free gas such as nitrogen introduced through gas inlet 25. De­ bouchment 27 is formed by one or more fine openings, with the result that it is possible for the water to remain under high pressure in the pipe 26. During the discharge thereof from debouchment 27 the pressure drops consider­ ably, as a result of which the gas dissolved in the water is released as fine bubbles. A considerable part of said bubbles adhere to sludge particles which at this point flow past along with the purified waste water out of riser pipe 3. The sludge particles thus separate from the purified waste water and retain said gas bubbles during the formation, along with some waste water, of a foam like floating layer on top of the liquid in flotation device 6, during the scraping off by scraper 8 and during the return flow though 10, 11 and 12 back to the reactor compartment 2. In the latter the downward liquid current will carry the sludge downwards, resulting in a sludge bed over a considerable height in which sludge particles float under the influence of the equilibrium between the downward force of the liquid flow thereon and the upward force resulting from the buoyancy of the adhering gas bubbles and the intrinsic weight of the sludge particles in the liquid. This sludge bed will have the tendency to contain few sludge particles, and primarily those sludge particles to which little or no gas is attached, at the bottom of the reactor, which sludge particles are carried downward by the waste water current and removed upwards by the riser pipe 3. It is thus precisely those sludge particles which do not have (any longer) a gas bubble which flow through zone 5 where they come into contact with gas bubbles from debouchment 27. At the beginning of the process active sludge ob­ tained in this manner can be introduced and initially, when the waste water is introduced, it will flow downward to a considerable extent in the reactor compartment 2 and flow upwards through the riser pipe 3 until it has been charged to a sufficient extent with gas at 5, 27. Since the purifying action is still low at this time, the waste water can also be circulated, for example by connecting outlet 17 from duct 16 to inlet pipe 12, until the sludge has formed a bed to a sufficient extent in reactor com­ partment 2 and the waste water which flows into the flot­ ation device 4 is purified to sufficient extent. Of course, all kinds of known measures can be taken to bring the temperature and the acidity of the waste water to, and hold it at, a desired value, etc. The reactor compartment 2 may, of course, have a section which is other than circular, for example it may be a cylinder (in the geometric sense) having a square section. A suitable reactor compartment height to be con­ sidered is approx. 20 - 60 m and a suitable diameter is approx. 2 - 4 m, but it is possible to deviate consider­ ably therefrom. If nitrogen is used, the pressure of the waste water in the flotation generator 24 is, for example, 5 bar. The gas is introduced preferably through freely flowing into the generator 24. The debouchment 27 is preferably constructed as an injection nozzle.

Claims: 1. Method for the anaerobic purification of waste water, characterized in that in a reactor compartment a downward flow of the waste water is produced and that an oxygen-free gas is brought into contact with the active sludge in a manner such that gas bubbles adhere to the sludge particles, as a result of which they experience an upward force which causes them to remain essentially in the reactor compartment despite the downward flow of the waste water therein. 2. Method according to Claim 1, characterized in that said gas is introduced under pressure into a pressurized part of the waste water from which the sludge has essen­ tially been separated and that part of the waste water is then brought into the vicinity of the sludge with a reduc­ tion in pressure. 3. Method according to Claim 1 or 2, characterized in that waste water and sludge is taken from the bottom of the reactor compartment to a flotation device placed on top of the reactor compartment, that sludge and puri­ fied waste water are separated in said flotation device, and that a part of said waste water is pressurized and an oxygen-free gas is introduced under pressure into it, af­ ter which said waste water part is introduced with reduc­ tion in pressure into the main current of waste water and sludge near the point where the upward flow enters the flotation device, while the sludge separated in the lat­ ter is largely returned to the uppermost part of the reactor compartment. 4. Anaerobic waste water purification plant, charac­ terized in that it has a waste water inlet at the top end of the reactor compartment thereof, and an outlet thereof near the bottom end of said compartment, with the result that a downward flow of the waste water can be maintained therein, and that means are provided for dis­ tributing an oxygen-free gas in the waste water so that gas bubbles can adhere to the sludge particles, as a result of which the sludge particles experience an upward force which causes them to remain essentially in the reactor compartment despite the downward flow of the waste water therein. 5. Plant according to Claim 4, characterized in that the bottom end of the reactor compartment is in communi­ cation through a pipe with a flotation device provided on top of the reactor chamber, from which device sludge floating upwards is removed via an overflow rim to be re­ turned wholly or partially to the top of the reactor com­ partment while purified waste water is removed from the flotation device at a lower level. 6. Plant according to Claim 5, characterized in that the riser pipe runs vertically and centrally through the reactor compartment. 7. Plant according to Claims 4, 5 or 6, character­ ized in that the gas evolved in the reactor compartment is collected at the top of said compartment and removed, while at the top of said compartment there is an inlet for the waste water to be treated and an inlet of sludge particles with adhering small gas bubbles. 8. Plant according to one of the Claims 4 to 7, incl., characterized in that a part of the waste water current is pressurized, that an oxygen-free gas is introduced in­ to it and that said current is introduced with a reduction in pressure into the main flow of the waste water through the reactor in a manner such that the gas bubbles released as a result of the reduction in pressure adhere to the sludge particles in the main flow. 9. Plant according to Claims 5 and 8, characterized in that the partial flow of waste water into which the gas is introduced is removed from the flotation device at or near the outlet of purified waste water and after flowing through the gas inlet device is introduced into the main flow of the waste water near the point where the pipe which connects the bottom end of the reactor com­ partment with the flotation device debouches into the latter. 10. Plant according to Claim 9, characterized in that an upright screen is provided around the inlet of the main flow of waste water which debouches at the bottom of the flotation device and that the partial flow of waste water is removed to the gas inlet device from the flota­ tion device on the other side of said screen. 11. Plant according to Claims 4 to 10 incl., charac­ terized in that the reactor compartment is essentially below the ground level. 12. Plant according to Claims 4 to 11 incl., charac­ terized in that the reactor compartment is essentially cylindrical and has a length (height) which is a multiple of the diameter or a comparable horizontal dimension thereof.

Inventors: ENGWIRDA, SIEBOUT
Applicants: MULTIREAKTOR B.V.
Application year: 1986
Main classification: C02F3
IPC codes: C02F3