Patent GB-753914-A (GB)
Title: Process and apparatus for sewage digestion
IPC: C02F3/28
Filed: 1954-04-29
Abstract: 753,914. Sewage digestion. CHICAGO PUMP CO. April 29, 1954 [June 8, 1953], No. 12413/54. Class 111. In anaerobic digestion of sewage sludge, methane - containing gas, which may be digester gas, is diffused upwardly through a diffuser whose greatest horizontal dimension is at least about 7 per cent of that of the sludge immediately above it, into the lowest third of the sludge in an amount of # to 2 cub. ft./min. per foot of the longest horizontal crosssectional dimension of the body of sludge to effect a circulatory movement thereof. Sludge from raw sewage is deposited in a settling tank 11, effluent being passed through an aeration tank 15 and final settling tank 18 before being treated in any known manner. Sludge from the tank 18 is pumped back to the tank 11 and the raw sludge from this tank flows to an aeration tank 29 where a diffuser introduces air amounting to from 25 to 100 per cent of the volume of the sludge and an adsorbent such as powdered coke, fuller's earth, silica gel or diatomaceous earth may be added. A heater 34<SP>1</SP> heats the sludge from the aeration tank 29 to 80 to 100 F. before its entry into a concentrator tank 32 supplied with methane-containing digester gas from a digester through a diffuser 47 which maintains a slow upward flow of gas, disturbance of the sludge being avoided by keeping the gas flow less than 0.1 cub. ft./min. per foot of the diameter of the tank. The diffuser may comprise radially disposed tubes 100, 101, Fig. 2, on a circular header, or, in the case of a rectangular tank parallel tubes on a straight-header disposed centrally or at one side of the digester. The gas floats the sludge to the top to be passed into a primary digester tank 43. Here, a fixed or floating cover 60 provides a dome 45 for collecting digester gas which is delivered by a blower 44 through pipes 62, 63<SP>1</SP> to a diffuser 63 disposed in the lowest third of the sludge content of the tank. The gas, which may be heated to 80 to 100 F., by steam from a generator 68, is introduced at a rate between # to 2 cub. ft./min. per foot of the diameter of the tank, provides a cylindrical rising column having a diameter of from 7 to 15 per cent of that of the tank and produces a circulatory movement of the material at from ¢ ft. to 1¢ ft. per second measured at a point that is 10 per cent of the depth of the material and spaced from the centre of the region of gas introduction by three-quarters of the longest horizontal distance from there to the farthest inner wall of the tank. The material may be circulated through an external heater 56. Periodically partially digested sludge is withdrawn through a pipe 52 to a secondary digester 143, similar to the digester 43, and its place taken by inflow from the concentrator tank 32. To accelerate the process sludge may be fed back to the concentrator 32 from the primary digester 43 and from the secondary digester 143 to the primary digester 43 to "seed" them, the " seed " sludge having ¢ to 5 times the volume of the material to be seeded. The digester 43 operates continuously but the digester 143 is stopped periodically to allow separation of the sludge and liquor for discharge therefrom. Digested sludge not used for seeding is delivered through a pipe 153 to the sludge beds while the supernatant liquid may be passed to either the sludge beds or the settling tank 11. Rectangular tanks may replace the circular ones shown, their' diagonals taking the place of the diameters for measurement purposes. Specification 638,185, [Group VI], is referred to.