초록 ▼

The invention relates to a static decanter (D) for prethickening liquid sludge in a water treatment plant, in particular wastewater, comprising an inclined bottom (8), the decanter being provided with a liquid sludge supply pump (13), a device for injecting a polymer in the liquid sludge, an overspi

The invention relates to a static decanter (D) for prethickening liquid sludge in a water treatment plant, in particular wastewater, comprising an inclined bottom (8), the decanter being provided with a liquid sludge supply pump (13), a device for injecting a polymer in the liquid sludge, an overspill discharge (23) and a pump (26) for extracting the prethickened sludge from the decanter. The decanter further includes a means for accelerating the sludge decantation, a means (M) for adjusting the concentration of suspended material in the prethickened sludge at the outlet, and capable of maintaining the concentration of the prethickened sludge extracted from the decanter at a substantially constant level despite the concentration variations at the inlet, and a means (M3) for adjusting the level of the sludge blanket (V) and capable of maintaining said level at the lowest possible level.

대표청구항 ▼

1. A static settler for prethickening liquid sludge in a water treatment plant for optimizing operation of one or more thickeners installed downstream of the settler, the settler comprising: a reactor having a sloped bottom converging toward a central recovery pit for extracting prethickened sludge

1. A static settler for prethickening liquid sludge in a water treatment plant for optimizing operation of one or more thickeners installed downstream of the settler, the settler comprising: a reactor having a sloped bottom converging toward a central recovery pit for extracting prethickened sludge from the reactor, a liquid sludge inlet, a device for injecting polymer into the liquid sludge, and an overflow discharge, wherein:means for accelerating settling of the sludge in the reactor,means (M) for controlling the suspended solids concentration of the prethickened sludge at an outlet of the reactor, the means for controlling the suspended solids concentration being configured to maintain the concentration of the prethickened sludge extracted from the settler substantially constant independent of concentration variations from the liquid sludge inlet, andmeans (M3) for controlling a level of the sludge blanket (V) in the reactor, the means for controlling the level of the sludge blanket being configured to maintain the level of the sludge blanket at or below a first predetermined level selected to minimize residence times of the prethickened sludge in the settler, wherein the means for controlling the level of the sludge blanket comprise a first probe for measuring the height of the sludge blanket, a variable speed polymer feed pump, a polymer flowmeter on the polymer injection line, and a first controller receiving data from the first probe measuring the height of the sludge blanket in the reactor and from the polymer flowmeter, the first controller configured to control the speed of the polymer feed pump in response to the received data, to control a flow rate of the polymer into the reactor, to adjust the flow rate of the polymer into the reactor to lower the level of the sludge blanket to be at or below the first predetermined level, to maintain the flow rate of the polymer at a predetermined rate when the level of the sludge blanket is at or below the first predetermined level and above a second predetermined level, and to cut off the flow rate of the polymer when the level of the sludge blanket falls below the second predetermined level. 2. The settler as claimed in claim 1, wherein the means for accelerating the settling of the sludge comprise an angle of inclination of the sloped bottom to the horizontal of between 20° and 45°, and a rotating, bottom scraper. 3. The settler as claimed in claim 2, wherein the scraper comprises an arm equipped with scraper blades disposed in a slatted arrangement so as to convey the settled sludge effectively and rapidly toward a central pit which is also scraped. 4. The settler as claimed in claim 3, wherein the arm is equipped with a harrow promoting the prethickening of the sludge. 5. A water treatment plant, comprising the settler of claim 1 having a settler extraction outlet connected directly to a sludge thickener without a thickened sludge buffer tank between the settler and the sludge thickener. 6. The settler as claimed in claim 1, wherein the means for controlling the concentration of prethickened sludge comprise means for controlling the mass flow rate of suspended solids entering the settler, and means for controlling the concentration of the prethickened sludge from the inlet mass flow rate. 7. The settler as claimed in claim 6, wherein the means for controlling the mass flow rate of suspended solids entering the settler comprise: a variable speed liquid sludge feed pump,a liquid sludge flowmeter,a second probe for measuring the suspended solids concentration of the liquid sludge, anda second controller which receives the data from the liquid sludge flowmeter and from the second probe, and controls the speed of the feed pump to maintain the feed mass flow rate substantially constant. 8. The settler as claimed in claim 6, wherein the means for controlling the concentration of the extracted sludge from the inlet mass flow rate comprise: a variable speed prethickened sludge extraction pump,a prethickened sludge flowmeter,a second probe for measuring the suspended solids concentration of the prethickened sludge, anda second controller which receives the data from the prethickened sludge flowmeter and from the second probe, and controls the speed of the extraction pump to maintain the concentration of prethickened sludge substantially constant, the initial extraction rate being calculated from the inlet mass flow rate (FM1) and an extracted sludge concentration setpoint (Stpt D2). 9. The settler as claimed in claim 1, wherein the first controller is configured to control the speed of the polymer feed pump to optimize the polymer consumption within the reactor. 10. The settler as claimed in claim 1, wherein the means for accelerating the settling of the sludge, the means for controlling the suspended solids concentration and the means for controlling the level of the sludge blanket are configured in combination to function so that a residence time of the sludge in the settler does not exceed two hours. 11. The settler as claimed, in claim 1, wherein the sloped bottom has a frustoconical shape, and the means (M3) for controlling the level of the sludge blanket is configured to maintain the level of the sludge blanket substantially at a level of a large base of the frustoconical shaped sloped bottom. 12. The settler as claimed in claim 2, wherein the peripheral speed of the scraper is between 10 cm/s and 20 cm/s.