Method and apparatus for treating sludge, and method and apparatus for treating wastewater utilizing the same
Abstract
A method and an apparatus for treating organic wastewater and sludge which remarkably reduce the generated amount of sludge at a much lower running cost, and which reduce the size and the capacity of the solubilization tank. The method and apparatus for treating sludge employs a biological treatment system, wherein a biological treatment of wastewater is carried out, and a solid-liquid separation unit for separating a solid from a liquid in the wastewater after the biological treatment, to obtain a treated wastewater and a sludge. The apparatus has a means for obtaining a withdrawn sludge from a part of the sludge and an alkali-treatment tank, wherein an alkali-treatment of the withdrawn sludge is carried out. The apparatus also has a biological solubilization tank which solubilizes the sludge after the alkali-treatment under an anaerobic, anoxic or microaerophilic condition, and a means for recycling the solubilized sludge to the biological treatment system.
Claims
exact text as granted — not AI-modified1 . A method for treating a sludge comprising the steps of:
(a) treating a wastewater biologically to generate a sludge; (b) treating the sludge from step (a) by an alkali-treatment to provide a treated sludge; and (c) solubilizing the treated sludge from step (b), biologically, under an anaerobic, an anoxic, or a microaerophilic condition.
2 . A method for treating a wastewater comprising the steps of:
(a) treating a wastewater biologically; (b) separating a solid from a liquid in the wastewater treated biologically from step (a), to obtain a treated wastewater and a sludge; (c) withdrawing a portion of the sludge from step (b) to obtain a withdrawn sludge; (d) treating the withdrawn sludge from step (c) by an alkali-treatment; and (e) biologically solubilizing and decomposing the withdrawn sludge from step (d), under an anaerobic, an anoxic or a microaerophilic condition.
3 . The method according to claim 1 , wherein a pH value is 7 to 9 during treating the sludge by the alkali-treatment.
4 . The method according to claim 2 , wherein a pH value is 7 to 9 during treating the sludge by the alkali-treatment.
5 . The method according to claim 2 , further comprising the step of thickening the sludge before treating the withdrawn sludge by the alkali-treatment.
6 . An apparatus for treating a sludge comprising:
(a) an alkali-treatment tank for treating a sludge by an alkali-treatment, said sludge being generated from a biologically treated wastewater; and (b) a biological solubilization tank, said biological solubilization tank being located at a downstream side of the alkali-treatment tank, said biological solubilization tank being connected with the alkali-treatment tank via a passage, said biological solubilization tank being capable of biologically solubilizing the sludge after treating the sludge by the alkali-treatment under an anaerobic, an anoxic, or a microaerophilic condition.
7 . An apparatus for treating a wastewater comprising:
(a) a biological treatment unit to biologically treat a wastewater; (b) a solid-liquid separation unit, said solid-liquid separation unit being located at a downstream side of the biological treatment unit, said solid-liquid separation unit being connected to the biological treatment unit via a passage, said solid-liquid separation unit being capable of separating the biologically treated wastewater from the biological treatment unit and obtaining a treated wastewater and a sludge; (c) a sludge thickening device for obtaining a withdrawn sludge from a part of the sludge; (d) an alkali-treatment tank to treat the withdrawn sludge by an alkali-treatment; (e) a biological solubilization tank to biologically solubilize the sludge after treating the sludge by the alkali-treatment under an anaerobic, an anoxic or a microaerophilic condition; and (f) a means for recycling the solubilized sludge to the biological treatment unit.
8 . The apparatus according to claim 6 , wherein the alkali-treatment tank is a plug flow tank.
9 . The apparatus according to according to claim 7 , wherein the alkali-treatment tank is a plug flow tank.
10 . The apparatus according to claim 6 , wherein the biological solubilization tank is a plug flow tank.
11 . The apparatus according to claim 7 , wherein the biological solubilization tank is a plug flow tank.
12 . A method for treating a sludge comprising the steps of:
(a) biologically treating a wastewater to generate a sludge; and (b) treating the sludge from step (a) by an alkali-treatment, by intermittently adding an alkali to the sludge at a determined interval.
13 . The method according to claim 12 , further comprising a step of biologically solubilizing a sludge after treating the sludge by the alkali-treatment under an anaerobic, an anoxic or a microaerophilic condition.
14 . The method according to claim 12 , wherein a retention time of the sludge in the alkali-treatment step is from 3 hours to 24 hours and a retention time of the sludge in the biological solubilization step is from 1 day to 3 days.
15 . The method according to claim 13 , wherein the alkali-treatment is carried out at a temperature of 5° C. to 35° C. and at atmospheric pressure; and the solubilizing of the sludge is carried out at a temperature of 5° C. to 35° C. and at atmospheric pressure.
16 . The method according to claim 14 , wherein the alkali-treatment is carried out at a temperature of 5° C. to 35° C. and at atmospheric pressure; and the solubilizing of the sludge is carried out at a temperature of 5° C. to 35° C. and at atmospheric pressure.
17 . An apparatus for treating a sludge comprising:
(a) an alkali-treatment tank for intermittently adding an alkali at a determined interval to a sludge generated by biologically treating a wastewater, and for treating the sludge by the alkali for a retention time of 3 hours to 24 hours; (b) a biological solubilization tank for biologically solubilizing the treated sludge by the alkali-treatment, at a temperature of 5° C. to 35° C. and at atmospheric pressure in an anaerobic, an anoxic or a microaerophilic condition, for a retention time of from 1 day to 3 days, wherein the biological solubilization tank is located at a downstream side of the alkali-treatment tank and is connected to the alkali-treatment tank via a passage; and (c) a means for transporting at least a part of the alkali-treated sludge into the biological solubilization tank.
18 . A method for treating a wastewater comprising:
(a) biologically treating a wastewater in a biological treatment system; (b) separating a solid from a liquid after treating the wastewater biologically, to obtain a treated wastewater and a sludge, and to obtain a withdrawn sludge from a part of the sludge; (c) treating the withdrawn sludge from step (b) in an alkali-treatment, by intermittently adding an alkali at a determined interval, wherein a retention time of the sludge after adding the alkali is from 3 hours to 24 hours; (d) biologically solubilizing the alkali-treated sludge from step (c) at a temperature of 5° C. to 35° C. and at atmospheric pressure in an anaerobic, an anoxic or a microaerophilic atmosphere, wherein a retention time after adding the alkali is from 1 day to 3 days; and (e) recycling the solubilized sludge from step (b) to the biological treatment system of step (a).
19 . An apparatus for treating a wastewater comprising:
(a) a means for biologically treating a wastewater in a biological treatment system; (b) a means for separating a solid from a liquid in the biologically treated wastewater from step (a), to obtain a treated wastewater and a sludge; (c) a means for obtaining a withdrawn sludge from a part of the sludge from step (b); (d) a means for treating the withdrawn sludge from step (c) by intermittently adding an alkali at a determined interval, and for treating the withdrawn sludge by the alkali for a retention time after adding the alkali of 3 hours to 24 hours; (e) a means for biologically solubilizing the withdrawn sludge after the alkali-treatment from step (d), wherein the biological solubilization is carried out at a temperature of 5° C. to 35° C. and at atmospheric pressure in an anaerobic, an anoxic or a microaerophilic atmosphere, wherein a retention time after adding the alkali is from 1 day to 3 days; and, (f) a means for recycling the solubilized sludge to the biological treatment system of step (a).
20 . A method for treating a wastewater comprising the steps of:
(a) biologically treating a wastewater in a biological treatment vessel to provide a biologically treated wastewater; (b) separating a solid from a liquid in the biologically treated wastewater from step (a) to obtain a treated wastewater and a sludge; (c) treating a part of the sludge from step (b) by an alkali-treatment, within a pH range of from 9 to 12.5; (d) biologically solubilizing the sludge from step (c) in an anaerobic, an anoxic or a microaerophilic condition; and (e) returning the solubilized sludge from step (d) to the biological treatment vessel of step (a).
21 . The method according to claim 20 further comprising a step of thickening the sludge before treating the sludge by the alkali-treatment.
22 . An apparatus for treating a wastewater comprising:
(a) a biological treatment tank to treat a wastewater biologically; (b) a solid-liquid separation unit to separate the wastewater discharged from the biological treatment tank to obtain a treated wastewater and a sludge; (c) an alkali-treatment tank to treat a part of the sludge by the alkali within a pH range of from 9 to 12.5; (d) a biological solubilization tank, said biological solubilization tank being connected to the alkali-treatment tank, said biological solubilization tank being capable of biologically solubilizing the sludge discharged from the alkali-treatment tank under an anaerobic, anoxic or microaerophilic condition; and (e) a means for recycling the sludge discharged from the biological solubilization tank to the biological treatment tank.Cited by (0)
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