JPH11188383A - Method for treating organic waste water - Google Patents

Abstract

PROBLEM TO BE SOLVED: To establish a method which can solve a conventional defect on wt. reduction of sludge in the treatment by a biological dephosphorization active sludge method and can remarkably decrease the amt. of generation of excess sludge and can perform stable and high removal of phosphorus. SOLUTION: In this method for treatment, org. waste water is clarified in an active sludge treating process 2 by a biological dephosphorization active sludge method and a part of the sludge in this active sludge treating process 2 is extracted and is made to flow into a sludge anaerobic storing tank 10 and after phosphate ion is sent out from the sludge, solid-liq. separation is performed and after this separated sludge 13 is oxidized with ozone, it is returned to the active sludge treating process 2 and metal ion for generating phosphate ion precipitation forming reaction is added into the separated liq. to remove phosphorus. As a kind of the metal ions for generating phosphate ion precipitation forming reaction, calcium is used.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

The present invention relates to a novel method for treating organic sewage, which is capable of purifying phosphorus-containing organic sewage such as sewage while obtaining a high phosphorus removal rate and significantly reducing the amount of excess biological sludge generated. About technology.

[0002]

2. Description of the Related Art As a technique for reducing the amount of excess sludge generated from an aerobic biological treatment facility for organic wastewater such as sewage,
A sludge reduction method using ozone is known. This technology is
In this method, a part of the sludge is extracted from the activated sludge treatment step of the organic wastewater, ozone oxidized, and then supplied to the aeration tank in the activated sludge treatment step. However, the conventional sludge reduction technology has the following essential disadvantages. Since phosphorus is not removed except in the form of being taken into biological sludge, unless the sludge that has taken up phosphorus is actively discharged out of the system as surplus sludge, the material balance of phosphorus will not be established, and therefore a sludge reduction process is incorporated. If the amount of surplus sludge is reduced to zero, the phosphorus removal rate will inevitably become zero. In other words, the conventional sludge reduction technology using ozone
It was essentially incompatible with the goal of high phosphorus removal.

[0003]

SUMMARY OF THE INVENTION The present invention solves the drawbacks of the conventional sludge reduction technology, establishes a new technology capable of remarkably reducing the amount of surplus sludge generated, and enabling stable and high-level phosphorus removal. Make it an issue.

[0004]

The present inventor has found that the above object can be achieved by combining a method of sludge oxidation with ozone and a method of removing biological phosphorus in a novel manner. That is, the present invention has solved the above-mentioned problems by the following means. (1) The organic wastewater is purified in an activated sludge treatment step by a biological dephosphorization activated sludge method, and a part of the sludge in the activated sludge treatment step is withdrawn, and the sludge is made to flow into a sludge anaerobic retention tank, thereby causing phosphate ions to be sludged. And then solid-liquid separation, ozone oxidation of the separated sludge, return to the activated sludge treatment step, and addition of metal ions that cause a phosphate ion precipitation formation reaction to the separated liquid to remove phosphorus. A method for treating organic wastewater, comprising the steps of: (2) The above (1), wherein calcium is used as a metal ion for causing the phosphate ion precipitation forming reaction.
The method for treating organic sewage according to the above.

[0005]

DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described with reference to the drawings. FIG. 1 shows a specific configuration example of the present invention. In FIG. 1, raw water 1 containing phosphorus is introduced into an anaerobic tank 3 in a biologically dephosphorized activated sludge treatment step 2, and at the same time, returned sludge 8 from a sedimentation tank 5 and ozone oxidized sludge flowing out from an ozone oxidation tank 18. 19 in the anaerobic tank 3 of the same process 2 and the aerobic tank 4 connected to the anaerobic tank 4
OD removal and phosphorus absorption to dephosphorus bacteria are performed. A part of the sludge in the same step is sent to the sedimentation tank 5, and the supernatant water in the sedimentation tank 5 is taken out as the treated water 6, and the settled sludge 7
Is recycled to the anaerobic tank 3 as returned sludge 8.

[0006] A part of the settled sludge 7 is branched, and flows into a sludge anaerobic stagnation tank 10 as a branched sludge 9 where it is retained under anaerobic conditions to discharge phosphorus from the phosphorus-containing sludge. The sludge in the sludge anaerobic storage tank is
Separation sludge 13 obtained by solid-liquid separation after solid-liquid separation by a solid-liquid separation means using an F membrane or the like, for example, a membrane separation tank 11
Is led to the ozone oxidation tank 18 and oxidized and decomposed by ozone to elute soluble organic substances. After returning the ozone oxidized sludge 19 generated in the ozone oxidizing tank 18 to the anaerobic tank 3 in the biologically dephosphorized activated sludge treatment step 2, it is allowed to flow into the aerobic tank 4,
Ozone-oxidized sludge (biodegradability by microorganisms) 19 is decomposed by microorganisms into carbon dioxide and water.

[0007] The activated sludge multiplied by the BOD removal of the raw water as described above circulates through the sludge anaerobic retention tank 10, the ozone oxidation tank 18, and the biologically dephosphorized activated sludge treatment step 2 so that carbon dioxide gas and water are removed. The excess sludge to be discharged outside the system becomes almost zero. As a result of such circulation, the activated sludge is oxidized and decomposed by ozone. As a result, the ozone-oxidized sludge 19 contains abundant soluble organic matter (BOD). Can actively spit out phosphorus. When the sludge is anaerobically stored in the anaerobic sludge holding tank 10 in advance in the ozone oxidation of the sludge in the ozone oxidation tank 18, the solubilization rate of the sludge is improved.

On the other hand, in a phosphorus chemical removal step 15, calcium, magnesium, aluminum, iron or the like is added to a solid-liquid separation water 12 from a membrane separation tank 11 which is a solid-liquid separation means after the sludge anaerobic retention tank 9. By adding metal ions that cause a precipitation reaction chemically with phosphorus, phosphorus is added to a calcium phosphate compound such as hydroxyapatite, magnesium ammonium phosphate (abbreviated as MAP), aluminum phosphate,
Alternatively, the precipitate is precipitated and separated as iron phosphate 17 and collected. In the case of FIG. 1, calcium hydroxide 14 is used as a metal ion,
Hydroxyapatite 17 is obtained. Among them, calcium ions are most preferable because phosphorus can be recovered in the form of apatite as a calcium phosphate fertilizer. As for magnesium ions, both ammonia and phosphorus can be recovered as MAP. MAP is a well-known valuable resource as a slow-acting fertilizer.

Since the separated water 16 in the phosphorus chemical removal step 15 contains BOD and ammonia, it is preferable to flow this into the activated sludge treatment step 3 for purification. According to the above method, in the sludge anaerobic retention tank 9, from the inside of the activated sludge cells such as dephosphorus bacteria that took in phosphorus in the raw water in the activated sludge treatment step 3, the sludge is converted into a liquid outside the system. Since phosphorus is eliminated, phosphorus is not accumulated too much in the biologically dephosphorized activated sludge treatment step, and the phenomenon of deteriorating phosphorus removal in the step does not occur, and phosphorus is continuously removed stably. As another embodiment, it is also possible to provide a denitrification tank and a nitrification tank in the aerobic tank 4 in the activated sludge treatment step 2 to simultaneously carry out biological dephosphorization and biological denitrification. In this way,
The present invention breaks down the stereotype that "it is impossible to achieve a high level of phosphorus removal in sludge reduction technology in terms of phosphorus material balance".

[0010]

The present invention will be specifically described below with reference to examples. However, the present invention is not limited to only this embodiment. Example A proof test of the present invention was performed according to the process shown in FIG. The average sewage quality used is shown in Table 1. Table 2 shows the test conditions for each processing step.

[0011]

[Table 1]

[0012]

[Table 2]

As a result of the experiment, the average of the quality of the treated water in the biologically dephosphorized activated sludge treatment step after the treatment condition became stable two months after the start of the treatment was as shown in Table 3, BOD had been removed. Although the excess sludge was not pulled out during the one-year test, it was found that the generation of the excess sludge was negligibly small since the MLSS of the aerobic tank was maintained at 3600 to 4000 mg / liter.

[0014]

[Table 3]

[0015]

Advantages of the Invention As a result of combining the sludge solubilization method using ozone, the biological dephosphorization method, and the chemical phosphorus removal method with a new concept, the amount of excess sludge generated can be reduced to almost zero, and the phosphorus removal can be performed stably. 2. The phosphorus ingested by the dephosphorus bacteria can be recovered as a valuable resource for fertilizers such as MAP and hydroxyapatite. 3. Since the BOD generated by the ozone of the sludge is used for discharging phosphorus in the anaerobic tank for the dephosphorus bacteria, stable phosphorus discharging action is performed.

[Brief description of the drawings]

FIG. 1 is a schematic view showing an embodiment of the present invention for treating organic wastewater.

[Explanation of symbols]

 DESCRIPTION OF SYMBOLS 1 Raw water 2 Biological dephosphorization activated sludge process 3 Anaerobic tank 4 Aerobic tank 5 Sedimentation tank 6 Treated water 7 Settled sludge 8 Returned sludge 9 Branched sludge 10 Sludge anaerobic retention tank 11 Membrane separation tank 12 Solid-liquid separation water 13 Separated sludge 14 Calcium hydroxide 15 Phosphorus chemical removal process 16 Separated water 17 Hydroxyapatite 18 Ozone treatment tank 19 Ozone oxidized sludge

Claims (2)

[Claims] 1. An organic wastewater is purified in an activated sludge treatment step by a biological dephosphorization activated sludge method, a part of the sludge is removed in the activated sludge treatment step, and the sludge is made to flow into a sludge anaerobic retention tank to form phosphate ions. Is discharged from the sludge, solid-liquid separated, the separated sludge is oxidized with ozone, and then returned to the activated sludge treatment step, and a metal ion causing a phosphate ion precipitation generation reaction is added to the separated liquid to remove phosphorus. A method for treating organic wastewater. 2. The method for treating organic sewage according to claim 1, wherein calcium is used as the metal ion causing the phosphate ion precipitation reaction.