JP5873744B2 - Organic wastewater and organic waste treatment method and treatment equipment - Google Patents

Description

  The present invention relates to a method for treating organic wastewater such as sewage and organic waste such as food waste and livestock waste, particularly when sewage sludge, food waste, livestock waste and the like are subjected to methane fermentation treatment. The present invention relates to a method for treating organic wastewater and organic waste, which is characterized by a method of using biogas.

  Methane fermentation treatment is a biological treatment method that decomposes organic matter into biogas such as methane gas or carbon dioxide gas by utilizing the metabolic reaction of anaerobic microorganisms that grow in anaerobic environment without oxygen.

  Compared with aerobic biological treatment, methane fermentation treatment has the advantage that it generates less sludge and does not require an electricity bill such as a blower (aeration), so there is no running cost, and the generated biogas is used as a fuel source. There are merits such as effective use. Therefore, in recent years, it has spread in fields such as sewage treatment, human waste treatment, and industrial wastewater treatment.

In addition, organic wastewater treatment methods that combine such methane fermentation treatment and aerobic biological treatment such as activated sludge method have been proposed.
For example, in Patent Document 1, wastewater discharged from a factory or the like is reused as fuel by decomposing organic matter in wastewater into methane gas in an anaerobic treatment process using anaerobic microorganisms. A method is disclosed in which inorganic substances such as phosphorus and nitrogen are removed in an aerobic biological treatment process using microorganisms, and chemical substances that adversely affect the environment are removed and then released.

  Patent Document 2 discloses an organic wastewater treatment method in which treated water is subjected to methane fermentation treatment, and the digested liquid after treatment is subjected to an aerobic biological treatment by an activated sludge method, wherein the organic matter concentration of the treated water is a set concentration. If it is above, the methane fermentation process is performed, and when the said setting density | concentration is not reached, the aerobic biological process with the said digestive liquid is disclosed, The organic waste water treatment method characterized by the above-mentioned is disclosed.

  In Patent Document 3, in the wastewater treatment method in which an acid generation process, a methane fermentation process, and an aerobic biological treatment process are sequentially performed on wastewater, the wastewater supplied to the acid generation process is terminated with the methane fermentation process. And the wastewater processing method characterized by preheating by carrying out heat exchange with the treated water sent to the said aerobic biological treatment process is disclosed.

JP 2003-71486 A Japanese Patent Laid-Open No. 2004-25051 JP 2008-173614 A

Compared with aerobic biological treatment, methane fermentation treatment has advantages such as not requiring aeration and lower operating power costs, as well as the ability to use the generated biogas as fuel for various power generation facilities. is there.
However, even if sewage sludge obtained by solid-liquid separation of sewage or sewage sludge obtained after biological nitrogen treatment of solid-liquid separation water obtained by solid-liquid separation is treated with methane fermentation Because the energy gained from the biogas generated takes a long time to recover the capital investment due to the introduction merit (difference from the running ghost), it is not profitable, so how to deal with the biogas generated instead? Sometimes it became a problem.

On the other hand, organic wastewater such as sewage contains nitrogen components in the form of NH ₄ -N (ammonia nitrogen) and cannot be discharged into the environment as it is. Has been done. Specifically, such organic wastewater is subjected to biological nitrogen treatment using activated sludge having nitrifying bacteria and denitrifying bacteria. However, when the soluble BOD / NH ₄ -N ratio (soluble BOD is the BOD value of the filtrate filtered through 1.0 μm filter paper) is in the range of 1.0 to 2.5, denitrification When organic wastewater such as sewage, which is not so high compared to the required 3.0, is treated with biological nitrogen, the denitrification reaction is not sufficient because the concentration of organic substances that are also a hydrogen source for the denitrification reaction is not high. There was a case where it did not advance.

  Accordingly, the present invention provides a new organic wastewater and organic waste treatment method that can utilize biogas generated during methane fermentation treatment as a hydrogen source for the denitrification reaction of biological nitrogen treatment. Is intended to provide.

For example, as shown in FIG. 1, the present invention uses a solid-liquid separation sludge obtained by solid-liquid separation of organic wastewater, or a solid-liquid separation water obtained by solid-liquid separation of organic wastewater. Wastewater and organic waste provided with a process of methane fermentation of surplus sludge obtained by chemical nitrogen treatment, organic waste, or a mixture of two or more of these In this treatment method, after desulfurizing the biogas obtained by the methane fermentation treatment, the biogas is brought into gas-liquid contact with an aqueous medium in a gas-liquid contact tank, and the methane gas in the biogas is dissolved in the aqueous medium. The dissolved aqueous medium is supplied to a denitrification step in a step of biological nitrogen treatment of solid-liquid separated water obtained by solid-liquid separation of organic wastewater as a hydrogen donor source. A treatment method for organic wastewater and organic waste

As shown in FIG. 2, the present invention also includes a method for treating organic wastewater, which comprises a step of subjecting organic wastewater as water to be treated to solid-liquid separation, and subjecting the obtained solid-liquid separated water to biological nitrogen treatment. , Solid-liquid separation sludge obtained by solid-liquid separation of organic waste water, or surplus sludge obtained by biological nitrogen treatment of solid-liquid separation water obtained by solid-liquid separation of organic waste water Or, biological waste obtained by desulfurizing biogas obtained by methane fermentation treatment of organic waste or a mixture of two or more of these, and then biological biological treatment. specifically nitrogen treated water and contacted liquid in the gas-liquid contact vessel to dissolve the methane of the bio-gas in said biological nitrogen treated water, a biological nitrogen treated water the methane dissolved, as a hydrogen donor source Supplying to the denitrification step within the biological nitrogen treatment step. Characterized proposes a method of processing organic waste water.

According to the method proposed by the present invention, biogas generated during methane fermentation treatment is brought into gas-liquid contact with an aqueous medium (for example, biological nitrogen-treated water obtained by biological nitrogen treatment), and biogas is produced. By dissolving methane gas in the gas in the aqueous medium and supplying it to the denitrification step in the biological nitrogen treatment step, it is used as a hydrogen source in the denitrification reaction of biological nitrogen treatment. be able to. Therefore, the denitrification reaction can be sufficiently promoted even in the case where the solid-liquid separation water of organic wastewater, such as sewage, whose solubility BOD / NH ₄ -N ratio is not so high is subjected to biological nitrogen treatment. In addition, the biogas generated when the methane fermentation treatment is performed can be used effectively.
Furthermore, by bringing the aqueous medium and biogas into gas-liquid contact, a larger amount of carbon dioxide can be dissolved in addition to methane gas, so the concentration of methane gas in the biogas can be increased, contributing to effective use of biogas. .

It is process drawing which showed an example of the processing method of the organic waste_water | drain and organic waste which this invention proposes. In addition, the dotted line in a figure means that it may be such a case. It is process drawing which showed an example of the processing method of the organic waste_water | drain proposed by this invention. It is the figure which showed the example of the structure of the biological nitrogen treatment apparatus, and an example of the supply method of the gas-liquid contact treatment water in that case. It is the figure which showed the example of a structure of the biological nitrogen treatment apparatus different from FIG. 3, and an example of the supply method of the gas-liquid contact treatment water in that case. It is the figure which showed the example of a structure of the biological nitrogen treatment apparatus different from FIG. 4, and an example of the supply method of the gas-liquid contact treatment water in that case. (A) (B) is the figure which showed an example of the gas-liquid contact apparatus. It is process drawing which showed the processing method of the organic waste_water | drain performed in the comparative example. It is the graph which showed the relationship between water temperature and the solubility with respect to the water of methane.

  Examples of embodiments of the present invention will be described below with reference to the drawings. The present invention is not limited to the following embodiments.

<This organic wastewater treatment method>
FIG. 2 is a diagram illustrating an example of a process of an organic wastewater treatment method (referred to as “the present organic wastewater treatment method”) according to an example of the present embodiment.
This organic wastewater treatment method includes a “biological nitrogen treatment process” in which solid-liquid separation water 2 obtained by solid-liquid separation of organic wastewater 1 is subjected to biological nitrogen treatment, and organic wastewater 1 is solid-liquid. Solid-liquid separation sludge 3 obtained by separation or surplus sludge 6 obtained by biological nitrogen treatment of solid-liquid separation water 2 obtained by solid-liquid separation of organic waste water 1 or organic Methane waste 18 or a mixture of two or more of these, a “methane fermentation process” in which methane fermentation is performed, and biogas 10 generated in the methane fermentation process is converted into biological nitrogen-treated water A gas-liquid contact process in which the methane dissolved in the gas-liquid contact process is dissolved in the biological nitrogen treatment process. It is the method characterized by supplying to.

(Processing equipment)
The organic wastewater treatment method includes, for example, a methane fermentation treatment tank 55, a pipe 60 for supplying the biogas 10 supplied from the methane fermentation treatment tank 55 to the gas-liquid contact tank 58, and the methane fermentation treatment tank 55. A gas-liquid contact tank 58 for bringing the supplied biogas 10 into gas-liquid contact with the biological nitrogen-treated water 14 and a gas-liquid contact-treated water 15 obtained by dissolving the methane obtained from the gas-liquid contact tank 58 are treated with biological nitrogen. A biological nitrogen treatment apparatus that biologically nitrogen-treats a pipe 61 supplied to the denitrification tank 51a of the apparatus 51 and solid-liquid separation water 2 obtained by solid-liquid separation of the organic waste water 1, which is a nitrification tank (Aerobic tank) It can implement by the processing apparatus provided with the biological nitrogen processing apparatus 51 provided with 51b and the denitrification tank 51a.

(Organic wastewater)
The organic waste water 1 is separated into solid-liquid separated water 2 and solid-liquid separated sludge 3 by solid-liquid separation in the solid-liquid separation device 50, and the solid-liquid separated water 2 is supplied to the biological nitrogen treatment device 51. On the other hand, the solid-liquid separation sludge 3 is supplied to the concentration facility 53 and supplied to the methane fermentation treatment tank 55 as the concentrated sludge 8.

Examples of the organic waste water 1 as the water to be treated include sewage and domestic waste water.
Further, methane fermentation treated water 9 obtained in the methane fermentation treatment process or, as shown in FIG. 2, dehydrated filtrate 13 obtained by dehydrating methane fermentation treated water 9 with a dehydrator 56 may be used as water to be treated. Good. Further, the methane fermentation treated water 9 or the dehydrated filtrate 13 may be added to the organic waste water 1 such as sewage to be treated water.
In the methane fermentation treatment, easily degradable organic substances are converted into methane gas by absolute anaerobic bacteria (obligate anaerobic bacteria), so that the organic substances contained in the methane fermentation treated water 9 are reduced. Therefore, when biological nitrogen treatment is performed as usual using methane fermentation treated water 9 as water to be treated, a hydrogen supply source for denitrification reaction is insufficient in the denitrification tank. Therefore, if the methane fermentation treated water 9 and the dehydrated filtrate 13 are treated water of the present organic wastewater treatment method, the effects of the present invention can be further enjoyed.

(Methane fermentation treatment process)
In the methane fermentation treatment step, solid-liquid separation sludge 3 (including the concentrated sludge 8 concentrated by the concentration facility 53) obtained by solid-liquid separation of the organic waste water 1 is used to methane using the methane fermentation treatment tank 55. Fermentation treatment.
At this time, as an object of methane fermentation treatment, solid-liquid separation sludge 3 obtained by solid-liquid separation of the organic waste water 1 (including the concentrated sludge 8 concentrated by the concentration facility 53), or organic Surplus sludge 6 obtained by biological nitrogen treatment of solid-liquid separated water 2 obtained by solid-liquid separation of waste water 1 (including concentrated sludge 17 obtained by concentrating surplus sludge 6 with a concentration facility 54) Alternatively, any one of the organic wastes 18 can be used as an object to be processed, and a mixture obtained by combining two or more of these can also be used as an object to be processed.
Examples of the organic waste 18 include food waste, food waste, livestock waste, and the like.

  As a method for methane fermentation treatment, for example, a complete mixing methane fermentation treatment method such as gas mixing or mechanical stirring can be appropriately employed. The temperature of the methane fermentation can be applied to any one of an optimum medium temperature methane fermentation at around 35 ° C. and an optimum high temperature methane fermentation at around 55 ° C.

Biogas 10 and methane fermentation treated water 9 are generated by the methane fermentation treatment.
The biogas 10 contains hydrogen sulfide (200 to 2000 ppm) in addition to methane (60 to 80% v / v) and carbon dioxide (20 to 40% v / v). After desulfurization in the desulfurization tower 57, it is preferable to supply the degassed biogas 11 to the gas-liquid contact tank 58. However, the biogas may be supplied to the gas-liquid contact tank 58 without desulfurization and desulfurized after the gas-liquid contact.

On the other hand, the methane fermentation treated water 9 is dehydrated by a dehydrator 56 to obtain a dehydrated cake 12 and a dehydrated filtrate 13, and these dehydrated cakes 12 can be discharged out of the field or can be dried and incinerated in the process field. .
As described above, the dehydrated filtrate 13 is preferably returned before the solid-liquid separator 50 and mixed with the organic waste water 1 such as sewage.

(Gas-liquid contact process)
The biogas 10 generated in the methane fermentation treatment step is desulfurized in a desulfurization tower 57 as necessary to obtain a biogas 11 after desulfurization, and is supplied to the gas-liquid contact tank 58. In the gas-liquid contact tank 58, the degassed biogas 11 is brought into gas-liquid contact with an aqueous medium such as biological nitrogen-treated water 14, and methane gas or the like in the biogas 11 after desulfurization is dissolved in the biological nitrogen-treated water 14. To obtain an aqueous medium containing dissolved methane.

However, the aqueous medium to be brought into gas-liquid contact in the gas-liquid contact step may be water. For example, in addition to the biological nitrogen-treated water 14, solid-liquid separated water 2 obtained by solid-liquid separation of the organic waste water 1 can also be used. However, since the solid-liquid separated water 2 contains a large amount of organic matter, foaming may occur in the gas-liquid contact tank 58, so it is preferable to add an antifoaming agent and supply it to the gas-liquid contact tank 58.
It is also possible to use water as an aqueous medium that draws water from outside the system and makes it gas-liquid contact in the gas-liquid contact step.
Further, a gas-liquid contact tank 58 is provided in the middle of a circulation line 62 of a biological nitrogen treatment apparatus 51A described later, and biogas is brought into contact with the nitrification liquid discharged from the aerobic tank 51b to enter the denitrification tank 51a. It is also possible to supply.

As the gas-liquid contact tank 58, either a tank type as shown in FIG. 6 (A) or a tower type as shown in FIG. 6 (B) can be used. Anyway, since a thing with high gas-liquid contact efficiency is preferable, it is preferable that the liquid level height is 4-10 m. The gas-liquid contact tower is preferably filled with a filler such as a plastic filter medium, a fiber filter medium, and a magnetic filter medium.
The method of supplying the biogas 11 after desulfurization to the gas-liquid contact tank 58 is such that the desulfurization tower 57 and the gas-liquid contact tank 58 are connected by a sealed pipe 60, and in the gas-liquid contact tank 58, a diffusion plate and a diffusion tower are connected. It is preferable to immerse the bubble generating means such as a membrane membrane in water and make the bubble diameter of the biogas 11 after desulfurization supplied into the water as fine as possible.

When the biological nitrogen-treated water 14 and the desulfurized biogas 11 are brought into gas-liquid contact in such a gas-liquid contact tank 58, a part of the methane gas and carbon dioxide gas in the biogas 11 after desulfurization is biological nitrogen. Dissolve in treated water 14 (aqueous medium).
At this time, the amount of methane dissolved after the gas-liquid contact can be adjusted by adjusting the water temperature of the biological nitrogen-treated water 14 (aqueous medium) to be brought into gas-liquid contact. That is, as shown in FIG. 8, the solubility of methane in water increases as the water temperature decreases, the amount of methane dissolution increases as the water temperature decreases, and the amount of methane dissolution decreases as the water temperature increases. The amount of methane dissolved after gas-liquid contact can be adjusted by adjusting the water temperature of the nitrogen-treated water 14 (aqueous medium).
Moreover, when the solubility BOD / NH ₄ -N ratio of the biological nitrogen-treated water 14 (aqueous medium) is high, the water temperature in the gas-liquid contact tank 58 is raised, and the biological nitrogen-treated water 14 (aqueous medium). When the solubility BOD / NH ₄ -N ratio is low, for example, when the BOD / NH ₄ -N ratio is less than 3, the water temperature in the gas-liquid contact tank 58 is lowered to increase the amount of dissolved methane. preferable.
Therefore, the gas-liquid contact tank 58 is preferably provided with a liquid temperature control means, or the liquid temperature control means is preferably provided in the middle of the supply pipe of the biological nitrogen-treated water 14 (aqueous medium).

  The aqueous medium in which methane is dissolved in this way, that is, the gas-liquid contact treated water 15 containing dissolved methane is supplied to the denitrification tank 51a of the biological nitrogen treatment apparatus 51 through the pipe 61, and is recovered after the gas-liquid contact. The gas 16 may be effectively used after being stored in the gas holder 59.

(Biological nitrogen treatment process)
In the biological nitrogen treatment step, the solid-liquid separated water 2 obtained by solid-liquid separation of the organic waste water 1 with the solid-liquid separation device 50 as described above is used for the biology using the biological nitrogen treatment device 51. Treat with nitrogen.
Biological nitrogen treatment means that NH ₄ —N in water is converted to NO ₂ —N and NO ₃ —N by the action of nitrifying and denitrifying bacteria, and then NO ₂ —N, In this process, NO ₃ —N is converted into nitrogen (gas) and diffused into the atmosphere.

  In the biological nitrogen treatment process, it is preferable to treat organic wastewater using activated sludge having nitrifying bacteria, denitrifying bacteria and other bacteria.

The biological nitrogen treatment apparatus 51 includes a nitrification tank (aerobic tank) 51b and a denitrification tank 51a. In the nitrification tank (aerobic tank) 51b, NH ₄ − N is converted into NO ₂ -N and NO ₃ -N, and in the denitrification tank 51a, NO ₂ -N and NO ₃ -N are converted into nitrogen (gas) by the action of denitrifying bacteria. In addition to biological nitrogen treatment, biological reactions by microorganisms that oxidatively degrade BOD are simultaneously progressing. To advance the nitrification reaction, the SRT (sludge retention time) is lengthened to ensure the amount of nitrifying bacteria. There is a need.

One feature of the present organic wastewater treatment method is that gas-liquid contact treated water 15 containing dissolved methane is supplied to the denitrification tank 51a as a hydrogen supply source to promote the denitrification reaction in the denitrification tank 51a. .
In particular, when the water to be treated in the biological nitrogen treatment step, that is, the solubility BOD / NH ₄ -N ratio of the solid-liquid separation water 2 is 3.0 or less, the hydrogen donor is insufficient in the denitrification reaction of the denitrification tank 51a. Since the possibility is high, it is effective to supply the gas-liquid contact treated water 15 containing dissolved methane to the denitrification tank 51a. Furthermore, when the soluble BOD / NH ₄ -N ratio of the solid-liquid separated water 2 is much lower, for example, when the soluble BOD / NH ₄ ratio is less than 3, the supply amount of the gas-liquid contact treated water 15 is increased. Is preferred.

Depending on the configuration of the biological nitrogen treatment apparatus 51, it is preferable to supply the gas-liquid contact treated water 15 to the denitrification tank 51a.
For example, the biological nitrogen treatment apparatus 51A configured as shown in FIG. 3 is disposed in the order of the denitrification tank 51a → the aerobic tank 51b from the inflow side of the solid-liquid separation water 2, and the treatment liquid discharged from the aerobic tank 51b. In other words, a part of the nitrification liquid is circulated to the denitrification tank 51 a by the circulation line 62.
In the biological nitrogen treatment apparatus 51 having such a configuration, the gas-liquid contact treated water 15 may be supplied to the denitrification tank 51a.

The nitrification liquid discharged from the aerobic tank 51b is circulated to the denitrification tank 51a, and the gas-liquid contact treated water 15 containing dissolved methane is supplied to the denitrification tank 51a. A denitrification reaction for converting nitrous acid and nitric acid in nitrification liquid into molecular nitrogen (nitrogen gas) can be promoted by using a hydrogen source of dissolved methane.
A part of the mixed treatment liquid 4 containing activated sludge discharged from the biological nitrogen treatment apparatus 51A is returned to the denitrification tank 51a.

The biological nitrogen treatment apparatus 51B having the configuration shown in FIG. 4 is configured from the inflow side of the solid-liquid separation water 2 in the order of the denitrification tank 51a → the aerobic tank 51b → the denitrification tank 51a → the aerobic tank 51b. It has.
In the biological nitrogen treatment apparatus 51B having such a configuration, it is preferable to supply gas-liquid contact treated water 15 to each denitrification tank 51a as shown in FIG.
At this time, the number of tanks of the denitrification tank 51a and the aerobic tank 51b is preferably adjusted as appropriate according to the TN (total nitrogen) level of the treated water.

In the biological nitrogen treatment apparatus 51B having such a configuration, the nitrification liquid is sent from the aerobic tank 51b to the denitrification tank 51a, and the denitrification tank 51a uses a hydrogen supply source of dissolved methane in the gas-liquid contact treated water 15. Thus, the denitrification reaction for converting nitrous acid and nitric acid in the nitrification solution into molecular nitrogen (nitrogen gas) can be promoted.
Even in this configuration, a part of the processing liquid discharged from the aerobic tank 51b, that is, a part of the nitrification liquid may be circulated to the denitrification tank 51a.

The biological nitrogen treatment apparatus 51C having the configuration shown in FIG. 5 is arranged in the order of the aerobic tank 51b → the denitrification tank 51a → the aerobic tank 51b → the denitrification tank 51a from the inflow side of the solid-liquid separation water 2. It has.
In the biological nitrogen treatment apparatus 51C having such a configuration, it is preferable to supply gas-liquid contact treated water 15 to each denitrification tank 51a as shown in FIG.
At this time, the number of tanks of the denitrification tank 51a and the aerobic tank 51b is preferably adjusted as appropriate according to the TN (total nitrogen) level of the treated water.

Also in the biological nitrogen treatment apparatus 51C having such a configuration, the nitrification liquid is sent from the aerobic tank 51b to the denitrification tank 51a, and the denitrification tank 51a uses a hydrogen supply source of dissolved methane in the gas-liquid contact treated water 15. The denitrification reaction of converting nitrous acid and nitric acid in the nitrification solution into molecular nitrogen (nitrogen gas) can be promoted.
In the biological nitrogen treatment apparatus 51C, a part of the treatment liquid discharged from the aerobic tank 51b, that is, the nitrification liquid may be circulated to the denitrification tank 51a.

The mixed treatment liquid 4 containing activated sludge discharged from the biological nitrogen treatment device 51 is separated into excess sludge 6 and biological nitrogen treated water 14 by a solid-liquid separation device 52.
Examples of the solid-liquid separation device 52 include a solid-liquid separation device such as a sedimentation basin, a centrifugal separator, and a membrane separation.
A part of the separated surplus sludge 6 is returned to the biological nitrogen treatment device 51 as return sludge 7, and the remaining surplus sludge 6 is concentrated by the concentrating facility 54 to obtain the concentrated sludge 17, and as a dehydrated cake after dehydration. It may be discharged out of the system, or may be subjected to methane fermentation treatment with the concentrated sludge 8 as shown in FIG.
On the other hand, a part of the biological nitrogen-treated water 14 is supplied to the gas-liquid contact tank 58 as described above, and the remaining biological nitrogen-treated water 14 is used as the treated water 5 of the present organic wastewater treatment method. What is necessary is just to discharge outside.

  Examples of the present invention and comparative examples will be described below. However, the present invention is not limited to the following examples.

(Example 1-4 and Comparative Example 1-4)
Example 1 was processed using the biological nitrogen treatment apparatus 51A shown in FIG. 3 in the flow shown in FIG. 2, and TN (mg / L) of the treated water 5 was measured. N (total nitrogen) removal rate was calculated.
Example 2 was processed using the biological nitrogen treatment apparatus 51C shown in FIG. 5 in the flow shown in FIG. 2, and the TN (mg / L) of the treated water 5 was measured. N (total nitrogen) removal rate was calculated.

Example 3 was processed using the biological nitrogen treatment apparatus 51A shown in FIG. 3 in the flow shown in FIG. 2, and the TN (mg / L) of the treated water 5 was measured. N (total nitrogen) removal rate was calculated.
Example 4 was processed using the biological nitrogen treatment apparatus 51C shown in FIG. 5 in the flow shown in FIG. 2, and the TN (mg / L) of the treated water 5 was measured. N (total nitrogen) removal rate was calculated.
In any of the examples, the water temperature in the gas-liquid contact tank 58 was 20 ° C.

Comparative Example 1 was treated in the same manner as in Example 1 except that the treatment was performed according to the flow shown in FIG. 7, that is, the flow in which the gas-liquid contact treated water 15 was not supplied to the biological nitrogen treatment apparatus 51.
Comparative Example 2 was processed in the same manner as Example 2 except that it was processed according to the flow shown in FIG.
Comparative Example 3 was processed in the same manner as Example 3 except that it was processed according to the flow shown in FIG.
Comparative Example 4 was processed in the same manner as Example 4 except that it was processed according to the flow shown in FIG.

  In Examples 1 and 2 and Comparative Examples 1 and 2, solid-liquid separated water 2 obtained by solid-liquid separation of a mixed liquid of organic waste water (sewage) 1 and dehydrated filtrate 13 of methane fermentation treated water 9 is obtained. Table 1 shows the properties of this solid-liquid separated water 2 as water to be treated. Moreover, in these Examples and Comparative Examples, concentrated sludge 8 obtained by concentrating solid-liquid separation sludge 3 obtained by solid-liquid separation of organic wastewater (sewage) 1 and organic wastewater (sewage). The mixture with the concentrated sludge 17 obtained by concentrating the excess sludge 6 obtained by subjecting the solid-liquid separated water 2 obtained by solid-liquid separation 1 to biological nitrogen treatment to the treated material of the methane fermentation treatment did.

  On the other hand, in Examples 3 and 4 and Comparative Examples 3 and 4, solid-liquid separation water 2 obtained by solid-liquid separation of organic waste water (sewage) 1 is treated water, and the properties of this solid-liquid separation water 2 are It is shown in Table 1. Moreover, in these Examples and Comparative Examples, concentrated sludge 8 obtained by concentrating solid-liquid separation sludge 3 obtained by solid-liquid separation of organic wastewater (sewage) 1 and organic wastewater (sewage). A concentrated sludge 17 obtained by concentrating excess sludge 6 obtained by subjecting solid-liquid separated water 2 obtained by solid-liquid separation 1 to biological nitrogen treatment, and garbage as organic waste 18; This mixture was used as an object to be treated for methane fermentation.

In Examples 1 and 3 (Comparative Examples 1 and 3), treatment was performed using the biological nitrogen treatment apparatus 51A shown in FIG. This biological nitrogen treatment apparatus 51A had an effective capacity of 25 L (denitrification tank capacity of 10 L, aerobic tank capacity of 15 L) and a solid-liquid separator (precipitation tank) of 10 L.
The inflow raw water amount was 50 L / d, the circulation amount from the aerobic tank 51b to the denitrification tank 51a was 75 L / d, and the MLSS concentration in the aerobic tank 51b and the denitrification tank 51a was operated to be in the range of 2000 to 4000 mg / L. . The water temperature was 15 to 20 ° C.
In Examples 1 and 3, the gas-liquid contact treated water 15 was supplied to the denitrification tank 51a in the range of 10 to 20 L / d.

In Examples 2 and 4 (Comparative Examples 2 and 4), treatment was performed using the biological nitrogen treatment apparatus 51C shown in FIG. This biological nitrogen treatment apparatus 51C had an effective capacity of 25 L (aerobic tank capacity 5 L × 3 tanks, denitrification tank capacity 5 L × 2 tanks) and a solid-liquid separator (precipitation tank) 10 L.
The inflow raw water amount was supplied to the first tank aerobic tank 51b, 20 L / d to the second tank denitrification tank 51a, and 15 L / d to the fourth tank denitrification tank 51a. Moreover, it operated so that the MLSS density | concentration of the denitrification tank 51a might become the range of 2000-4000 mg / L. The water temperature was 15 to 20 ° C.
In Examples 2 and 4, the gas-liquid contact treated water 15 was supplied to the second denitrification tank 51a and the fourth denitrification tank 51a in the range of 5 to 10 L / d.

Results of Examples 1 and 2 (Comparative Examples 1 and 2) in which solid-liquid separated water 2 obtained by solid-liquid separation of a mixed liquid of organic waste water (sewage) 1 and dehydrated filtrate 13 was treated water As a result, the TN removal rate was 60% in Comparative Example 1 treated using the biological nitrogen treatment apparatus 51A shown in FIG. 3, whereas the TN removal rate in Example 1 was 60%. 65%.
On the other hand, in Comparative Example 2 processed using the biological nitrogen treatment apparatus 51C shown in FIG. 5, the TN removal rate was 70%, whereas in Example 2, the TN removal rate was 75. %Met.
In any case, it was found that by supplying the gas-liquid contact treated water 15 containing dissolved methane gas to the biological nitrogen treatment apparatus 51, the TN removal rate is increased by 5%.

Regarding the results of Examples 3 and 4 (Comparative Examples 3 and 4) in which the mixture of the concentrated sludge 8, the concentrated sludge 17 and the raw garbage was treated with the methane fermentation treated water 9, the biological results shown in FIG. In Comparative Example 3 processed using the nitrogen treatment apparatus 51A, the TN removal rate was 50%, whereas in Example 3, the TN removal rate was 68%.
On the other hand, in the comparative example 4 processed using the biological nitrogen processing apparatus 51C shown in FIG. 5, the TN removal rate was 55%, whereas in the example 4, the TN removal rate was 70. %Met.
In any case, it was found that by supplying gas-liquid contact treated water 15 containing dissolved methane gas to the biological nitrogen treatment apparatus 51, the TN removal rate is increased by 15 to 18%.

The solubility BOD / NH ₄ -N ratio of sewage solid-liquid separated water including return water such as dehydrated filtrate of methane fermentation treatment for sewage sludge and garbage is 2.0, and methane for sewage sludge Hydrogen for denitrification because the solubility BOD / NH ₄ -N ratio of the sewage solid-liquid separated water containing the return water such as the dehydrated filtrate of the fermentation treatment is lower than that of 2.3 and there are few hydrogen sources for denitrification. Since there were few donor sources, it is thought that the TN removal rate of an Example and a comparative example differed.

  From the above results, it was found that the nitrogen treatment results can be improved by supplying the gas-liquid contact treated water 15 containing dissolved methane gas to the denitrification tank of the biological nitrogen treatment apparatus 51.

DESCRIPTION OF SYMBOLS 1 Organic waste water 2 Solid-liquid separation water 3 Solid-liquid separation sludge 4 Mixed treatment liquid 5 Treatment water 6 Excess sludge 7 Return sludge 8 Concentrated sludge 9 Methane fermentation treated water 10 Biogas 11 Desulfurized biogas 12 Dehydrated cake 13 Dehydrated filtrate 14 Biological nitrogen-treated water (water supplied to gas-liquid contact tank)
15 Gas-liquid contact treated water 16 Gas (after gas-liquid contact)
17 Concentrated sludge 18 Organic waste 51 Biological nitrogen treatment equipment 51A Biological nitrogen treatment equipment 51B Biological nitrogen treatment equipment 51C Biological nitrogen treatment equipment 51a Denitrification tank 51b Nitrification tank (aerobic tank)
50 Solid-liquid separation device 53 Concentration facility 54 Concentration facility 55 Methane fermentation treatment tank 56 Dehydrator 57 Desulfurization tower 58 Gas-liquid contact tank 59 Gas holder 60 Pipe 61 Pipe 62 Circulation line

Claims (4)

Solid-liquid separation sludge obtained by solid-liquid separation of organic waste water, or excess sludge obtained by biological nitrogen treatment of solid-liquid separation water obtained by solid-liquid separation of organic waste water, or In the method of treating organic wastewater or organic waste, comprising a step of subjecting organic waste or a mixture of two or more of these to methane fermentation treatment,
After desulfurization of the biogas obtained by the methane fermentation treatment, gas-liquid contact is made with an aqueous medium in a gas-liquid contact tank, methane gas in the biogas is dissolved in the aqueous medium, and the aqueous medium in which the methane is dissolved is dissolved. , Characterized by supplying solid-liquid separated water obtained by solid-liquid separation of organic wastewater as a hydrogen donor source to a denitrification step in the process of biological nitrogen treatment. Waste disposal method. In a method for treating organic wastewater comprising a step of subjecting organic wastewater as treated water to solid-liquid separation and biological nitrogen treatment of the obtained solid-liquid separated water,
Solid-liquid separation sludge obtained by solid-liquid separation of organic waste water, or excess sludge obtained by biological nitrogen treatment of solid-liquid separation water obtained by solid-liquid separation of organic waste water, or , Organic waste, or biological nitrogen obtained by the biological nitrogen treatment after desulfurization of biogas obtained by methane fermentation treatment of a mixture of two or more of these Gas-liquid contact is performed with treated water in a gas-liquid contact tank, methane gas in the biogas is dissolved in the biological nitrogen-treated water, and the biological nitrogen-treated water in which the methane is dissolved is used as a hydrogen donor source. A method for treating organic wastewater, which is supplied to a denitrification step in a biological nitrogen treatment step.   Methane fermentation treated water obtained by methane fermentation treatment or its dehydrated filtrate is treated water in a biological nitrogen treatment process, or the methane fermentation treated water or its dehydrated filtrate is treated with organic waste water. The method for treating organic waste water according to claim 2, wherein the treated water is used in addition to the water to be treated.   Solid-liquid separation sludge obtained by solid-liquid separation of organic waste water, or excess sludge obtained by biological nitrogen treatment of solid-liquid separation water obtained by solid-liquid separation of organic waste water, or Organic waste, or a mixture of two or more of these, a methane fermentation treatment tank that performs a methane fermentation treatment, and a biogas supplied from the methane fermentation treatment tank is supplied to the gas-liquid contact tank And a gas-liquid contact tank for degassing the biogas supplied from the methane fermentation treatment tank and bringing it into gas-liquid contact with an aqueous medium to dissolve methane in the aqueous medium to obtain a methane-soluble aqueous medium; Biological nitrogen treatment of solid-liquid separated water obtained by solid-liquid separation of organic waste water and piping for supplying the methane-dissolved aqueous medium supplied from the liquid contact tank to the denitrification tank of the biological nitrogen treatment device Biological nitrogen treatment device comprising a nitrification tank Organic wastewater processing apparatus and a biological nitrogen treatment apparatus having a beauty denitrification tank.

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