JP4691938B2 - Nitrogen-containing liquid processing method and apparatus - Google Patents

Description

  The present invention relates to a method and apparatus for treating a nitrogen-containing liquid, and in particular, a nitrogen-containing liquid containing ammonia nitrogen is partially nitrified by ammonia-oxidizing bacteria, and nitrite nitrogen in the treatment liquid of the nitritation step The present invention relates to a method and apparatus for treating a nitrogen-containing liquid in which ammonia nitrogen is reacted with anammox bacteria to be converted into nitrogen gas and denitrified.

  Nitrogen components contained in the nitrogen-containing effluent, in particular ammonia nitrogen, are one of the causative substances of eutrophication in rivers, lakes, and the ocean, and must be efficiently removed in the effluent treatment process. In general, most of the organic nitrogen component in the nitrogen-containing liquid undergoes biological decomposition and is converted to ammoniacal nitrogen. In the conventional treatment method for nitrogen-containing liquids, nitrification is performed by oxidizing ammonia nitrogen to nitrite nitrogen by the action of ammonia oxidizing bacteria, and further oxidizing nitrite nitrogen to nitrate nitrogen by nitrite oxidizing bacteria. And a denitrification process in which these nitrite nitrogen and nitrate nitrogen are converted to nitrogen gas by using an organic substance such as methanol as an electron donor by denitrifying bacteria which are heterotrophic bacteria. Biological nitrification and denitrification, which is removed from wastewater through biological reactions, is common. In nitrification and denitrification treatment using such heterotrophic bacteria, organic matter such as methanol is required, and ammonia nitrogen is nitrated to nitrite nitrogen through nitrite nitrogen. Is required.

  As a treatment method for improving such a point, for example, Patent Document 1 discloses a nitrification denitrification treatment method using autotrophic denitrification bacteria. This method utilizes autotrophic denitrifying microorganisms that can generate nitrogen gas by reacting ammonia nitrogen as an electron donor and nitric acid or nitrite nitrogen as an electron acceptor under anaerobic conditions. Thus, it is a denitrification method, and it is not necessary to add organic substances. Patent Document 1 describes an example in which a part of the treatment liquid in the denitrification reaction tank is circulated to the denitrification reaction tank when nitrate ions are added and reacted with ammonia to denitrify, but partial nitrification is described. There is no description of nitritation based on specific examples.

  In Patent Document 2, a part of ammonia nitrogen is oxidized to nitric acid and / or nitrous acid, and nitric acid and / or nitrite nitrogen in the partial nitrification solution and ammonia nitrogen are reacted by autotrophic denitrifying bacteria. And a denitrification method in which it is converted to nitrogen gas is described. And the processing method which provides a pH adjustment tank between the partial nitrification process and the denitrification process, circulates the denitrification process liquid of a denitrification process to a pH adjustment tank, and adjusts to pH 7-8 suitable for a denitrification process. Are listed. Here, the pH adjusting tank has the role of adjusting the pH and, at the same time, increasing the amount of bound oxygen denitrifying bacteria under appropriate pH conditions and feeding it into the denitrifying step. Patent Document 2 describes a case where a part of ammonia nitrogen is oxidized to nitrate nitrogen, and this is reacted with ammonia nitrogen for denitrification. In this case, the nitrification rate required for denitrification is about Example of circulating a part of the treatment liquid in the denitrification reaction tank to the denitrification reaction tank because the pH required to achieve 40% is around 6.0 while the pH is 7 to 8 suitable for the denitrification treatment. Is described. However, nitritation and partial nitrification therefor are not described based on specific examples.

In both methods of Patent Documents 1 and 2, in order to adjust the pH to be suitable for the denitrification treatment, a denitrification process in the denitrification process is performed by providing a pH adjustment tank directly or between the partial nitrification process and the denitrification process. The pH is adjusted by circulating the treatment liquid, which is presumed to be because the pH suitable for nitrification and the pH suitable for denitrification differ greatly when oxidized to nitrate nitrogen. Further, in Patent Document 2, it is supposed that pH adjustment is possible without adding a pH adjusting agent, but this is also presumed to be a phenomenon peculiar when oxidizing to nitrate nitrogen. However, in the case of partial nitritation that oxidizes to nitrite nitrogen and does not perform nitrification, if the pH of the partial nitritation process is not adjusted, the activity of ammonia oxidizing bacteria decreases with the progress of nitritation, Nitrite is stopped and denitrification cannot be performed. When a pH adjuster (alkali) is injected in the nitritation step, it is necessary to inject a pH adjuster (acid) in the denitrification step, which increases the cost of the drug.
Japanese National Patent Publication No. 3-501099 JP-A-8-192185

  The problem of the present invention is that the aeration power for nitrification is small, pH adjustment is easy, the cost of the pH adjustment tank and the pH adjuster is reduced, and the treatment is efficiently performed to obtain a high-quality treatment solution, The object is to provide a method and apparatus for treating a nitrogen-containing liquid that can reduce the amount of generated sludge.

The present invention is the following method and apparatus for treating a nitrogen-containing liquid.
(1) A partial nitritation step of aeration of an ammoniacal nitrogen-containing liquid in the presence of ammonia-oxidizing bacteria and oxidizing 50 to 60% of the ammoniacal nitrogen component to nitrite nitrogen;
A denitrification step of reacting nitrite nitrogen and ammoniacal nitrogen in the treatment liquid of the partial nitritation step in the presence of anammox bacteria to convert to nitrogen gas;
The treatment liquid in the denitrification process is circulated to the partial nitritation process to adjust the pH of the reaction liquid in the partial nitritation process to 6.8 to 8.7, and the nitrite property at the inlet of the denitrification process . And a pH adjusting step for adjusting the nitrogen concentration to be 500 mg / L or less.
(2) The method according to (1) above, wherein the pH is adjusted by further injecting an alkali into the partial nitritation step.
(3) A partial nitritation tank that aerated ammonia nitrogen-containing liquid in the presence of ammonia-oxidizing bacteria and oxidizes 50 to 60% of the ammonia nitrogen component to nitrite nitrogen;
A denitrification tank that reacts nitrite nitrogen and ammonia nitrogen in the treatment liquid of the partial nitrification tank in the presence of anammox bacteria to convert to nitrogen gas;
The treatment liquid in the denitrification tank is circulated to the partial nitritation tank to adjust the pH of the reaction liquid in the partial nitritation tank to 6.8 to 8.7, and the nitrite nitrogen at the inlet of the denitrification tank is adjusted. A nitrogen-containing liquid treatment apparatus comprising: a pH adjustment apparatus that adjusts the concentration to be 500 mg / L or less.
(4) The apparatus according to (3) above, wherein the pH adjusting device includes a circulation path for circulating the treatment liquid in the denitrification tank to the partial nitritation tank and a chemical injection path for injecting alkali into the partial nitritation tank.

  The liquid to be treated in the present invention is a nitrogen-containing liquid containing ammoniacal nitrogen, which may contain nitrite nitrogen, organic nitrogen, and other nitrogen, sewage, human waste, food wastewater, Examples include fertilizer factory wastewater and other industrial wastewater. These nitrogen-containing liquids may be liquids to be treated containing ammoniacal nitrogen at the stage of treatment by the treatment method and apparatus of the present invention. When organic nitrogen is contained, the organic liquid is treated by anaerobic treatment or aerobic treatment in advance. Nitrogen can be decomposed into ammoniacal nitrogen and subjected to the treatment of the present invention. What does not contain nitrate nitrogen is preferable.

  In the present invention, the ammonia-oxidizing bacterium used for nitritation of ammonia nitrogen is a bacterium used for nitritation of ammonia nitrogen, which oxidizes ammonia nitrogen and converts it to nitrite nitrogen under aerobic conditions. Bacteria to do. Such ammonia-oxidizing bacteria can be generated by aerobically oxidizing a liquid to be treated containing ammoniacal nitrogen, but the sludge collected from the nitritation step of organic wastewater treatment is used as it is or as a carrier. It can be used by adhering to.

  The anammox bacterium used for denitrification in the present invention is a bacterium belonging to Plantomycetes, which is a denitrification bacterium that reacts ammonia nitrogen and nitrite nitrogen in an anaerobic atmosphere to directly convert to nitrogen gas, and is ammoniacal. It is a bacterium that does not react with nitrogen and nitrate nitrogen. Unlike the heterotrophic denitrification bacteria used for conventional denitrification, such anammox bacteria are autotrophic bacteria, so methanol and the like that were necessary for conventional denitrification bacteria during denitrification No additional nutritional sources are required. In addition, the anammox bacterium reacts ammonia nitrogen and nitrite nitrogen and converts them directly into nitrogen gas, so that ammonia nitrogen and nitrite nitrogen can be removed at the same time, and no harmful waste is generated. Such anammox bacteria can be generated by anaerobic reaction of denitrified liquid containing ammonia nitrogen and nitrite nitrogen, but sludge collected from the denitrification process of nitrogen-containing liquids. Can be used as is or attached to a carrier.

  In the present invention, as a partial nitritation step, first, a liquid to be treated is introduced into a partial nitritation tank and aerated in the presence of ammonia-oxidizing bacteria to oxidize a part of the ammonia nitrogen component to nitrite nitrogen. To do. In this case, partial nitritation is performed by bringing biological sludge containing ammonia-oxidizing bacteria into contact with the liquid to be treated in an aerobic state. The processing described above may employ any processing method such as a continuous method, a batch method, or a semi-batch method. Since the ammonia-oxidizing bacteria have a slow growth rate, it is preferable that the ammonia-oxidizing bacteria are loaded by introducing a carrier into the tank. As the carrier, a light granular material having open cells such as sponge is preferable, but other carriers may be used. The particle size of the granular carrier is arbitrary, but for example, a granular carrier of about 1 to 5 mm can be used.

  Aeration is performed under the condition that 50 to 60%, preferably 55 to 58%, more preferably 56 to 57% of ammonia nitrogen in the liquid to be treated is oxidized to nitrite nitrogen. In order to perform partial nitritation so as to achieve such a nitritation rate, the ammonia nitrogen concentration at the inlet and outlet of the partial nitritation process is measured, and the ammonia nitrogen concentration ratio at the inlet and outlet is the above. It is preferable to control the amount of aeration (oxygen supply amount) so as to correspond to the nitritation rate, but other control means may be used. In the present invention, ammonia nitrogen may be oxidized to nitrite nitrogen, so that the amount of oxygen supplied for oxidation may be smaller than that in the case of oxidizing ammonia nitrogen to nitrate nitrogen. The aeration power for nitrification decreases, and the processing cost decreases.

  Further, aeration is performed under the condition that the activity of the ammonia-oxidizing bacteria does not decrease and the nitrite-oxidizing bacteria do not increase in order to prevent the nitrite nitrogen from being oxidized to nitrate nitrogen. Such conditions include, for example, operating conditions in which aeration is performed while adding carbonate or bicarbonate to maintain the inorganic carbonate concentration at 50 mg-C / L or more, or at a C / N ratio with respect to ammonia in raw water. The operating condition etc. which add carbonate or bicarbonate so that it may become 0.5 or more are mentioned. As a pH condition of the nitrification tank, aeration is performed by adjusting the pH so as to be pH 6.8 to 8.7, preferably pH 7.0 to 8.0, and more preferably 7.5 to 8.0.

  In the denitrification process following the partial nitritation process, the treatment liquid of the partial nitritation process is maintained in an anaerobic state in the presence of anammox bacteria in the denitrification tank, and the nitrite nitrogen produced in the partial nitritation process The remaining ammoniacal nitrogen is reacted by the action of anammox bacteria, converted to nitrogen gas, and denitrified. In this case, the stirring state is maintained, and the biological sludge containing anammox bacteria is brought into contact with the treatment liquid of the partial nitritation step. Since anammox bacteria also have a slow growth rate, it is preferable to support them on a carrier or to form granular sludge. When granule sludge is formed, it takes a period of time for granule formation only with microorganisms. Therefore, it is desirable to add a substance serving as a nucleus and form a biofilm of anammox bacteria around the nucleus. In this case, examples of the nucleus include microbial granules and abiotic carriers.

Examples of the microbial granules used as the nucleus include anaerobic organisms such as methane bacteria granules and heterotrophic denitrifying granules. Methane granule is used in methane fermentation tanks where methane fermentation is performed by UASB (Upflow Anaerobic Sludge Blanket) method or EGSB (Expanded Granule Sludge Bed) method. You can apply what you have. The heterotrophic denitrification granules can be those used in a normal USB denitrification tank. These granules can be used as they are or as crushed materials thereof. Anammox bacteria are more economical than using abiotic materials as nuclei, which tend to adhere to such microbial granules and reduce the time required to form the granules.
Examples of the abiotic material used as the core include activated carbon, zeolite, silica sand, diatomaceous earth, fired ceramic, ion exchange resin, and the like, preferably made of activated carbon, zeolite, and the like, and a particle size of 50 to 200 μm, preferably 50. A carrier having an average specific gravity of 1.01 to 2.5, preferably 1.1 to 2.0, can be mentioned.

In order to form a biofilm of anammox bacteria on such a carrier or granulated material such as granule sludge, the core substance is added to a denitrification tank in which anammox bacteria are present and maintained in an anaerobic state for denitrification. By performing the treatment, biological sludge having a biofilm formed thereon can be generated.
When denitrification treatment is performed using biological sludge in which a biofilm of anammox bacteria is formed on a carrier or granule sludge, the biological sludge is developed and fluidized as in the UASB method or EGSB method. The treatment liquid and biological sludge are brought into contact in an anaerobic state. Thereby, nitrite nitrogen and ammonia nitrogen in the treatment liquid of the partial nitritation step react with each other by the action of the anammox bacteria, and are converted into nitrogen gas for denitrification.

  The nitritation reaction by ammonia-oxidizing bacteria in the partial nitritation step is represented by the following formula (1), where acid (nitrite) is generated and the pH is lowered. In addition, the denitrification reaction by anammox bacteria in the denitrification process is represented by the following formula (2), where ammonia nitrogen and nitrite nitrogen react at about 1: 1.32, and alkali is generated to increase the pH. To do. In the overall reaction via Formula (1) and Formula (2), the amount of acid produced is greater, and the pH decreases even if all the alkali in the denitrification solution is recovered.

NH ₄ ⁺ + 3 / 2O ₂ ⁻ → NO ₂ ⁻ + H ₂ O + 2H ⁺ (1)
1.0NH ₄ ⁺ + 1.32NO ₂ ⁻ + 0.066HCO ₃ ⁻ →
1.02N ₂ + 0.26NO ₃ ⁻ + 0.066CH ₂ O _0.5 N _0.15 + 2.03H ₂ O + 0.13OH ⁻ (2)

  In this way, in the partial nitritation process, when ammonia is oxidized, acid is generated and the pH is lowered, so it is necessary to add an alkali agent, and in the denitrification process, alkali is generated and the pH is raised. Therefore, it is necessary to add an acid agent. In addition, since anammox bacteria that perform autotrophic denitrification are inhibited by high concentrations of nitrous acid, conventionally, if the nitrogen concentration in the partial nitritation process treatment solution is high, the treatment solution of the denitrification step is used. It was circulated to reduce the nitrous acid concentration near the entrance of the denitrification tank. Since the treatment liquid to be circulated is already in a high pH state, a pH adjustment tank is provided in the middle of the circulation process or between the nitrification process and the denitrification process, and a chemical (acid) is added to adjust the pH. There was a need. In particular, when the ammoniacal nitrogen concentration of the liquid to be treated was high, the circulation amount increased in proportion to this, and a large amount of chemicals for pH adjustment were required.

  In the present invention, in order to increase the pH of the partial nitritation step and to prevent inhibition by high concentration of nitrous acid, the treatment liquid of the denitrification step is circulated in the previous partial nitritation step. Thereby, it becomes possible to adjust the pH of the inflow water of an autotrophic denitrification process, without providing a pH adjustment tank. In the partial nitrification step of oxidizing to nitrate nitrogen in Patent Document 2, the pH required to achieve a nitrification rate of about 40% is around 6.0, and pH adjustment is not necessary. In the partial nitritation step by bacteria, it was found that the pH required for partial nitritation of 50 to 60% of ammoniacal nitrogen in the liquid to be treated was 6.8 to 8.7. For this reason, pH adjustment is required in the partial nitritation step, but if the treatment liquid in the denitrification step having a high pH is circulated, pH adjustment and dilution can be performed. In addition, since the pH in the partial nitritation process decreases due to the reaction, it is not necessary to input an acid agent to the treatment liquid in the denitrification process, which was necessary in the prior art. Can be omitted.

As described above, the concentration of nitrite nitrogen at the inlet of the denitrification step is 500 mg / L from the viewpoint that in a denitrification step by anammox bacteria, if a high concentration of nitrous acid flows, the denitrification reaction does not proceed easily. or less, preferably 400 mg / L or less, more preferably you adjust the amount of the processing solution circulating to be equal to or less than 300 mg / L. On the other hand, from the viewpoint of realizing a rapid reaction in the partial nitritation step, the ammoniacal nitrogen concentration of the mixed liquid of the liquid to be treated and the circulating treatment liquid is 50 mg / L or more, preferably 100 mg / L or more, more preferably It is preferable to adjust the amount of the circulating treatment liquid so that the concentration is 200 mg / L or more.

  Thus, even if the pH of the denitrification process is circulated to the partial nitritation process and the pH is adjusted, the amount of acid generated in the partial nitritation process is large and the pH is lowered. It is preferable to adjust to a pH (6.8 to 8.7) suitable for the subsequent denitrification step by adding an alkali agent such as sodium hydroxide or sodium bicarbonate. Even in this case, since the circulating treatment liquid is alkaline, the amount of the alkaline agent used can be reduced as compared with the conventional method. Since the pH range suitable for the partial nitritation process and the pH range suitable for the denitrification process are almost the same, a pH adjustment tank is provided between the partial nitritation process and the denitrification process, and the treatment liquid is circulated in the pH adjustment tank. Such conventional operation is not necessary.

  The pH adjusting device for adjusting the pH in such a partial nitritation step is configured to adjust the pH by circulating the treatment liquid in the denitrification step to the partial nitritation step, and the treatment liquid in the denitrification tank It can comprise so that the circulation path circulating to a partial nitritation tank and the chemical injection path | route which inject | pours an alkali into a partial nitritation tank may be included. Both the circulation path and the chemical injection path can be equipped with a pump, but the circulation path pump is set so as to circulate a constant amount of the processing solution so as to be approximately in the pH range and the concentration range. It is preferable that the pump is controlled by a pH meter so as to be accurately in the pH range.

  By the above treatment, first, in the partial nitritation step, the liquid to be treated is introduced into the partial nitritation tank and aerated in the presence of ammonia-oxidizing bacteria, so that a part of the ammonia nitrogen component is converted into nitrite nitrogen. Until oxidized. In the denitrification process following the partial nitritation process, the nitrite treatment solution is introduced into the denitrification tank and maintained in an anaerobic state in the presence of anammox bacteria, and the nitrite produced in the partial nitritation process Nitrogen and the remaining ammoniacal nitrogen are bioreacted by the action of anammox bacteria, converted into nitrogen gas, detoxified, and denitrified. A part (most part) of the treatment liquid in the denitrification process is circulated in the partial nitritation process to be used for adjusting the pH of the reaction liquid, and the other part is discharged out of the system.

  In the above treatment, it is only necessary to oxidize part of ammonia nitrogen to nitrite nitrogen, so the aeration power for nitrification is reduced, and ammonia nitrogen is efficiently treated by autotrophic denitrification by anammox bacteria. A high-quality treatment liquid can be obtained. And since anammox bacteria have a slow growth rate, the amount of generated sludge can be reduced.

As described above, according to the method for treating a nitrogen-containing liquid of the present invention, in the partial nitritation step, the ammoniacal nitrogen-containing liquid is aerated in the presence of ammonia-oxidizing bacteria to reduce 50-60% of the ammoniacal nitrogen component. It is oxidized to nitrite nitrogen, and in the denitrification process, in the presence of anammox bacteria, nitrite nitrogen and ammonia nitrogen in the treatment liquid of the partial nitritation process are reacted to convert to nitrogen gas, In the pH adjustment process, the treatment liquid in the denitrification process is circulated to the partial nitritation process to adjust the pH of the reaction liquid in the partial nitritation process to 6.8 to 8.7, and at the inlet of the denitrification process. Since the concentration of nitrite nitrogen in the tank is adjusted to 500 mg / L or less, there is little aeration power for nitrification, pH adjustment is easy, the cost of the pH adjustment tank and pH adjuster is reduced, and efficiency Process well, With obtaining the treating solution for water quality, it is possible to reduce the generation amount of sludge.

Moreover, according to the nitrogen-containing liquid treatment apparatus of the present invention, the ammonia-containing nitrogen-containing liquid is aerated in the presence of ammonia-oxidizing bacteria to oxidize 50 to 60% of the ammoniacal nitrogen component to nitrite nitrogen. In the presence of nitrification tank, anammox bacteria, denitrification tank that reacts nitrite nitrogen and ammonia nitrogen in reaction liquid of partial nitritation tank to convert into nitrogen gas, and treatment liquid of denitrification tank Circulating in the partial nitritation tank, the pH of the reaction liquid in the partial nitritation process is adjusted to 6.8 to 8.7, and the concentration of nitrite nitrogen at the inlet of the denitrification process is 500 mg / L. Since the pH adjusting device is adjusted so as to be as follows, the above treatment can be performed efficiently.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a flowchart showing a method and apparatus for treating a nitrogen-containing liquid according to an embodiment of the present invention. In FIG. 1, 1 is a partial nitritation tank, 2 is a denitrification tank, and 3 is a relay tank.

  The partial nitritation tank 1 contains the reaction solution 4, and nitrite sludge 5 in which ammonia-oxidizing bacteria are attached to a light granular carrier having open cells such as sponge is dispersed in the reaction solution 4. An aeration device 6 is provided at the bottom and a screen 7 is provided at the top. The partial nitritation tank 1 is connected to the liquid introduction path L 1, the circulation path L 2, and the chemical injection path L 3, and the air supply path L 4 is connected to the aeration apparatus 6. L5 communicates with the relay tank 3. The denitrification tank 2 contains a reaction liquid 11, a denitrification sludge 12 in which anammox bacteria are adhered to granule sludge is formed in a sludge blanket shape in the reaction liquid 11, and a solid-gas-liquid separator 13 is provided at the top. Yes. The transfer path L6 from the relay tank 3 communicates with the bottom of the denitrification tank 2, the circulation path L2 communicates from the solid-gas-liquid separator 13 to the partial nitritation tank 1, and the processing liquid take-out path L7 communicates outside the system. is doing. The pH is a pH meter, and P1 to P3 are pumps.

In the method for treating a nitrogen-containing liquid by the apparatus of FIG. 1, first, as a partial nitritation step, the liquid to be treated is introduced into the partial nitritation tank 1 from the liquid introduction path L1 and the treatment liquid is circulated from the circulation path L2. Then, the air is supplied from the air supply path L4 and aerated by the aeration apparatus 6, and the nitrite sludge 5 to which ammonia-oxidizing bacteria are attached is brought into contact with the reaction solution 4 in an aerobic manner, thereby producing ammonia. Part of the nitrogen component is oxidized to nitrite nitrogen. The treatment liquid in the partial nitritation tank 1 is taken out through the screen 7 to the separation liquid section 8 while preventing the nitrite sludge 5 from flowing out, introduced into the relay tank 3 from the transfer path L5, stored, and transferred by the pump P1. It introduce | transduces into the bottom part of the denitrification tank 2 from the path | route L6.

In the denitrification tank 2, as the denitrification step, the denitrification sludge 12 to which the anammox bacteria are attached is brought into contact with the partial nitritation treatment solution in an anaerobic state, and nitrite nitrogen generated in the partial nitritation step; The remaining ammoniacal nitrogen is bioreacted by the action of anammox bacteria, converted into nitrogen gas, detoxified, and denitrified. The reaction liquid 11 that is treated by raising the denitrification tank 2 is subjected to solid-gas-liquid separation in the solid-gas-liquid separator 13, and a part (most) of the processing liquid 14 that has separated the solid and gas. Is circulated from the circulation path L2 to the partial nitritation tank 1 by the pump P2 to adjust the pH of the reaction solution 4, and is used to adjust the concentration of nitrite nitrogen at the inlet of the denitrification tank 2. The part is discharged out of the system from the processing liquid outlet L7. In the partial nitritation tank 1, the pH of the reaction solution 4 is measured with a pH meter pH, and the pump P3 is controlled so that the pH becomes 6.8 to 8.7, and an insufficient amount of alkaline agent is injected from the drug injection path L3. To adjust the pH.

FIG. 2 shows an example in which the pH adjustment method of Patent Document 2 is applied to the apparatus of FIG. 1 as a reference example. In the apparatus of FIG. 1, a pH adjustment tank 15 is provided instead of the relay tank 3, and treatment is performed from the circulation path L2. In addition to communicating to circulate the liquid, a pH meter pH2 is provided to control the pump P4 and communicate to inject the acid from the medicinal channel L8.
The treatment method of the nitrogen-containing liquid by this apparatus is carried out in substantially the same manner as in FIG. 1, but in the partial nitritation tank 1, the pump P3 is controlled by the pH meter pH, and alkali is injected from the drug injection path L3. In the pH adjustment tank 15, the treatment liquid is circulated from the circulation path L2 to adjust the pH, and the pH P2 is controlled by the pH meter pH2, and the pH of the treatment liquid circulated by injecting the acid from the drug injection path L8. Adjust to lower. For this reason, compared with the case of FIG. 1, pH adjustment is complicated and the quantity of the chemical | medical agent for pH adjustment also increases.

Example 1:
Processing was performed with the apparatus of FIG. The liquid to be treated is a synthetic waste water mainly composed of ammonium sulfate, and has an NH ₄ —N concentration of 1000 mg / L. As the partial nitritation tank 1, an aeration tank with a capacity of 6L was used, and a 40% sponge carrier was introduced into the tank to attach ammonia oxidizing bacteria. A wedge wire screen was used as the screen 7 for solid-liquid separation of the nitrite sludge 5 containing the carrier and the treatment liquid. As the denitrification tank 2, an up-flow type reaction tank with a capacity of 3L was used, and 2L of granule of autotrophic denitrification bacteria was introduced into the tank to attach anammox bacteria. The denitrification process treatment liquid in the denitrification tank 2 was circulated to the partial nitritation tank 1. Other experimental conditions are shown in Table 1.

Comparative Example 1:
The same liquid to be treated was processed using the reaction tank having the same capacity as that of Example 1 using the apparatus shown in FIG. The treatment liquid in the denitrification tank 2 was circulated to the pH adjustment tank 15, mixed with the partial nitritation process treatment liquid, and then introduced into the denitrification tank 2. The solution in the pH adjusting tank 15 was adjusted to pH 7.6.

As a result of Example 1 and Comparative Example 1,
In both Example 1 and Comparative Example 1, the treatment could be performed satisfactorily, but there was a difference in the amount of chemical used. That is, in Example 1, the same treatment as in Comparative Example 1 was possible without using an acid, and the amount of alkaline agent used was reduced by about 10%.
Table 2 shows the water quality of the treatment liquid in each step of Example 1 and Comparative Example 1.

  The present invention can be used in a treatment method and apparatus for biologically denitrifying a nitrogen-containing liquid containing ammoniacal nitrogen.

It is a flowchart which shows the processing method and apparatus of the nitrogen containing liquid by embodiment of this invention. As a reference example, it is a flowchart which shows the example which applied the pH adjustment method of patent document 2 to the apparatus of FIG.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Partial nitritation tank 2 Denitrification tank 3 Relay tank 4 Reaction liquid 5 Nitrite sludge 6 Aeration apparatus 7 Screen 8 Separation liquid part 11 Reaction liquid 12 Denitrification sludge 13 Solid-gas-liquid separator 14 Treatment liquid 15 pH adjustment Tank

Claims (4)

A partial nitritation step of aeration of an ammoniacal nitrogen-containing liquid in the presence of ammonia oxidizing bacteria to oxidize 50 to 60% of the ammoniacal nitrogen component to nitrite nitrogen;
A denitrification step of reacting nitrite nitrogen and ammoniacal nitrogen in the treatment liquid of the partial nitritation step in the presence of anammox bacteria to convert to nitrogen gas;
The treatment liquid in the denitrification process is circulated to the partial nitritation process to adjust the pH of the reaction liquid in the partial nitritation process to 6.8 to 8.7, and the nitrite property at the inlet of the denitrification process . And a pH adjusting step for adjusting the nitrogen concentration to be 500 mg / L or less. The method according to claim 1, wherein the pH is adjusted by further injecting an alkali into the partial nitritation step. A partial nitritation tank in which an ammoniacal nitrogen-containing liquid is aerated in the presence of ammonia-oxidizing bacteria to oxidize 50 to 60% of the ammoniacal nitrogen component to nitrite nitrogen;
A denitrification tank that reacts nitrite nitrogen and ammonia nitrogen in the treatment liquid of the partial nitrification tank in the presence of anammox bacteria to convert to nitrogen gas;
The treatment liquid in the denitrification tank is circulated to the partial nitritation tank to adjust the pH of the reaction liquid in the partial nitritation tank to 6.8 to 8.7, and the nitrite nitrogen at the inlet of the denitrification tank is adjusted. A nitrogen-containing liquid treatment apparatus comprising: a pH adjustment apparatus that adjusts the concentration to be 500 mg / L or less.   The apparatus according to claim 3, wherein the pH adjusting device includes a circulation path for circulating the treatment liquid of the denitrification tank to the partial nitritation tank and a chemical injection path for injecting alkali into the partial nitritation tank.

Images