JP6139300B2 - Sludge reforming apparatus and sludge reforming method, sludge reforming apparatus control apparatus, and control method - Google Patents

Description

  The present invention relates to a sludge reforming apparatus, a reforming method, a control apparatus for a sludge reforming apparatus, and a control method that can be applied to a sludge tank for sewage treatment such as a gravity concentration tank or a sedimentation basin.

  Conventionally, research and development for applying a microbial fuel cell to a sewage sludge treatment process has been performed. This research and development was to recover the energy of sewage sludge using a microbial fuel cell. This conventional microbial fuel cell includes a pair of electrodes, an external circuit electrically connected to these electrodes, and a diaphragm that separates the pair of electrodes, and one electrode side has an extracellular electron transfer capability. The microorganism which has is hold | maintained (patent document 1).

JP 2010-218690 A

  By the way, the present inventor has not only performed the original action that the microbial fuel cell collects the energy of the sewage sludge in the process of research and development to apply the microbial fuel cell to the sewage sludge treatment process, but also the sewage sludge. It has been found that it also has a secondary effect of reducing the viscosity of itself.

  The sewage sludge reforming performance of this microbial fuel cell is excellent in reducing the amount of coagulant used in the dehydrator and reducing the capacity of the dehydrator when applied as a pretreatment of the sewage sludge that is put into the dehydrator. Expected to be effective.

  The present invention has been made in view of the above, and its object is to apply the sewage sludge reforming performance of the microbial fuel cell as a pretreatment of sewage sludge that is put into a dehydrator. To provide a sludge reforming device and a sludge reforming method, a sludge reforming device control device, and a control method capable of realizing power saving and a reduction in the amount of coagulant used in a dewatering device is there.

  In order to solve the above-described problems and achieve the above object, a sludge reforming apparatus according to the present invention stores liquid, organic matter, and sludge containing electron-donating microorganisms that decompose organic matter and release electrons. Sometimes a tank that maintains two layers, a supernatant layer mainly composed of liquid and a sludge layer mainly composed of sludge, is installed with at least a part buried in the sludge layer, and electrons from the electron-donating microorganisms are installed. Anode electrode to be supplied, a cathode electrode which is electrically connected to the anode electrode and installed so as to be at least partially immersed in the supernatant layer, and discharge of sludge from the sludge layer and to the sludge layer Sludge replacement means for supplying the sludge, current measurement means for measuring the current flowing between the anode electrode and the cathode electrode, and replacing at least a part of the sludge in the sludge layer based on the measured current value. And a control means for controlling the mud replacement unit, and a sludge by electrons flow supplied from the electron-donating microorganism between the cathode and anode electrodes, characterized in that to modify.

  In the sludge reforming apparatus according to the present invention, in the above invention, the control means calculates the accumulated electric energy by accumulating the current value flowing between the cathode electrode and the anode electrode supplied from the current measuring means over time. And when accumulated electric energy becomes more than predetermined value, the control which replaces at least one part of sludge by a sludge replacement | exchange means is performed.

  The sludge reforming apparatus according to the present invention further comprises sludge homogenizing means for homogenizing sludge in the sludge layer while maintaining two layers of the sludge layer and the supernatant liquid layer in the above invention, and the control means is Then, after replacing at least part of the sludge in the sludge layer by the sludge replacement means, the sludge homogenization means is controlled to homogenize the sludge in the sludge layer.

  The sludge reforming apparatus according to the present invention is characterized in that, in the above invention, the cathode electrode is installed such that a part of the cathode electrode is exposed on the liquid surface.

  The sludge reforming method according to the present invention stores liquid, organic matter, and sludge containing electron-donating microorganisms that decompose organic matter and release electrons, and the supernatant liquid layer and sludge mainly occupied by liquid at the time of storage are mainly A sludge treatment step for maintaining two layers of an occupied sludge layer, an anode electrode at least partially embedded in the sludge layer, an electron electrode supplied with electrons from an electron donating microorganism, and an anode electrode electrically A sludge reforming step for reforming sludge by flowing electrons supplied from an electron-donating microorganism between a cathode electrode that is connected and at least partially immersed in the supernatant layer; A sludge replacement step for discharging sludge from the sludge layer and for introducing sludge into the sludge layer; a current measurement step for measuring the current value flowing between the anode electrode and the cathode electrode; Based on the value, so replacing at least a portion of the sludge of the sludge layer, characterized in that it comprises a control step of controlling the sludge replacement means for performing exchange of sludge, the.

  The control device of the sludge reforming apparatus according to the present invention stores liquid, organic matter, and sludge containing electron donating microorganisms that decompose organic matter and release electrons, and the supernatant liquid layer and sludge that the liquid mainly occupies at the time of storage An anode electrode that is provided in a tank that maintains two layers of a sludge layer that mainly occupies, is at least partially embedded in the sludge layer, and is supplied with electrons from an electron-donating microorganism; A cathode electrode that is electrically connected and at least partially immersed in the supernatant layer, and sludge is generated by electrons supplied from the electron donating microorganism flowing between the cathode electrode and the anode electrode. The sludge replacement means for discharging the sludge from the sludge layer and feeding the sludge into the sludge layer, after flowing at least a part of the sludge, and flows between the anode electrode and the cathode electrode Based on the current values, and controls to switch the at least a portion of the sludge in the sludge layer.

  The control method of the sludge reforming apparatus according to the present invention stores liquid, organic matter, and sludge containing electron-donating microorganisms that decompose organic matter and release electrons, and the supernatant liquid layer and sludge mainly occupied by liquid at the time of storage While maintaining two layers of the sludge layer, which is mainly occupied by at least a part of the sludge layer, the anode electrode is supplied with electrons from the electron-donating microorganism, and the anode electrode is electrically When the sludge is reformed by the electrons supplied from the electron-donating microorganisms flowing between the cathode electrode that is connected and at least partially immersed in the supernatant layer, the anode electrode Sludge so as to replace at least a part of the sludge in the sludge layer based on a current measurement step for measuring a current value flowing between the cathode electrode and the cathode electrode, and a current measurement value in the current measurement step. By controlling the sludge replacement means for performing replacement, characterized in that it comprises a control step for controlling the discharge of sludge from the sludge layer and the sludge to the sludge layer on, the.

  According to the sludge reforming apparatus and sludge reforming method, the sludge reforming apparatus control apparatus, and the control method according to the present invention, the sewage sludge having the microbial sewage sludge reforming performance introduced into the dehydrator Therefore, it is possible to realize power saving, a reduction in the amount of the coagulant used, and the like in the dehydrator provided in the subsequent stage.

FIG. 1 is an example of a sludge treatment system when a sludge reforming apparatus according to an embodiment of the present invention is a sludge tank. FIG. 2 is a schematic diagram showing a sludge reforming apparatus according to an embodiment of the present invention. FIG. 3 is a graph showing measured values of current output for each elapsed day in the sludge reforming apparatus used in Experimental Example 1 and Experimental Example 2 of one embodiment of the present invention. FIG. 4 is a graph showing measured values of current output for each elapsed day when a part of sludge is replaced in the sludge reforming apparatus used in Experimental Example 3 of one embodiment of the present invention. FIG. 5 is a graph showing measured values of current output for each elapsed day in the sludge reforming apparatus according to Experimental Example 4 of one embodiment of the present invention. FIG. 6 is a graph showing values before and after the start of TS and VS in sludge in the sludge reformer according to the comparative example. FIG. 7 is a graph showing values before and after the start of TS and VS in Experimental Example 4 in one embodiment of the present invention. FIG. 8 is a graph showing the amount of filter paper filtered for the sludge before the experiment, the sludge by the comparative example, and the sludge in the experimental example 4. FIG. 9 is a graph showing changes in COD _Cr and BOD before and after the experiment according to a comparative example. FIG. 10 is a graph showing changes in COD _Cr and BOD before and after the experiment according to Experimental Example 4 in one embodiment of the present invention. FIG. 11 is a flowchart for explaining a sludge reforming method according to an embodiment of the present invention. FIG. 12 is a graph showing the elapsed time dependency of the power generation amount used for controlling the replacement of a part of sludge according to an embodiment of the present invention.

  Hereinafter, an embodiment of the present invention will be described with reference to the drawings. In all the drawings of the following embodiment, the same or corresponding parts are denoted by the same reference numerals. Further, the present invention is not limited to the embodiments described below.

  First, a sludge tank to which a sludge reforming apparatus according to an embodiment of the present invention is applied and a sludge treatment system including the same will be described. FIG. 1 shows a sludge tank and a sludge treatment system as sludge reforming apparatuses according to this embodiment.

  As shown in FIG. 1, the sludge treatment system 1 according to this embodiment includes a sludge tank 10 as a tank, a dehydrator 2 as a dewatering means provided in the subsequent stage, and a combustion means provided in the subsequent stage. A combustion furnace 3, a control unit 4 as a control device or control means, and an ammeter 5 as current measurement means are provided. The dewatering device 2 is composed of, for example, a gravity dewatering device or a belt press type dewatering device, and dewaters the sludge discharged from the sludge layer 10 to obtain a dewatered cake. The combustion furnace 3 is composed of, for example, a gasification furnace or a fluidized incinerator, and incinerates the dehydrated cake carried out from the dehydrator 2 at a high temperature.

  Moreover, this sludge tank 10 is comprised from solid-liquid separators, such as a gravity concentration tank and a sedimentation tank, for example, and the anode electrode 12 and the cathode electrode 13 as a pair of electrodes are provided. When sewage treatment is performed in the sludge tank 10, the inside of the sludge tank 10 is separated into a sludge layer 11 a mainly made of sludge formed by sludge and a subsequent water treatment facility (not shown). It is substantially separated into two layers such as a liquid and a supernatant liquid layer 11b mainly composed of liquid, and these two layers are always maintained. Inside the sludge tank 10, there is provided an input pipe 10a configured to be able to supply input sludge to the sludge layer 11a from the outside.

  In addition, a sludge discharge valve 14 is provided in the lower part of the sludge tank 10, and a part of sludge is discharged from the sludge layer 11 a through the sludge discharge valve 14 as concentrated sludge. The opening / closing operation of the sludge discharge valve 14 is controlled by the control unit 4. The input pipe 10a and the sludge discharge valve 14 constitute sludge replacement means.

  Further, in the sludge tank 11a in the sludge tank 10, a scraper 15 and a swing mixer 16 are provided as sludge homogenizing means for homogenizing the sludge in the sludge layer 11a. The scraper 15 is connected to a motor 15b by a shaft 15a. The rotation of the motor 15b is controlled by the control unit 4. The scraper 15 is rotated in the sludge tank 11 a by the rotation of the motor 15 b under the control of the control unit 4. The rotation of the motor 15b is controlled by the control unit 4. The swing mixer 16 is connected to a motor 16b through a swivel strut 16a. The rotation of the motor 16b is controlled by the control unit 4. The swing mixer 16 generates a water flow slightly downward in the circumferential direction while turning by the rotation of the motor 16 b under the control of the control unit 4. Thereby, the sludge layer 11a can be kneaded. Since the water flow from the swing mixer 16 toward the outer periphery is a downward flow by the inner wall surface of the sludge tank 10, it is possible to homogenize the sludge by kneading only the sludge layer 11a. It becomes possible to maintain two layers of the sludge layer 11a and the supernatant layer 11b.

The anode electrode 12 is disposed so that at least a part, preferably all, of the anode electrode 12 is buried in the sludge layer 11a so that the electron donating microorganisms having extracellular electron transfer capability contained in the sludge adhere to the outer surface. Further, since the cathode electrode 13 needs to be brought into contact with air in order to obtain oxygen (O ₂ ) in microbial power generation described later, a part of the cathode electrode 13 is exposed on the upper surface of the supernatant liquid layer 11b. Furthermore, as described above, the sludge layer 11a and the supernatant liquid layer 11b in the sludge tank 10 are maintained in two layers. As a result, a current (electron flow) flows between the anode electrode 12 and the cathode electrode 13. Hereinafter, the principle of current flow will be described.

That is, in the sludge layer 11a, closely related species of Geobacter as an electron donating microorganism adhere to the anode electrode 12. Thereby, for example, a reaction such as the following formula (1) occurs, and in the anode electrode 12, carbon dioxide (CO ₂ ), hydrogen ions (H ⁺ ), and electrons (e ⁻ ) Is generated. Electrons (e ⁻ ) generated at this time are supplied from the anode electrode 12 to the cathode electrode 13. Further, the current as the movement of the electrons is measured by the ammeter 5 and the measured current value is supplied to the control unit 4.

On the other hand, the produced carbon dioxide (CO ₂ ) is released to the outside, and the hydrogen ions (H ⁺ ) move to the supernatant layer 11b. In the supernatant layer 11b, oxygen (O ₂ ) and hydrogen ions (H ⁺ ) receive electrons (e ⁻ ) from the cathode electrode 13 and react with water (H ₂ ) by a reaction such as the following equation (2), for example. O). Thus, current flows from the cathode electrode 13 to the anode electrode 12. At this time, since supply of oxygen is necessary for the cathode electrode 13, a part of the cathode electrode 13 is exposed to the outside of the supernatant layer 11b as necessary as described above.

C ₆ H ₁₂ O ₆ + 6H ₂ O → 6CO ₂ + 24H ⁺ + 24e ⁻ (1)
6O ₂ + 24H ⁺ + 24e ⁻ → 12H ₂ O (2)

  In the sludge tank 10 configured as described above, by installing various electric machines and electrical appliances that use electric power between the cathode electrode 13 and the anode electrode 12, electric power (current) is obtained from the sludge in the sludge tank 10. It can be taken out and various devices can be driven.

  And this inventor performed various experiment using the sludge reforming apparatus of the structure similar to the sludge tank 10 mentioned above. FIG. 2 is a schematic diagram showing a sludge reforming apparatus according to this embodiment.

  As shown in FIG. 2, the sludge reforming apparatus 20 according to this embodiment includes a sludge storage tank 21, an upper lid 22 provided on the upper part, an anode electrode 24, and a cathode electrode 25, as with the sludge tank 10. ing. The anode electrode 24 is disposed so as to be buried in the sludge layer 23 a made of sludge stored in the sludge storage tank 21. The cathode electrode 25 is arranged so that a part of the cathode electrode 25 is exposed on the upper surface of the supernatant layer 23b.

  The sludge reforming apparatus 20 is provided with a scraper 21a as a stirring means for appropriately stirring the sludge in the sludge layer 23a. The scraping machine 21a may be another stirring means, and may be made to flow by introducing and discharging sludge. Furthermore, the sludge reforming apparatus 20 is provided with a monitoring unit 26 that measures the current flowing between the cathode electrode 25 and the anode electrode 24 and can store the measured value as sequential data.

(Experimental Examples 1 and 2)
And this inventor performed microbial power generation using the actual sludge sludge such as the gravity concentration tank drawing sludge in the sludge concentration treatment facility using a plurality of sludge reforming apparatuses 20 configured as described above. (Experimental examples 1 and 2). The power generation amount was continuously monitored by the monitoring unit 26, and the room temperature and the water temperature of the supernatant layer 23b were continuously monitored in order to grasp changes in environmental conditions. FIG. 3 shows a graph of the measurement results. From FIG. 3, it was confirmed that in the sludge reforming apparatus 20, after a power generation rising period (acclimation period) of about 7 to 10 days, the current value stably increased and microbial power generation could be performed stably. In other words, it was confirmed that at least about 7 to 10 days or more is necessary until microbial power generation occurs from the cathode electrode 25 and the anode electrode 24 of the sludge reforming apparatus 20. In addition, when this inventor monitored the pH of the supernatant liquid layer 23b, it was confirmed that microbial power generation occurred at pH 7 or higher, and it was also found that measurement of pH is suitable for monitoring microbial power generation.

(Experimental example 3)
Next, Experimental Example 3 according to this embodiment will be described. In Experimental Example 3, in order to obtain the same state as the flow of sludge input and discharge in the sludge tank 10, a part of the sludge layer 23a, for example 1 / 4 sludge was taken out and the same amount of new sludge was added. In this case, the result of the daily change of the measured current value is shown in FIG. From FIG. 4, it was confirmed that by replacing some of the sludge at the time when a portion of the sludge was replaced, the current was temporarily reduced, but it was possible to recover to the original power generation level within a few days. That is, it was confirmed that a high power generation level can be maintained in the sludge tank 10 such as a gravity concentration tank into which sludge is intermittently charged.

(Experimental example 4, comparative example)
Next, a sludge reforming apparatus 20 according to Experimental Example 4 according to this embodiment and a comparative example for comparing the effects of sludge reforming will be described. That is, as Experimental Example 4, the same sludge reforming apparatus 20 as in Experimental Example 1 is used, and the current can be taken out by electrically connecting the anode electrode 24 and the cathode electrode 25 via the monitoring unit 26. The configuration (hereinafter, closed circuit) was adopted. On the other hand, in the comparative example, in the sludge reforming apparatus 20 similar to the experimental example 1, the anode electrode 24 and the cathode electrode 25 are not electrically connected and no current is taken out (hereinafter referred to as open circuit). Thus, the present inventor evaluated the difference in sludge reforming and weight reduction depending on whether or not current is taken out from the sludge. In both Experimental Example 4 and Comparative Example, the experimental period was 41 days.

  FIG. 5 is a graph showing a change with time of current generated by microbial power generation in Experimental Example 4. From FIG. 5, in Experimental Example 4, microbial power generation is started about 12 days after the start of the sludge reforming apparatus 20, and the current increases until the 41st day at the end of the experimental period of Experimental Example 4. I understand that. On the other hand, in the comparative example, no current is taken out because it is an open circuit. Moreover, when this inventor confirmed the supernatant liquid layer 23b in the sludge reforming apparatus 20 visually, it was observed that the supernatant liquid became clear with progress of days also in any of Experimental example 4 and a comparative example. It was. As a result, it was found that the supernatant layer 23b was not clarified because of current extraction.

(Sludge reduction effect)
FIGS. 6 and 7 show the concentration of sludge evaporation residue (TS: Total Solids) and the volatile organic matter (VS) in Comparative Example and Experimental Example 4, respectively, at the start and end of the experiment. It is a graph which shows a density | concentration. From FIG. 6, in the comparative example employing the open circuit, TS decreased from about 3600 mg / L to about 3000 mg / L at the start and end of the experiment, and VS decreased from about 2700 mg / L to about 3000 mg / L. It turns out that it has decreased to 2000 mg / L. That is, it was confirmed that the TS reduction rate was about 18.5% and the VS reduction rate was about 24.6%. On the other hand, from FIG. 7, in Experimental Example 4 employing the closed circuit, TS decreased from about 3900 mg / L to about 2900 mg / L at the start and end of the experiment, and VS was about It can be seen that there is a decrease from 2900 mg / L to about 2100 mg / L. That is, it was confirmed that the TS reduction rate was about 23.8% and the VS reduction rate was about 29.5%.

  And when the reduction rate of TS of these experimental examples 4 and a comparative example was compared, in experimental example 4, it was confirmed that the reduction rate of TS improved 1.3 time compared with the comparative example. Similarly, when the VS reduction rate was compared between the experimental example 4 and the comparative example, it was confirmed that in the experimental example 4, the VS reduction rate was improved by 1.2 times compared to the comparative example. Therefore, as in Experimental Example 4, it was confirmed that the sludge can be further reduced by extracting the current from the sludge layer 23a in the sludge reformer 20.

(Dehydration effect)
In addition, the present inventor conducted a sludge dewaterability evaluation test by measuring the amount of filter paper filtered water as a dewaterability index. Specifically, a filter paper was installed in a funnel attached to the clamp, and 30 ml of sludge was passed through the filter paper, and the amount of water filtered (amount of filtered water) was measured for 5 minutes. FIG. 8 shows the amount of filtered water in the sludge before and after the experiment of Comparative Example and Experimental Example 4 obtained by this dehydration evaluation test.

  From FIG. 8, the amount of filtered water in the sludge before the experiment is an average of 2.1 ml of 2.0 to 2.2 ml, whereas in the comparative example employing an open circuit, the amount of filtered water at the end is 1.9 to It can be seen that the average of 2.2 ml is 2.0 ml, and there is almost no difference. On the other hand, in Experimental Example 4 employing a closed circuit, the amount of filtered water at the end was an average of 2.6 ml of 2.4 to 2.9 ml, which is 1.2 to 1.3 compared to the pre-experiment and comparative examples. It can be seen that the amount of filtered water increases about twice. That is, it was confirmed that by taking out the current from the sludge layer 23a in the sludge reforming apparatus 20, the dewaterability of the sludge was improved and the sludge was reformed.

(Chemical oxygen demand reduction effect)
In addition, the present inventor examines whether or not the sludge reforming apparatus 20 is applied to a sludge tank, which influences a reaction tank such as an anaerobic tank, a nitrification tank, and a denitrification tank provided in a subsequent stage of the sludge tank. Went. Here, in Experimental Example 4 and Comparative Example, the reduction rate of the biochemical oxygen demand (BOD) of the supernatant liquid layer 23b to be treated water and the chemical oxygen demand (COD _Cr ) due to potassium dichromate are shown. It was measured. 9 and 10 are graphs showing changes in BOD and COD _{Cr in the} supernatant layer 23b before and after the experiment in the comparative example and the experimental example 4, respectively.

From FIG. 9, in the comparative example employing the open circuit, the COD _{Cr of the} supernatant layer 23b before the experiment is about 1100 mg / L, and the COD _{Cr of the} supernatant layer 23b after the experiment is about 280 mg / L. I understand that there is. That is, in the comparative example, it can be seen that the COD _Cr of the supernatant layer 23b is reduced by about 75% before and after the experiment. Moreover, in this comparative example, it turns out that BOD of the supernatant liquid layer 23b before an experiment is about 730 mg / L, and BOD of the supernatant liquid layer 23b after an experiment is about 85 mg / L. That is, in the comparative example, it can be seen that the BOD of the supernatant layer 23b is reduced by about 88% before and after the experiment.

On the other hand, from FIG. 10, in Experimental Example 4 employing a closed circuit, the COD _{Cr in the} supernatant layer 23b before the experiment is about 1100 mg / L, and the COD _{Cr in the} supernatant layer 23b after the experiment is It turns out that it is about 220 mg / L. That is, in Experimental Example 4, it was confirmed that COD _Cr in the supernatant layer 23b was reduced by about 80% before and after the experiment. In Experimental Example 4, it can be seen that the BOD of the supernatant layer 23b before the experiment is 750 mg / L, and the BOD of the supernatant layer 23b after the experiment is 100 mg / L. That is, in Experimental Example 4, it was confirmed that the BOD of the supernatant layer 23b was reduced by 87% before and after the experiment.

When the COD _Cr reduction rate and the BOD reduction rate in the comparative example and the experimental example 4 are compared, respectively, the reduction rate of the BOD is comparable between the comparative example and the experimental example 4 from FIGS. 9 and 10. On the other hand, it can be seen that there is a difference of 5 points in the reduction rate of COD _Cr . That is, in Experimental Example 4, it can be seen that the reduction rate of COD _Cr is increased by extracting the current from the sludge layer 23a. As a result, it was confirmed that even when a current was taken out from the sludge layer 23a as in Experimental Example 4 and a reaction vessel or the like was provided in the subsequent stage, there was almost no influence on the reaction vessel by microbial power generation.

According to Experimental Example 4 according to the embodiment described above, the removal rate of TS and the removal rate of VS can be improved as compared with the comparative example, and the dewatering performance is improved because the filtration amount is increased. It can be seen that the reduction rate of COD _Cr can also be improved. Therefore, according to the sludge reforming apparatus according to one embodiment of the present invention, it was confirmed that sludge can be reduced and reformed by taking out current from the sludge.

(Sludge reforming method)
Next, the sludge reforming method by the sludge treatment system 1 as the sludge reforming apparatus according to the above-described embodiment based on the experimental results obtained as described above will be described. FIG. 11 is a flowchart showing a sludge reforming method according to this embodiment, and shows a control method in which the control unit 4 controls the sludge treatment system 1 based on the principle of MFC (Microbial Fuel Cell). Further, FIG. 12 is a graph showing an outline of current fluctuation when the processing elapsed time dependency and a part of the sludge are replaced in the power generation amount from the sludge treatment system 1.

  First, in the sludge treatment system 1 shown in FIG. 1, as described above, power generation is performed in a state where the sludge tank 11a and the supernatant liquid layer 11b are formed in the sludge tank 10, and the system waits for a predetermined time. Thereby, the power generation by microorganisms in the sludge tank 10 is stabilized (step ST1 in FIG. 11).

  Next, the control unit 4 constantly continuously monitors the measured value of the current supplied from the ammeter 5 (step ST2 in FIG. 11). In the monitoring by the control unit 4, for example, an increase in current due to elapsed time as shown in FIG. 12 is observed.

  On the other hand, in the sludge tank 10, the control unit 4 controls the motor 15b to gently rotate the scraper 15 to stir the sludge in the sludge layer 11a (step ST3 in FIG. 11). The scraper 15 may be rotated intermittently. At this time, the control unit 4 controls the scraper 15 so as to maintain the two layers of the sludge tank 11a and the supernatant liquid layer 11b, and more gently than the stirring of the sludge layer 11a by the swing mixer 16 described later. Knead and stir. By stirring the sludge layer 11a by the scraper 15, various sludges in the sludge layer 11a are brought into continuous and continuous contact with the anode electrode 12 sequentially. Thereby, during the power generation in the sludge tank 10, the sludge in the sludge layer 11a can be homogenized and the gas generated along with the decomposition of the sludge can be degassed. Can be

  And as shown in FIG. 12, the electric current value measured by the ammeter 5 in the sludge tank 10 increases. The control unit 4 calculates the accumulated power generation amount by integrating the current value in a state where the current changes with the elapsed time as shown in FIG. 12 with the elapsed time (step ST4 in FIG. 11).

  Next, the control unit 4 shown in FIG. 1 determines whether or not the calculated cumulative power generation value is less than a predetermined power amount set in advance (step ST5 in FIG. 11). When it is determined that the value of the accumulated power generation amount is equal to or greater than the predetermined power amount set in advance (step ST5: No), the control unit 4 proceeds to step ST6. On the other hand, when the control unit 4 determines in step ST5 that the value of the cumulative power generation amount is less than the preset predetermined power amount (step ST5: Yes), the process proceeds to step ST2 where the value of the cumulative power generation amount is determined. The processes in steps ST2 to ST4 are repeated until the predetermined amount of power set in advance is reached. Note that the predetermined value of the accumulated power generation amount corresponds to the area of the portion indicated by the oblique lines shown in FIG.

  In step ST6 shown in FIG. 11, the control unit 4 controls the sludge discharge valve 14 to perform an opening operation, whereby a part of sludge constituting the sludge layer 11a from the lower part of the sludge tank 10, specifically, For example, about 1/4 of the sludge of the sludge layer 11a is extracted as concentrated sludge and discharged. The details of the amount of concentrated sludge discharged will be described later. The discharged concentrated sludge is supplied to the subsequent dewatering device 2 and dehydrated.

  Next, after the control unit 4 controls the sludge discharge valve 14 to perform the closing operation, the sludge is introduced into the sludge layer 11a from the upper part of the sludge tank 10 through the introduction pipe 10a (step ST7 in FIG. 11). The amount of sludge input at this time is set to be approximately the same as the amount of sludge discharged as concentrated sludge. After the sludge is introduced, the control unit 4 controls the motor 16b to operate the swing mixer 16. As a result, when the sludge is initially charged, the sludge is gently stirred to such an extent that the two-layer structure can be maintained without destroying the interface between the sludge tank 11a and the supernatant layer 11b. Then, the newly introduced sludge is mixed with the sludge already deposited on the bottom of the sludge tank 10, and the sludge is homogenized in the sludge layer 11a. Thereby, the sludge containing microorganisms that contact the surface of the anode electrode 12 and contribute to power generation is homogenized.

  And when partial replacement | exchange of sludge is performed by the discharge | emission of a part of the above concentrated sludge, and the injection | throwing-in of new sludge, as shown in FIG. 12, power generation amount will fall rapidly. Thereafter, the current generated by the presence of the microorganism increases with time. By such partial replacement of sludge, power generation by microorganisms is continued in the sludge layer 11a of the sludge tank 10.

  After the homogenization of the sludge in the sludge layer 11a is completed in step ST8, the control by the control unit 4 returns to step ST2, and the processes of steps ST2 to ST8 are sequentially repeated. As described above, the sludge reforming process according to the embodiment of the present invention is executed.

  In the above sludge reforming process, the predetermined value of the accumulated power generation amount after the partial replacement of the sludge until the next partial replacement of the sludge is determined as follows. That is, first, the sludge reforming coefficient is calculated in advance for each sludge treatment system 1 and each kind of sludge by the above-described experiment or the like. Specifically, the amount of improvement (reformation amount) (mL) of the filter paper filtration amount described above, and the cumulative power generation amount (mA · day) corresponding to the modification amount, for each sludge treatment system 1 and each type of sludge, Measure in advance.

Then, the sludge reforming coefficient is calculated for each sludge treatment system 1 and each sludge type from the following equation (3), and stored in a predetermined recording area of the control unit 4.
Sludge reforming coefficient = improvement amount of filter paper filtration (reforming amount) (mL) / cumulative power generation (mA / day) (3)
In this embodiment, the sludge to be treated has a sludge reforming coefficient of, for example, 0.08 mL / mA · day.

Next, in the sludge treatment system 1 including the sludge tank 10 and the dewatering device 2, a reforming amount (hereinafter referred to as an optimal reforming amount) is calculated so that the total amount of power used is minimized. Based on the following equation (4) obtained by modifying equation (3) from the sludge reforming coefficient calculated as described above, a predetermined value of the accumulated power generation amount that triggers partial replacement of sludge by the control unit 4 is obtained. Calculated.
Predetermined value of accumulated power generation amount = optimum reforming amount (mL) / sludge reforming coefficient (mL / mA · day) (4)

  Then, based on the elapsed time dependency of the power generation amount by microorganisms in the sludge shown in FIG. 12, the sludge discharge valve 14 and the amount of sludge to be input by the control unit 4 for each predetermined value of the cumulative power generation amount calculated as described above. By controlling, the partial replacement of sludge is controlled.

  According to the sludge treatment system and the sludge reforming method according to the embodiment described above, it is optimal to minimize the amount of power used in consideration of the amount of power used by the sludge layer 10 and the subsequent dewatering device 2. A reforming amount is calculated, a predetermined value of the cumulative power generation amount is calculated based on the optimum reforming amount, and a value obtained by integrating the measurement value of the ammeter 5 of the sludge treatment system 1 with the elapsed time is a predetermined value of the cumulative power generation amount. By partially replacing the sludge every time, the sludge can be efficiently reformed in consideration of the efficiency of the equipment such as the subsequent dewatering device 2 and the incinerator 3. .

  Although one embodiment of the present invention has been specifically described above, the present invention is not limited to the above-described embodiment, and various modifications based on the technical idea of the present invention are possible. For example, the numerical values given in the above-described embodiment are merely examples, and different numerical values may be used as necessary.

  In the above-described method for determining the predetermined value of the accumulated current generation, the reforming amount is calculated so that the total amount of power used by the sludge treatment system 1 and the dewatering device 2 is minimized. The amount of reforming may be calculated so that the total cost of adding the amount of coagulant used in the dehydrator 2, the cost due to the amount of power used, and the cost due to the amount of coagulant added is minimized. The reforming amount may be calculated so that the total amount of carbon dioxide to be discharged is minimized. Further, not only the sludge treatment system 1 and the dehydrator 2 but also the amount of power used, the cost, or the amount of carbon dioxide discharged from the incinerator 3 can be included in the calculation of the reforming amount. Further, the amount of electric power used, the cost, the amount of carbon dioxide discharged, or the like of the equipment downstream from the incinerator 3 may be included in the calculation of the reforming amount.

DESCRIPTION OF SYMBOLS 1 Sludge treatment system 2 Dehydrator 3 Combustion furnace 4 Control part 5 Ammeter 10 Sludge tank 10a Input pipe 11a, 23a Sludge layer 11b, 23b Supernatant liquid layer 12, 24 Anode electrode 13, 25 Cathode electrode 14 Sludge discharge valve 15 Scratch Axis 15a Shaft 15b, 16b Motor 16 Swing mixer 16a Swivel strut 20 Sludge reformer 21 Sludge storage tank 21a Scraper 22 Upper lid 26 Monitoring unit

Claims (6)

Two layers of a liquid, an organic substance, and sludge containing an electron-donating microorganism that decomposes the organic substance and emits electrons, and a liquid layer mainly occupied by the liquid and a sludge layer mainly occupied by the sludge at the time of storage A tank to maintain,
An anode electrode that is at least partially embedded in the sludge layer and is supplied with electrons from the electron-donating microorganism;
A cathode electrode that is electrically connected to the anode electrode and that is placed so that at least a portion is immersed in the supernatant layer;
Sludge replacement means for discharging sludge from the sludge layer and charging the sludge into the sludge layer;
Current measuring means for measuring a current flowing between the anode electrode and the cathode electrode;
Control means for controlling the sludge replacement means to replace at least a part of the sludge of the sludge layer, based on the measured value of the current,
With
A sludge reforming device for reforming the sludge by allowing electrons supplied from the electron donating microorganisms to flow between the cathode electrode and the anode electrode ;
The control means calculates a cumulative power amount by accumulating the current value flowing between the cathode electrode and the anode electrode supplied from the current measuring means over time, and the cumulative power amount is equal to or greater than a predetermined value. When it becomes, the control to replace at least a part of the sludge by the sludge replacement means,
The predetermined value is determined on the basis of the correlation between the sludge reforming amount and the accumulated power amount, which is an improvement in the amount of filtered paper filtered water of the sludge, and the predetermined sludge reforming amount,
The predetermined amount of sludge reforming is determined based on the total power consumption of the sludge reforming device and the subsequent dewatering device, the amount of flocculant added by the dewatering device, or the cost and the dewatering by the total power consumption. A sludge reforming apparatus characterized in that the total cost of flocculants added by the apparatus is set to a sludge reforming amount that minimizes the sludge reforming amount . The sludge homogenizing means for homogenizing the sludge in the sludge layer while maintaining the two layers of the sludge layer and the supernatant liquid layer is further provided, and the control means is a sludge in the sludge layer by the sludge replacement means at least part of the post-replacement, sludge reforming apparatus according to claim 1, by controlling the sludge homogenizing means, characterized in that to homogenize the sludge in the sludge layer. The sludge reforming apparatus according to claim 1 or 2 , wherein the cathode electrode is installed such that a part of the cathode electrode is exposed on a liquid surface of the liquid. A sludge reforming method using a sludge reformer having a tank, an anode electrode and a cathode electrode,
A liquid, an organic substance, and a sludge containing an electron-donating microorganism that decomposes the organic substance and emits electrons, are stored in the tank; a supernatant liquid layer mainly occupied by the liquid at the time of storage; a sludge layer mainly occupied by the sludge; A sludge treatment step that maintains two layers of
Together with at least a part is installed is buried in the sludge layer, and the anode electrode where electrons supplied from the electron donor microorganism, along with and is electrically connected to the anode electrode, at least said portion sludge reforming step of reforming the sludge by flowing electrons supplied from the electron-donating microorganism between the cathode electrode installed is so immersed in the supernatant layer,
Sludge replacement step for discharging sludge from the sludge layer and feeding sludge into the sludge layer;
A current measurement step for measuring a current value flowing between the anode electrode and the cathode electrode;
Based on the measured value of the current, a control step for controlling sludge replacement means for replacing sludge so as to replace at least part of the sludge of the sludge layer,
The A including sludge modification method,
In the control step,
The accumulated electric energy is calculated by accumulating the value of the current flowing between the cathode electrode and the anode electrode over time, and when the accumulated electric energy exceeds a predetermined value, the sludge replacement means removes the sludge. At least a part of the control
The predetermined value is determined on the basis of the correlation between the sludge reforming amount and the accumulated power amount, which is an improvement in the amount of filtered paper filtered water of the sludge, and the predetermined sludge reforming amount,
The predetermined amount of sludge reforming is determined based on the total power consumption of the sludge reforming device and the subsequent dewatering device, the amount of flocculant added by the dewatering device, or the cost and the dewatering by the total power consumption. A sludge reforming method characterized in that the total cost of the flocculant added in the apparatus is set to a sludge reforming amount that minimizes the total cost . A control device for controlling a sludge reforming apparatus having a tank, an anode electrode, a cathode electrode, and sludge replacement means,
Two layers of a liquid, an organic substance, and sludge containing an electron-donating microorganism that decomposes the organic substance and emits electrons, and a liquid layer mainly occupied by the liquid and a sludge layer mainly occupied by the sludge at the time of storage provided in the tank to maintain, at least the anode electrode partially electrons from the electron-donating microorganism with are installed is buried in the sludge layer is supplied, electrically connected to the anode electrode and the cathode electrode at least partially with and is installed so as to dip into the supernatant layer, said by flowing electrons supplied from the electron-donating microorganism between the cathode electrode and the anode electrode Sludge replacement means for discharging sludge from the sludge layer and feeding the sludge into the sludge layer after reforming at least a part of the sludge,
A control device that controls to replace at least a part of the sludge of the sludge layer based on a current value flowing between the anode electrode and the cathode electrode ,
The accumulated electric energy is calculated by accumulating the value of the current flowing between the cathode electrode and the anode electrode over time, and when the accumulated electric energy exceeds a predetermined value, the sludge replacement means removes the sludge. At least a part of the control
The predetermined value is determined on the basis of the correlation between the sludge reforming amount and the accumulated power amount, which is an improvement in the amount of filtered paper filtered water of the sludge, and the predetermined sludge reforming amount,
The predetermined amount of sludge reforming is determined based on the total power consumption of the sludge reforming device and the subsequent dewatering device, the amount of flocculant added by the dewatering device, or the cost and the dewatering by the total power consumption. A control apparatus for a sludge reforming apparatus, characterized in that the total cost of the flocculant added by the apparatus is set to a sludge reforming amount that minimizes the total cost . A control method for controlling a sludge reforming apparatus having a tank, an anode electrode and a cathode electrode,
A liquid, an organic substance, and a sludge containing an electron-donating microorganism that decomposes the organic substance and emits electrons in the tank; a supernatant layer mainly occupied by the liquid at the time of storage; a sludge layer mainly occupied by the sludge; while maintaining the two layers of, along with are installed at least partially be buried in the sludge layer, the anode electrode is electrically connected to the anode electrode where electrons supplied from the electron-donating microorganism together are, when modifying the sludge by electron at least part of which is supplied from the electron-donating microorganism between the cathode electrode being disposed so as to dip into the supernatant layer flows, the A current measurement step for measuring a current value flowing between the anode electrode and the cathode electrode;
Based on the measured current value in the current measuring step, the sludge replacement means for replacing the sludge is controlled so as to replace at least a part of the sludge in the sludge layer, and the sludge discharge from the sludge layer and A control step for controlling the introduction of sludge into the sludge layer;
The A including control method,
In the control step,
The accumulated electric energy is calculated by accumulating the value of the current flowing between the cathode electrode and the anode electrode over time, and when the accumulated electric energy exceeds a predetermined value, the sludge replacement means removes the sludge. At least a part of the control
The predetermined value is determined on the basis of the correlation between the sludge reforming amount and the accumulated power amount, which is an improvement in the amount of filtered paper filtered water of the sludge, and the predetermined sludge reforming amount,
The predetermined amount of sludge reforming is determined based on the total power consumption of the sludge reforming device and the subsequent dewatering device, the amount of flocculant added by the dewatering device, or the cost and the dewatering by the total power consumption. A control method for a sludge reforming apparatus, characterized in that a total cost obtained by adding up the costs of flocculants added by the apparatus is set to a sludge reforming amount that minimizes the sludge reforming amount .

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