JP6361041B2 - Circulating biohydrogen production facility using biomass - Google Patents

Description

The present invention relates to a circulating biohydrogen production facility that uses biomass such as woody biomass, which is a renewable resource, as a raw material.

A conventional representative method for producing biohydrogen has been a method in which organic matter such as biomass is subjected to hydrogen fermentation using microorganisms. (For example, see Document 1 and Document 2)

However, in conventional biohydrogen production, the efficiency of hydrogen production from organic acids using photosynthetic bacteria, which is indispensable in the final stage of microbial treatment, is low, and the energy conversion efficiency is far inferior to bioethanol. The development of the hydrogen production process using organic acids has been an issue.

Under such circumstances, Logan et al. At the University of Pennsylvania have a hydrogen production yield of 3.65 mol H in hydrogen production using a microbial electrolysis cell (synonymous with a microbial electrolysis cell, hereinafter referred to as a microbial electrolysis cell) using acetic acid as a substrate. ₂ / mol acetate, a hydrogen production rate of 46 mL / L / h was reported, and a great response was received (Reference 3).

The results of Logan et al. Strongly suggest that hydrogen production from woody biomass may exceed the efficiency of bioethanol as an energy production efficiency by using a system that combines a hydrogen fermentation process and a microbial electrolysis cell ( Reference 4).

However, in the microbial electrolysis cell of Logan et al., Since a platinum catalyst electrode is used as a hydrogen generation electrode, there has been a problem in terms of cost when deployed to an actual plant.

At present, biohydrogen lags behind deployment in actual plants compared to bioethanol, but hydrogen can be converted into electric energy in combination with fuel cells, so it can be used for electric vehicles and power generation. There is great expectation as a new renewable energy, and there has been a demand for the development of biohydrogen production technology that can be applied to actual plants that achieve energy conversion efficiency equivalent to or higher than that of bioethanol.

“Asian Biomass Handbook -Guide for Utilization of Biomass-” “Asia 2007 Environmental Conservation Agricultural Partnership Support Project (Commissioned by Ministry of Agriculture, Forestry and Fisheries)” Japan Society of Energy Editorial Board Chair Shinya Yokoyama (University of Tokyo) Yukihiko Matsumura (Hiroshima University Graduate School) W. M. Alalayah et al .: “Bio-Hydrogen Production Using a Two-Stage Fermentation Process”, Pakistan Journal of Biological Sciences, 12 (22), 1462-1467 (2009). S. Cheng and B. E. Logan: “Sustainable and efficient biohydrogen production via electrohydrogenesis”, Proc. Natl. Acad. Sci. USA, 104, 18871-18873 (2007). P.-C. Maness et al .: “Fermentation and Electrohydrogenic Approaches to Hydrogen Production”, DOE Hydrogen Program FY 2010 Annual Progress Report.

The conventional biohydrogen production method is a method in which organic matter such as biomass is fermented using microorganisms, but the efficiency of hydrogen production from organic acids using photosynthetic bacteria, which is indispensable in the final stage of microbial treatment, is high. Low, improvement of hydrogen production yield and hydrogen production rate of hydrogen production process using organic acid has been a technical issue.

The efficiency of hydrogen production processes using organic acids can be improved by using a microbial electrolysis cell with a structure in which an electrode on which microorganisms such as G. sulfurreducens capable of assimilating organic acids are immobilized is used as an anode and a hydrogen catalyst electrode as a cathode. This can be achieved by using a solution containing an acid as an electron donor for the anode. However, in conventional microbial electrolysis cells, carbon or the like is used as an anode for immobilizing microorganisms, so that electrons of immobilized microorganisms such as Geobacter sulfurreducen are used. Electron transfer coupling between the reductant metabolized by the transfer system and immobilized microorganisms such as G. sulfurreducens and the anode is not formed efficiently, and a large potential barrier is formed between the electrode and the efficiency is low. It was a thing.

Moreover, in the conventional microbial electrolysis cell, since a platinum catalyst electrode is used as a hydrogen generation electrode, there has been a problem in terms of cost in developing to an actual plant.

Therefore, the present invention solves the above-mentioned problems, and has a catalytic function for a plurality of reactions at the anode of a microbial electrolysis cell, and the surface is subjected to electrolytic oxidation of carbon in an ammonium carbamate solution to form nitrogen functional groups such as amino groups on the surface. By using a catalyst electrode (aminated carbon electrode) into which a catalyst is introduced to construct a novel microbial electrolysis cell, the electron transfer system of immobilized microorganisms such as G. sulfurreducens and the reduction produced by immobilized microorganisms such as G. sulfurreducens are metabolized. It is important to form an electron transfer coupling between the body and the anode efficiently, and to dramatically improve the hydrogen production yield and hydrogen production rate compared with the hydrogen conversion of organic acids using photosynthetic bacteria. One purpose.

In addition, the present invention solves the above-mentioned problems, and a novel microorganism using an electrolytically modified carbon electrode (platinum complex / aminated carbon electrode) having a hydrogen generation catalytic ability instead of a platinum catalyst electrode as a cathode of a microorganism electrolysis cell. By constructing an electrolysis cell, it is possible to overcome the cost problems and dramatically improve the hydrogen production yield and hydrogen production rate compared to hydrogen conversion of organic acids using photosynthetic bacteria. It is intended.

Further, the present invention solves the above-mentioned problem, and combines the hydrogen production by microorganisms capable of decomposing cellulose and the hydrogen production by microbial electrolysis cells, thereby using a recyclable type using renewable resources such as woody biomass as a raw material. The third purpose is to realize a biohydrogen production facility.

The present invention achieves the above first object as follows. The invention according to claim 1 uses a catalyst electrode (aminated carbon electrode) in which a nitrogen-containing functional group such as an amino group is introduced on the surface by electrolytic oxidation of carbon in an ammonium carbamate solution as an anode of a microbial electrolysis cell. In addition, an electrolytically modified carbon electrode (platinum complex / aminated carbon electrode) having a hydrogen generation catalytic ability is used for the cathode.

The above-mentioned electrolytically modified aminated carbon electrode has a nitrogen-containing functional group or a nitrogen-containing structure such as a structure in which an amino group or pyridine is substituted on a carbon atom on the surface of carbon, and a carbon atom in the carbon structure is substituted with a nitrogen atom. It is known that it has catalysis of many kinds of chemical reactions. This aminated carbon electrode is produced by electrolytic oxidation of carbon in an ammonium carbamate solution.

Moreover, the electrolytically modified carbon electrode used for the hydrogen generation electrode (cathode) is produced by subjecting the aminated carbon electrode to an electrolytic reduction treatment in a strong acid such as sulfuric acid. In this electrolytic reduction process, a small amount of platinum used as the counter electrode elutes in sulfuric acid at the atomic ion level, and it is intermolecular with the nitrogen-containing functional groups such as multiple amino groups and imino groups on the aminated carbon electrode surface. A platinum complex is formed by the interaction. Thereby, the hydrogen generation catalytic action can be realized with a very small amount of platinum.

The present invention also achieves the above third object as follows. A circulatory hydrogen production facility is realized by using the microbial electrolysis cell according to claim 1 and the organic material supplied to the anode using the treated biomass as a renewable resource according to claim 2. It is.

The method for treating biomass uses the three types of methods described in claim 3 and, as appropriate, produces biohydrogen from biomass by a method that optimally combines these three types of methods. The organic acid, which is the main component, is converted to hydrogen using a microbial electrolysis cell. This organic acid is supplied to the anode of the microbial electrolysis cell, and hydrogen is generated at the cathode.

As described in claim 4, the extraction liquid component or organic acid composed of saccharides, organic acid, etc., produced by the high-temperature high-pressure water treatment of the woody biomass is converted into hydrogen by the microbial electrolysis cell.

The insoluble components (mostly cellulose components, including some lignin-decomposing components) that cannot be converted into solubilized components of sugar and organic acid by high-temperature and high-pressure water treatment of woody biomass have cellulase activity as described in claim 3. Use as a substrate for the anode of a microbial electrolysis cell by converting it into a fermentation broth containing hydrogen and organic acids as the main components using hydrogen-producing microorganisms, or by solubilizing it as a sugar by treatment with cellulolytic enzyme Is possible.

According to the present invention, hydrogen is generated by a novel system in which a microbial hydrogen fermentation and a microbial electrolysis cell using an electrolytically modified carbon electrode as an anode and a cathode are combined using a renewable resource such as woody biomass as a raw material. The yield and hydrogen production rate were dramatically improved, enabling a recycling hydrogen production facility that produces biohydrogen with higher energy conversion efficiency than bioethanol.

As described above, in the present invention, biomass hydrogen fermentation and microbial electrolytic cell treatment, in the case of woody biomass, physicochemical means for converting biomass to organic matter, microbial means for hydrogen fermentation of organic matter, and cellulose By combining biochemical means using cellulolytic enzymes to break down water into soluble organic matter and optimizing each processing process, biohydrogen production with higher energy conversion efficiency than bioethanol is realized. There is an effect that can be done.

Furthermore, the use of an electrolytically modified carbon electrode (platinum complex / aminated carbon electrode) as a hydrogen generation electrode in a microbial electrolysis cell eliminates the need for an expensive platinum catalyst electrode, which is essential for actual plant development. Effective cost overcoming problems.

Furthermore, by connecting the circulating biohydrogen production facility of the present invention with a fuel cell power generation system, there is an effect that natural energy power generation using a renewable resource called biomass becomes possible.

Furthermore, it is possible to effectively utilize the thermal energy in the integrated facility by integrating the heat and power generation between the electricity and thermal cogeneration facility using woody biomass and the circulating biohydrogen production facility using woody biomass. effective.

The configuration of the present invention will be described below with reference to the drawings.

The aminated carbon electrode was produced by the following production process using carbon felt (GF-20-5FB manufactured by Nippon Carbon Co., Ltd.) as a starting material.
<Carbon felt wettability improvement treatment>
(1) Immerse in 95% EtOH solution Stir with a stirrer (about 30 minutes)
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(2) Hold the felt with your finger and call for 95% EtOH into the pores in the felt
↓
(3) Transfer to ion exchange water
↓
(4) Hold the felt with your finger to draw ion exchange water into the pores in the felt
↓
(5) Evacuate in a vial bottle with a butyl rubber stopper to prevent generation of bubbles
↓
<Amination electrolytic modification treatment>
(6) Separately prepare 0.1M ammonium carbamate phosphate buffer solution, soak the felt that has been hydrophilized in the process up to (5) in 0.1M ammonium carbamate phosphate buffer solution, and hold the felt with your finger. The ammonium carbamate solution into the pores of the felt.
↓
(7) Using a potentiostat, with the carbon felt as the working electrode in the state after the treatment of (6) above, +1.1 V is applied with reference to the Ag / AgCl reference electrode, and a constant potential electrolytic oxidation treatment is performed for 2 hours.
↓
(8) (7) Transfer the treated electrolytically modified carbon felt into ion-exchanged water, stir with stirring (overnight) to remove the ammonium carbamate remaining in the pores of the carbon felt and use ion-exchanged water. Replace
As described above, an aminated carbon electrode was produced by the operations (1) to (8).

The production process of the platinum complex / aminated carbon electrode is as follows. By electroreducing the aminated carbon electrode with a potentiostat or galvanostat for 5 to 50 hours in a 0.1 to 2 mol sulfuric acid or nitric acid solution with the aminated carbon electrode as the working electrode and the platinum electrode as the counter electrode The platinum used for the counter electrode elutes in a very small amount at the atomic ion level in the sulfuric acid or nitric acid solution. Between the eluted platinum ions and nitrogen-containing functional groups such as amino groups and imino groups present on the aminated carbon electrode surface. Due to the intermolecular interaction, a platinum complex is formed on the electrode surface. As a result, a platinum complex / aminated carbon electrode capable of realizing a hydrogen generation catalytic action with a very small amount of platinum is produced.

Preparation of the microorganism-immobilized / aminated carbon electrode is as follows.
(1) The microorganism G. sulfurreducens is a kind of iron-reducing bacteria classified as gram-negative anaerobic bacilli, so the ATCC51573 inoculum is mixed gas (CO2 (20%) / N2 (80%) in an anaerobic culture tube) ) 10ml of ATCC # 1957Broth (containing sodium fumarate as electron acceptor) in the atmosphere under static conditions at 29 ℃ constant temperature for 10 days, with orange / pink diameter of about 1mmφ or less on the bottom and side walls of the test tube Get a colony. This is suspended with a shaker to prepare a microorganism culture solution.
(2) An electrolyte solution containing the following components is prepared as an electrolyte solution of a microbial electrolysis cell.
Concentration of components in 1 liter electrolyte solution: 0.25 g NH4Cl, 0.1 g KCl, 10 mL, vitamins, and 10 mL minerals, 0.6 g NaH2PO4, 2.5 g / L NaHCO3 (pH = 7)
(3) The electrolytic solution prepared in (2) was sealed in an electrolytic cell using an aminated carbon electrode as the anode and a platinum complex / aminated carbon electrode as the cathode, and sodium acetate (1 g / liter as the substrate for the anode chamber) ), And the gas phase of the microbial electrolysis cell is replaced with a gas mixture of CO2 (20%) / N2 (80%), and the culture suspension of G. sulfurreducens obtained in (1) is used as the amount of electrolyte. 5% volume (0.5 ml culture solution / 10 ml electrolyte solution) is added to the anode chamber, DC 0.7 V is applied, and it is allowed to stand in a 29 ° C. constant temperature bath.
(4) Since the operation in (3) can be regarded as culturing of microorganism G. sulfurreducens using the anode as an electron acceptor, G. sulfurreducens is immobilized on the aminated carbon electrode as the anode with the elapse of time after application of DC 0.7V. Is done. The progress of the microbial immobilization reaction can be monitored by the current value flowing through the electrolytic cell.
(5) The current flowing in the electrolytic cell hardly flows for several days, and the current starts flowing after several days. When acetic acid as a substrate is consumed, the current value converges to zero, and the microbial immobilization reaction ends. .

Immobilization of G. sulfurreducens on the anode surface is known to form a biofilm with a thickness of several tens of μm that has electrical conductivity and storage capacity. It has been suggested that nanowires are involved. In addition, cytochrome c, OmcZ, is localized at high density on the contact surface between the biofilm and the electrode, suggesting that OmcZ has a function of promoting electron transfer from the biofilm to the electrode.

FIG. 1 is a schematic diagram of a cell configuration and electrode electron transfer reaction of a microbial electrolysis cell according to the present invention.

The amination modified carbon electrode according to the present invention was used for the anode of the microbial electrolysis cell, and the electrolytic modification carbon electrode according to the present invention was used for the cathode.

Electrogenic bacteria capable of electron transfer with the electrode were immobilized on the anode. Various microorganisms are known as electrogenic bacteria. Here, Geobacter sulfurreducens, which is a typical electrogenic bacterium, was used.

As the substrate serving as the electron donor for the anode of the microbial electrolysis cell, a wide variety of organic substances can be used as long as the organic substances can be assimilated by Electrogenic bacteria. A mixed solution of the high-temperature and high-pressure water treatment extract (A, B) was used, and the organic component concentration of the electrolyte derived from the woody biomass of the anode chamber was 0.96 mg / l.
(1) Wood flour slurry (20wt%) 50mg treated at 5.5MPa; 190 ° C for 10min ↓
(2) Extract (A) (14.5 ml; pH 4.1) + Filtration residue (C) (28.3 g)
(Separate experiment: dry weight of filtration residue (C): 6.54 g (drying treatment: 80 ° C. 13 hr + vacuum drying 8 hr)
◎ Second step
(3) Wood flour slurry (filtered residue (C) (28.3 g) + ion-exchanged water (21.7 g))
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(4) High-temperature and high-pressure water treatment (260 ℃ 7.5MPa 60min)
With the combination of autoclave and heater used in the experiment, the set temperature could be controlled, but due to the heat capacity of the experimental system (autoclave and aluminum heater), it was difficult to control the temperature rise time and temperature drop time, and the processing conditions were averaged. 7.5 MPa; treatment at 260 ° C. for 60 minutes.
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(5) Extract (B) (37 ml; pH 2.7) + Filtration residue (D)
Dry weight of residual filtration (D): 3.74 g (drying process: 80 ° C. 13 hr + vacuum drying 8 hr)

FIG. 2 shows changes over time in the electrical characteristics (cell current and cathode potential) of the microbial electrolysis cell from the start time point to 40 hours later when 0.7 V is applied to the microbial electrolysis cell as a power supply voltage. For comparison, the electrical characteristics are shown when a pure acetic acid solution (1 g / l) is used as the anode electrolyte as a representative example of the organic acid generated by the high-temperature and high-pressure treatment.
From the cyclic voltammogram of the electrolytically modified carbon felt electrode used as the cathode, hydrogen generation started at a cathode potential of -650 mV (vs. Ag / Agcl), and at -900 mV, the hydrogen generation activation energy was sufficiently exceeded to the cathode. Found that hydrogen was generated.
In the evaluation of hydrogen generation, first, from the holding time of TCD measurement using Molecular Sieve as a column carrier using a reference hydrogen gas (room temperature 25 ° C., 1 atm), it was identified that the gas component generated in the cathode chamber was hydrogen. . The concentration of organic components extracted from woody biomass in the electrolyte supplied to the anode chamber is 0.96 g / l. From this, a value of 52 ml / l / h was obtained as the average hydrogen production rate from the start of voltage application to 40 hours later. On the other hand, the acetic acid concentration was 1 g / l, and an average hydrogen production rate of 25 ml / l / h was obtained.
The hydrogen production rate should be based on the surface area of the electrode, but since the experimental system uses a carbon felt electrode, it is not measured in units as a strict production rate at this stage. Since the above value is an average speed of 40 hours, the maximum speed can be estimated to be about 2 to 3 times the above value. When acetic acid is used as the electrolyte, the average hydrogen production rate is reported. In the case of hydrogen production from acetic acid using photosynthesis bacteria, there is a report that the hydrogen production rate is 6.5 ml / l / h. Compared with, the hydrogen production rate using the newly developed microbial electrolysis cell is about an order of magnitude faster than when using photosynthetic bacteria.
The conversion efficiency per weight from woody biomass extract (electrolyte 8ml) to hydrogen is 1350ml / g in 40 hours after applying voltage of 0.7V, reported value in the case of glucose hydrogen fermentation (about 300ml / g) More than 4 times higher value was obtained. The woody biomass extract is composed of many kinds of organic components such as C5 sugar-derived components, C6 sugar-derived components, and organic acids, and the molar concentration of each component has not been evaluated, so the molar conversion efficiency has not been evaluated. The conversion efficiency per weight of acetic acid to hydrogen was 650 ml / g in 40 hours after applying a voltage of 0.7V. The space volume of the cathode gas phase part of the microbial electrolysis cell is about 12 ml, and CO2 / N2 (20:80) gas is substituted at the start of the experiment. Therefore, if acetic acid is converted to 100% hydrogen, the amount of hydrogen produced by the microbial electrolysis cell is 0.39 times the gas chroma signal intensity of 1 atm of pure hydrogen. The experimental result was 0.26 times the gas chromatographic signal intensity of 1 atm of pure hydrogen, and the energy conversion efficiency in 67 hours after the application of electrolysis was determined to be 67%. Logan et al. Of the University of Pennsylvania have reported energy conversion efficiencies exceeding 90% with 0.6V applied. Since our energy conversion efficiency is a value 40 hours after voltage application, it is in the middle of hydrogen generation, and the actual energy conversion efficiency is even higher, but we are aware of the actual plant operating conditions. Assessed after 40 hours. Since the experimental conditions of Logan et al. Are not accurately understood, quantitative comparison of energy conversion efficiency is difficult. The reason why the hydrogen production rate and the weight conversion efficiency of the woody biomass extract as the electron donor for the anode is about twice that of the case where acetic acid is used as the electron donor is that the woody biomass extract contains acetic acid. However, because other components include sugars such as glucose and xylose which are higher energy compounds than acetic acid and their oligosaccharides, the rate of hydrogen generation is increased.

FIG. 3 shows a representative example of the entire process of a circulating biohydrogen production facility and a power generation facility using woody biomass as a raw material.

Extracted liquid components produced by high-temperature, high-pressure water treatment in a circulating biohydrogen production facility are hemicellulose and cellulose degradation products, c5 sugars such as xylose and oligosaccharides thereof, and C6 sugars such as glucose and mannose. And its oligosaccharides. This extracted liquid component is used as a substrate for the anode chamber of the microbial electrolysis cell to produce biohydrogen. On the other hand, the solid component remaining after the high-temperature and high-pressure treatment is cellulose. In order to use the solid components produced by this high-temperature and high-pressure water treatment as a substrate for hydrogen fermentation, it is insoluble by using hydrogen-producing bacteria (such as Costridium thermocellum and Thermoanaerobacterium thermosaccharolyticum) that have enzymes that degrade cellulose. Cellulose is saccharified and biohydrogen is produced by subsequent hydrogen fermentation. Organic acids such as acetic acid and lactic acid contained in the fermentation liquid after hydrogen fermentation are supplied as an electron donor for the anode of the microbial electrolysis cell, and biohydrogen is produced from the cathode.
The treatment conditions of Step 1 of the high temperature / high pressure water treatment are 140 to 230 ° C. and 0.1 to 10 MPa, and the treatment conditions of the high temperature / high pressure water treatment Step 2 are 230 to 270 ° C. and 0.1 to 10 MPa. Temperature and pressure conditions. The treatment time for high temperature / high pressure water treatment is in the range of 2-60 minutes.
The biohydrogen produced in this way is stored or supplied online to the fuel cell power generation system, and as a whole system, circulating natural energy power generation using biomass is realized.

Fig. 4 shows the high-temperature and high-pressure water treatment process flow and thermal energy flow (black arrows) when the circulating biohydrogen production facility is in thermal cooperation with an electric / thermal cogeneration facility that uses woody biomass as a raw material. .

As shown in the figure, in a circulating biohydrogen production facility, there is a process of treating raw materials at high temperature and high pressure water, and a large amount of heat energy is required. This thermal energy is supplied by the flow of hot water from heat exchangers A and B as indicated by the black arrows in the figure. Since the required temperature conditions are different in each process of the circulating biohydrogen production facility, the flow of high-temperature water is not shown in the figure, but a predetermined temperature required in each process by the temperature controller. Supplied by adjusting the temperature.

In the figure, soluble component 1 is mainly a hemicellulose degradation product, insoluble component 1 is mainly cellulose and lignin, soluble component 2 is mainly a cellulose degradation product, and insoluble component 2 is mainly Cellulose and lignin.

The figure shows the process of wood biomass in the circulating biohydrogen production facility that is largely related to the thermal cooperation with the electric / thermal cogeneration facility. There are a plurality of hydrogen fermentation facilities that require this heat, and the heat energy required in these facilities is supplied by high-temperature water indicated by black arrows in the figure. The high-temperature water supplied in this way is used after being adjusted to a predetermined temperature by a temperature controller.

Electrode Electron Transfer Reaction Using Microbial Electrolyzer Configuration and Woody Biomass Extract Component (Sugars and Organic Acids as Main Components) as an Anode Substrate Showing an Embodiment of the Present Invention Changes over time of microbial electrolysis cell electrical characteristics showing an embodiment of the present invention (a) When woody biomass extract (0.96 g / l) is used as electrolyte (b) Acetic acid (1 g / l) is used as electrolyte Case Overall configuration diagram of the recycling biohydrogen production facility and power generation facility Thermal energy flow between an electrical / thermal cogeneration facility and a refinery facility for hydrogen production in a circulating biohydrogen production facility showing an embodiment of the present invention (black arrow)

Claims (5)

Microorganism immobilization / amino which immobilizes microorganisms that cause electron transfer to the outside of an aminated carbon electrode having nitrogen-containing functional groups such as amino groups and imino groups on the surface of the carbon electrode on the anode of an electrolytic cell that generates hydrogen A platinum complex was formed on the surface of the aminated carbon electrode in an electrolytic cell having a functional structure using an organic carbon electrode as an anode and an organic substance that can be assimilated by microorganisms in the process of energy metabolism of the microorganism . A microbial electrolytic cell characterized in that a platinum complex / aminated carbon electrode is used as a cathode . A circulation type hydrogen production facility comprising means for supplying an organic substance to be supplied to an anode of a microbial electrolytic cell according to claim 1 from biomass, and producing hydrogen from biomass. In recycling the hydrogen production facility according to claim 2, using physicochemical means for converting biomass to organic, microbiological means of organics is hydrogen fermentation, and cellulolytic enzyme to decompose and soluble organics cellulose biochemical And a circulating hydrogen production facility having means for separating and extracting organic components from biomass in which the three means are combined in combination. 4. The circulating hydrogen production facility according to claim 3, wherein the organic substance at the anode of the microbial electrolyzer is separated and extracted from the separation and extraction means using a combination of the physicochemical means, hydrogen fermentation, or cellulose-degrading enzyme. A recyclable hydrogen production facility characterized by using organic acid. A recycle-type hydrogen production facility according to claim 2 and a fuel cell power generation facility that obtains electric energy using hydrogen produced from the recycle-type hydrogen production facility as fuel , enabling CO2 emission reduction using renewable resources as a raw material recycling natural energy power generation facility, characterized in that it was.