JP2005087035A - Method for producing hydrogen with microorganism - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing hydrogen with a microorganism, by which the hydrogen useful for operating, for example, fuel batteries can profitably be produced at a practically sufficient rate substantially without accompanying the by-production of injurious CO. <P>SOLUTION: This method for producing the hydrogen with the microorganism is characterized by culturing the microorganism having a formate dehydrogenation enzyme gene and a hydrogenase gene in a formate-containing culture solution under an aerobic condition, adding a reduced state solution for producing the hydrogen to the culture solution, and then supplying an organic substrate to the solution. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a method for producing hydrogen by microorganisms, and more particularly to a highly efficient method for producing hydrogen by anaerobic microorganisms using an organic substrate as a carbon source. Hydrogen produced by the method of the present invention can be suitably used as a fuel for fuel cells and the like.

  Unlike fossil fuels, hydrogen is attracting attention as the ultimate clean energy source that does not generate substances of concern due to environmental problems such as carbon dioxide and sulfur oxides even when burned. The amount of heat per unit mass is more than three times that of petroleum, If supplied to the fuel cell, it can be converted into electric energy and heat energy with high efficiency.

Conventionally, hydrogen production has been proposed as a chemical production method, such as pyrolysis steam reforming of natural gas or naphtha. This method requires high-temperature and high-pressure reaction conditions, and since the produced synthesis gas contains CO (carbon monoxide), it is used to prevent deterioration of the fuel cell electrode catalyst when used as fuel for fuel cells. Therefore, it is necessary to perform CO removal with a high degree of technical problem resolution.
On the other hand, the biological hydrogen production method using microorganisms is a reaction condition at normal temperature and pressure, and the generated gas does not contain CO, so that removal thereof is unnecessary.
From such a viewpoint, biological hydrogen production by microorganisms is a more preferable method as a fuel supply method for fuel cells.

Despite the excellent features of biological hydrogen production methods, there has been no significant progress in fuel cell fuel supply methods so far. The productivity of hydrogen production, particularly the rate of hydrogen generation per unit volume (STY) ; Space Time Yield) is low and economically impractical.
Biological hydrogen production methods are roughly classified into a method using a photosynthetic microorganism and a method using a non-photosynthetic microorganism (mainly anaerobic microorganisms). Since the former method uses light energy for hydrogen generation, there are many practical issues that need to be solved, such as the price problem of hydrogen generators that require a large light collection area due to its low light energy utilization efficiency and the difficulty of maintenance. It ’s not the right level.

  Since the conventional hydrogen production method using the latter anaerobic microorganisms is dependent on the division and growth of these anaerobic microorganisms, the growth is extremely slow (Patent Document 1, Non-Patent Document 1), and the anaerobic microorganisms. The reason for the mitotic growth of other microorganisms has not been clarified, but the free space required for mitotic growth (proportional to the "field" or reactor volume required for culture) is greater. Because of the large need, the steady-state cell concentration that anaerobic microorganisms can reach in an anaerobic culture that is necessary for hydrogen generation is absolute compared to that of other microorganisms. For example, the hydrogen generation rate (STY) is not sufficient due to the fact that it is low, and further improvement is required in this respect.

  So far, the inventors have cultivated a microorganism having a formate dehydrogenase gene and a hydrogenase gene under aerobic conditions in Japanese Patent Application No. 2003-046095, and cultured the resulting cells under anaerobic conditions. A biological hydrogen production method was provided in which a hydrogen generation solution in a reduced state was added after culturing in, and an organic substrate was supplied to the solution. The present invention provides a more efficient method for producing biological hydrogen.

In addition, when hydrogen produced by a biological production method is supplied to a fuel cell having a certain electric capacity, a rapid response to supply of an organic substrate serving as a hydrogen source to a hydrogen generation reaction vessel and generation of electric current. Is practically necessary. With respect to this point as well, the present invention is a technique having a practically sufficient quick response.
U.S. Pat.No. 5,834,264 R. Nandi et al., Enzyme and Microbial Technology 19: 20-25, 1996

The above-mentioned problems of the conventional hydrogen production method depending on the division and growth of anaerobic microorganisms are, in other words, the acquisition of high-density anaerobic microorganisms in the hydrogen generation reactor and the hydrogen generation function of the anaerobic microorganisms. This is because we have not found a way to achieve the acquisition of
In this regard, the proposed technique (Japanese Patent Application No. 2003-046095) by the present inventors is an effective method for solving the problems of the conventional hydrogen production method using anaerobic microorganisms, but the present invention is anaerobic having a hydrogen generation function. The present invention proposes a method that can more efficiently acquire sex microorganisms.

  That is, the present invention aims to solve these technical problems relating to a method for producing hydrogen by anaerobic microorganisms, such as the problem of an insufficiently low hydrogen generation rate and anaerobic microorganisms as described in the above-mentioned US Patent Publication. To solve the problem of the method that has to depend on 200 hours of mitotic growth to reach a steady concentration, and the hydrogen generation rate is sufficiently high from the beginning of the reaction to operate the fuel cell at a practical level It provides a possible method.

  Various metabolic pathways are known for hydrogen generation in anaerobic microorganisms (hydrogen generation as a metabolite in the degradation pathway of glucose to pyruvate, and pathway in which acetic acid is generated by pyruvate through acetyl-CoA. Generation of hydrogen as a metabolite and pathway of hydrogen generation from formic acid derived from pyruvic acid). The present invention relates to a biological hydrogen production method mainly using a metabolic pathway in which hydrogen is generated from formic acid in a microbial cell.

  Conventionally, in order to express the hydrogen generation function of anaerobic microorganisms, it was thought that it was necessary to culture under anaerobic conditions to express the formate dehydrogenase gene and the hydrogenase gene. In particular, the present inventors have found that anaerobic microorganisms express a hydrogen generation function if formic acids are present even under aerobic culture conditions.

According to the present invention, it is not necessary to repeat mitotic growth that is slow in anaerobic conditions many times, and it is possible to develop hydrogen generation ability in a short period even under aerobic conditions where mitotic growth is fast. In addition, since microorganisms are cultured under aerobic conditions, it is possible to obtain microorganisms having a high-density hydrogen production ability.
If the cells are cultured in a formic acid-containing culture medium under aerobic conditions and then further cultured in a formic acid-containing culture medium under anaerobic conditions, the hydrogen generation capacity can be further improved. is there.

In addition, the fuel cell can be operated at a practical level by using the technique of the present invention.
That is, the present invention includes (1) culturing a microorganism having a formate dehydrogenase gene and a hydrogenase gene in a formic acid-containing culture solution under aerobic conditions, and then adding the solution to a hydrogen generation solution in a reduced state. A biological hydrogen production method characterized by supplying an organic substrate to
(2) The above (1), wherein the microorganism is cultured under an aerobic condition, further cultured in a formic acid-containing culture solution under an anaerobic condition, and added to the hydrogen generation solution in a reduced state. Biological hydrogen production method according to
(3) Use of hydrogen produced by the method according to any one of (1) and (2) as a fuel gas for a fuel cell,
About.

  According to the present invention, hydrogen useful for operating a fuel cell, for example, can be industrially advantageously produced at a practically sufficient speed without substantially generating harmful CO.

  The microorganism used in the present invention includes formate dehydrogenase gene (F. Zinoni, et al., Proc. Natl. Acad. Sci. USA, Vol. 83, pp4650-4654, July 1986 Biochemistry) and hydrogenase gene (R. Boehm, et al., Molecular Microbiology (1990) 4 (2), 231-243) and mainly anaerobic microorganisms.

  Examples of specific anaerobic microorganisms used in the present invention include microorganisms belonging to the genus Escherichia, such as Escherichia coli ATCC 9637, ATCC 11775, ATCC 4157, etc., microorganisms belonging to the genus Klebsiella, such as Klebsiella. pneumoniae ATCC 13883, ATCC 8044, etc.), Enterobacter microorganisms, such as Enterobacter aerogenes ATCC 13048, ATCC 29007, etc. and Clostridium microorganisms, such as Clostridium beijerinck25 .

  These anaerobic microorganisms are first cultured under aerobic conditions. In this sense, facultative anaerobic microorganisms are preferably used rather than obligate anaerobic microorganisms. Among the above microorganisms, Escherichia coli, Enterobacter aerogenes and the like are preferably used.

In the present invention, it is an essential requirement that formic acids are contained in the culture solution under aerobic conditions. Here, formic acids are substances having a chemical functional group [HCOO ⁻ ]. It is a compound selected from formic acid, zinc formate, sodium formate, potassium formate, cesium formate, nickel formate, barium formate, calcium formate, manganese formate, ammonium formate, and the like. From the viewpoint of solubility in water, formic acid, sodium formate, potassium formate, calcium formate, and ammonium formate are preferred. Furthermore, formic acid, sodium formate and ammonium formate are more preferred. Formic acids may be used alone or a mixed culture solution of plural types of formic acids may be used.

  Formic acid concentration in the formic acid-containing solution is less than 1 mM (millimolar: millimol / liter), the expression of hydrogen generation function during aerobic culture is low, and if it exceeds 300 mM, the expression of hydrogen generation function is possible. The culture time is increased because the division and growth rate is reduced. In order to express a high hydrogen generation function, the concentration is preferably 10 mM to 300 mM.

By performing division growth under aerobic conditions in a formic acid-containing culture solution, a hydrogen production function can be expressed, and at the same time, culture at a high concentration is possible.
As an aerobic cell culture method, a normal nutrient medium containing a carbon source, a nitrogen source, a mineral source and the like can be used. Examples of the carbon source include glucose, fructose, molasses, etc., and examples of the nitrogen source include inorganic nitrogen sources such as ammonia, ammonium salts, and nitrates, and organic nitrogen sources such as urea, amino acids, and proteins. Each can be used alone or in combination. Both inorganic and organic forms can be used in the same manner. Further, as the mineral source, for example, potassium monohydrogen phosphate, magnesium sulfate, etc., mainly containing K, P, Mg, S and the like can be used. In addition to these, nutrients such as various vitamins such as peptone, meat extract, yeast extract, corn steep liquor, casamino acid, biotin and thiamine can be added to the medium as necessary.

  As aerobic culture conditions, it is usually preferable to carry out the culture at a temperature of 20 ° C. to 45 ° C., preferably 25 ° C. to 40 ° C. under conditions such as aeration and stirring. The pH is preferably 5 to 10, preferably 6 to 8. It is preferable to control PH at the same time, and it is also possible to adjust PH using acid or alkali. In the temperature range and the PH range, the above range is the optimum temperature range and PH range for the microorganism. Usually, the carbon source concentration at the start of the culture is preferably 0.1 to 20% (W / V), more preferably 1 to 5% (W / V). The culture period is 0.5 to 7 days.

In order to develop a hydrogen generation function consisting of formate dehydrogenase and hydrogenase, it is preferable to contain a trace amount of metal components in the culture solution. The trace metal component varies depending on the microorganism species, and examples thereof include iron, molybdenum, selenium, and nickel. In addition, since these trace metal components may be contained to some extent in natural nutrient sources such as yeast extract, in such cases, addition is not necessarily required.
Bacteria cultured under aerobic conditions can be directly subjected to a hydrogen generation reaction under reduced conditions, but once aerobically cultured cells are separated, the cells are transferred to a reduced hydrogen generation solution. It is preferable. As a separation method, methods such as centrifugation and membrane separation can be used.

Further, it is preferable to subject the separated cells to further hydrogenation reaction after further culturing under anaerobic conditions because the ability of microorganisms to generate hydrogen can be further improved.
It is preferable that formic acids are present in the culture solution under anaerobic conditions additionally carried out, but this is not limitative. When formic acids are used, the same ones used during aerobic culture are used. The concentration of formic acid present in the culture solution under anaerobic conditions is preferably 1 to 100 mM. The presence effect of formic acids does not appear at a concentration lower than 1 mM, and the effect of carrying out at a higher concentration is not observed at a concentration higher than 100 mM.
Microorganisms divide and grow during culturing under anaerobic conditions to improve the hydrogen production ability of the cells, but a preferable change in the number of cells for mitotic growth can be determined as appropriate. Prolonged divisional growth is not efficient for obtaining cells having a hydrogen generating function, and divisional growth that is too short has no effect. The time is approximately 0.5 to 6 hours. The change in the number of cells at that time can be easily known by measuring the bacterial optical density.
A carbon source is also necessary for the microbial cell to divide and proliferate. For this, a normal carbon source such as a saccharide such as glucose, an organic acid, or an alcohol is used.

The microorganism of the present invention cultured in a formic acid-containing culture solution under aerobic conditions or additionally under anaerobic conditions is added to the hydrogen generation solution in a reduced state to supply an organic substrate. By doing so, hydrogen is generated.
The reduction state referred to here is a reduction state in which the oxidation-reduction potential of the hydrogen generating solution is defined by −100 mV (millivolt) to −500 mV (millivolt), and preferably a reduction state defined by −200 mV to −500 mV. is there. Examples of the method for realizing the reduced state of the present invention include a method of removing dissolved gas by heat treatment or reduced pressure treatment. Specifically, as a method for removing dissolved gas, particularly dissolved oxygen in the hydrogen generating solution, about 13.33 × 10 ² Pa or less, preferably about 6.67 × 10 ² Pa or less, more preferably about 4. By performing the treatment under reduced pressure of 00 × 10 ² Pa or less for about 1 to 60 minutes, preferably about 5 to 60 minutes, a hydrogen generating solution under reducing conditions can be obtained. Further, if necessary, a reducing agent can be added to the aqueous solution to adjust the reduced aqueous solution. Examples of the reducing agent used include thioglycolic acid, ascorbic acid, cysteine hydrochloride, mercaptoacetic acid, thiolacetic acid, glutathione, and sodium sulfide. It is also possible to use one of these or a combination of several types.

  The hydrogen generation method is carried out by supplying an organic substrate continuously or intermittently. As a method for supplying organic substrates, a method for directly supplying formic acids (direct supply method) or a saccharide (for example, glucose, fructose, xylose, arabinose, etc.) that is converted into formic acids in the metabolic pathway of the microbial cell. Saccharides and disaccharides such as sucrose and maltose and molasses.) (Indirect supply method). A direct supply method and an indirect supply method can be used in combination.

The supply rate of the organic substrate is not particularly limited as long as the pH of the hydrogen generating solution is controlled in the range of 5.0 to 9.0.
The reaction temperature of the hydrogen generation reaction is preferably 20 ° C. to 45 ° C., more preferably 30 ° C. to 40 ° C., although it depends on the microorganism species used.
The microbial cell concentration is carried out in the concentration range of 0.1% (w / w) to 80% (w / w) (wet state microbial mass standard). From the viewpoint of increasing the viscosity of the hydrogen generating solution, the bacterial cell concentration is preferably 0.1% (w / w) to 70% (w / w) (wet cell mass standard). More preferably, the bacterial cell concentration is 10% (w / w) to 70% (w / w) (wet cell mass standard).
In the present invention, since the hydrogen generation rate is high, it is preferable to add an antifoaming agent to the reaction solution during hydrogen generation. About an antifoamer, a well-known thing is used. Specifically, silicone-based and polyether-based antifoaming agents are used.
Hydrogen produced in the present invention is used as fuel gas for fuel cells.

  In the hydrogen production method using the microorganism of the present invention, a gas mainly composed of hydrogen and carbon dioxide is generated. Generally, when a cracked gas such as natural gas is used as a fuel for a polymer electrolyte fuel cell, a system for removing carbon monoxide (CO) in the cracked gas (CO) in order to prevent expensive electrode catalyst deterioration. Using a transformer, a CO remover, etc.), the CO needs to be reduced to about 10 ppm. In the system using the hydrogen production method of the present invention as fuel for a fuel cell, a system for removing CO is unnecessary, and the apparatus can be simplified. Further, the generated gas obtained by the present invention is different from the case where the cracked gas such as natural gas passes through the CO modifier, and is in a state containing the vapor in the reaction solution. The fuel cell system using the hydrogen production method of the present invention, such as eliminating the need for special humidification on the side, can realize an excellent system.

  EXAMPLES Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited thereto.

[Example 1]
Biological hydrogen production method using Escherichia coli strain (ATCC9637).
This strain was added to 500 ml (milliliter) of a culture solution having the composition shown in Table 1 below, followed by shaking culture (preculture) overnight at 37 ° C. under aerobic conditions.

Next, a portion of the culture solution which has been subjected to overnight shaking culture (pre-culture) under aerobic conditions is collected and added to the culture solution having the composition shown in Table 2 below and containing sodium formate for 12 hours at 37 ° C. Shaking culture (main culture) was performed.

Subsequently, the main culture solution was centrifuged (5000 rpm, 15 minutes), and the supernatant was removed to obtain bacterial cells having a hydrogen generation function.
The bacterial cells were separated by centrifugation and then suspended in 100 ml of a hydrogen generation solution under reduced conditions shown in the composition of Table 3 below (bacterial cell concentration: about 40% wet cell mass standard).

The reaction vessel for hydrogen generation is equipped with a formic acid supply nozzle, a stirring device, a pH adjusting device, a temperature maintaining device, and an oxidation-reduction potential measuring device, and is placed in a constant temperature water tank set at 37 ° C.
A 10 M (mol) / L (liter) concentration formic acid aqueous solution was continuously supplied to the reaction vessel at a feed rate of 25 ml / hr using a micropump, and the amount of gas generated was measured.
Gas generation occurred simultaneously with the supply of formic acid, and gas generation continued during the continuous supply of formic acid (for the experiment time of about 6 hours). The collected gas was analyzed by gas chromatography. As a result, the generated gas contained 50% hydrogen and the remaining carbon dioxide gas. The hydrogen generation rate measured by the gas flow meter was approximately constant 45 L (H ₂ ) / hr / L (reaction volume) during the experiment time.

[Comparative Example 1]
An experiment was carried out under the same method and conditions as in Example 1 except that the aerobic culture medium in Example 1 did not contain sodium formate (Table 2). As a result, gas was generated from the hydrogen generating solution. Was hardly recognized.
From the results of Example 1 and Comparative Example 1, it is clear that culturing in a culture solution containing formic acid under aerobic conditions is essential for obtaining a microorganism capable of expressing a hydrogen generating function.

[Example 2]
After culturing under aerobic conditions according to the same conditions and methods as in Example 1, the cells were centrifuged (5000 rpm, 15 minutes), and the supernatant was removed to obtain cells. The cells were suspended in an induction medium under anaerobic conditions having the same composition as that used in Example 1 shown in Table 2 above.
The induction medium solution was previously heated at 120 ° C. for 10 minutes, and immediately after that, the dissolved oxygen was removed for 20 minutes under reduced pressure conditions (up to about 4.00 × 10 ² Pa), and a stirring apparatus under a nitrogen atmosphere And introduced into a glass container having an internal volume of 10 L (liter) equipped with a temperature maintaining device and an oxidation-reduction potential measuring device.
The suspension was prepared so that the cell concentration of the separated cells was 2% (wet cell mass standard), and induction culture was performed under anaerobic conditions for 6 hours (additional addition of the present invention). Improved hydrogen generation function under anaerobic conditions in the presence of formic acid). After culturing, it was centrifuged (5000 rpm, 15 minutes), and the supernatant was removed to obtain bacterial cells. The obtained microbial cells having a hydrogen generation function were introduced into a hydrogen generation solution, and the hydrogen generation function was examined under the same conditions and methods as in Example 1.
The hydrogen generation rate was measured in the same manner as in Example 1. As a result, it was 55 L (H 2) / hr / L (reaction volume).
According to the results of Example 1 and Example 2, after culturing under aerobic conditions, further induction culture under anaerobic conditions improves the expression of the hydrogen generation function of the microorganism, It was revealed that the hydrogen generation rate increased.

[Examples 3 to 7]
Biological hydrogen production method using Escherichia coli strain (ATCC9637).
The concentration of sodium formate in the medium cultured under aerobic conditions is 0.5 mM (Example 3), 1 mM (Example 4), 100 mM (Example 5), 300 mM (Example 6), 500 mM ( Except for Example 7), the hydrogen generation rate was measured by the same method and conditions as in Example 2. These results are shown in FIG.
FIG. 1 shows the correlation between the formic acid concentration and the hydrogen generation rate with respect to the aerobic hydrogen generation function expression method in the presence of formic acid.
It is apparent that the hydrogen generation rate is greatly improved by culturing under aerobic conditions where the formic acid concentration is 1 mM or more.
Moreover, it is shown that even if the formic acid concentration is too high, the expression effect of the hydrogen generation function proportional to the concentration is not recognized.

  Hydrogen produced by the present invention is useful as clean energy for operating a fuel cell, for example.

Relationship between formic acid concentration and hydrogen generation rate in aerobic hydrogen generation function expression method.

Claims (3)

  After culturing a microorganism having a formate dehydrogenase gene and a hydrogenase gene in a formic acid-containing culture solution under aerobic conditions, the microorganism is added to the hydrogen generation solution in a reduced state, and an organic substrate is supplied to the solution. A biological hydrogen production method.   The organism according to claim 1, wherein the microorganism is cultured in an aerobic condition, further cultured in a formic acid-containing culture solution under an anaerobic condition, and added to the hydrogen generation solution in a reduced state. Hydrogen production method. Use of hydrogen produced by the method according to claim 1 as fuel gas for a fuel cell.

Images