JP3025204B2 - Selenate reducing bacteria and wastewater treatment method - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

The present invention relates to a wastewater treatment method capable of effectively removing Se, especially hexavalent Se, from wastewater containing Se (selenium).

[0002]

2. Description of the Related Art Generally, as a flue gas desulfurization apparatus provided in a thermal power generation facility or the like, the flue gas is brought into contact with an absorbent slurry (eg, limestone slurry) to absorb and remove sulfur oxides in the flue gas. In recent years, wet flue gas desulfurization apparatuses that separate and collect gypsum from slurry in an absorption tower as a by-product have become widespread. However, in the wastewater discharged from this flue gas desulfurization unit,
Since the harmful substances existing in the flue gas are dissolved and contained, it is necessary to remove these harmful substances before releasing or reusing. In particular, in a flue gas desulfurization device for a coal-fired boiler, the harmfulness of Se contained in coal at a content of up to about 10 mg / kg has recently become a problem, and it is removed from the wastewater to make it harmless and treated. It is desired.

Since Se has toxicity similar to that of arsenic compounds and there are cases of obstacles and emission regulations abroad, it was newly added to regulation items in Japan in February 1994, and the environmental standards (0.01 mg / liter) were adopted. ), Drainage standard (0.1mg
/ Liter), dissolution standard for landfill disposal (0.3 mg
/ Liter) was enacted. Se in the wastewater contains tetravalent Se (main form: SeO ₃ ^2- selenite) and 6
Exists as trivalent Se (main form: SeO ₄ ^2- selenate), and hexavalent Se in particular has high solubility (solubility 95% at
20 ° C) Easy to elute.

[0004] The current flue gas desulfurization apparatus is usually provided with a wastewater treatment apparatus, and the wastewater purification treatment is performed in this apparatus. However, the conventional wastewater treatment apparatus is configured to sequentially perform coagulation sedimentation treatment, COD (chemical oxygen demand) treatment, denitrification treatment by microorganisms, and the like, and does not consider the Se removal treatment.

[0005] Conventionally, the tetravalent Se is FeC
l ₃ or Fe ₂ (SO ₄ ) ₃ , a chelating agent (for example, made of Miyoshi resin: EPORAS MX-7), or a polymer heavy metal collecting agent (for example, made of Miyoshi resin: Epofloc L-1)
For example, a method has been considered in which the solution is insolubilized by, for example, removal by solid-liquid separation. However, the conventional hexavalent S
For e, no effective removal method has been found.

[0006]

For this reason, conventionally, when selenium (particularly hexavalent Se) is contained in wastewater, desulfurization wastewater or the like is diluted with, for example, a large amount of water in order to comply with the above-mentioned elution standards and the like. There is a problem that complicated and costly processing is required.

Accordingly, the present invention is to find a selenate-reducing bacterium capable of effectively reducing selenate, and to effectively remove selenium (especially hexavalent Se) in wastewater, and at a low cost, to elute the selenium. It aims to provide a wastewater treatment method that can achieve compliance with standards and the like.

[0008]

In order to achieve the above object, the ferric selenate-reducing bacterium FERM BP- according to claim 1 is required.
5661 is a bacterium newly discovered by the present inventors and belongs to the genus Pseudomonas and has the ability to reduce hexavalent Se.

[0009] The wastewater treatment method according to claim 2 is a wastewater treatment method for removing at least hexavalent Se from wastewater containing Se, and at least selenate-reducing bacteria according to claim 1.
And reducing the hexavalent Se in the wastewater to tetravalent Se and / or elemental Se by a microbial treatment using , followed by solid-liquid separation.

[0010] According to a third aspect of the present invention, in the wastewater treatment method, the microorganism treatment includes a microorganism having a denitrifying ability and a microorganism according to the first aspect.
A microbial treatment using activated sludge containing at least a renic acid-reducing bacterium , characterized in that in the microorganism treatment, a denitrification treatment is performed together with the reduction of Se.

In a fourth aspect of the present invention, in the microorganism treatment, a treatment agent for insolubilizing tetravalent Se is added to the wastewater.

According to a fifth aspect of the present invention, there is provided the wastewater treatment method, wherein a treatment agent for insolubilizing tetravalent Se is added to the wastewater before the solid-liquid separation or after the solid-liquid separation. Is provided.

[0013]

Embodiments of the present invention will be described below. (First Example) First, a first example of the embodiment of the wastewater treatment method of the present invention will be described with reference to FIG. In FIG. 1, a desulfurization apparatus 1 is, for example, an absorption tower (not shown) in which a tank for supplying limestone slurry (absorbent slurry) is formed at the bottom.
By sending the absorbent slurry in the tank of the absorption tower to the tower main body of the absorption tower by a circulation pump (not shown), and making gas-liquid contact with the smoke exhaust passing through the tower main body,
It absorbs and removes sulfur oxides in flue gas. In the case of the tank oxidation method, the absorbent slurry that comes into contact with the flue gas and flows down into the tank is oxidized by air blown into the tank, and gypsum (solid content) as a by-product in the tank is formed. It is configured to generate.

In this case, part of the slurry in the tank is continuously withdrawn and separated into solid and liquid, whereby gypsum having a low water content is continuously collected, while most of the separated water is mixed with the gypsum. It is used cyclically as the water that makes up the limestone slurry newly supplied into the tank. A part of the separated water is discharged out of the desulfurization apparatus as so-called desulfurization wastewater A. This is an essential process to prevent impurities dissolved in the slurry from the flue gas from excessively accumulating in the circulating water constituting the slurry and impairing the desulfurization performance. In the desulfurization wastewater A, particularly in the case of a coal-fired boiler, a considerable amount of Se is dissolved from the flue gas. For example, hexavalent Se
Is contained in an amount of about 0.3 mg / l.

The desulfurized wastewater A is subjected to a coagulation and sedimentation step in the wastewater treatment apparatus 2 in this case, as shown in FIG.
Through a COD treatment step, a microorganism treatment step, and a tetravalent Se removal step, it is discharged as treated waste water B. Here, the coagulation sedimentation step is a step of removing fine solids (particles) that could not be separated in the solid-liquid separation processing for gypsum collection in the desulfurization apparatus 1 by a coagulation sedimentation apparatus. This is a step of removing inorganic pollutants in order to make the value not more than the reference value. This COD treatment step can be carried out by a method of boiling waste water at a high temperature to thermally decompose pollutants or a known method of selectively adsorbing a specific pollutant by an adsorption resin. A part or all of the tetravalent Se contained in the waste water reacts with the coagulant in the coagulation and sedimentation process to become selenite and is precipitated and removed on the solid phase side. Se is also discharged to the downstream side while being dissolved in the wastewater in the coagulation sedimentation step and the COD treatment step.

In the microbial treatment step, aerobic treatment (aerobic microorganism treatment), anaerobic treatment (anaerobic microorganism treatment), and sedimentation treatment (solid-liquid separation) are sequentially performed. The aerobic treatment here includes nitrite (a bacterium having the property of oxidizing NH ₄ ⁺ to generate NO ₂ ⁻ ) and nitric acid bacterium (oxidizing NO ₂ ⁻ and NO ₃ ⁻
Activated sludge containing germs having the property of producing activated sludge) is added to a stirred tank in which the activated sludge is suspended or suspended.
The wastewater after the D treatment step is introduced and agitated, and air is blown as necessary to aerate (expose to air). In this aerobic treatment, after a considerable residence time, NH ₄ ⁺ in the wastewater is oxidized by nitrite in the activated sludge to NO ₂ ⁻ ,
Furthermore the NO ₂ ^- it is oxidized with nitric acid bacteria in the activated sludge NO ₃ ^- becomes. The wastewater after the aerobic treatment is subjected to a sedimentation treatment or the like as necessary, and is preferably not contained as much as the activated sludge used for the aerobic treatment. Etc.).

Next, in the anaerobic treatment, a microorganism having a selenium-reducing ability to reduce hexavalent Se to tetravalent Se and / or simple Se (for example, the selenate-reducing bacterium FERM BP-
And 5661), denitrifying bacteria (NO ₃ ^- in the stirring tank that uses an active sludge containing the bacteria) which have the property to produce N ₂ by reducing, the activated sludge is suspended or suspension, the aerobic treatment The wastewater is introduced and agitated, and the anaerobic environment is maintained in a sealed state while supplying nutrient sources. As a nutrient source, an organic acid (eg, acetate), alcohol (eg, methanol), aldehyde, ketone, sugar (eg, glucose) and the like can be used. In this anaerobic treatment, after a considerable residence time, NO ₃ ⁻ in the wastewater is reduced to N ₂ by denitrifying bacteria in the activated sludge, and at the same time, the hexavalent wastewater in the wastewater is reduced by microorganisms having selenium reducing ability. Se (main form:
Selenate SeO ₄ ^2- ) is reduced to tetravalent Se (SeO ₃ ^2- ), or further becomes elemental Se.

In the sedimentation treatment, the wastewater after the above-described anaerobic treatment is introduced into, for example, a sedimentation separation device or the like, and is sent to the downstream (tetravalent Se removal step) after sludge (solid content) is removed. At this time, the simple substance Se has an extremely low solubility and is mostly precipitated as a solid content, and the tetravalent Se is also converted to the hexavalent Se.
Partially precipitates because the solubility is lower than that of. For this reason,
Most Se is taken up in sludge and removed from the wastewater except for a small amount of tetravalent Se dissolved in the wastewater. The sludge removed by the sedimentation treatment may be treated as waste as it is. For example, after adding and mixing a treating agent for insolubilizing tetravalent Se, the sludge is dehydrated by a centrifugal sedimenter or the like and discarded as a cake. It will be easier to handle,
There are few problems of selenium elution.

Then, in the tetravalent Se removing step, an insolubilization treatment (tetravalent Se insolubilization treatment), an aggregation precipitation treatment (solid-liquid separation)
Are performed in order. In the insolubilization treatment, the wastewater after the microorganism treatment step is introduced into a stirring tank, and a treatment agent (for example, FeCl ₃ or Fe ₂ (S
O ₄ ) ₃ ) is added and mixed into the wastewater. According to this processing, the tetravalent Se contained in the wastewater (main form:
Selenite SeO3 ^2-) is, treatment agent, for example, the following reaction formula (1), (2) or (3), (causing the reaction shown by 4) selenite iron (Fe ₂ (SeO _{3) 3} ) and become insoluble.

[0020]

Embedded image FeCl ₃ → Fe ³⁺ + 3Cl ⁻ (1) 2Fe ³⁺ + 3SeO ₃ ^2- → Fe ₂ (SeO ₃ ) ₃ ↓ (2) or Fe ₂ (SO ₄ ) ₃ → 2Fe ³⁺ + 3SO ₄ ^2- (3) 2Fe ³⁺ + 3SeO ₃ ^2- → Fe ₂ (SeO ₃ ) ₃ ↓ (4)

For this reason, when the waste water is subjected to solid-liquid separation by a coagulation sedimentation device or the like in the subsequent coagulation sedimentation treatment, the tetravalent Se is separated into iron selenite on the solid phase side and the solid content discharged (Sludge) is insolubilized and mixed. Therefore, the treated wastewater B discharged from the wastewater treatment device 2
It contains little selenium, and satisfies the above emission standards sufficiently.

The sludge removed by the coagulation and sedimentation treatment may be directly treated as industrial waste.
For example, if dewatered by a centrifugal sedimenter or the like and discarded as a cake, handling becomes easy. In this sludge, most selenium is present in an insolubilized state, so that the selenium elution standard can be sufficiently satisfied even when discarded as a cake. In addition, here, an example is described in which a treating agent for insolubilizing tetravalent Se is added to the wastewater after the separation of the sludge after the microorganism treatment step, but the wastewater before the separation of the sludge after the microorganism treatment step is added to the wastewater. A treatment agent may be added to separate the insolubilized Se together with the sludge in the subsequent solid-liquid separation step.

According to the above-described wastewater treatment method, hexavalent Se, which had not been able to be removed conventionally, is sufficiently removed from the wastewater, as demonstrated in the examples described later. The standard (0.1 mg / l) can be easily cleared. Moreover, since the reduction of hexavalent Se is performed simultaneously with the denitrification treatment, the apparatus configuration for the microbial treatment process is the same as that of the conventional wastewater treatment in which nitrification treatment (aerobic treatment) and denitrification treatment (anaerobic treatment) are performed. The present invention can be realized as it is with the same device configuration as the device (device configuration excluding activated sludge). In this case, the present invention can be easily and inexpensively applied to existing devices only by installing a device for the tetravalent Se removal process. Further, compared to the case where the reduction of hexavalent Se and the denitrification treatment are performed in separate steps, the entire treatment time can be remarkably reduced.

Depending on the Se concentration in the wastewater or the management of the volume and metabolic state of the microorganism treatment tank, Se (mainly tetravalent) remaining in the wastewater after the microorganism treatment process may be removed by the Se removing action in the microorganism treatment process. Since the concentration of Se) is equal to or lower than the emission reference value, the tetravalent Se removing step is not necessarily required.

(Second Example) Next, a second example of the embodiment of the wastewater treatment method of the present invention will be described with reference to FIG. This example is an example of a method of recycling activated sludge including the above-described nitrite, nitrate, selenate-reducing bacterium, and denitrifying bacterium in the microorganism treatment step in the wastewater treatment apparatus 2a.

That is, the wastewater after the COD treatment step is introduced into an aerobic treatment step in which activated sludge containing various bacteria floats, and is aerated by blowing air. In this aerobic treatment step, after a considerable residence time, NH ₄ ⁺ in the wastewater is oxidized by nitrite bacteria in the activated sludge to NO ₂ ⁻ , and this NO ₂ ⁻
Is oxidized by nitric acid bacteria in activated sludge to NO ₃ ⁻ .
The wastewater after the aerobic treatment is led to the next anaerobic treatment step together with the activated sludge.

In the anaerobic treatment, agitation is performed to the extent that the activated sludge floats, and the anaerobic environment is maintained in a sealed state while supplying nutrient sources. As a nutrient source, as described above, organic acids (eg, acetate), alcohols (eg, methanol), aldehydes, ketones, sugars (eg, glucose) and the like can be used. In this anaerobic treatment, a microorganism having a selenium reducing ability (for example, a selenium reducing bacterium of the present invention)
According to FERM BP-5661), hexavalent Se in wastewater
Is reduced to tetravalent Se or / and single element Se,
NO in the effluent ₃ ^- is N ₂ is reduced by denitrifying bacteria activated sludge.

Since the nutrients remaining in the anaerobic treatment step will cause an increase in COD as it is, in the next oxidation treatment step, for example, air is blown and aerated, and the remaining nutrients are aerobic by microorganisms in the activated sludge. Decompose by metabolism.
Then, the waste water after the oxidation treatment step is led to the next precipitation treatment step together with the activated sludge. In this sedimentation treatment step, the activated sludge and wastewater are separated by, for example, a sedimentation separation device.

Here, a part of the activated sludge settled and separated and concentrated is returned to the treatment tank in the aerobic treatment step and recycled. The amount of this recycling is the amount of C flowing into the treatment tank in the aerobic treatment process in order to maintain the treatment performance of the wastewater with high reliability.
The drainage amount after the OD treatment step is, for example, about twice. The wastewater from which activated sludge (solid content) has been removed in the precipitation treatment step is sent to the downstream (tetravalent Se removal step).

In the above microbial treatment step, when the total amount of activated sludge increases due to the growth of bacteria, etc.,
It may be adjusted by appropriately extracting the activated sludge concentrated in the precipitation treatment step and discharging it out of the system. Further, in order to stably maintain the activity of the microorganisms in the activated sludge, it is preferable to appropriately add a common nutrient (for example, phosphoric acid) of various bacteria to the aerobic treatment step.

According to the wastewater treatment method of the second example described above, the following effects are obtained in addition to the effects similar to those of the first example. That is, in the microorganism treatment step, 1
The recycling system that uses various types of activated sludge is adopted, eliminating the need for large-scale solid-liquid separation (separation of activated sludge) in each processing step, and taking activated sludge into and out of the equipment. Work and handling, and bacteria management are facilitated, and further simplification of the apparatus and maintenance work can be facilitated. In addition, there is an advantage that the stirring (mixing) state of the activated sludge is easily maintained satisfactorily, and high activity can be secured.

(Third Example) Next, a third example of the embodiment of the wastewater treatment method of the present invention will be described with reference to FIG. In this example, in the wastewater treatment device 2b, a tetravalent Se insolubilizer is introduced into wastewater in the microorganism treatment step. That is, a treating agent (eg, FeCl ₃ or Fe ₂ (SO ₄ ) ₃ )
For example, as shown in FIG. 3, the wastewater treatment apparatus 2b is put into a stirring tank in aerobic treatment or put into a stirring tank in anaerobic treatment to be mixed into wastewater.

In this case, most of the tetravalent Se that was originally dissolved in the wastewater or the tetravalent Se generated by reducing the hexavalent Se in the anaerobic treatment is a stirring tank in the aerobic treatment or a stirring tank in the anaerobic treatment. In the above, the reaction represented by the above-mentioned reaction formula (1), (2) or (3), (4) occurs with the added treating agent, and iron selenite (Fe ₂ (S
eO ₃ ) ₃ ), which is insolubilized and contained in solid matter (sludge) during the precipitation treatment and is removed.

Therefore, the treated wastewater B hardly contains selenium, and the above-mentioned discharge standard is sufficiently satisfied. Moreover, in this case, the tetravalent Se removal step after the microorganism treatment step is unnecessary, and a wastewater treatment apparatus having substantially the same configuration as that of the conventional wastewater treatment apparatus in which the apparatus configuration for the tetravalent Se removal step is deleted is sufficient. For this reason, the apparatus configuration is extremely simplified, and a selenium removal function can be added to existing equipment without increasing the equipment cost of the wastewater treatment apparatus. In addition, the total processing time is further reduced by the absence of the tetravalent Se removal step after the microorganism treatment step.

In this case, since sludge generated in the sedimentation treatment in the microorganism treatment step is almost insoluble in selenium, solid-liquid separation is performed as necessary to form a cake, which can be discarded without any problem. . In addition, S4
As a treatment agent for insolubilizing e, a treatment agent containing divalent Fe (for example, FeSO ₄ ) may be used. Even in this case, divalent Fe becomes trivalent Fe by natural oxidation or forced oxidation by aeration in aerobic treatment, and is also represented by the above reaction formula (1), (2) or (3), (4). Reaction occurs, and the tetravalent Se can be insolubilized.

[0036]

Next, as an embodiment of the wastewater treatment method of the present invention, an experiment conducted by the inventors will be described below. In the following experiments, activated sludge containing denitrifying bacteria and selenate-reducing bacteria used for denitrification treatment in a wastewater treatment system of an existing flue gas desulfurization system was treated with a hexavalent Se concentration of 10 pp.
m, and used in a sealed anaerobic environment for about 14 days.

As a microorganism that reduces hexavalent Se in the activated sludge, at least one strain belonging to the genus Pseudomonas was discovered by the inventors as described below and identified as a novel bacterium, and FERM BP- Order No. 5661. Further, the following experiment employs a method of growing microorganisms in a system (so-called batch system) in which a new culture solution (in this case, desulfurization drainage or the like) is not taken in and out during the treatment. In this case, acetate was added to the activated sludge as a nutrient source of the microorganism.

(Experiment 1) First, in Experiment 1, under the conditions shown in Table 1, 50 ml of the above activated sludge and 450 ml of desulfurization wastewater were mixed and stirred in a flask, and sealed to form an anaerobic environment. And stirred for 24 hours. Thereafter, the solid content was precipitated and only the supernatant water was taken out. The hexavalent Se concentration or the tetravalent Se concentration in the supernatant water, and nitrogen (N
The concentration of O ₃ ⁻ ) was analyzed.

[0039]

[Table 1]

As shown in Table 2, the results of the analysis were hexavalent Se.
The concentration decreased remarkably, and the concentration of tetravalent Se, which could hardly be measured in the wastewater before treatment, increased remarkably.

[0041]

[Table 2]

After the above treatment, F was added to the supernatant water.
After adding and mixing and stirring with eCl ₃ , coagulation and sedimentation treatment was performed, so that the total Se concentration in the solution was 0.08 mg / l, which sufficiently cleared the discharge standard (0.1 mg / l).

(Experiment 2) Next, in Experiment 2, 50 cc of the activated sludge and 450 cc of desulfurization wastewater (concentration of hexavalent Se before treatment of 8 ppm) were introduced into a flask, and FeSO ₄ was further added as a tetravalent Se insolubilizing agent. Add 0.5 g, mix and stir, seal and create an anaerobic environment, hold at 25 ° C. with stirring for 24 hours, then precipitate solids, extract only supernatant water, and hexavalent in supernatant water Alternatively, the tetravalent Se concentration was analyzed. As a result, neither hexavalent Se nor tetravalent Se could be measured, and hardly existed in the liquid. The pH during the treatment was 7 to 7.8.

The wastewater treatment method of the present invention is not limited to the above-described embodiment, but may have various embodiments. For example, Se
As a treatment agent for insolubilizing Fe, FeCl ₃ or Fe ₂ (S
In addition to O ₄ ) ₃ , a chelating agent (for example, manufactured by Miyoshi resin: EPORAS MX-7) and a polymer heavy metal collector (for example,
Made of Miyoshi resin: Epofloc L-1) or the like can be used. As described above, a compound containing divalent Fe (FeSO ₄ ) may be added as the treating agent.

As described above, when the concentration of Se (mainly tetravalent Se) remaining in the wastewater after the microorganism treatment step becomes lower than a desired value due to the Se removing action in the microorganism treatment step, 4 The step of removing Se is not always necessary. Further, the wastewater treatment method of the present invention can be applied to any wastewater containing not only desulfurization wastewater but also hexavalent Se.

Next, the selenate-reducing bacteria FERM of the present invention
An example of a method for culturing and isolating BP-5661 will be described. The inventors isolated microorganisms from activated sludge used for denitrification treatment in a conventional wastewater treatment apparatus by the following method in order to search for microorganisms that effectively reduce selenic acid, As a result of examining the reducing ability of selenate, it was found that the strain is a new strain of Pseudomonas which effectively reduces selenate. So, Pseudomon
as sp. Named SR-34, deposited at the National Institute of Advanced Industrial Science and Technology, National Institute of Advanced Industrial Science and Technology, resulted in FERM BP-566
Accepted as 1.

Selenate-reducing bacteria FERM BP of the present invention
Culture for isolating -5661 (hereinafter referred to as the present strain) was performed using a PYG selenate medium shown in Table 3. First, 3 ml of PYG selenate medium was placed in a 7 ml screw-cap test tube with a screw cap, and 3% of the activated sludge sample used in the above-mentioned denitrification treatment was added thereto. The cells were cultured under the same conditions. “Selenate” in Table 3 means hexavalent selenium,
Specifically, it is Na ₂ SeO ₄ .

[0048]

[Table 3]

In order to examine the characteristics of the present strain, glucose (Glucos) in a PYG selenate medium was sometimes used.
e) was changed to sodium acetate (Sodium Acetate), and a PYA selenate medium shown in Table 4 and an inorganic salt selenate shown in Table 5 obtained by adding 20 mM selenate to an inorganic salt medium containing acetic acid as a single carbon source Medium was also used.

[0050]

[Table 4]

[0051]

[Table 5]

The composition of the Hutner inorganic salt solution in Table 5 is shown in Table 6, and the composition of Metals "44" in Table 6 is shown in Table 7. Here, “Nitrilotriac” in Table 6
"eticAcid" means nitrilotriacetic acid, and "EDTA" in Table 7 is ethylenediaminetetraacetic acid (Ethylene
Diamine Traacetic Acid). Hutner's inorganic salt solution was prepared by dissolving Nitrilotriacetic Acid in distilled water, neutralizing with about 7.3 g of potassium hydroxide, and adding the remaining salts. Also, a few drops of sulfuric acid were added to Metals "44" to prevent the formation of a precipitate.

[0053]

[Table 6]

[0054]

[Table 7]

Then, this strain was isolated as follows. That is, a culture solution (that is, one having selenate reduction ability) in which a red precipitate was generated due to the generation of elemental selenium in the above culture treatment was diluted and plated on a PYG selenate plate medium, and anaerobically at 27 ° C. For 7 days. Thereafter, the colonies that exhibited red color in this plate medium were selected as selenate-reducing bacteria, and single colony isolation was repeated under the same medium and culture conditions,
The selenate-reducing bacteria were purified. In addition, the single colony isolation means that a specific strain is selected by inoculating only a specific colony generated on a medium into a new medium.

Next, the microbiological characteristics of the present strain will be described. Biochemical characterization of this strain was performed according to "Classification and identification of microorganisms (2)" (edited by Takeharu Hasegawa, published by Gakkai Shuppan Center). Also, ID test NF-18 (Nissui Pharmaceutical) and BBL CRY which are commercially available simple identification kits
A simple identification test using STAL NF / E (Becton Dickinson) was also performed. First, the microbiological characteristics of this strain are shown in Table 8.

[0057]

[Table 8]

This strain is a gram-negative bacillus (Kankin).
It has motility due to polar flagella. In the facultative anaerobic bacteria, the oxidase test and catalase test were positive,
Aerobic acid production from glucose (OF test =
O). In addition, the colony forms a thin and wide spread colony on the plate medium. From these basic characteristics, this strain is identified as a bacterium belonging to the genus Pseudomonas. This strain is grown on an inorganic salt medium using acetic acid as a single carbon source, and is considered to have no auxotrophy.

Next, the results of the Nissui Pharmaceutical ID test NF-18 are summarized in Table 9. The results were compared with the attached database, but no strains corresponded to this strain.

[0060]

[Table 9]

Next, BBL CRYSTAL NF / E
Are shown in Tables 10 and 11. When this result was compared with the database, this strain was found to have a Pseu probability of 83%.
It was determined that the microorganism belongs to domonas aeruginosa. As for bacteria belonging to Pseudomonas aeruginosa, there are no known reports of strains capable of reducing Se. Therefore, this strain is considered a new strain.

[0062]

[Table 10]

[0063]

[Table 11]

Next, the test for the reduction of selenate by the purely isolated strain of the present invention will be described. As described above, PY
When this strain was cultured on a G selenate plate medium, the colonies showed a red color, indicating that selenate was reduced to elemental selenium. In the PYG plate medium to which selenate was not added, the colonies did not turn red.

Further, a reduction test was performed in a methanol medium containing hexavalent Se shown in Table 12. This methanol medium 1
Add 250 mg / L of this strain to 1 L
The mixture was stirred and mixed in a flask, closed to form an anaerobic environment, and maintained at 25 ° C. with stirring for 24 hours to culture. As a result of analyzing hexavalent Se of the supernatant, the initial 1
What was 0 mg / liter was not detected after 24 hours. The precipitate formed as a result of the culturing was red, and as a result of energy dispersive X-ray spectroscopy, it was confirmed that the precipitate was Se alone. Therefore, most hexavalent Se
Was reduced to elemental Se, and it was demonstrated that the above-described wastewater treatment of the present invention can be effectively realized by the present strain even when methanol is used as a nutrient source.

[0066]

[Table 12]

Since the present strain has low specificity for a nutrient source, it can be cultured in a medium other than the above-mentioned medium. For example, the inventors have confirmed that culturing can also be performed with Heart In Fusion Bouillon (manufactured by Nissui Pharmaceutical). The cultivation of the present strain itself is also possible under aerobic conditions.

[0068]

According to the present invention, the selenate reducing bacterium FER according to claim 1 is provided.
MBP-5661 is a new strain belonging to the genus Pseudomonas and has the ability to reduce hexavalent Se. For this reason, the separation and removal treatment of hexavalent Se, which was difficult to treat conventionally, can be easily performed by the microorganism treatment with the present strain, and is extremely useful, for example, for use in wastewater treatment of a flue gas desulfurization device.

According to the wastewater treatment method of claim 2, hexavalent Se in the wastewater is reduced to tetravalent Se and / or simple substance Se in the microorganism treatment, so that it can be easily removed as a solid content. Simple substance Se has extremely low solubility and tetravalent Se
Also, since the solubility is lower than that of hexavalent Se, a large amount of Se can be removed as a solid by this treatment. For this reason, even when hexavalent Se, which cannot be removed conventionally, exists in the wastewater, the concentration can be significantly reduced.

According to the wastewater treatment method of the third aspect, the activity containing at least a microorganism having a denitrifying ability and a microorganism having a selenium reducing ability for reducing hexavalent Se to tetravalent Se and / or simple Se. Since the sludge is used and the denitrification treatment is performed together with the reduction of Se in the microorganism treatment, the configuration of the wastewater treatment device is simplified. That is, for example, when the Se removal treatment is performed in a separate process using activated sludge different from the denitrification treatment, it is necessary to separately provide a device dedicated to the Se removal treatment (for example, a stirring tank for treating microorganisms). However, with the configuration of the present invention, the same device can be shared. In other words, existing wastewater treatment equipment that has conventionally been performing denitrification treatment by microbial treatment can be used simply by changing the activated sludge used without modifying the equipment configuration.
The processing method of the present invention can be carried out as it is, and the hexavalent Se removal processing can be performed. In addition, with this configuration, since the denitrification treatment is performed at the same time as the reduction of Se, the treatment time required for the entire wastewater treatment can be shortened.

According to the wastewater treatment method of the present invention, since a treatment agent for insolubilizing tetravalent Se is added to wastewater in the treatment of microorganisms, the wastewater originally existed in the untreated wastewater.
Most of the valent Se and the tetravalent Se generated by the reduction of hexavalent Se in the microorganism treatment are insolubilized and can be removed by a solid content removal treatment (for example, a precipitation treatment). Therefore,
It is possible to further reduce the total Se concentration in the wastewater after the treatment, and to comply with the regulation values such as the wastewater standard with a large margin.
Moreover, in this case, since the treatment agent is added to the wastewater in the microorganism treatment, it can be implemented only by providing a device for adding the treatment agent to the treatment tank in the microorganism treatment, and the stirring for mixing the treatment agent into the wastewater is performed. Since there is no need to separately provide a tank or the like, the equipment cost of the wastewater treatment device is low, and the remodeling of the existing device is extremely easy.

According to the wastewater treatment method of the fifth aspect, in the step after the microorganism treatment, a treatment agent for insolubilizing tetravalent Se is added to the wastewater after the microorganism treatment, and solid-liquid separation is performed. For this reason, tetravalent S that originally existed in the untreated wastewater
e and most of the remaining tetravalent Se generated by the reduction of hexavalent Se in the microbial treatment and which could not be removed as a solid in the microbial treatment are removed in this step after the microbial treatment. Therefore, it is possible to further reduce the total Se concentration in the treated wastewater and to comply with the regulation values such as the wastewater standard with a large margin.

[Brief description of the drawings]

FIG. 1 is a diagram showing a desulfurization wastewater treatment system (first example) to which a wastewater treatment method of the present invention is applied.

FIG. 2 is a diagram showing a desulfurization wastewater treatment system (second example) to which the wastewater treatment method of the present invention is applied.

FIG. 3 is a diagram showing a desulfurization wastewater treatment system (third example) to which the wastewater treatment method of the present invention is applied.

[Explanation of symbols]

 1 desulfurization equipment 2, 2a, 2b wastewater treatment equipment A desulfurization wastewater B treated wastewater

Continued on the front page (51) Int.Cl. ⁷ Identification symbol FI C02F 3/12 C02F 3/34 ZAB ZAB B01D 53/34 ZAB 3/34 101 125R ZAB // (C12N 1/20 C12R 1:38) (72) ) Inventor Naohiko Ugawa 4-2-2 Kannon Shinmachi, Nishi-ku, Hiroshima City, Hiroshima R & D Co., Ltd. (72) Inventor Takashi Haruki 4-2-2 Kannon Shinmachi, Nishi-ku, Hiroshima City Inside the Hiroshima Laboratory, Mitsubishi Heavy Industries, Ltd. (72) Katsuharu Yoshimi 1-8-1, Koura, Kanazawa-ku, Yokohama-shi Mitsubishi Heavy Industries, Ltd. (72) Inventor Kazuaki Kimura 2-5-1 Marunouchi, Chiyoda-ku, Tokyo Inside Mitsubishi Heavy Industries, Ltd. (72) Inventor Tatsuto Nagayasu 5-1-1 Marunouchi, Chiyoda-ku, Tokyo Inside Mitsubishi Heavy Industries ( 72) Inventor Taku Shimizu Marunouchi, Chiyoda-ku, Tokyo Go No.5-1 inside Mitsubishi Heavy Industries, Ltd. (72) Inventor Kiyoshi Okazoe 2-5-1 Marunouchi, Chiyoda-ku, Tokyo Inside Mitsubishi Heavy Industries, Ltd. (56) References JP-A-51-127570 (JP, A) JP-A-3-182665 (JP, A) JP-A-9-248595 (JP, A) JP-B-53-27915 (JP, B2) PRMS Microbiology Letters, Vol. 61, (1989), p. 195-198 (58) Field surveyed (Int. Cl. ⁷ , DB name) C12N 1/00-1/38 B01D 53/00-53/96 C02F 3/00-3/34 BIOSIS (DIALOG) WPI (DIALOG) )

Claims (5)

(57) [Claims] 1. A selenate-reducing bacterium FERM BP- belonging to the genus Pseudomonas and having the ability to reduce hexavalent Se.
5661. 2. At least hexavalent S from wastewater containing Se
A wastewater treatment method for removing e, wherein at least the selenate-reducing bacteria according to claim 1 are used.
A wastewater treatment method comprising a step of reducing hexavalent Se in the wastewater to tetravalent Se and / or simple substance Se by biological treatment and then performing solid-liquid separation. 3. The microorganism treatment using activated sludge containing at least a microorganism having a denitrifying ability and the selenate-reducing bacterium according to claim 1 , wherein Se is reduced in the microorganism treatment. The wastewater treatment method according to claim 2, wherein a denitrification treatment is performed together with the wastewater treatment. 4. The wastewater treatment method according to claim 2, wherein a treatment agent for insolubilizing tetravalent Se is added to the wastewater in the microorganism treatment. 5. The method according to claim 1, wherein a treatment agent for insolubilizing tetravalent Se is added to the wastewater which has been subjected to the microorganism treatment and before or after the solid-liquid separation, and the solid-liquid separation is further performed. The wastewater treatment method according to any one of claims 2 to 3, wherein