WO2010147345A2 - Bacillus subtilis gu1 and use thereof - Google Patents

Bacillus subtilis gu1 and use thereof Download PDF

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Publication number
WO2010147345A2
WO2010147345A2 PCT/KR2010/003803 KR2010003803W WO2010147345A2 WO 2010147345 A2 WO2010147345 A2 WO 2010147345A2 KR 2010003803 W KR2010003803 W KR 2010003803W WO 2010147345 A2 WO2010147345 A2 WO 2010147345A2
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WIPO (PCT)
Prior art keywords
bacillus subtilis
strain
weight
vinegar
biofilter
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PCT/KR2010/003803
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French (fr)
Korean (ko)
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WO2010147345A3 (en
Inventor
허관
이상석
방민우
김선호
Original Assignee
Heo Kwan
Lee Sang Suk
Bang Min Woo
Kim Sun Ho
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Priority claimed from KR1020090052950A external-priority patent/KR100949670B1/en
Priority claimed from KR1020090069326A external-priority patent/KR100963053B1/en
Application filed by Heo Kwan, Lee Sang Suk, Bang Min Woo, Kim Sun Ho filed Critical Heo Kwan
Publication of WO2010147345A2 publication Critical patent/WO2010147345A2/en
Publication of WO2010147345A3 publication Critical patent/WO2010147345A3/en

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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K10/00Animal feeding-stuffs
    • A23K10/10Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/12Animal feeding-stuffs obtained by microbiological or biochemical processes by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K10/00Animal feeding-stuffs
    • A23K10/10Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/16Addition of microorganisms or extracts thereof, e.g. single-cell proteins, to feeding-stuff compositions
    • A23K10/18Addition of microorganisms or extracts thereof, e.g. single-cell proteins, to feeding-stuff compositions of live microorganisms
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K50/00Feeding-stuffs specially adapted for particular animals
    • A23K50/30Feeding-stuffs specially adapted for particular animals for swines
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K50/00Feeding-stuffs specially adapted for particular animals
    • A23K50/70Feeding-stuffs specially adapted for particular animals for birds
    • A23K50/75Feeding-stuffs specially adapted for particular animals for birds for poultry
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • C12N1/205Bacterial isolates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/95Specific microorganisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/90Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/07Bacillus
    • C12R2001/125Bacillus subtilis ; Hay bacillus; Grass bacillus

Definitions

  • the present invention relates to a microorganism isolated from bamboo vinegar and the use of the microorganism, the microorganism of the present invention is used in conjunction with the vinegar solution to bring the effect of reducing the mortality rate of livestock, shorten the shipping period, increase the history of history, reduce the smell of meat and improve meat quality It can be used as a feed additive and used as a microorganism for biofilters to absorb, adsorb, and decompose complex odorous gases such as ammonia, hydrogen sulfide, hydrocarbons, lower fatty acids and VOCs.
  • Wood vinegar contains about 100 kinds of trace components such as organic acids, alcohols, neutral components and basic components, and main components include organic acids such as acetic acid and functional substances such as alcohols and polyphenols. It is used.
  • ammonia, sulfur compounds, fatty acids, amines, hydrocarbons, VOCs, etc. generated from odorous sources such as livestock manure treatment plant, food storage and treatment plant, sewage treatment plant, by-product fertilizer plant, waste storage and treatment plant, sewage relay pump plant, and village sewage treatment plant.
  • Adsorption deodorization method, chemical liquid cleaning method and biofilter method are mainly used to collect and remove air pollution (odor) substances.
  • Adsorption deodorization method passes odorous substances through adsorbents such as activated carbon and removes them by adsorbing gaseous air pollution (odor) substances into fine pores, and adsorbents filled with air pollution (odor) substances are frequently used to maintain high removal efficiency. It has to be recycled or exchanged and has low processing efficiency.
  • the chemical liquid cleaning method is a method of removing the odorous substances to be deodorized by selecting and using a chemical that removes the odorous substances to be deodorized by spraying finely diluted circulating water in the reactor to make contact with air pollution (odor) substances.
  • odor air pollution
  • the biofilter method is environmentally friendly and high in deodorization efficiency to remove odor gas by mechanisms such as absorption, adsorption and decomposition of microorganisms, but in case of high concentration of odor gas generated in large quantities, it requires excessive installation site to secure sufficient contact time. Since the initial investment cost is high and the ammonia gas in the atmosphere is absorbed and treated in the circulating water, there is a disadvantage of greatly increasing the total nitrogen content in the water treatment process of the circulating water waste liquid.
  • the method of spraying deodorant and disinfectant with high pressure sprayer is mainly used for the improvement of livestock environment such as odor gas removal and disinfection of livestock house (pig, duck, chicken, etc.), but liquid deodorant or disinfectant is diluted with water and sprayed.
  • livestock environment such as odor gas removal and disinfection of livestock house (pig, duck, chicken, etc.)
  • liquid deodorant or disinfectant is diluted with water and sprayed.
  • the deodorization efficiency of antibiotics to improve the safety of food and functional microorganisms for improving meat quality and existing deodorization methods are low, and to overcome the problems of handling and environmental pollution, the efficiency of deodorizers and the efficiency of deodorizing devices The need for development is increasing.
  • the present invention is used together with the wood vinegar solution, which is difficult to achieve by the wood vinegar alone, the effect as a feed additive and the odorous substance removal effect to improve the weight gain, carcass rate, meat color and physicochemical properties and physical properties, the content of unsaturated fatty acids, etc.
  • new strains having a synergistic effect are isolated and identified, and the new strains are used in a biofilter apparatus using a feed additive containing wood vinegar and wood vinegar.
  • the present invention provides Bacillus subtilis GU1 [Accession No. KCCM 10890P], which is isolated from bamboo vinegar and is capable of growing in a medium containing 0.1 to 50% by weight of wood vinegar.
  • the present invention provides a culture in which Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain is fermented in a medium containing 0.5 to 10% by weight of wood vinegar.
  • the medium is characterized in that the solid medium.
  • the present invention provides a feed additive comprising a culture fermented Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain in a medium containing 0.5 to 10% by weight of wood vinegar.
  • the present invention provides a biofilter comprising a blower for introducing a malodorous substance into the biofilter device, a humidifier for supplying moisture into the biofilter device, and a carrier having microorganisms attached thereto, wherein the humidifier is a wood-choice solution composition.
  • Bacillus subtilis GU1 [Accession number KCCM, characterized in that the sprayed washing herbaceous scrubber, wherein the microorganisms attached to the carrier are separated from the bamboo vinegar solution and grow in a medium containing 0.5 to 50% by weight of bamboo vinegar solution. 10890P] to provide a biofilter device for removing odorous substances.
  • the microorganism is Nitrosomonas sp., Bacillus sp., Pseudomonas sp., Nitrosomonas sp. .) Strains, nitrobacter sp. ( Nitrobacter sp.) Strains, genus Bacillus (Thiobacill us sp.) Is characterized in that any one or more strains are further included.
  • the ablution vinegar disk rabeo the derived Bacillus from wood vinegar with wood vinegar composition subtilis (Bacillus subtilis) GU1 [Accession No. KCCM 10890P] strain and Bacillus subtilis (Bacillus subtilis ) GU2 [Accession No. KCCM 10891P] is characterized in that any one or more strains selected from among the strains are sprayed together.
  • Bacillus subtilis GU1 of the present invention is mixed with wood vinegar or fermented in a medium containing wood vinegar solution as a feed additive that can not be achieved conventional animal vinegar mortality mortality reduction, shorten the shipping period, increase the history of history, reduce the smell of meat and meat quality It brings the effect of improvement.
  • the biofilter device of the present invention is excellent in removing odorous substances due to Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain isolated from bamboo vinegar solution, and particularly, a scrubber for spraying wood vinegar solution with a humidifier. By using it can significantly reduce the concentration of foreign matter and ammonia-odorous odor substances introduced into the biofilter.
  • FIG. 1 is a schematic view of a biofilter apparatus using a cleaning throat (chochu) vinegar scrubber as one of the embodiments of the present invention.
  • FIG. 2 is a schematic view of a biofilter apparatus to which a chemical cleaning apparatus or a metal catalyst deodorizing apparatus, which is one of embodiments of the present invention, is added.
  • Figure 3 is a graph showing the number of bacteria after treatment of the strain of the present invention at each temperature for 10 minutes.
  • the strain of the present invention was isolated and identified in bamboo vinegar solution of pH 2.6 produced in Damyang, Jeollanam-do, and the isolated strain was identified as Bacillus subtilis .
  • the strain was named Bacillus subtilis GU1 and was deposited internationally in accordance with the Budapest Treaty under the deposit number KCCM 10890P on November 21, 2007.
  • the strain of the present invention has the effect of reducing livestock mortality that can not be achieved alone, in the form of a culture solution fermented in the medium containing or mixed with the wood vinegar solution, shorten the shipping period, increase the history of history, reduce the smell of stalk and improve the meat quality Bring.
  • the wood vinegar used as an active ingredient of feed additives or odorant removal agent is conifers, deciduous trees, trees, shrubs, evergreens, deciduous trees, evergreen conifers, deciduous conifers, evergreen softwoods, deciduous softwoods Cooling and condensing liquids or essential oils or vapors produced by one or more processes selected from pyrolysis, bath, heating, distillation, extraction, and weeding of any one or more selected from leaves, stems, roots, fruits and flowers of vegetation; It can be prepared through one or more processing selected from, separation, ripening, filtration, evaporation, and distillation.
  • the wood vinegar of the present invention is one or two selected from conifers, deciduous trees, arbors, shrubs, evergreens, deciduous trees, evergreen conifers, deciduous conifers, evergreen hardwoods, deciduous hardwoods, and leaves, stems, roots, fruits, and flowers of vegetation.
  • the process is carried out in a cauldron at a temperature not pyrolyzed and carbonized, and heated at 80 to 150 ° C. under atmospheric pressure or reduced pressure, or repeated heating and heating, followed by extraction, heating, distillation, or steaming by solvent extraction or supercritical fluid extraction.
  • the wood vinegar composition prepared by capturing a liquid substance or steam or essential oil which occurs in the process of cooling, condensation and separation is preferable because of its low tar content.
  • the wood vinegar of the present invention can be used by mixing two or more kinds of wood vinegar with different raw materials or manufacturing methods.
  • the medium may be liquid or solid, and when used as a feed additive, it is preferable to use a solid medium because it may be easily mixed uniformly with a solid feed, and the solid medium may be a nutrient source.
  • the preferred raw material for the solid medium may be a by-product of plant processing including cereals, soybeans, yeast or wood, which are used as raw materials for feed, and various raw materials such as skimmed steel, soybean meal, sawdust, etc. may be used in combination as necessary. Can be.
  • the content of wood vinegar is 0.5 to 10% by weight, more preferably 2 to 10% by weight, most preferably 2 to 5% by weight, based on the weight of the medium added to the medium to be inoculated with the strain of the present invention.
  • the incubation time is 12 hours or more, preferably 24 hours or more, more Preferably 36 hours or more, even more preferably 48 hours, the maximum incubation time is not particularly limited, but even if culture for 48 hours or more because the strain amount of the present invention is not increased within 60 hours.
  • the biofilter device 10 includes a blower 19 for introducing malodorous substances into the biofilter device, a humidifier 20 for supplying moisture into the biofilter device, and a carrier 14 to which microorganisms are attached. Any conventional biofilter device may be used.
  • the humidifying apparatus 20 may be a cleaning wood-vinegar scrubber sprayed with a wood-choice solution composition.
  • the wood vinegar composition reacts with ammonia gas, hydrogen sulfide, and methyl mercaptan, which are odor pollutants, and is neutralized and adsorbed with ammonium acetate salt, hydrogen sulfide ion, methyl mercaptan ion, etc., and is discharged to the outside together with sludge as shown in the following reaction formula.
  • Wastewater discharged from the exchange of scrubber circulating water does not affect the increase of nitrogen compound content in the sewage water treatment process, which is the biggest problem in the existing biofilter process. Deviation is not a big problem.
  • ammonia gas from the atmosphere is carried out by dissolving acetic acid (CH 3 COOH), the main component of the wood vinegar composition, into acetate ions (CH 3 COO ⁇ ) and hydrogen ions (H + ) as shown in Scheme 1 below.
  • acetic acid CH 3 COOH
  • CH 3 COO ⁇ acetate ions
  • H + hydrogen ions
  • ammonia (NH 3 ) gas among the malodorous substances flowing into the wood vinegar scrubber is hydrolyzed in an aqueous solution as in Scheme 2 and dissociated into ammonium ions (NH 4 + ) and hydroxide ions (OH ⁇ ).
  • the ammonia gas introduced into the wood vinegar scrubber body increases the pH of the wood vinegar aqueous solution due to the increase of ammonium ions and hydroxyl ions produced by the hydrolysis reaction in the wood vinegar aqueous solution.
  • the removal of the ammonia gas from the odorous substance is determined to remove the odor as ammonium acetate (CH 3 COONH 4 ) dissociated in the aqueous solution of the wood vinegar to the acid ions and acid-base reaction as in Scheme 3.
  • the expected reaction scheme of the wood vinegar composition is as follows.
  • the removal of hydrogen sulfide gas from the sulfur compounds in the air is odor due to the formation of fixed non-volatile salts of acetic acid (CH 3 COOH) and HS - by reaction with acetic acid ion and acid base generated by dissociation of acetic acid in aqueous solution of wood vinegar.
  • CH 3 SH methyl mercaptan
  • a reaction mechanism is expected in which odor is removed as fixed nonvolatile salts of acetic acid (CH 3 COOH) and CH 3 S ⁇ are generated as in Scheme 5.
  • the expected reaction scheme of the wood vinegar composition is as follows.
  • Devices for satisfying the conditions necessary for the growth of microorganisms inside the biofilter device may be further added.
  • Those that may be added to the biofilter device include a nutrient medium supply tank 15, an alkali supply tank 16 or an acid supply tank 17 for adjusting pH conditions to a range suitable for microbial growth, and also a temperature for microbial growth.
  • the heater or cooler may be installed in the warmer or cooler inside the biofilter, or may be installed in such a manner as to surround the outside of the biofilter device like a jacket.
  • air or an oxygen supply device may be further provided to increase the oxygen concentration in the biofilter.
  • any organic material such as pit, bark, compost, or organic carrier such as porous foamed polymer may be used as well as inorganic carrier such as porous ceramic.
  • a porous ceramic carrier having high microbial activity per unit weight, easy maintenance and high water content is used.
  • the microorganism attached to the carrier of the biofilter device of the present invention is Bacillus subtilis GU1 [Accession No. KCCM 10890P] isolated from bamboo liquor, and the strain is excellent in removing odorous substances, and bamboo vinegar solution (usually pH 2.6). Because it can grow inside and outside), even if the internal pH of the biofilter device drops sharply, the microorganisms are not affected by pH and do not interfere with the treatment of odorous substances.
  • Bacillus subtilis GU1 which is highly resistant to acidic acid, has a low pH because organic acids are continuously produced during fermentation in addition to carbon dioxide and water as odorous substances are decomposed by microorganisms fixed on the carrier. It is advantageous properties as a microorganism for biofilters.
  • Bacillus subtilis GU2 [Accession No. KCCM 10891P] strain isolated from bamboo shoot liquid by the present inventors together with Bacillus subtilis GU1 is to be used by Bacillus subtilis GU1 alone. It is more advantageous in that the removal efficiency is increased in adsorbing and decomposing odorous substances such as ammonia and sulfur compounds.
  • the biofilter device of the present invention further comprises a microbial incubator 18 and a microbial supply device for transferring the microorganisms cultured in the microbial incubator to the biofilter device, the microorganisms being supplied from the outside and injected into the carrier of the biofilter. It is advantageous in lowering the cost.
  • the microorganism incubator 18 preferably treats the outside of the incubator with a heat insulator to maintain a constant temperature in the incubator in order to adjust the growth conditions of the microorganisms, or more preferably, is provided with a heater.
  • the incubator may be equipped with a cooler, but most of the microorganisms for removing odorous substances are mesophilic bacteria, and the use frequency is low since domestic summer temperatures rarely exceed 37 °C.
  • the microorganisms cultured at a predetermined concentration or a predetermined number of bacteria in the microorganism incubator are supplied into the biofilter device through a microorganism supply device consisting of a transfer pump and a transfer tube.
  • a microorganism supply device consisting of a transfer pump and a transfer tube.
  • the microorganism is supplied to the biofilter device may be used either in a continuous or intermittent manner of supplying a certain amount or a method of supplying a variable by a pre-programmed formula.
  • the microbial incubator 18 is preferably added with a supply device for supplying air or oxygen.
  • the nutritional medium supply device 15 is connected to the microbial incubator 18 so that the nutritional medium can be supplied to supplement the microorganisms.
  • the humidifier 20 is preferably a cleaning wood-choice scrubber to which the wood-choice composition is injected, in that it can simultaneously perform the removal of humidification and odorous substances, especially ammonia-based substances.
  • Any type of clean scrubber can be used without limitation, but the demister must be removed from the outlet through which the treated air is discharged from the clean scrubber so that water can be supplied to the biofilter device.
  • the cleaning wood vinegar scrubber of the present invention is provided with a blower 19 in the inlet 22, the cleaning scrubber provided with a wood vinegar composition spray nozzle 21 in the upper portion of the main body to the wood vinegar composition supply unit Can be used. It is preferable to form a swirl flow to increase the time for which odorous substances forced into the main body through the blower stay in the main body, and forced inflow of pollutants by the blower increases the effect of contact with the deodorant of the present invention. It also increases efficiency and prevents odors from escaping.
  • One or more spray nozzles are installed in the upper region of the main body for the widespread spraying of the wood vinegar composition.
  • the number of spray nozzles to be installed is determined by the pressure of the blower, the rate of rise of odorous substances, and the desired treatment efficiency.
  • the spray nozzles are installed upwards or downwards and it would be economically advantageous for the number and spacing of these spray nozzles not to overlap each other with the total volume of the spray space and the sprayed up or down regions.
  • the lower portion of the main body may be provided with a reservoir 25 for storing the falling wood vinegar composition
  • a circulation pump 26 may be provided to recycle the wood vinegar composition stored in the reservoir to the spray nozzle.
  • a filler layer 24 such as polling having a large surface area of various forms may be provided to increase the contact efficiency of the vinegar liquor in the form of droplets sprayed by the spray nozzle inside the main body and odorous substances.
  • wood vinegar of the present invention or the wood vinegar mixed with two or more kinds of wood vinegar, or a mixture or the above-mentioned wood vinegar, plant pyrolysis composition, metal catalyst, photocatalyst, plant essential oil, plant extract, oxidizing agent, reducing agent, phytonutrient, organic acid, fermenting agent, flavoring agent, adsorbent , Microorganisms, microbial agents, clay solution, ocher solution, mud flats, surfactants or fragrances may be mixed (hereinafter, wood-vinegar composition) to be used.
  • Mixing ratio may be used to 0.01 to 90% by weight based on the total weight of wood vinegar.
  • 0.01 ⁇ 10% by weight of deodorant, deodorant, disinfectant, fungicide, etc. may be added as necessary in a range that does not inhibit the growth or proliferation of the Bacillus subtilis GU1 strain of the present invention.
  • wood vinegar is mixed with a solvent, such as water of 2 to 1000 times the weight of wood vinegar solution or alcohol of 1 to 4 carbon atoms, or separately evaporated Accelerators may be added.
  • a solvent such as water of 2 to 1000 times the weight of wood vinegar solution or alcohol of 1 to 4 carbon atoms, or separately evaporated Accelerators may be added.
  • Bacillus subtilis GU1 strain, Bacillus subtilis GU2 strain, or mixtures thereof may be added to the wood vinegar to increase the odor gas removal efficiency which is treated in the cleaned wood vinegar scrubber before entering the biofilter device of the present invention.
  • the concentration is 1.00E + 02 ⁇ 1.00E + 08 cfu / ml, preferably 1.00E + 03 ⁇ 1.00E + 08 cfu / ml, more preferably 1.00E + 04 ⁇ 1.00E + It is preferably added at a concentration of 08 cfu / ml.
  • one or more deodorizers may be used in series at the front end or the rear end, and a separate chemical cleaning device, a filter deodorizer, a membrane vaporizer, an ozone deodorizer, a biofilter deodorizer, and a metal catalyst deodorizer may be used.
  • Adsorption deodorizer, plasma deodorizer, incineration deodorizer and single or two or more types can be connected and used in series.
  • the addition of the acid gas or VOCs chemical liquid cleaning device 30 or the metal catalyst (photocatalyst) deodorizer to the front stage of the biofilter device or the scrubber wood scrubber attached to the biofilter device is the microorganisms in the acid gas. It is not preferable to the impact caused by the impact, and to increase the efficiency of removing the odorous substances of the biofilter device, it is desirable in terms of economic and operational.
  • bamboo vinegar with pH 2.6 produced in Damyang, Jeollanam-do, which had been aged for more than 6 months, was used.
  • MRS agar medium MRS agar medium
  • PDA agar medium PDA agar medium
  • mannitol eggyolk polymyxine (MEP) medium MRS agar medium
  • MEP mannitol eggyolk polymyxine
  • DNA extracted from the strain and 16s rDNA analysis showed the highest homology with Bacillus subtilis HDYM-11 strain and identified as Bacillus subtilis (1511 matches among 1515 sequences, 99% phase). Homosexual).
  • the sequence of 16s rDNA obtained is shown in SEQ ID NO: 1.
  • Another strain was identified as Bacillus subtilis with 99% homology with 1512 sequences among Bacillus subtilis and 1517 sequences, and the sequence of 16s rDNA obtained was shown in SEQ ID NO: 2.
  • Bacillus microorganisms produce a variety of useful substances, including enzymes, non-toxic antibacterial substances, pesticides, etc., and is also a gram-positive bacteria, characterized by the formation of spores at high temperatures.
  • the absorbance (Opical Density, 600nm) value is 1.0
  • the number of bacteria after heat treatment for 10 minutes at each temperature was measured and shown in FIG.
  • the viability was excellent even when treated at 80 ° C., far exceeding 60 ° C., which is a common killing temperature of lactic acid bacteria used as a useful microorganism of feed additives.
  • the Bacillus subtilis GU02 strain also did not differ from before the heat treatment up to 45 °C bacteria number 1.00E + 08 cfu / ml, and maintained at more than 1.00E + 08 cfu / ml at 60 °C.
  • bamboo vinegar is a strong acidic condition of pH 2.6, after diluting the bamboo vinegar in distilled water at a constant ratio, the growth change according to the incubation time of the strain (GU01) of the present invention at each concentration is measured by the change in absorbance at 600 nm is shown in Table 1 In addition, the change in the number of microbial microorganisms with incubation time is shown in Table 2.
  • bamboo liquor was diluted 10, 20, 30, 40 and 50% by weight in distilled water, respectively, and the initial microbial inoculation concentration was 1.00E + 05 cfu / ml and incubated at 37 ° C.
  • Table 1 time 10% 20% 30% 40% 50% 0 0.239 0.254 0.280 0.288 0.319 24 0.335 0.378 0.423 0.456 0.375 48 0.375 0.385 0.477 0.523 0.516
  • the growth (absorbance of 600 nm) of the strain of the present invention was increased as the incubation time was increased, increased to 40% by weight of bamboo vinegar concentration, but no longer increased from 50% by weight.
  • the number of bacteria of the strain of the present invention was increased up to 24 hours, even if incubated for 48 hours, the change in the number of bacteria was insignificant, and the change in the number of other bacteria in the bamboo shoot concentration was also insignificant.
  • the strain of the present invention was able to grow in a medium containing more than 0.1% by weight of bamboo vinegar, especially in the medium added up to 50% bamboo vinegar was determined that the growth will not be significantly affected.
  • the degreasing steel whose water content was adjusted to 40% by weight was added to the group (Comparative Example 1) and degreasing steel instead of the feed additive.
  • Addition of 2% by weight of bamboo vinegar solution and a feed additive (Comparative Example 2) in which the water content was adjusted to 40% by weight were used by adding 0.2% by weight to the feed for general broilers.
  • broiler chickens of the same size were stocked in the barns of Comparative Examples 3 and 4 and Example 3, respectively. After breeding broilers for 35 days, the number of shoots and growth rate were measured, and 10 broilers were randomly selected from each experimental group to analyze the start weight, end weight, weight gain and broiler chemical characteristics.
  • Example 1 Comparative Example 1
  • the test animal barn was 638 m 2 (11m X 8m), respectively, and 0.2 wt% of the feeds of Example 1 and Comparative Example 1 were added to the general broiler feed.
  • 14,000 broiler chicks of the same size were stocked in stalls of Comparative Example 1 and Example 1, respectively.
  • Example 1 Test 14,000 14,000 Starting weight (g) 42.0 42 End weight (g) 1,789 1,870 Breeding days 35 35 Daily gain (g / d) 49.91 52.23 Feed Intake (kg) 2.68 3.24 Dead shooter 426 419 Growth rate (%) 96.96 97.01
  • the weight gain per day was 52.23g in Example 1 and 49.91g in Comparative Example 1, which was 2.32g higher than in Comparative Example 1, and Example 1 was 97.09% and Comparative Example 1 in the growth rate. 96.96%, which is 0.13% higher (Table 4).
  • the feed additive of the present invention By feeding the feed additive of the present invention to broiler chickens, it is thought that the reduction of mortality and the increase in the daily weight gain are caused by the increase of immunity by the microorganisms and the death by disease is reduced.
  • the synergistic effect of the mixed strain of the present invention and bamboo vinegar increased the digestibility of broilers and inhibited the growth of intestinal harmful bacteria.
  • the heating loss (%) is a sample (250 ⁇ 50g) formed into a certain shape, then put in a polyethylene bag and placed in a water bath at 80 ° C to be completely immersed in water, heated for 40 minutes, and cooled in water for 20 minutes. . After the water of the cooled sample was removed, the weight loss was calculated. Shear force was measured by using a salter (Warner Bratzler Shear, USA) as the shear force measurement sample, which was removed from the surface portion of the sample from which the heating loss was measured.
  • a salter Warner Bratzler Shear, USA
  • the sample was placed in a filter tube (VIDAS tube, BIOMERIEUX, France) for the measurement of water holding capacity, placed in an 80 ° C water-bath, heated for 20 minutes, and allowed to cool for 10 minutes.
  • the cooled tube was centrifuged at 2000 ° C. for 10 minutes at 10 ° C., and the free moisture and the water holding capacity were calculated by the formula.
  • Free moisture [(difference in weight before and after centrifugation) / sample weight] X fat coefficient (1-fat content) X 100
  • Example 1 was significantly lower than that of Comparative Example 1 in shearing force, and the meat was lightly cut well, and in Example 1, it was confirmed that the water holding capacity was excellent.
  • Example 1 In flesh color, Example 1 had a higher brightness and a lower yellowness than Comparative Example 1, indicating that it had a bright flesh color, and the redness was lower.
  • Example 1 the content of crude ash was lower than that of Comparative Example 1, and it was found that crude fat and crude protein were higher to provide better meat quality.
  • Fatty acid content was measured using gas chromatography (model name: Varian 3600).
  • Example 1 was found to provide a broiler of good quality with a lower content of saturated fatty acids and a higher content of unsaturated fatty acids than Comparative Example 1.
  • the scale of the test animal house was 400 m 2 (10m X 40m), respectively, and Example 2 and Comparative Example 4 were used by adding 0.2% by weight of the general duck breeding feed to the general duck breeding feed. 10,000 ducks of the same size were stocked in stalls of Example 2 and Comparative Example 1, respectively. After 43 days of duckling, the number of dead and growth rates were measured, and 100 groups of ducks were randomly selected from each experimental group to analyze the initiation weight, end weight, weight gain and feed efficiency.
  • Example 9 Item Comparative Example 1
  • Test 10,000 10,000 Starting weight (g) 48 48 End weight (g) 3.190 3.280 Breeding days 43 43 Daily weight gain (g) 74.19 76.27 Feed Intake (kg) 65.709 65.922 Average weight (g) 3.190 3.280 Dead shooter 141 118 Feed requirement (g) 2.10 2.03 Growth rate (%) 96.96 97.09
  • Example 2 the weight gain, feed efficiency and growth rate per day were improved compared to Comparative Example 1.
  • the daily weight gain was 74.19 g
  • Example 2 was 76.27 g
  • Example 2 was higher
  • the growth rate was 98.82% in Example 2, 98.57% in Comparative Example 1, and 0.25% in Comparative Example 1. High.
  • Example 2 SE Amount 0.2 wt% 0.1 wt% 0.2 wt% - Daily weight gain (g) 772 b 825 a 821 a 13.3 Feed Intake (g) 2,356 2,480 2,413 65.3 Feed efficiency (%) 32.8 33.3 34.0 0.009
  • Example 2 Compared to Comparative Example 1, in Example 2, the addition amount was 0.1 wt% or 0.2 wt%, and the weight gain per day was significantly increased, the feed intake was increased, and the feed efficiency was also confirmed.
  • the feed additive of Example 2 of the present invention in the pig farm in Jeongeup replaces the feed additive including the general lactic acid bacteria and added 0.2% by weight to the feed for general pigs, as a result, compared to the feed additive containing the common lactic acid bacteria Feeding date of pigs was reduced by 9 days and mortality decreased from 7 ⁇ 8% to less than 3%.
  • Example 4 inoculated with +05 cfu / ml
  • GU2 strain of the present invention in 100 ml of water
  • Example 5 inoculated with 1.00E + 05 cfu / ml
  • Example 6 was prepared inoculated with 5.00E + 04 cfu / ml.
  • Comparative Example 3 in which only bamboo vinegar solution was added, decreased to 4.5 ppm from the initial 15 ppm to 12 hours, but increased again after 24 hours.
  • Comparative Example 3 in which only bamboo vinegar solution was added, decreased to 4.5 ppm from the initial 15 ppm to 12 hours, but increased again after 24 hours.
  • Examples 3 to 6 of the present invention was found to decrease from 4.5ppm to 9.0ppm from the initial 16ppm to 12 hours and lowered by the metabolism of the strain over time, compared to the initial odorous substance concentration is reduced The ratio was constantly kept low.
  • the ammonia-reducing effect at 12 hours was slightly higher than that of Comparative Example 3 containing only bamboo liquor solution.
  • the concentration of ammonia was increased in 2, but in Examples 3, 5, and 6, it was confirmed that the concentration was significantly lower.
  • the biofilter apparatus of the present invention 200 g of portant cement, 260 g of silica sand powder, 20 g of lime component, 40 g of alumina cement, and 80 g of peat material were strongly stirred for about 3 minutes with 290 g of water mixed with 20 g of a surfactant, and the prepared mixture was stirred.
  • the carrier After casting to a mold of the size of 100mm x 100mm x l00mm, the carrier was pre-cured for 6 hours at 50 °C and hydrothermally cured for 8 hours at 180 °C in an oatclave.
  • the dry specific gravity of the carrier was found to be about 0.33, and the pH of the solution was measured by mixing 10 g of the prepared carrier with 100 g of water and the pH of the solution was about 7.7.
  • microorganisms of Table 12 were fixed to the carriers, respectively, to obtain biofilter devices of Examples 7 to 9 and Comparative Example 4.
  • Example 7 Bacillus subtilis GU1
  • Example 8 Bacillus subtilis GU1, Nitrosomonas europaea strain, Nitrobacter agilis strain, Nitrosomonas sp.
  • Example 9 Bacillus subtilis GU1, Bacillus subtilis GU2, Pseudomonas sp., Thiobacillus sp., Bacillus sp. Comparative Example 4 Activated Sludge Collected from Sewage Treatment Plant
  • 5 ml of the effective volume filled with the carrier was inoculated with 500 ml of the culture medium (absorbance of 0.5) of each microorganism cultured in a general nutrient medium.
  • Examples 8 and 9 were inoculated in 500 ml total aliquots of each microorganism.
  • the carrier was supported on an activated sludge of 5 g / L of MLSS and aerated for 24 hours, followed by filling into a biofilter of 5 l of effective volume.
  • the biofilter filled with the microorganism-attached carrier passes through the odor gas generated in the livestock manure public treatment plant collection tank (standard 18,000W ⁇ 14,000L ⁇ 5,000H, effective capacity: 1,008 m 3 ) for 10 weeks by 10 L / min. To stabilize the microorganisms.
  • the concentration of the tower stay in the biofilter was adjusted to 5 seconds, and the concentration of the malodorous gas generated in the livestock manure public treatment plant collection tank was measured at the inlet and the outlet, respectively.
  • Malodorous items are ammonia (NH 3 ), hydrogen sulfide (H 2 S), methylmerethane (CH 3 SH), and complex odor, and the measurement method is shown in Table 13.
  • Table 14 shows the results of removing pollutants by measuring the inflow and outflow concentrations on each of the malodorous substances on the 1st, 31st and 91st days.
  • a biofilter device In order to construct the pilot biofilter device of the present invention, a biofilter device, a cleaning scrubber used as a humidifier of the biofilter device, and an acid gas removal chemical cleaning device installed in front of the cleaning scrubber are prepared on a pilot scale, respectively. Connected.
  • the biofilter device of Example 10 is 1,800W ⁇ 1,400L ⁇ 2,600H (6,550 L), and the carrier with the microorganism of Example 6 attached therein is filled with an effective volume of 1,400 L in a single layer, Without adjusting the pH adjusting agent such as medium, acid, or alkali, the internal temperature of the biofilter device was adjusted to be maintained at 15 ° C or higher, and the air column residence time was 16 seconds and the air velocity (SV) was 0.16 m / s. The water was circulated in the following scrubber as a humidifier.
  • the pH adjusting agent such as medium, acid, or alkali
  • the size of the main body of the cleaning scrubber is 1,600W ⁇ 1,000L ⁇ 1,600H (2,500L), and a blower (capacity 25 m 3 / min) is installed at the bottom of the main body so that the residence time is 6 seconds.
  • Capacity 1,000 L was made to continuously spray water into two spiral nozzles by a circulating water supply pump (capacity 50 L / min).
  • the biofilter apparatus of Example 11 uses the apparatus of Example 10, but uses bamboo vinegar dilution water diluted with 0.5% by weight of bamboo vinegar in place of water in a scrubber.
  • the biofilter device of Example 12 was inoculated at the concentration of 1.00E + 05 cfu / ml of Bacillus subtilis GU1 strain by using the device of Example 10, but diluted with 0.5% by weight of bamboo vinegar diluted with bamboo vinegar instead of water of the scrubber.
  • One GU1- bamboo liquor dilution water was used.
  • the biofilter device of Example 13 is an acid gas removal chemical cleaning device in front of the bamboo vinegar cleaning scrubber of the biofilter device of Example 11, the chemical cleaning device is 1,600W ⁇ 1,000L ⁇ 1,600H (2,500 L), and a blower (capacity 25 m 3 / min) was installed at the bottom of the main body so that the residence time was 6 seconds, and the bottom of the main body was supplied with a circulating water supply pump (capacity 50 L / min) ) To continuously spray into two spiral nozzles.
  • Table 15 shows the removal efficiency of pollutants by measuring the inflow and outflow concentrations for each odorous substance at 1st, 31st and 91st day.
  • Table 15 shows the deodorization efficiency test using the pilot plant. The deodorization efficiency was higher than the test results using the laboratory scale test apparatus shown in Table 14.
  • Example 13 the concentration of hydrogen sulfide and methyl mercaptan at the outlet was significantly lower than that of Comparative Example 9, which was determined by the addition of an acid gas removal chemical cleaning device in front of the bamboo vinegar cleaning scrubber of the biofilter device of Example 11. do.
  • Example 12 the concentration of ammonia, hydrogen sulfide, methylmercaptan, and complex odor at the outlet was lower than that of Example 11.
  • the Bacillus subtilis GU1 strain in the bamboo vinegar-cleaning scrubber circulating water of the biofilter device of Example 11 It is judged to be the result of using GU1- bamboo vinegar dilution water.

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Abstract

The present invention relates to novel microorganism Bacillus subtilis GU01 separated from bamboo smoke distillates, and to a use thereof. The microorganism of the present invention can be grown in a culture medium containing 0.1 to 50 weight % of pyroligneous liquor, and therefore, can be used as an ingredient of feed additives containing a pyroligneous liquor, and further can be used as a microorganism for a bio-filter which sprays a pyroligneous liquor for removing malodorous substances.

Description

바실러스 서브틸리스 GU1와 그 이용Bacillus subtilis GU1 and use
본 발명은 죽초액으로부터 분리한 미생물 및 그 미생물의 용도에 관한 것으로, 본 발명의 미생물은 목초액과 함께 사용되어 가축 폐사율 감소, 출하기간 단축, 항병력 증가, 축분 냄새저감 및 육질 개선 등의 효과를 가져오는 사료첨가제로 사용될 수 있고, 바이오필터용 미생물로서 사용되어 암모니아, 황화수소, 탄화수소, 저급지방산, VOCs 등의 복합악취 가스를 흡수, 흡착, 분해 제거한다.The present invention relates to a microorganism isolated from bamboo vinegar and the use of the microorganism, the microorganism of the present invention is used in conjunction with the vinegar solution to bring the effect of reducing the mortality rate of livestock, shorten the shipping period, increase the history of history, reduce the smell of meat and improve meat quality It can be used as a feed additive and used as a microorganism for biofilters to absorb, adsorb, and decompose complex odorous gases such as ammonia, hydrogen sulfide, hydrocarbons, lower fatty acids and VOCs.
목초액은 유기산과 알코올류, 중성 성분, 염기성 성분 등 100여 종의 미량 성분이 함유되어 있으며, 주요 성분으로는 초산 등의 유기산과 알코올류, 폴리페놀류 등의 기능성 물질이 함유되어 악취물질의 제거 등에 이용되고 있다.Wood vinegar contains about 100 kinds of trace components such as organic acids, alcohols, neutral components and basic components, and main components include organic acids such as acetic acid and functional substances such as alcohols and polyphenols. It is used.
최근 신종유해물질로 인한 식품안전사고로 위생과 안전 축산물에 대한 소비자 관심의 증대와 더불어 이제는 축산물을 선택할 때 양보다는 맛과 안전에 더욱 비중을 두고 있는 것이 현실이다. 또한 국제적으로도 식품안전관리기준이 강화되고 있으며, 국내 축산물의 해외 수출을 위해서도 안전성 확보는 가장 중요한 과제로 떠오르고 있다. 이와 같이 축산물의 완전개방화에 따른 대응전략으로 우리 축산물의 고급화에 대한 전략이 시급한 시점에서 우리 국민이 건강식품으로 선호하고 있는 오리, 육계, 돼지고기에 대한 고급 브랜드화에 관심이 고조되고 있는 실정이다. With the recent increase in consumer interest in hygiene and safe livestock products due to food safety accidents caused by new harmful substances, the reality is that now more emphasis is placed on taste and safety than on sheep. In addition, food safety management standards are being strengthened internationally. Securing safety is also the most important task for overseas export of domestic livestock products. As the response strategy for the full opening of livestock products is urgently needed, the high-level branding of ducks, broilers, and pork, which Koreans prefer as a health food, is increasing.
한편, 가축분뇨처리장, 음식물 보관 및 처리장, 하폐수처리장, 부산물비료 제조장, 폐기물 저장 및 처리장, 하수중계펌프장, 마을하수처리장 등의 악취 배출원에서 발생되는 암모니아, 황화합물, 지방산류, 아민류, 탄화수소, VOCs 등의 대기오염(악취) 물질을 포집하여 제거하는 기존의 방법으로는 흡착 탈취법과 약액 세정법 및 바이오필터법이 주로 사용된다. Meanwhile, ammonia, sulfur compounds, fatty acids, amines, hydrocarbons, VOCs, etc. generated from odorous sources such as livestock manure treatment plant, food storage and treatment plant, sewage treatment plant, by-product fertilizer plant, waste storage and treatment plant, sewage relay pump plant, and village sewage treatment plant. Adsorption deodorization method, chemical liquid cleaning method and biofilter method are mainly used to collect and remove air pollution (odor) substances.
흡착 탈취법은 활성탄과 같은 흡착제에 악취물질을 통과시켜서 미세 기공에 가스 상태의 대기오염(악취) 물질을 흡착시켜 제거시키고 대기오염(악취) 물질로 충진된 흡착제는 제거효율을 높게 유지하기 위해서는 수시로 재생시키거나 교환하여야 하고 처리효율이 낮은 단점이 있다. Adsorption deodorization method passes odorous substances through adsorbents such as activated carbon and removes them by adsorbing gaseous air pollution (odor) substances into fine pores, and adsorbents filled with air pollution (odor) substances are frequently used to maintain high removal efficiency. It has to be recycled or exchanged and has low processing efficiency.
약액 세정법은 반응기 내에서 약품을 희석한 순환수를 미세 분사하여 대기오염(악취) 물질과 접촉하도록 하여 제거하는 방법으로 탈취 대상 악취물질을 제거하는 약품을 선정하여 사용함으로써 탈취 대상 악취물질 제거효율을 높이는 장점은 있으나, 화학약품 사용으로 작업자 보건위생과 주변환경을 오염시키는 문제가 야기될 뿐만 아니라 탈취장치 폐액 처리에 따른 수질오염도 증가 등의 단점이 있다. The chemical liquid cleaning method is a method of removing the odorous substances to be deodorized by selecting and using a chemical that removes the odorous substances to be deodorized by spraying finely diluted circulating water in the reactor to make contact with air pollution (odor) substances. Although there is an advantage in height, the use of chemicals not only causes problems of worker health hygiene and polluting the surrounding environment, but also has disadvantages such as increased water pollution due to the treatment of waste deodorizer.
바이오필터법은 미생물의 흡수, 흡착, 분해 등의 기작에 의해서 악취가스를 제거하는 친환경적이고 탈취효율이 높으나, 다량 발생되는 고농도의 악취가스인 경우에는 충분한 접촉시간 확보를 위한 설치 부지가 과다 소요되어 초기투자비가 높고 대기 중의 암모니아성 가스가 순환수에 흡수되어 처리됨으로써 순환수 폐액의 수처리 과정에서 총질소 함량을 크게 높이는 등의 단점이 있다. The biofilter method is environmentally friendly and high in deodorization efficiency to remove odor gas by mechanisms such as absorption, adsorption and decomposition of microorganisms, but in case of high concentration of odor gas generated in large quantities, it requires excessive installation site to secure sufficient contact time. Since the initial investment cost is high and the ammonia gas in the atmosphere is absorbed and treated in the circulating water, there is a disadvantage of greatly increasing the total nitrogen content in the water treatment process of the circulating water waste liquid.
또한 축사(돼지, 오리, 닭 등)시설의 악취가스 제거와 소독 등의 축사환경개선을 위해서 탈취제, 소독제를 고압분무기로 분무하는 방법이 주로 사용되지만, 액상의 탈취제 또는 소독제를 물에 희석하여 살포하면 가축에게 스트레스를 주고 살포한 순간에는 효과가 크게 나타나지만 지속시간이 짧아 주기적으로 살포해 주어야 하기 때문에 인력 소요와 약액 소모량이 많은 단점이 있다. In addition, the method of spraying deodorant and disinfectant with high pressure sprayer is mainly used for the improvement of livestock environment such as odor gas removal and disinfection of livestock house (pig, duck, chicken, etc.), but liquid deodorant or disinfectant is diluted with water and sprayed. When the stress is applied to the livestock and the effect is greatly effected, but the duration is short, because it has to be sprayed periodically, there is a drawback of manpower consumption and drug consumption.
위와 같은 식품의 안전도를 높이기 위한 항생제 사용규제와 육질개선을 위한 기능성 미생물과 기존 탈취공법의 탈취효율이 낮고, 취급과 주변 환경오염 문제를 극복하기 위해서는 탈취장치의 효율화와 함께 탈취효율이 뛰어난 미생물의 개발 필요성이 증대되고 있다. The deodorization efficiency of antibiotics to improve the safety of food and functional microorganisms for improving meat quality and existing deodorization methods are low, and to overcome the problems of handling and environmental pollution, the efficiency of deodorizers and the efficiency of deodorizing devices The need for development is increasing.
본 발명은 목초액과 함께 사용되어 목초액 단독으로 달성하기 힘든, 가축의 증체량, 도체율, 육색 및 이화학적 특성 및 물리적 특성, 불포화지방산의 함량 등의 향상을 가져오는 사료첨가제로서의 효과 및 악취물질 제거 효과에 있어서, 상승효과를 가져오는 신균주를 분리 및 동정하고, 이 신균주를 목초액을 함유한 사료첨가제 및 목초액을 이용하는 바이오필터장치에 이용하는 것이다.The present invention is used together with the wood vinegar solution, which is difficult to achieve by the wood vinegar alone, the effect as a feed additive and the odorous substance removal effect to improve the weight gain, carcass rate, meat color and physicochemical properties and physical properties, the content of unsaturated fatty acids, etc. In the present invention, new strains having a synergistic effect are isolated and identified, and the new strains are used in a biofilter apparatus using a feed additive containing wood vinegar and wood vinegar.
본 발명은 죽초액에서 분리되고 목초액을 0.1 ~ 50 중량% 포함하는 배지에서 생육가능한 것을 특징으로 하는 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P]를 제공한다.The present invention provides Bacillus subtilis GU1 [Accession No. KCCM 10890P], which is isolated from bamboo vinegar and is capable of growing in a medium containing 0.1 to 50% by weight of wood vinegar.
본 발명은 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주를 목초액을 0.5 ~ 10 중량% 포함하는 배지에서 발효시킨 배양물을 제공한다.The present invention provides a culture in which Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain is fermented in a medium containing 0.5 to 10% by weight of wood vinegar.
본 발명의 배양물에서 상기 배지는 고체배지인 것을 특징으로 한다.In the culture of the present invention, the medium is characterized in that the solid medium.
본 발명은 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주를 목초액을 0.5 ~ 10 중량% 포함하는 배지에서 발효시킨 배양물을 포함하는 사료첨가제를 제공한다.The present invention provides a feed additive comprising a culture fermented Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain in a medium containing 0.5 to 10% by weight of wood vinegar.
본 발명은 악취물질을 바이오필터 장치 내부로 유입시키는 송풍기와, 바이오필터 장치 내부로 수분을 공급하는 가습장치와, 미생물이 부착된 담체를 포함하는 바이오필터 장치에 있어서, 상기 가습장치는 목초액 조성물이 분사되는 세정식 목초액 스크라버이고, 상기 담체에 부착된 미생물은 죽초액에서 분리되고 죽초액을 0.5 ~ 50 중량% 포함하는 배지에서 생육가능한 것을 특징으로 하는 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P]인 것을 특징으로 하는 악취물질 제거용 바이오필터 장치를 제공한다.The present invention provides a biofilter comprising a blower for introducing a malodorous substance into the biofilter device, a humidifier for supplying moisture into the biofilter device, and a carrier having microorganisms attached thereto, wherein the humidifier is a wood-choice solution composition. Bacillus subtilis GU1 [Accession number KCCM, characterized in that the sprayed washing herbaceous scrubber, wherein the microorganisms attached to the carrier are separated from the bamboo vinegar solution and grow in a medium containing 0.5 to 50% by weight of bamboo vinegar solution. 10890P] to provide a biofilter device for removing odorous substances.
본 발명의 악취물질 제거용 바이오필터 장치에서 상기 미생물은 니트로소모나스 속(Nitrosomonas sp.) 균주, 바실러스 속(Bacillus sp.) 균주, 슈도모나스 속(Pseudomonas sp.) 균주, 니트로소모나스 속(Nitrosomonas sp.) 균주, 니트로박터 속(Nitrobacter sp.) 균주, 치오바실러스 속(Thiobacillus sp.) 균주 중에서 어느 하나 이상의 균주가 더 포함된 것을 특징으로 한다.In the biofilter device for removing odorous substances of the present invention, the microorganism is Nitrosomonas sp., Bacillus sp., Pseudomonas sp., Nitrosomonas sp. .) Strains, nitrobacter sp. ( Nitrobacter sp.) Strains, genus Bacillus (Thiobacill us sp.) Is characterized in that any one or more strains are further included.
본 발명의 악취물질 제거용 바이오필터 장치에서, 상기 세정식 목초액 스크라버에서는 목초액 조성물과 함께 목초액에서 유래된 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주 및 바실러스 서브틸리스(Bacillus subtilis) GU2 [기탁번호 KCCM 10891P] 균주 중에서 선택된 어느 하나 이상의 균주가 함께 분사되는 것을 특징으로 한다.In the bio-filter device for removing the odor substance of the present invention, the ablution vinegar disk rabeo the derived Bacillus from wood vinegar with wood vinegar composition subtilis (Bacillus subtilis) GU1 [Accession No. KCCM 10890P] strain and Bacillus subtilis (Bacillus subtilis ) GU2 [Accession No. KCCM 10891P] is characterized in that any one or more strains selected from among the strains are sprayed together.
본 발명의 신균주 바실러스 서브틸리스 GU1은 목초액과 혼합사용되거나 목초액을 함유한 배지에서 발효되어 사료첨가제로서 기존 목초액이 달성할 수 없는 가축 폐사율 감소, 출하기간 단축, 항병력 증가, 축분 냄새저감 및 육질 개선 등의 효과를 가져온다.Bacillus subtilis GU1 of the present invention is mixed with wood vinegar or fermented in a medium containing wood vinegar solution as a feed additive that can not be achieved conventional animal vinegar mortality mortality reduction, shorten the shipping period, increase the history of history, reduce the smell of meat and meat quality It brings the effect of improvement.
또한 본 발명의 바이오필터 장치는 죽초액에서 분리된 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주로 인하여 악취물질 제거 효과가 뛰어나고, 특히 가습장치로 목초액을 분사하는 세정식 스크라버가 이용됨으로 인하여 바이오필터로 유입되는 이물질과 암모니아성 악취물질 등의 농도를 현저히 낮출 수 있다.In addition, the biofilter device of the present invention is excellent in removing odorous substances due to Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain isolated from bamboo vinegar solution, and particularly, a scrubber for spraying wood vinegar solution with a humidifier. By using it can significantly reduce the concentration of foreign matter and ammonia-odorous odor substances introduced into the biofilter.
도 1은 본 발명의 실시예 중 하나인 가습장치로 세정식 목(죽)초액 스크라버를 사용한 바이오필터 장치의 개략도이다.1 is a schematic view of a biofilter apparatus using a cleaning throat (chochu) vinegar scrubber as one of the embodiments of the present invention.
도 2는 본 발명의 실시예 중 하나인 약액 세정장치 또는 금속촉매 탈취장치가 부가된 바이오필터 장치의 개략도이다.2 is a schematic view of a biofilter apparatus to which a chemical cleaning apparatus or a metal catalyst deodorizing apparatus, which is one of embodiments of the present invention, is added.
도 3은 본 발명의 균주를 각각의 온도에서 10분간 처리한 후의 균수 변화를 나타낸 그래프이다.Figure 3 is a graph showing the number of bacteria after treatment of the strain of the present invention at each temperature for 10 minutes.
[도면의 주요부분에 대한 부호설명][Code Description of Main Part of Drawing]
10: 바이오필터 장치 11, 21, 31: 분무노즐10: biofilter unit 11, 21, 31: spray nozzle
12, 22, 32: 유입구 13, 23, 33: 배출구12, 22, 32: inlet 13, 23, 33: outlet
14: 담체 15: 영양배지 공급탱크14: carrier 15: nutrient medium supply tank
16: 알카리 공급탱크 17: 산 공급탱크16: Alkaline supply tank 17: Acid supply tank
18: 미생물 배양기 19: 송풍기18: microbial incubator 19: blower
20: 가습장치[세정식 목초액 스크라버] 24, 34: 충진재층20: humidifier [washing wood vinegar scrubber] 24, 34: filling material layer
25, 35: 저수조 26, 36: 순환펌프25, 35: reservoir 26, 36: circulation pump
27: 목초액 30: 약액 세정장치27: wood vinegar 30: chemical cleaning device
37: 약액37: chemical
전라남도 담양에서 생산된 pH 2.6 내외의 죽초액에서 본 발명의 균주를 분리 및 동정하였고, 분리된 균주는 바실러스 서브틸리스(Bacillus subtilis)로 동정되었다. 상기 균주는 바실러스 서브틸리스(Bacillus subtilis) GU1로 명명하고, 한국유전자은행에 2007년 11월 21일 기탁번호 KCCM 10890P로 부다페스트조약에 따라 국제기탁하였다.The strain of the present invention was isolated and identified in bamboo vinegar solution of pH 2.6 produced in Damyang, Jeollanam-do, and the isolated strain was identified as Bacillus subtilis . The strain was named Bacillus subtilis GU1 and was deposited internationally in accordance with the Budapest Treaty under the deposit number KCCM 10890P on November 21, 2007.
본 발명의 균주는 목초액과 혼합되거나 또는 목초액을 함유하는 배지에서 발효된 배양액의 형태로 목초액 단독으로 달성할 수 없는 가축 폐사율 감소, 출하기간 단축, 항병력 증가, 축분 냄새저감 및 육질 개선 등의 효과를 가져온다.The strain of the present invention has the effect of reducing livestock mortality that can not be achieved alone, in the form of a culture solution fermented in the medium containing or mixed with the wood vinegar solution, shorten the shipping period, increase the history of history, reduce the smell of stalk and improve the meat quality Bring.
본 발명의 균주의 배양을 위한 배지, 사료첨가제의 유효성분 또는 악취물질 제거제의 유효성분으로 사용되는 목초액은 침엽수, 활엽수, 교목, 관목, 상록수, 낙엽수, 상록침엽수, 낙엽침엽수, 상록활엽수, 낙엽활엽수, 및 초목의 잎, 줄기, 뿌리, 열매, 꽃 중에서 선택된 어느 하나 이상을 열분해, 중탕, 가온, 증류, 추출, 및 덖음 중에서 선택된 하나 이상의 과정에서 생성한 액체 또는 정유 또는 증기를 회수하여 냉각, 응축, 분리, 숙성, 여과, 증발, 및 증류 중에서 선택된 하나 이상의 가공 과정을 통하여 제조될 수 있다. 예를 들어, 본 발명의 목초액은 침엽수, 활엽수, 교목, 관목, 상록수, 낙엽수, 상록침엽수, 낙엽침엽수, 상록활엽수, 낙엽활엽수, 및 초목의 잎, 줄기, 뿌리, 열매, 꽃 중에서 선택된 하나 또는 둘 이상을 혼합하여 150 내지 350 ℃에서 직접 또는 간접 열분해 하거나, 가온을 반복하여 중탕하거나, 가마솥에서 대기압 또는 감압 상태에서 80 내지 150 ℃로 가온하거나, 용매 추출 또는 초임계유체 추출 방법에 의하여 추출하거나, 또는 가마솥에서 데워 익히는 덖음을 하고, 상기 열분해, 중탕, 가온, 추출, 또는 덖음 과정에서 발생하는 액체 물질 또는 증기를 포집하여 이를 냉각 및 응축하고, 상기 냉각 또는 응축된 목초액 속에 함유된 식물 정유 성분을 회수하기 위하여 유수 분리하고, 상기 목초액 속에 함유된 이물질 및 타르를 여과하고, 상기 목초액을 화학적 안정화를 위하여 상온 또는 가온하여 숙성하고, 상기 목초액 속에 함유된 이물질 및 타르를 분리하여 제조한다. 특히 열분해하여 탄화시키지 않은 온도에서 가마솥에 넣어 상압 또는 감압 상태로 80 내지 150 ℃에서 가온하거나, 가온을 반복하여 중탕하거나, 용매 추출 또는 초임계유체 추출 방법에 의하여 추출하거나, 가온 또는 증류 또는 덖는 과정에서 발생하는 액체 물질 또는 증기 또는 정유를 포집하고 이를 냉각 및 응축 및 분리 과정을 거쳐 제조된 목초액 조성물이 타르 함량이 낮아 바람직하다. 본 발명의 목초액은 원재료나 제조방법이 다른 2종 이상의 목초액을 혼합하여 사용할 수 있다. The medium for the culture of the strain of the present invention, the wood vinegar used as an active ingredient of feed additives or odorant removal agent is conifers, deciduous trees, trees, shrubs, evergreens, deciduous trees, evergreen conifers, deciduous conifers, evergreen softwoods, deciduous softwoods Cooling and condensing liquids or essential oils or vapors produced by one or more processes selected from pyrolysis, bath, heating, distillation, extraction, and weeding of any one or more selected from leaves, stems, roots, fruits and flowers of vegetation; It can be prepared through one or more processing selected from, separation, ripening, filtration, evaporation, and distillation. For example, the wood vinegar of the present invention is one or two selected from conifers, deciduous trees, arbors, shrubs, evergreens, deciduous trees, evergreen conifers, deciduous conifers, evergreen hardwoods, deciduous hardwoods, and leaves, stems, roots, fruits, and flowers of vegetation. Mixing the above to direct or indirect pyrolysis at 150 to 350 ℃, repeated heating in hot water, warmed to 80 to 150 ℃ in atmospheric pressure or reduced pressure in a cauldron, extraction by solvent extraction or supercritical fluid extraction method, Or steaming and cooking in a cauldron, collecting and cooling liquid condensate or vapor generated during the pyrolysis, bath, warming, extraction, or steaming process, and cooling down and condensing the plant essential oil components contained in the cooled or condensed wood vinegar solution. The oil and water are separated for recovery, the foreign matter and tar contained in the wood vinegar are filtered and the wood vinegar is Aged at room temperature or warmed for stabilization, and is prepared by separating the foreign matter and tar contained in the wood vinegar. Particularly, the process is carried out in a cauldron at a temperature not pyrolyzed and carbonized, and heated at 80 to 150 ° C. under atmospheric pressure or reduced pressure, or repeated heating and heating, followed by extraction, heating, distillation, or steaming by solvent extraction or supercritical fluid extraction. The wood vinegar composition prepared by capturing a liquid substance or steam or essential oil which occurs in the process of cooling, condensation and separation is preferable because of its low tar content. The wood vinegar of the present invention can be used by mixing two or more kinds of wood vinegar with different raw materials or manufacturing methods.
본 발명의 균주가 목초액을 포함하는 배지에서 발효된 배양물은 목초액이 가지는 영양학적 또는 면역학적 특성을 현저히 상승시킴과 동시에 악취제거 효율을 높인다. 상기 배지는 액상 또는 고상일 수 있고, 사료첨가제로 사용되는 경우에는 고체상의 사료에 균일하게 혼합되기 쉽고, 고체 배지 자체가 영양원이 될 수 있으므로 고체 배지를 사용하는 것이 바람직하다. 고체 배지의 원료로 바람직한 것은 사료의 원료로 사용되는 곡류, 두류, 효모 또는 목재를 포함한 식물체 가공의 부산물이 이용될 수 있고, 탈지강, 대두박, 톱밥 등 다양한 원료가 필요에 따라 하나 이상 조합되어 사용될 수 있다.Cultures fermented by the strain of the present invention in a medium containing wood vinegar significantly increases the nutritional or immunological characteristics of wood vinegar and at the same time increases the odor removal efficiency. The medium may be liquid or solid, and when used as a feed additive, it is preferable to use a solid medium because it may be easily mixed uniformly with a solid feed, and the solid medium may be a nutrient source. The preferred raw material for the solid medium may be a by-product of plant processing including cereals, soybeans, yeast or wood, which are used as raw materials for feed, and various raw materials such as skimmed steel, soybean meal, sawdust, etc. may be used in combination as necessary. Can be.
본 발명의 균주가 접종될 배지에 첨가되는 배지 중량을 기준으로 목초액의 함량은 0.5 ~ 10 중량%, 더욱 바람직하게는 2~10 중량%인 것이고, 가장 바람직하게는 2~5 중량%이다. 또한 본 발명의 배양물은 15 ~ 45 ℃, 바람직하게는 20 ~ 42 ℃, 더욱 바람직하게는 30 ~ 40 ℃에서 배양하는 것이 바람직하면, 배양시간은 12시간 이상, 바람직하게는 24시간 이상, 더욱 바람직하게는 36시간 이상, 더더욱 바람직하게는 48시간 배양하는 것이고, 최대 배양시간은 특별히 한정할 필요는 없으나, 48시간 이상을 배양하더라도 본 발명의 균주량이 증대되지 않으므로 60시간 이내에서 배양하는 것이다.The content of wood vinegar is 0.5 to 10% by weight, more preferably 2 to 10% by weight, most preferably 2 to 5% by weight, based on the weight of the medium added to the medium to be inoculated with the strain of the present invention. In addition, if the culture of the present invention is preferably incubated at 15 ~ 45 ℃, preferably 20 ~ 42 ℃, more preferably 30 ~ 40 ℃, the incubation time is 12 hours or more, preferably 24 hours or more, more Preferably 36 hours or more, even more preferably 48 hours, the maximum incubation time is not particularly limited, but even if culture for 48 hours or more because the strain amount of the present invention is not increased within 60 hours.
또한 본 발명의 균주는 목초액과 혼합되어 발효과정을 거치지 않은 상태로 제형화되어 사료첨가제나 악취물질 제거제로 사용되는 경우에도, 제형화가 이루어진 후 후발효가 진행되어 본 발명의 사료첨가제로서의 효과를 달성할 수 있다.In addition, even if the strain of the present invention is mixed with wood vinegar and formulated without fermentation, and used as a feed additive or odor removing agent, post-fermentation proceeds after the formulation is achieved to achieve the effect as a feed additive of the present invention can do.
이하 도 1 및 도 2에 예시된 도면을 참조하여 본 발명의 오염물질 제거용 바이오필터 장치를 설명한다. 바이오필터 장치(10)는 악취물질을 바이오필터 장치 내부로 유입시키는 송풍기(19)와, 바이오필터 장치 내부로 수분을 공급하는 가습장치(20)와, 미생물이 부착된 담체(14)를 포함하는 통상의 바이오필터 장치이면 어느 것이나 이용될 수 있다.Hereinafter, a biofilter device for removing contaminants of the present invention will be described with reference to the drawings illustrated in FIGS. 1 and 2. The biofilter device 10 includes a blower 19 for introducing malodorous substances into the biofilter device, a humidifier 20 for supplying moisture into the biofilter device, and a carrier 14 to which microorganisms are attached. Any conventional biofilter device may be used.
본 발명의 바이오필터 장치에서 상기 가습장치(20)는 목초액 조성물이 분사되는 세정식 목초액 스크라버가 이용될 수 있다. 바이오필터 본체에서 목초액 조성물은 악취오염물질인 암모니아 가스와 황화수소 및 메틸머캅탄과 반응하여 초산암모늄염, 황화수소 이온, 메틸머캅탄 이온 등으로 중화 및 흡착시켜 아래 반응식과 같이 슬러지와 함께 외부로 배출됨으로 인하여 스크라버 순환수의 교환 과정에서 배출되는 폐액이 하폐수처리 공정의 질소화합물 함량 증가에 영향을 주지 않아 기존 바이오필터 공법에서 가장 큰 문제가 되고 있는 총질소 증가 문제와 유입되는 악취오염도에 따라 탈취효율의 편차가 큰 문제가 없다. 또한, 고농도 악취가스가 유입되더라도 목초액 조성물이 분사되는 세정식 목초액 스크라버에서 80내지 90% 제거되기 때문에 저농도의 잔여가스가 바이오필터 장치에 유입되기 때문에 탈취효율이 높다. In the biofilter device of the present invention, the humidifying apparatus 20 may be a cleaning wood-vinegar scrubber sprayed with a wood-choice solution composition. In the biofilter body, the wood vinegar composition reacts with ammonia gas, hydrogen sulfide, and methyl mercaptan, which are odor pollutants, and is neutralized and adsorbed with ammonium acetate salt, hydrogen sulfide ion, methyl mercaptan ion, etc., and is discharged to the outside together with sludge as shown in the following reaction formula. Wastewater discharged from the exchange of scrubber circulating water does not affect the increase of nitrogen compound content in the sewage water treatment process, which is the biggest problem in the existing biofilter process. Deviation is not a big problem. In addition, even if a high concentration of malodorous gas is introduced, since 80 to 90% is removed from the cleansing wood-vinegar scrubber sprayed with the wood-vinegar composition, the low-density residual gas is introduced into the biofilter device, so the deodorizing efficiency is high.
대기 중의 암모니아 가스제거는 목초액 조성물의 주성분인 초산(CH3COOH)은 목초액 조성물 수용액 중에서 아래 반응식 1과 같이 아세트산이온(CH3COO-)과 수소이온(H+)으로 해리된다. 또한, 목초액 스크라버에 유입되는 악취물질 중 암모니아(NH3) 가스는 반응식 2와 같이 수용액 중에 가수분해하여 암모늄이온(NH4 +)과 수산이온(OH-)으로 해리한다. 따라서 목초액 스크라버 본체 내로 유입된 암모니아 가스는 목초액 수용액 중에서 가수분해 반응에 의해 생성된 암모늄이온과 수산이온의 증가로 인해서 목초액 수용액의 pH를 상승시킨다. 악취물질 중 암모니아 가스의 제거는 목초액 수용액 중에서 해리된 암모늄이온이 초산이온과 산 염기 반응에 의해 반응식 3에서와 같이 초산암모늄염(CH3COONH4)이 되면서 악취가 제거된 것으로 판단된다. 목초액 조성물의 예상되는 반응식은 다음과 같다. The removal of ammonia gas from the atmosphere is carried out by dissolving acetic acid (CH 3 COOH), the main component of the wood vinegar composition, into acetate ions (CH 3 COO ) and hydrogen ions (H + ) as shown in Scheme 1 below. In addition, ammonia (NH 3 ) gas among the malodorous substances flowing into the wood vinegar scrubber is hydrolyzed in an aqueous solution as in Scheme 2 and dissociated into ammonium ions (NH 4 + ) and hydroxide ions (OH ). Therefore, the ammonia gas introduced into the wood vinegar scrubber body increases the pH of the wood vinegar aqueous solution due to the increase of ammonium ions and hydroxyl ions produced by the hydrolysis reaction in the wood vinegar aqueous solution. The removal of the ammonia gas from the odorous substance is determined to remove the odor as ammonium acetate (CH 3 COONH 4 ) dissociated in the aqueous solution of the wood vinegar to the acid ions and acid-base reaction as in Scheme 3. The expected reaction scheme of the wood vinegar composition is as follows.
<반응식 1><Scheme 1>
CH3COOH → CH3COO- + H+ CH 3 COOH → CH 3 COO - + H +
<반응식 2><Scheme 2>
NH3 + H2O → NH4 + + OH- NH 3 + H 2 O → NH 4 + + OH -
<반응식 3><Scheme 3>
CH3COO- + NH4 + → CH3COONH4 CH 3 COO - + NH 4 + → CH 3 COONH 4
대기 중의 황화합물 중에서 황화수소가스 제거는 목초액 수용액 중에서 초산이 해리되면서 생성된 초산이온과 산 염기반응에 의해 아래 반응식 4에서와 같이 초산(CH3COOH)과 HS-의 고착된 비휘발성 염이 생성되면서 악취가 제거되며, 메틸머캅탄(CH3SH) 가스의 경우는 반응식 5와 같이 초산(CH3COOH)과 CH3S-의 고착된 비휘발성 염이 생성되면서 악취가 제거되는 반응 메카니즘이 예상된다. 목초액 조성물의 예상되는 반응식은 다음과 같다.The removal of hydrogen sulfide gas from the sulfur compounds in the air is odor due to the formation of fixed non-volatile salts of acetic acid (CH 3 COOH) and HS - by reaction with acetic acid ion and acid base generated by dissociation of acetic acid in aqueous solution of wood vinegar. In the case of methyl mercaptan (CH 3 SH) gas, a reaction mechanism is expected in which odor is removed as fixed nonvolatile salts of acetic acid (CH 3 COOH) and CH 3 S are generated as in Scheme 5. The expected reaction scheme of the wood vinegar composition is as follows.
<반응식 4><Scheme 4>
H2S + CH3COO- → CH3COOH + HS- H 2 S + CH 3 COO - → CH 3 COOH + HS -
<반응식 5>Scheme 5
CH3SH + CH3COO- → CH3COOH + CH3S- CH 3 SH + CH 3 COO - → CH 3 COOH + CH 3 S -
바이오필터 장치 내부를 미생물 생육에 필요한 조건을 충족시키기 위한 장치들이 추가로 부가될 수 있다. 바이오필터 장치에 부가될 수 있는 것들로는 영양배지 공급탱크(15), pH 조건을 미생물 생육에 적합한 범위로 조정하기 위한 알카리 공급탱크(16) 또는 산 공급탱크(17), 또한 온도를 미생물 생육에 적합한 범위로 조정하기 위한 바이오필터 외부의 단열재 또는 히터나 냉각기를 구비한 온도조절장치 등을 들 수 있다. 히터나 냉각기는 가온 또는 냉각기가 바이오필터 내부에 설치될 수도 있고, 바이오필터 장치 외부를 자켓처럼 감싸는 방식으로 설치될 수 있다. 또한 필요에 따라서는 바이오필터 내부의 산소농도를 높이기 위해 공기 또는 산소 공급장치가 더 구비될 수도 있다.Devices for satisfying the conditions necessary for the growth of microorganisms inside the biofilter device may be further added. Those that may be added to the biofilter device include a nutrient medium supply tank 15, an alkali supply tank 16 or an acid supply tank 17 for adjusting pH conditions to a range suitable for microbial growth, and also a temperature for microbial growth. And a thermostat equipped with a heater or a cooler outside the biofilter for adjusting to a suitable range. The heater or cooler may be installed in the warmer or cooler inside the biofilter, or may be installed in such a manner as to surround the outside of the biofilter device like a jacket. In addition, if necessary, air or an oxygen supply device may be further provided to increase the oxygen concentration in the biofilter.
본 발명에서 미생물이 부착되는 담체(14)로는 피트, 나무껍질, 퇴비 등의 자연물질, 또는 다공성 발포고분자와 같은 유기성 담체는 물론 다공성 세라믹과 같은 무기성 담체 어느 것이나 사용될 수 있다. 바람직하게는 단위 무게당 미생물 활성이 높고 유지관리가 용이하며 수분함유율이 높은 다공성 세라믹 담체를 사용하는 것이다.In the present invention, as the carrier 14 to which the microorganism is attached, any organic material such as pit, bark, compost, or organic carrier such as porous foamed polymer may be used as well as inorganic carrier such as porous ceramic. Preferably, a porous ceramic carrier having high microbial activity per unit weight, easy maintenance and high water content is used.
본 발명의 바이오필터 장치의 담체에 부착되는 미생물은 죽초액에서 분리된 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P]로서, 상기 균주는 악취물질 제거활성이 현저히 뛰어나고, 죽초액(보통 pH 2.6 내외)에서도 생육할 수 있으므로 바이오필터 장치의 내부 pH가 급격히 하락하더라도 미생물이 pH 충격을 받지않고 악취물질을 처리하는데 지장이 없다. 특히 이러한 점은 담체에 고정된 미생물에 의해 악취물질이 분해되면서 이산화탄소와 물 이외에 발효과정에서 유기산이 지속적으로 생산되어 pH를 낮춘다는 점에서 산성에 내성이 큰 바실러스 서브틸리스(Bacillus subtilis) GU1 은 바이오필터용 미생물로서 유리한 특성이 된다.The microorganism attached to the carrier of the biofilter device of the present invention is Bacillus subtilis GU1 [Accession No. KCCM 10890P] isolated from bamboo liquor, and the strain is excellent in removing odorous substances, and bamboo vinegar solution (usually pH 2.6). Because it can grow inside and outside), even if the internal pH of the biofilter device drops sharply, the microorganisms are not affected by pH and do not interfere with the treatment of odorous substances. In particular, Bacillus subtilis GU1, which is highly resistant to acidic acid, has a low pH because organic acids are continuously produced during fermentation in addition to carbon dioxide and water as odorous substances are decomposed by microorganisms fixed on the carrier. It is advantageous properties as a microorganism for biofilters.
본 발명의 담체에 부착되는 미생물로는 상기 바실러스 서브틸리스 GU1 균주와 함께 악취물질 제거에 사용되는 다른 니트로소모나스 속(Nitrosomonas sp.) 균주, 바실러스 속(Bacillus sp.) 균주, 슈도모나스 속(Pseudomonas sp.) 균주, 니트로소모나스 속(Nitrosomonas sp.) 균주, 니트로박터 속(Nitrobacter sp.) 균주, 치오바실러스 속(Thiobacillus sp.) 균주 중에서 어느 하나 이상의 균주가 함께 사용될 경우 악취물질의 종류에 관계없이 안정적으로 바이오필터 장치를 운용할 수 있다는 점에서 바람직하다. A microorganism attached to the carrier of the present invention wherein the Bacillus subtilis in other nitro consumption eggplant is used to remove malodorous substances with GU1 strain (Nitrosomonas sp.) Strain, Bacillus (Bacillus sp.) Strain, Pseudomonas species (Pseudomonas sp.) strain, Nitrosomonas sp., Nitrobacter sp., Thiobacillus sp. It is preferable in that the biofilter device can be stably operated without the need.
특히 본 발명에서는 바실러스 서브틸리스 GU1와 함께 본 발명자에 의해 죽초액에서 분리된 바실러스 서브틸리스(Bacillus subtilis) GU2 [기탁번호 KCCM 10891P] 균주를 함께 사용하는 것이 바실러스 서브틸리스 GU1 단독으로 사용하는 것 보다 암모니아와 황화합물 등의 악취물질을 흡착, 분해하는데 제거효율을 높인다는 점에서 유리하다.In particular, in the present invention, using Bacillus subtilis GU2 [Accession No. KCCM 10891P] strain isolated from bamboo shoot liquid by the present inventors together with Bacillus subtilis GU1 is to be used by Bacillus subtilis GU1 alone. It is more advantageous in that the removal efficiency is increased in adsorbing and decomposing odorous substances such as ammonia and sulfur compounds.
바실러스 서브틸리스 GU1 균주와 GU2 균주는 모두 전라남도 담양에서 생산된 pH 2.6 내외의 죽초액에서 본 발명의 균주를 분리된 것으로 한국유전자은행에 2007년 11월 21일 각각 기탁번호 KCCM 10890P 및 KCCM 10891P 로 부다페스트조약에 따라 국제기탁하였다.Both Bacillus subtilis GU1 and GU2 strains were isolated from the bamboo vinegar solution at pH 2.6 produced in Damyang, Jeollanam-do, and were reported to Korea Gene Bank on November 21, 2007, under the deposit numbers KCCM 10890P and KCCM 10891P, respectively. It has been deposited internationally under the Treaty.
본 발명의 바이오필터 장치는 미생물 배양기(18) 및 상기 미생물 배양기에서 배양된 미생물을 상기 바이오필터 장치로 이송하는 미생물 공급장치를 더 구비하는 것이 미생물을 외부에서 공급 받아 바이오필터의 담체에 주입하는 것 보다 비용을 낮춘다는 점에서 유리하다. 미생물 배양기(18)는 미생물의 생육 조건을 조정하기 위해서 배양기 내의 온도를 일정하게 유지하게 하기 위해 단열재로 배양기 외부를 처리하거나, 더욱 바람직하게는 히터가 구비되는 것이 바람직하다. 배양기에는 냉각기도 구비될 수 있으나 악취물질 제거용 미생물이 대부분 중온균으로 국내 하절기 기온이 37 ℃를 넘는 경우는 드물기 때문에 사용빈도는 낮다. 상기 미생물 배양기에서 일정 농도 또는 일정 균수 이상으로 배양된 미생물은 이송펌프 및 이송관으로 이루어진 미생물 공급장치를 통해 바이오필터 장치 내로 공급된다. 바람직하게는 담체에 고루 부착될 수 있도록 분무노즐(11)을 통해 공급하는 것이 바람직하고, 산 또는 알카리 공급장치와 일정 거리 이격된 위치에 공급하는 것이 바람직하다. 미생물이 바이오필터 장치로 공급되는 방식은 연속식 또는 간헐적으로 일정량을 공급하는 방식 또는 미리 프로그램된 수식에 의해 가변적으로 공급하는 방식 어느 것이나 이용될 수 있다. 또한 상기 미생물 배양기(18)에는 공기 또는 산소를 공급할 수 있는 공급장치가 부가되는 것이 바람직하다.The biofilter device of the present invention further comprises a microbial incubator 18 and a microbial supply device for transferring the microorganisms cultured in the microbial incubator to the biofilter device, the microorganisms being supplied from the outside and injected into the carrier of the biofilter. It is advantageous in lowering the cost. The microorganism incubator 18 preferably treats the outside of the incubator with a heat insulator to maintain a constant temperature in the incubator in order to adjust the growth conditions of the microorganisms, or more preferably, is provided with a heater. The incubator may be equipped with a cooler, but most of the microorganisms for removing odorous substances are mesophilic bacteria, and the use frequency is low since domestic summer temperatures rarely exceed 37 ℃. The microorganisms cultured at a predetermined concentration or a predetermined number of bacteria in the microorganism incubator are supplied into the biofilter device through a microorganism supply device consisting of a transfer pump and a transfer tube. Preferably, it is preferable to supply through the spray nozzle 11 so as to be evenly attached to the carrier, it is preferable to supply to a position spaced a certain distance from the acid or alkali supply device. The microorganism is supplied to the biofilter device may be used either in a continuous or intermittent manner of supplying a certain amount or a method of supplying a variable by a pre-programmed formula. In addition, the microbial incubator 18 is preferably added with a supply device for supplying air or oxygen.
미생물 배양기에서 미생물이 배출된 경우 이를 보충하기 위해 영양배지가 공급될 수 있도록 영양배지 공급장치(15)가 미생물 배양기(18)에 연결되어 있는 것이 바람직하다.When the microorganism is discharged from the microbial incubator, it is preferable that the nutritional medium supply device 15 is connected to the microbial incubator 18 so that the nutritional medium can be supplied to supplement the microorganisms.
본 발명의 바이오필터 장치에서 가습장치(20)는 목초액 조성물이 분사되는 세정식 목초액 스크라버인 것이 가습과 악취물질 특히 암모니아성 물질의 제거를 동시에 수행할 수 있다는 점에서 바람직하다. 통상의 세정식 스크라버이면 어떠한 형태의 것이든 제한없이 사용할 수 있으나, 바이오필터 장치로 수분이 공급될 수 있도록 세정식 스크라버에서 처리된 공기가 배출되는 배출구에 데미스터는 반드시 제거되어야 한다.In the biofilter apparatus of the present invention, the humidifier 20 is preferably a cleaning wood-choice scrubber to which the wood-choice composition is injected, in that it can simultaneously perform the removal of humidification and odorous substances, especially ammonia-based substances. Any type of clean scrubber can be used without limitation, but the demister must be removed from the outlet through which the treated air is discharged from the clean scrubber so that water can be supplied to the biofilter device.
본 발명의 세정식 목초액 스크라버의 하나의 구현예로는 유입구(22)에 송풍기(19)가 구비되고, 목초액 조성물 공급부로 본체 상부에 목초액 조성물 분무노즐(21)이 구비되는 세정식 스크라버가 이용될 수 있다. 송풍기를 통해 본체로 강제 유입되는 악취물질이 본체에 체류하는 시간을 증가시키기 위해 선회류를 형성하도록 하는 것이 바람직하고, 송풍기에 의한 오염물질의 강제유입은 본 발명의 탈취제와의 접촉효과를 높여 처리 효율을 증가시키는 역할을 하고, 악취물질이 외부로 빠져나가지 못하게 하는 역할도 한다. 본체의 상부 영역에는 목초액 조성물을 광범위하게 분사시키기 위한 분사노즐이 하나 이상 설치된다. 설치되는 분무노즐의 수는 송풍기의 압력, 그에 따른 악취물질의 상승 속도 그리고 목적하는 처리 효율 등에 따라 결정된다. 분무노즐은 상향 또는 하향으로 설치되며 이들 분무 노즐의 수와 간격은 분무 공간의 전체 용적과 분무되는 상향 또는 하방 영역이 상호 중복되지 않도록 하는 것이 경제적으로 유리할 것이다. 또한 본체 하부에는 낙하되는 목초액 조성물을 저장하기 위한 저장조(25)가 구비될 수 있고, 저장조에 저장된 목초액 조성물을 분무노즐로 재순환시키기 위해 순환펌프(26)가 구비될 수 있다. 또한 본체 내부에서 분무노즐에 의해 분무된 액적 형태의 목초액과 악취물질의 접촉효율을 증대시키기 위해 다양한 형태의 표면적이 넓은 폴링과 같은 충진재층(24)이 구비될 수 있다. In one embodiment of the cleaning wood vinegar scrubber of the present invention is provided with a blower 19 in the inlet 22, the cleaning scrubber provided with a wood vinegar composition spray nozzle 21 in the upper portion of the main body to the wood vinegar composition supply unit Can be used. It is preferable to form a swirl flow to increase the time for which odorous substances forced into the main body through the blower stay in the main body, and forced inflow of pollutants by the blower increases the effect of contact with the deodorant of the present invention. It also increases efficiency and prevents odors from escaping. One or more spray nozzles are installed in the upper region of the main body for the widespread spraying of the wood vinegar composition. The number of spray nozzles to be installed is determined by the pressure of the blower, the rate of rise of odorous substances, and the desired treatment efficiency. The spray nozzles are installed upwards or downwards and it would be economically advantageous for the number and spacing of these spray nozzles not to overlap each other with the total volume of the spray space and the sprayed up or down regions. In addition, the lower portion of the main body may be provided with a reservoir 25 for storing the falling wood vinegar composition, a circulation pump 26 may be provided to recycle the wood vinegar composition stored in the reservoir to the spray nozzle. In addition, a filler layer 24 such as polling having a large surface area of various forms may be provided to increase the contact efficiency of the vinegar liquor in the form of droplets sprayed by the spray nozzle inside the main body and odorous substances.
본 발명의 목초액은 또는 2종 이상의 목초액이 혼합된 목초액이 혼합물 또는 상기의 목초액에 식물열분해조성물, 금속촉매, 광촉매, 식물 정유, 식물추출물, 산화제, 환원제, 식물영양제, 유기산, 발효제, 향료, 흡착제, 미생물, 미생물제제, 점토액, 황토액, 갯벌, 계면활성제 또는 방향제 중 하나 이상을 혼합(이하, 목초액 조성물)하여 사용할 수 있다. 혼합비율은 목초액 전체 중량을 기준으로 0.01 ~ 90 중량%가 되도록 사용할 수 있다. 또한, 본 발명의 바실러스 서브틸리스 GU1 균주의 생육이나 증식을 저해하지 않는 범위에서 필요에 따라 탈취제, 소취제, 소독제, 살균제 등이 0.01~10 중량% 첨가될 수 있다.In the wood vinegar of the present invention or the wood vinegar mixed with two or more kinds of wood vinegar, or a mixture or the above-mentioned wood vinegar, plant pyrolysis composition, metal catalyst, photocatalyst, plant essential oil, plant extract, oxidizing agent, reducing agent, phytonutrient, organic acid, fermenting agent, flavoring agent, adsorbent , Microorganisms, microbial agents, clay solution, ocher solution, mud flats, surfactants or fragrances may be mixed (hereinafter, wood-vinegar composition) to be used. Mixing ratio may be used to 0.01 to 90% by weight based on the total weight of wood vinegar. In addition, 0.01 ~ 10% by weight of deodorant, deodorant, disinfectant, fungicide, etc. may be added as necessary in a range that does not inhibit the growth or proliferation of the Bacillus subtilis GU1 strain of the present invention.
또한 목초액과 악취물질의 반응속도를 높이고 기화량을 조절하거나 기화를 촉진하기 위해서, 목초액에는 목초액 중량의 2~1000 배 중량의 물 또는 탄소수 1 ~ 4의 알코올 등의 용매를 혼합하거나, 별도의 기화촉진제를 첨가할 수 있다. In addition, to increase the reaction rate of wood vinegar and odorous substances, to control the amount of evaporation or to promote evaporation, wood vinegar is mixed with a solvent, such as water of 2 to 1000 times the weight of wood vinegar solution or alcohol of 1 to 4 carbon atoms, or separately evaporated Accelerators may be added.
본 발명의 바이오필터 장치에 유입되기 전 세정식 목초액 스크라버에서 처리되는 악취가스 제거 효율을 높이가 위해서 바실러스 서브틸리스 GU1 균주, 바실러스 서브틸리스 GU2 균주, 또는 이들의 혼합물이 목초액에 첨가될 수 있고, 그 첨가농도는 목초액에 대하여 1.00E+02 ~ 1.00E+08 cfu/ml, 바람직하게는 1.00E+03 ~ 1.00E+08 cfu/ml, 더욱 바람직하게는 1.00E+04 ~ 1.00E+08 cfu/ml 농도로 첨가되는 것이 바람직하다.Bacillus subtilis GU1 strain, Bacillus subtilis GU2 strain, or mixtures thereof may be added to the wood vinegar to increase the odor gas removal efficiency which is treated in the cleaned wood vinegar scrubber before entering the biofilter device of the present invention. The concentration is 1.00E + 02 ~ 1.00E + 08 cfu / ml, preferably 1.00E + 03 ~ 1.00E + 08 cfu / ml, more preferably 1.00E + 04 ~ 1.00E + It is preferably added at a concentration of 08 cfu / ml.
본 발명의 바이오필터 장치에는 하나 이상의 탈취장치를 전단 또는 후단에 직렬연결하여 사용할 수 있고, 별도의 약액 세정장치, 필터 탈취장치, 멤브레인 기화장치, 오존 탈취장치, 바이오필터 탈취장치, 금속촉매 탈취장치, 흡착 탈취장치, 프라즈마 탈취장치, 소각 탈취장치와 단독 또는 2종 이상을 직렬로 연결하여 변형하여 사용할 수 있다. 바람직하게는 바이오필터 장치 또는 바이오필터 장치에 부착된 세정식 목초액 스크라버의 전단계에 산성가스 또는 VOCs 제거용 약액 세정장치(30) 또는 금속촉매(광촉매) 탈취장치를 부가시키는 것이 미생물이 산성가스에 의한 충격을 받지 않도록 하고 바이오필터 장치의 악취물질 제거효율을 높이며, 경제성과 운영적인 측면에서도 바람직하다.In the biofilter device of the present invention, one or more deodorizers may be used in series at the front end or the rear end, and a separate chemical cleaning device, a filter deodorizer, a membrane vaporizer, an ozone deodorizer, a biofilter deodorizer, and a metal catalyst deodorizer may be used. Adsorption deodorizer, plasma deodorizer, incineration deodorizer and single or two or more types can be connected and used in series. Preferably, the addition of the acid gas or VOCs chemical liquid cleaning device 30 or the metal catalyst (photocatalyst) deodorizer to the front stage of the biofilter device or the scrubber wood scrubber attached to the biofilter device is the microorganisms in the acid gas. It is not preferable to the impact caused by the impact, and to increase the efficiency of removing the odorous substances of the biofilter device, it is desirable in terms of economic and operational.
이하, 본 발명을 실시예 및 실험예에 의해 상세히 설명한다. 단, 하기 실시예 및 실험예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 이에 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail by Examples and Experimental Examples. However, the following Examples and Experimental Examples are merely illustrative of the present invention, but the content of the present invention is not limited thereto.
실시예 1: 균주의 분리, 동정 및 특성Example 1 Isolation, Identification and Characterization of Strains
(1) 분리(1) separation
죽초액에서 내산성이 강한 유용균주를 분리하기 위해서 6개월 이상 숙성시킨 전라남도 담양에서 생산한 pH 2.6 내외의 죽초액을 사용하였다. 죽초액에 존재하는 미생물을 분리하기 위하여 LB 한천배지, MRS 한천배지, PDA 한천배지 및 MEP(mannitol eggyolk polymyxine) 배지에 도말하였다. 이들 배지중 미생물이 성장한 PDA 한천배지와 MEP 배지에서 성장한 균주를 1차 선발한 후, 1차 선발된 균주중에서 pH 2.6에서 성장이 빠르며 아밀라아제 및 프로테아제 활성이 우수한 균주를 최종 선발하였다. 최종 선발된 균주는 광학현미경을 이용하여 확인하였고 그람염색법을 실시하였다. 상기 균주는 죽초액의 낮은 pH조건에서 기타 미생물의 성장이 어려운 조건에서 성장이 가능하고 고체배지에서 성장이 가능한 균주로서 확인되었다.In order to separate useful acid-resistant strains from bamboo vinegar, bamboo vinegar with pH 2.6 produced in Damyang, Jeollanam-do, which had been aged for more than 6 months, was used. In order to isolate the microorganisms present in the bamboo vinegar solution was plated on LB agar medium, MRS agar medium, PDA agar medium and mannitol eggyolk polymyxine (MEP) medium. After the first selection of microorganism-grown PDA agar medium and strains grown in MEP medium, the strains were grown at pH 2.6, and the final strain was selected with excellent amylase and protease activity. The final selected strains were identified using an optical microscope and Gram staining was performed. The strain was identified as a strain capable of growing in a solid medium and difficult to grow other microorganisms at low pH conditions of bamboo vinegar solution.
(2) 분자생물학적 동정(2) Molecular Biology Identification
상기 균주에서 DNA를 추출하고 16s rDNA를 분석한 결과 바실러스 서브틸리스(Bacillus subtilis) HDYM-11 균주와 가장 높은 상동성을 나타내어 바실러스 서브틸리스로 동정하였다(1515개 서열 중 1511개 일치, 99% 상동성). 얻어진 16s rDNA의 서열은 서열목록 1에 나타내었다. 다른 하나의 균주도 바실러스 서브틸리스와 1517개 서열 중 1512개 일치하여 99%의 상동성으로 바실러스 서브틸리스로 동정하였고, 얻어진 16s rDNA의 서열은 서열목록 2에 나타내었다.DNA extracted from the strain and 16s rDNA analysis showed the highest homology with Bacillus subtilis HDYM-11 strain and identified as Bacillus subtilis (1511 matches among 1515 sequences, 99% phase). Homosexual). The sequence of 16s rDNA obtained is shown in SEQ ID NO: 1. Another strain was identified as Bacillus subtilis with 99% homology with 1512 sequences among Bacillus subtilis and 1517 sequences, and the sequence of 16s rDNA obtained was shown in SEQ ID NO: 2.
(3) 내열성(3) heat resistance
사료첨가제로 사용되기 위해서는 일반 펠렛팅처리(80 ℃)나 압출(120 ℃) 등과 같은 고온 고압 조건에서 생존할 수 있어야 한다. 일반적으로 바실러스 속 미생물은 효소, 무독성 항균물질, 살충물질 등을 포함한 여러 가지의 유용한 물질들을 생산하며 또한 그램양성(陽性)균으로 높은 온도에서 포자(胞子)를 형성하는 특징이 있다.To be used as a feed additive, it must be able to survive under high temperature and high pressure conditions such as general pelleting (80 ° C.) or extrusion (120 ° C.). In general, Bacillus microorganisms produce a variety of useful substances, including enzymes, non-toxic antibacterial substances, pesticides, etc., and is also a gram-positive bacteria, characterized by the formation of spores at high temperatures.
본 발명의 바실러스 서브틸리스 GU01 균주의 내열성 검사를 위해 흡광도(Opical Density, 600nm) 값이 1.0 일때 각각의 온도에서 10분동안 열처리 후 균수를 측정하여 도 3에 나타내었다. 도 3에 나타낸 바와 같이 사료첨가제의 유용미생물로 많이 사용되는 유산균의 통상적인 사멸온도인 60℃를 훨씬 초과하는 80℃ 로 처리한 경우에도 생존력이 매우 뛰어남을 확인할 수 있었다. 또한 바실러스 서브틸리스 GU02 균주 역시 45℃ 까지는 균수가 1.00E+08 cfu/ml 이상으로 열처리 전과 차이가 없었고, 60℃ 에서도 균수가 1.00E+08 cfu/ml 이상을 유지하였다.In order to test the heat resistance of the Bacillus subtilis GU01 strain of the present invention, when the absorbance (Opical Density, 600nm) value is 1.0, the number of bacteria after heat treatment for 10 minutes at each temperature was measured and shown in FIG. As shown in FIG. 3, the viability was excellent even when treated at 80 ° C., far exceeding 60 ° C., which is a common killing temperature of lactic acid bacteria used as a useful microorganism of feed additives. In addition, the Bacillus subtilis GU02 strain also did not differ from before the heat treatment up to 45 ℃ bacteria number 1.00E + 08 cfu / ml, and maintained at more than 1.00E + 08 cfu / ml at 60 ℃.
(4) 죽초액내 미생물 균수의 변화(4) Change of microbial bacteria in bamboo vinegar
죽초액은 pH 2.6의 강산성 조건으로서, 죽초액을 증류수에 일정비율로 희석한 후 각 농도에서의 본 발명의 균주(GU01)의 배양시간에 따른 성장변화를 600 nm에서 흡광도 변화로 측정하여 표 1에 나타내었고, 또한 배양시간에 따른 미생물 균수의 변화를 표 2에 나타내었다. 죽초액은 증류수에 각각 10, 20, 30, 40 및 50 중량%로 희석하였고, 초기 미생물 접종농도는 1.00E+05 cfu/ml 이고, 37 ℃에서 배양하였다.Bamboo vinegar is a strong acidic condition of pH 2.6, after diluting the bamboo vinegar in distilled water at a constant ratio, the growth change according to the incubation time of the strain (GU01) of the present invention at each concentration is measured by the change in absorbance at 600 nm is shown in Table 1 In addition, the change in the number of microbial microorganisms with incubation time is shown in Table 2. Bamboo liquor was diluted 10, 20, 30, 40 and 50% by weight in distilled water, respectively, and the initial microbial inoculation concentration was 1.00E + 05 cfu / ml and incubated at 37 ° C.
표 1
시간 10% 20% 30% 40% 50%
0 0.239 0.254 0.280 0.288 0.319
24 0.335 0.378 0.423 0.456 0.375
48 0.375 0.385 0.477 0.523 0.516
Table 1
time 10% 20% 30% 40% 50%
0 0.239 0.254 0.280 0.288 0.319
24 0.335 0.378 0.423 0.456 0.375
48 0.375 0.385 0.477 0.523 0.516
표 2
시간 10% 20% 30% 40% 50%
0 4.00E+05 8.00E+05 6.00E+05 2.00E+05 1.40E+06
24 1.00E+07 1.20E+07 7.00E+06 6.00E+06 3.00E+07
48 1.03E+07 1.04E+07 1.04E+07 1.07E+07 1.07E+07
TABLE 2
time 10% 20% 30% 40% 50%
0 4.00E + 05 8.00E + 05 6.00E + 05 2.00E + 05 1.40E + 06
24 1.00E + 07 1.20E + 07 7.00E + 06 6.00E + 06 3.00E + 07
48 1.03E + 07 1.04E + 07 1.04E + 07 1.07E + 07 1.07E + 07
본 발명의 균주의 성장(600 nm의 흡광도)은 배양시간이 증가할수록 증대되었고, 죽초액 농도 40중량%까지는 증대되다가 50 중량%부터는 더이상 증대되지 않았다. 또한 본 발명의 균주의 균수는 24 시간까지 증대되다가 48 시간 배양하더라도 균수의 변화는 미미했고, 죽초액 농도에 다른 균수의 변화도 미미했다.The growth (absorbance of 600 nm) of the strain of the present invention was increased as the incubation time was increased, increased to 40% by weight of bamboo vinegar concentration, but no longer increased from 50% by weight. In addition, the number of bacteria of the strain of the present invention was increased up to 24 hours, even if incubated for 48 hours, the change in the number of bacteria was insignificant, and the change in the number of other bacteria in the bamboo shoot concentration was also insignificant.
따라서 본 발명의 균주는 죽초액이 0.1 중량% 이상 포함된 배지에서 생육가능하고, 특히 죽초액이 50%까지 첨가된 배지에서도 그 성장에는 큰 영향을 받지 않을 것으로 판단되었다.Therefore, the strain of the present invention was able to grow in a medium containing more than 0.1% by weight of bamboo vinegar, especially in the medium added up to 50% bamboo vinegar was determined that the growth will not be significantly affected.
실험예 1: 육계의 생산성에 미치는 효과Experimental Example 1: Effect on broiler productivity
본 발명의 실시예의 사료첨가제에 포함되는 죽초액이 육계의 생산성에 미치는 영향을 확인하기 위하여, 수분함량을 40 중량%로 조정한 탈지강을 사료첨가제 대신 첨가한 군(비교예 1) 및 탈지강에 죽초액 2 중량% 첨가하고 수분함량을 40 중량%로 조정한 사료첨가제(비교예 2)를 각각 일반 육계용 사료에 0.2 중량% 첨가하여 사용하였다.In order to confirm the effect of the bamboo vinegar solution contained in the feed additive of the embodiment of the present invention on the broiler productivity, the degreasing steel whose water content was adjusted to 40% by weight was added to the group (Comparative Example 1) and degreasing steel instead of the feed additive. Addition of 2% by weight of bamboo vinegar solution and a feed additive (Comparative Example 2) in which the water content was adjusted to 40% by weight were used by adding 0.2% by weight to the feed for general broilers.
크기가 동일한 육계용 병아리 175수를 비교예 3 및 4와 실시예 3의 축사에 각각 입식하였다. 육계를 35일간 사육한 후, 폐사수 및 육성율을 측정하였고 각 실험군에서 10 수의 육계를 임의로 선발하여 개시체중, 종료체중, 증체량 및 육계의 화학적 특성을 분석하였다.175 broiler chickens of the same size were stocked in the barns of Comparative Examples 3 and 4 and Example 3, respectively. After breeding broilers for 35 days, the number of shoots and growth rate were measured, and 10 broilers were randomly selected from each experimental group to analyze the start weight, end weight, weight gain and broiler chemical characteristics.
표 3
항목 비교예 1 비교예 2
시험수 175 175
개시체중(g) 44.82±0.15 44.86±0.10
종료체중(g) 2079.29±1.67 2055.71±9.18
사육일수 35 35
증체량(g) 2034.46±1.79 2010.86±9.17
사료섭취량(g) 3453.99±1.78 3416.86±1.81
TABLE 3
Item Comparative Example 1 Comparative Example 2
Test 175 175
Starting weight (g) 44.82 ± 0.15 44.86 ± 0.10
End weight (g) 2079.29 ± 1.67 2055.71 ± 9.18
Breeding days 35 35
Weight gain (g) 2034.46 ± 1.79 2010.86 ± 9.17
Feed Intake (g) 3453.99 ± 1.78 3416.86 ± 1.81
비교예 1 및 2를 비교한 결과 사료에 죽초액만을 첨가한 경우에는 죽초액 무첨가군과 증체량 및 사료섭취량에서 차이를 나타내지 않았고, 오히려 더 나쁜 결과를 가져와 죽초액의 첨가만으로는 육계의 증체량 및 사료섭취량에 긍정적인 영향을 주지 않는 것으로 판단되었다.Comparing Comparative Examples 1 and 2, only the addition of bamboo vinegar to the feed did not show any difference in the addition of bamboo vinegar and the weight gain and feed intake, but rather worse, the addition of bamboo vinegar was positive for the weight gain and feed intake of broilers. It was judged not to affect.
본 발명의 본 발명 균주와 죽초액을 고체발효시킨 사료첨가제의 효과를 확인하기 위하여, 탈지강에 죽초액 2 중량%, 본 발명의 균주 1.00E+05 cfu/ml 농도로 증류수에 희석된 균주 희석액 2 중량%를 첨가하고 수분함량을 40 중량%로 조정한 후 37 에서 48시간 발효시켜 고체상의 사료첨가제(실시예 1)를 제조하였다. In order to confirm the effect of the feed additive of the present invention strain and the bamboo vinegar solid fermentation, 2% by weight of bamboo vinegar solution in the skimmed steel, the strain dilution 2 weight diluted in distilled water at a concentration of 1.00E + 05 cfu / ml strain of the present invention % Was added and the water content was adjusted to 40% by weight, followed by fermentation at 37 to 48 hours to prepare a solid feed additive (Example 1).
상기 실시예 1과 수분함량을 40 중량%로 조정한 탈지강을 사료첨가제 대신 첨가한 군(비교예 1)을 대비하여 본 발명의 효과를 확인하였다. 시험동물 축사의 규모는 각각 638 m2(11m X 8m)로 일반 육계용 사료에 실시예 1 및 비교예 1의 사료를 0.2 중량% 첨가하여 사용하였다. 크기가 동일한 육계용 병아리 14,000수를 비교예 1 및 실시예 1의 축사에 각각 입식하였다. 육계를 35일간 사육한 후, 폐사수 및 육성율을 측정하였고 각 실험군에서 100 수의 육계를 임의로 선발하여 개시체중, 종료체중, 증체량 및 육계의 화학적 특성을 분석하였다.The effect of the present invention was confirmed in comparison with the group 1 (Comparative Example 1) in which the degreasing steel, in which the moisture content was adjusted to 40% by weight, was added instead of the feed additive. The test animal barn was 638 m 2 (11m X 8m), respectively, and 0.2 wt% of the feeds of Example 1 and Comparative Example 1 were added to the general broiler feed. 14,000 broiler chicks of the same size were stocked in stalls of Comparative Example 1 and Example 1, respectively. After breeding broilers for 35 days, the number of shoots and growth rate were measured, and 100 broilers were randomly selected from each experimental group to analyze the start weight, end weight, weight gain, and chemical characteristics of broilers.
표 4
항목 비교예 1 실시예 1
시험수 14,000 14,000
개시체중(g) 42.0 42
종료체중(g) 1,789 1,870
사육일수 35 35
일당증체량(g/d) 49.91 52.23
사료섭취량(kg) 2.68 3.24
폐사수 426 419
육성율(%) 96.96 97.01
Table 4
Item Comparative Example 1 Example 1
Test 14,000 14,000
Starting weight (g) 42.0 42
End weight (g) 1,789 1,870
Breeding days 35 35
Daily gain (g / d) 49.91 52.23
Feed Intake (kg) 2.68 3.24
Dead shooter 426 419
Growth rate (%) 96.96 97.01
사육시험 결과 일당 증체량은 실시예 1이 52.23g, 비교예 1이 49.91g로 비교예 1에 비해 실시예 1이 2.32g 높게 나타났으며, 육성율의 경우도 실시예 1이 97.09%, 비교예 1이 96.96%로 0.13% 더 높게 나타났다(표 4). 육계에 본 발명의 사료첨가제를 급여함으로써 폐사율감소, 일당증체량 증가는 미생물에 의해 면역력이 증가하여 질병에 의한 폐사가 줄어든 것으로 사료된다. 또한 본 발명의 균주와 죽초액의 혼합 첨가에 의한 상승 작용을 하여 육계의 소화율을 증가시키고 장내 유해균의 성장을 억제하였기 때문이라고 사료된다.As a result of the breeding test, the weight gain per day was 52.23g in Example 1 and 49.91g in Comparative Example 1, which was 2.32g higher than in Comparative Example 1, and Example 1 was 97.09% and Comparative Example 1 in the growth rate. 96.96%, which is 0.13% higher (Table 4). By feeding the feed additive of the present invention to broiler chickens, it is thought that the reduction of mortality and the increase in the daily weight gain are caused by the increase of immunity by the microorganisms and the death by disease is reduced. In addition, it is believed that the synergistic effect of the mixed strain of the present invention and bamboo vinegar increased the digestibility of broilers and inhibited the growth of intestinal harmful bacteria.
실험예 2: 육계의 육질, 육색, 일반 성분 및 지방산 조성에 미치는 효과Experimental Example 2 Effects on Meat Quality, Meat Color, General Components and Fatty Acid Composition of Broilers
실험예 1에서의 실시예 1 및 비교예 1의 35일 사육 후의 육계의 가슴살 부위를 채취하여 육질, 육색, 일반성분 및 지방산 조성에 미치는 효과를 대비하여 각각 표 5 내지 8에 나타내었다.In Example 1 and Comparative Example 1 in Experimental Example 1 after the 35 days of broiler meat was collected and compared to the effects on meat quality, meat color, general components and fatty acid composition are shown in Tables 5 to 8, respectively.
가열감량(%)은 시료를 일정한 모양으로 정형(250±50g)한 후, 폴리에틸렌 백에 넣어 80℃ Water bath에 넣고 물속에 완전히 잠기도록 한 후, 40분간 가열하고, 흐르는 물속에서 20분간 수냉하였다. 냉각된 시료의 물기를 제거한 후 무게를 재어 가열감량을 계산하였다. 가열감량을 측정한 시료의 표면부를 제거한 속부분을 전단력 측정 시료로 하여 Salter(Warner Bratzler Shear, USA)를 이용해 전단력을 측정하였다.The heating loss (%) is a sample (250 ± 50g) formed into a certain shape, then put in a polyethylene bag and placed in a water bath at 80 ° C to be completely immersed in water, heated for 40 minutes, and cooled in water for 20 minutes. . After the water of the cooled sample was removed, the weight loss was calculated. Shear force was measured by using a salter (Warner Bratzler Shear, USA) as the shear force measurement sample, which was removed from the surface portion of the sample from which the heating loss was measured.
보수력 측정을 위해서 시료를 필터관(VIDAS 튜브, BIOMERIEUX, 프랑스) 넣고, 80℃ water-bath에 넣고 20분간 가열한 후, 10분간 방냉시켰다. 방냉시킨 필터관을 2000rpm에서 10℃, 10분간 원심분리하여, 계산식으로 유리수분과 보수력을 계산하였다.The sample was placed in a filter tube (VIDAS tube, BIOMERIEUX, France) for the measurement of water holding capacity, placed in an 80 ° C water-bath, heated for 20 minutes, and allowed to cool for 10 minutes. The cooled tube was centrifuged at 2000 ° C. for 10 minutes at 10 ° C., and the free moisture and the water holding capacity were calculated by the formula.
유리수분=[(원심분리전후 무게의 차이)/시료무게]X지방계수(1-지방함량)X100Free moisture = [(difference in weight before and after centrifugation) / sample weight] X fat coefficient (1-fat content) X 100
보수력(%)=[(전수분-유리수분)/전수분]X100Water-retaining power (%) = [(whole water-free water) / total water] X100
표 5
분석항목 비교예 1 실시예 1
가열감량 22.48 22.36
전단력(kg/0.5inch2) 1.81 1.21
보수력 60.53 61.18
pH 5.96 5.88
Table 5
Analysis item Comparative Example 1 Example 1
Heating loss 22.48 22.36
Shear force (kg / 0.5inch 2 ) 1.81 1.21
Conservative 60.53 61.18
pH 5.96 5.88
전단력에서 실시예 1이 비교예 1에 비해 현저히 낮아 육질이 연하게 잘 잘라지는 것을 알 수 있었고, 역시 실시예 1에서 수분을 보존하는 보수력이 우수함을 확인할 수 있었다. It was found that Example 1 was significantly lower than that of Comparative Example 1 in shearing force, and the meat was lightly cut well, and in Example 1, it was confirmed that the water holding capacity was excellent.
표 6
분석항목 비교예 1 실시예 1
L(명도) 45.66 51.79
a(적색도) 3.53 4.77
b(황색도) 4.46 4.25
Table 6
Analysis item Comparative Example 1 Example 1
L (brightness) 45.66 51.79
a (red) 3.53 4.77
b (yellow) 4.46 4.25
육색에서 실시예 1이 비교예 1에 비해 명도가 높고 황색도가 낮아 밝은 육색을 띰을 알 수 있었고, 적색도는 더 낮았다. In flesh color, Example 1 had a higher brightness and a lower yellowness than Comparative Example 1, indicating that it had a bright flesh color, and the redness was lower.
표 7
분석항목 비교예 1 실시예 1
수분 75.73 75.26
조지방 0.17 0.49
조단백질 22.95 23.13
조회분 1.16 1.12
TABLE 7
Analysis item Comparative Example 1 Example 1
moisture 75.73 75.26
Crude fat 0.17 0.49
Crude protein 22.95 23.13
View minutes 1.16 1.12
실시예 1에서 조회분의 함량은 비교예 1보다 더 낮았고, 조지방 및 조단백질은 더 높아 더 나은 육질을 제공함을 알 수 있었다.In Example 1, the content of crude ash was lower than that of Comparative Example 1, and it was found that crude fat and crude protein were higher to provide better meat quality.
지방산 함량은 가스크로마토그래피(모델명 : Varian 3600)을 이용하여 측정하였다.Fatty acid content was measured using gas chromatography (model name: Varian 3600).
표 8
지방산 비교예 1 실시예 1
Myristic acid (C14:0) 0.89 0.83
Palmitic acid (C16:0) 25.06 23.55
Stearic acid (C18:0) 6.82 6.41
Palmitoleicacid (C16:ln7) 5.32 5.65
Oleic acid (C18:ln9) 44.76 45.76
Vaccenic acid (C18:ln7) 0.01 0.02
Linoleic acid (C18:2n6) 15.52 15.91
v-Linoleic acid (C18:3n6) 0.16 0.19
Linolenic acid (C18:3n3) 0.66 0.68
Eicosenoic acid (C20:ln9) 0.50 0.55
Arachidonic acid (C20:4n6) 0.30 0.44
Eicosapentaenoicacid(EPA)(C20:5n3) 0.00 0.00
Docosatetraenoic acid (C22:4n6) 0.00 0.00
Docosahexaenoicacid(DHA)(C22:6n3) 0.00 0.00
Total 100.00 100.00
saturated fatty acid 32.76 30.79
Unsaturated fatty acid 67.24 69.21
Table 8
fatty acid Comparative Example 1 Example 1
Myristic acid (C14: 0) 0.89 0.83
Palmitic acid (C16: 0) 25.06 23.55
Stearic acid (C18: 0) 6.82 6.41
Palmitoleicacid (C16: ln7) 5.32 5.65
Oleic acid (C18: ln9) 44.76 45.76
Vaccenic acid (C18: ln7) 0.01 0.02
Linoleic acid (C18: 2n6) 15.52 15.91
v-Linoleic acid (C18: 3n6) 0.16 0.19
Linolenic acid (C18: 3n3) 0.66 0.68
Eicosenoic acid (C20: ln9) 0.50 0.55
Arachidonic acid (C20: 4n6) 0.30 0.44
Eicosapentaenoicacid (EPA) (C20: 5n3) 0.00 0.00
Docosatetraenoic acid (C22: 4n6) 0.00 0.00
Docosahexaenoic acid (DHA) (C22: 6n3) 0.00 0.00
Total 100.00 100.00
saturated fatty acid 32.76 30.79
Unsaturated fatty acid 67.24 69.21
지방산의 조성에 있어서도, 실시예 1은 비교예 1에 비해 포화지방산의 함량이 낮고 불포화지방산의 함량이 높은 우수한 품질의 육계를 제공함을 확인할 수 있었다.Also in the fatty acid composition, Example 1 was found to provide a broiler of good quality with a lower content of saturated fatty acids and a higher content of unsaturated fatty acids than Comparative Example 1.
실험예 3: 오리의 생산성에 미치는 효과Experimental Example 3: Effect on Duck Productivity
본 발명 균주와 죽초액을 고체발효시킨 사료첨가제의 효과를 확인하기 위하여, 탈지강에 죽초액 2 중량%, 본 발명의 균주 1.00E+05 cfu/ml 농도로 증류수에 희석된 균주 희석액 2 중량%, 락토바실러스 애시도필러스 1.00E+05 cfu/ml 농도로 증류수에 희석된 균주 희석액 0.2 중량%, 락토바실러스 플란타룸 1.00E+05 cfu/ml 농도로 증류수에 희석된 균주 희석액 0.2 중량%, 맥반석 0.5 중량%, 대나무 숯가루 0.1 중량%를 첨가하고 수분함량을 40 중량%로 조정한 후 37 에서 48시간 발효시켜 고체상의 사료첨가제(실시예 2)를 제조하였다. 대조군으로 수분을 40 중량%로 조정한 탈지강을 사료첨가제 대신 첨가한 군(비교예 1)을 이용하였다.In order to confirm the effect of the feed additive in the solid fermentation of the strain of the present invention and bamboo vinegar, 2% by weight of bamboo vinegar solution in the skim steel, 2% by weight of the dilution of the strain diluted in distilled water at a concentration of 1.00E + 05 cfu / ml strain of the present invention, lactose 0.2 wt% strain diluted in distilled water at a concentration of Bacillus ashidophilus 1.00E + 05 cfu / ml, 0.2 wt% strain diluted in distilled water at a concentration of 1.00E + 05 cfu / ml Lactobacillus plantarum, 0.5 wt% By weight, bamboo charcoal powder 0.1% by weight was added and the water content was adjusted to 40% by weight and then fermented at 37 to 48 hours to prepare a solid feed additive (Example 2). As a control, a group in which degreasing steel having a water content of 40% by weight was added instead of a feed additive (Comparative Example 1) was used.
시험동물 축사의 규모는 각각 400 m2(10m X 40m)로 일반 오리 사육용 사료에 실시예 2 및 비교예 4를 일반 오리 사육용 사료의 0.2 중량% 첨가하여 사용하였다. 크기가 동일한 오리 10,000수를 실시예 2 및 비교예 1의 축사에 각각 입식하였다. 오리를 43일간 사육한 후, 폐사수 및 육성율을 측정하였고 각 실험군에서 100 수의 오리를 임의로 선발하여 개시체중, 종료체중, 증체량 및 사료효율을 분석하였다. The scale of the test animal house was 400 m 2 (10m X 40m), respectively, and Example 2 and Comparative Example 4 were used by adding 0.2% by weight of the general duck breeding feed to the general duck breeding feed. 10,000 ducks of the same size were stocked in stalls of Example 2 and Comparative Example 1, respectively. After 43 days of duckling, the number of dead and growth rates were measured, and 100 groups of ducks were randomly selected from each experimental group to analyze the initiation weight, end weight, weight gain and feed efficiency.
표 9
항목 비교예 1 실시예 2
시험수 10,000 10,000
개시체중(g) 48 48
종료체중(g) 3.190 3.280
사육일수 43 43
일당증체량(g) 74.19 76.27
사료섭취량(kg) 65.709 65.922
평균체중(g) 3.190 3.280
폐사수 141 118
사료요구량(g) 2.10 2.03
육성율(%) 96.96 97.09
Table 9
Item Comparative Example 1 Example 2
Test 10,000 10,000
Starting weight (g) 48 48
End weight (g) 3.190 3.280
Breeding days 43 43
Daily weight gain (g) 74.19 76.27
Feed Intake (kg) 65.709 65.922
Average weight (g) 3.190 3.280
Dead shooter 141 118
Feed requirement (g) 2.10 2.03
Growth rate (%) 96.96 97.09
실시예 2에서 비교예 1에 비해 일당 증체량, 사료효율 및 육성율이 개선되었다. 비교예 1은 일당증체량이 74.19g인데 비해 실시예 2는 76.27g으로 실시예 2가 높게 나타났으며, 육성율도 실시예 2가 98.82%, 비교예 1이 98.57%로 비교예 1이 0.25% 더 높게 나타났다.In Example 2, the weight gain, feed efficiency and growth rate per day were improved compared to Comparative Example 1. In Comparative Example 1, the daily weight gain was 74.19 g, whereas Example 2 was 76.27 g, and Example 2 was higher, and the growth rate was 98.82% in Example 2, 98.57% in Comparative Example 1, and 0.25% in Comparative Example 1. High.
실험예 4: 양돈의 생산성에 미치는 효과Experimental Example 4: Effect on productivity of swine
평균 체중이 79.66±0.12 kg인 60마리의 돼지를 최초 평균체중이 동일하게 3개군으로 나누어서, 수분함량을 40중량%로 조정하여 사료첨가제를 대신한 것(비교예 1)을 일반 양돈용 사료에 0.2 중량% 첨가한 군, 실시예 2의 사료첨가제를 일반 양돈용 사료에 0.1 중량% 첨가한 군, 실시예 2의 사료첨가제를 일반 양돈용 사료에 0.2 중량% 첨가한 군으로 구분하여 4주간 동일 조건에서 생육시키면서, 일당증체량, 일당사료섭취량 및 사료효율을 계산하여 표 10에 나타내었다.60 pigs with an average body weight of 79.66 ± 0.12 kg were divided into three groups with the same average body weight, and the water content was adjusted to 40% by weight to replace the feed additive (Comparative Example 1). It was grown in the same conditions for 4 weeks by dividing into the group added by weight, 0.1 wt% of the feed additive of Example 2 to the feed for general pigs, and 0.2 wt% added to the feed additive of Example 2 to the feed for general pigs. While increasing the daily weight gain, daily feed intake and feed efficiency are shown in Table 10.
표 10
구분 비교예1 실시예2 실시예2 SE
첨가량 0.2중량% 0.1중량% 0.2중량% -
일당증체량(g) 772b 825a 821a 13.3
사료섭취량(g) 2,356 2,480 2,413 65.3
사료효율(%) 32.8 33.3 34.0 0.009
Table 10
division Comparative Example 1 Example 2 Example 2 SE
Amount 0.2 wt% 0.1 wt% 0.2 wt% -
Daily weight gain (g) 772 b 825 a 821 a 13.3
Feed Intake (g) 2,356 2,480 2,413 65.3
Feed efficiency (%) 32.8 33.3 34.0 0.009
비교예1에 비해 실시예2는 첨가량을 0.1 중량% 또는 0.2 중량% 사용한 군 모두 일당 증체량이 현저히 증가하고, 사료섭취량도 증가하였으며, 사료효율 또한 증대되었음을 확인할 수 있었다.Compared to Comparative Example 1, in Example 2, the addition amount was 0.1 wt% or 0.2 wt%, and the weight gain per day was significantly increased, the feed intake was increased, and the feed efficiency was also confirmed.
한편, 본 발명의 실시예 2의 사료첨가제를 정읍의 양돈농가에서 일반 유산균을 포함한 사료첨가제를 대체하여 일반 양돈용 사료에 0.2 중량% 첨가하여 급이한 결과, 일반 유산균을 포함한 사료첨가제에 비하여 실시예 2의 사료첨가제 사용시 돼지의 출하일은 9일 단축되었고, 폐사율은 7~8%에서 3%미만으로 감소하였다.On the other hand, the feed additive of Example 2 of the present invention in the pig farm in Jeongeup replaces the feed additive including the general lactic acid bacteria and added 0.2% by weight to the feed for general pigs, as a result, compared to the feed additive containing the common lactic acid bacteria Feeding date of pigs was reduced by 9 days and mortality decreased from 7 ~ 8% to less than 3%.
실험예 5: 직접 혼합에 의한 악취물질 제거 효과Experimental Example 5: Removal of odorous substances by direct mixing
본 발명의 균주의 악취물질 제거 효과를 확인하기 위하여, 물 100 ml에 본 발명의 GU1 균주를 1.00E+05 cfu/ml를 접종한 실시예 3, 죽초액 100 ml에 본 발명의 GU1 균주를 1.00E+05 cfu/ml를 접종한 실시예 4, 물 100 ml에 본 발명의 GU2 균주를 1.00E+05 cfu/ml를 접종한 실시예 5, 물 100 ml에 본 발명의 GU1 균주와 GU2 균주를 각각 5.00E+04 cfu/ml를 접종한 실시예 6를 제조하였다. 대조군으로 악취물질 제거제를 사용하지 않고 물 100 ml만 첨가한 군(비교예2) 및 죽초액 100ml 만 첨가한 군(비교예 3)을 제조하여 실험에 사용하였다. 본 실험예에 사용된 죽초액은 전남 담양에서 생산된 것으로 30cm로 절단된 대나무를 250~300℃에서 간접 가열하고 이 때 연돌의 연기 속에 함유된 수액 증기를 80~150℃의 온도에서 포집하여 냉각 및 응축시킨 조죽초액을 6개월 이상 숙성하고 기공이 5.0㎛ 인 필터로 1회 여과하여 제조된 것이다.In order to confirm the odor removing effect of the strain of the present invention, Example GU1 strain inoculated 1.00E + 05 cfu / ml of the GU1 strain of the present invention in 100 ml of water, 1.00E of the GU1 strain of the present invention in 100 ml of bamboo vinegar solution Example 4 inoculated with +05 cfu / ml, GU2 strain of the present invention in 100 ml of water Example 5 inoculated with 1.00E + 05 cfu / ml, GU1 strain and GU2 strain in 100 ml of water, respectively Example 6 was prepared inoculated with 5.00E + 04 cfu / ml. As a control, a group to which only 100 ml of water was added (Comparative Example 2) and a group to which only 100 ml of bamboo vinegar solution was added (Comparative Example 3) were used for the experiment. The bamboo vinegar used in this experiment was produced in Damyang, Jeonnam, and indirectly heated bamboo cut to 30cm at 250 ~ 300 ℃, and the sap vapor contained in smoke of stack was collected at 80 ~ 150 ℃ for cooling and The condensed crude bamboo vinegar was aged for at least 6 months and filtered once with a filter having a pore size of 5.0 μm.
아이오와 대학에서 사용되는 PVC컬럼을 이용한 악취물질 제거 효과실험방법을 이용하였다(www.nationalhogfarmer.com). 길이 15 inch인 PVC 컬럼에 돼지분뇨 4 ft. 넣고 실시예 3 내지 6의 균주 희석액, 비교예 2는 증류수, 비교예 3의 죽초액을 돼지분뇨의 0.2 중량% 첨가한 후 악취물질의 함량 변화(단위 ppm)를 시간에 따라 측정하여 표 11에 나타내었다.A test method for removing odorous substances using a PVC column used at the University of Iowa was used (www.nationalhogfarmer.com). 4 ft. Pig manure on a PVC column 15 inches long. The strain dilution of Examples 3 to 6, Comparative Example 2 is added to the distilled water, bamboo paste solution of Comparative Example 3 0.2% by weight of pig manure after measuring the change in the content of odorous substances (unit ppm) as shown in Table 11 It was.
표 11
구분 hr 암모니아 황화수소
비교예 2 0 18 6.0
12 10 5.5
24 12 5.5
48 14 5.5
비교예 3 0 15 6.5
12 4.5 5.0
24 7.5 4.5
48 8.0 5.0
실시예 3 0 16 6.0
12 6.5 3.5
24 3.0 3.0
48 3.0 2.0
실시예 4 0 16 6.0
12 4.5 3.0
24 3.5 2.5
48 2.5 2.0
실시예 5 0 16 6.0
12 9.0 4.0
24 5.0 3.0
48 3.5 2.5
실시예 6 0 16 6.0
12 5.0 3.0
24 3.0 2.0
48 2.5 1.5
Table 11
division hr ammonia Hydrogen sulfide
Comparative Example 2 0 18 6.0
12 10 5.5
24 12 5.5
48 14 5.5
Comparative Example 3 0 15 6.5
12 4.5 5.0
24 7.5 4.5
48 8.0 5.0
Example 3 0 16 6.0
12 6.5 3.5
24 3.0 3.0
48 3.0 2.0
Example 4 0 16 6.0
12 4.5 3.0
24 3.5 2.5
48 2.5 2.0
Example 5 0 16 6.0
12 9.0 4.0
24 5.0 3.0
48 3.5 2.5
Example 6 0 16 6.0
12 5.0 3.0
24 3.0 2.0
48 2.5 1.5
비교예 2에 비해 죽초액만 첨가한 비교예 3은 암모니아 저감효과가 초기 15ppm에서 12시간까지 4.5ppm으로 감소하였으나 24시간 이후 다시 증가하였다. 반면에 본 발명의 실시예 3 내지 6에서는 초기 16ppm에서 12시간까지 4.5~9.0ppm으로 감소하고 시간이 경과함에 따라 균주의 대사작용에 의해서 낮아지는 것으로 나타났으며, 초기 악취물질 농도에 비해 저감되는 비율을 지속적으로 낮게 유지하고 있었다. 특히 실시예 3, 5 및 6에서는 12시간째의 암모니아 저감효과는 죽초액만 포함된 비교예 3에 비해 다소 높은 농도를 나타냈지만, 24시간 및 48시간으로 반응을 오래 시킬수록 죽초액만을 첨가한 비교예 2에서는 오히려 암모니아 농도가 상승함에 비해 실시예 3, 5, 및 6에서는 지속적으로 낮아져 현저히 낮은 농도를 나타냄을 확인할 수 있었다.Compared with Comparative Example 2, Comparative Example 3, in which only bamboo vinegar solution was added, decreased to 4.5 ppm from the initial 15 ppm to 12 hours, but increased again after 24 hours. On the other hand, in Examples 3 to 6 of the present invention was found to decrease from 4.5ppm to 9.0ppm from the initial 16ppm to 12 hours and lowered by the metabolism of the strain over time, compared to the initial odorous substance concentration is reduced The ratio was constantly kept low. In particular, in Examples 3, 5 and 6, the ammonia-reducing effect at 12 hours was slightly higher than that of Comparative Example 3 containing only bamboo liquor solution. In contrast, the concentration of ammonia was increased in 2, but in Examples 3, 5, and 6, it was confirmed that the concentration was significantly lower.
황화수소의 저감효과는 비교예 2에 비해 죽초액만 첨가한 비교예 3은 암모니아 저감효과가 초기 6.5ppm에서 12시간까지 5.5ppm으로 감소하였고 이후 48시간까지 유지하였으며, 실시예 3 내지 6에서는 초기 6.0ppm에서 시간이 지날수록 감소되어 48시간째에 1.5~2.5ppm으로 감소하였다. The reduction effect of hydrogen sulfide was compared with Comparative Example 2 in Comparative Example 3 added only bamboo shoot liquid ammonia reduction effect from the initial 6.5ppm to 12ppm to 5.5ppm and then maintained for 48 hours, in Examples 3 to 6 the initial 6.0ppm The elongation decreased with time and decreased to 1.5 ~ 2.5ppm at 48 hours.
실험예 6: 바이오필터 장치에서의 악취물질 제거 효과Experimental Example 6: Effect of Removing Odor Substances in a Biofilter Device
본 발명의 바이오필터 장치에는 포틀란트시멘트 200g, 실리카 모래분말 260g, 석회성분 20g, 알루미나시멘트 40g과 이탄재 80g을 계면활성제 20g을 혼합한 물 290g과 약 3분간 강하게 교반시키고, 제조된 혼합물을 100mm x 100mm x l00mm크기의 형틀에 주형시킨 후, 50℃에서 6시간 동안 전양생시킨 다음 오트클레이브에서 180℃에서 8시간 수열양생시킨 담체를 사용하였다. 상기 담체의 건조비중은 약 0.33로 나타났으며, 제조된 담체를 10g을 물100g과 혼합하여 pH를 측정한 결과 용액의 pH는 7.7정도의 중성을 나타내었다.In the biofilter apparatus of the present invention, 200 g of portant cement, 260 g of silica sand powder, 20 g of lime component, 40 g of alumina cement, and 80 g of peat material were strongly stirred for about 3 minutes with 290 g of water mixed with 20 g of a surfactant, and the prepared mixture was stirred. After casting to a mold of the size of 100mm x 100mm x l00mm, the carrier was pre-cured for 6 hours at 50 ℃ and hydrothermally cured for 8 hours at 180 ℃ in an oatclave. The dry specific gravity of the carrier was found to be about 0.33, and the pH of the solution was measured by mixing 10 g of the prepared carrier with 100 g of water and the pH of the solution was about 7.7.
상기 담체에 표 12의 미생물을 각각 고정하여 이를 실시예 7 내지 9 및 비교예 4의 바이오필터 장치로 하였다.The microorganisms of Table 12 were fixed to the carriers, respectively, to obtain biofilter devices of Examples 7 to 9 and Comparative Example 4.
표 12
구분 미생물
실시예 7 바실러스 서브틸리스 GU1
실시예 8 바실러스 서브틸리스 GU1, 니트로소모나스 유로파(Nitrosomonas europaea) 균주, 니트로박터 아지리스(Nitrobacter agilis) 균주, 니트로소모나스 속(Nitrosomonas sp.) 균주
실시예 9 바실러스 서브틸리스 GU1, 바실러스 서브틸리스 GU2, 슈도모나스 속(Pseudomonas sp.) 균주, 치오바실러스 속(Thiobacillus sp.) 균주, 바실러스 속(Bacillus sp.) 균주
비교예 4 하수처리장에서 채취한 활성슬러지
Table 12
division microbe
Example 7 Bacillus subtilis GU1
Example 8 Bacillus subtilis GU1, Nitrosomonas europaea strain, Nitrobacter agilis strain, Nitrosomonas sp.
Example 9 Bacillus subtilis GU1, Bacillus subtilis GU2, Pseudomonas sp., Thiobacillus sp., Bacillus sp.
Comparative Example 4 Activated Sludge Collected from Sewage Treatment Plant
상기 담체를 채운 유효부피 5l의 바이오필터에 일반 영양배지에서 배양한 각각의 미생물의 배양액(흡광도 0.5) 500 ml를 각각 접종하였다. 실시예 8 및 9는 각각의 미생물을 동량씩 나누어 총 500 ml을 접종하였다. 단, 비교예 4는 MLSS 5g/L의 활성슬러지에 담체를 담지시켜 24시간 폭기시킨 후 유효부피 5l의 바이오필터에 충진하였다.5 ml of the effective volume filled with the carrier was inoculated with 500 ml of the culture medium (absorbance of 0.5) of each microorganism cultured in a general nutrient medium. Examples 8 and 9 were inoculated in 500 ml total aliquots of each microorganism. However, in Comparative Example 4, the carrier was supported on an activated sludge of 5 g / L of MLSS and aerated for 24 hours, followed by filling into a biofilter of 5 l of effective volume.
상기 미생물이 부착된 담체가 충진된 바이오필터에 1주일 동안 가축분뇨공공처리장 집수조(규격 18,000W × 14,000L × 5,000H, 유효용량 : 1,008 m3)에서 발생하는 악취가스를 10 L/min씩 통과하게 하여 미생물을 안정화시켰다.The biofilter filled with the microorganism-attached carrier passes through the odor gas generated in the livestock manure public treatment plant collection tank (standard 18,000W × 14,000L × 5,000H, effective capacity: 1,008 m 3 ) for 10 weeks by 10 L / min. To stabilize the microorganisms.
상기 바이오필터의 미생물을 안정화시킨 후 바이오필터 내의 공탑체류시간을 5초로 조정하여 상기 가축분뇨공공처리장 집수조에서 발생하는 악취가스의 농도를 유입구와 유출구에서 각각 측정하였다. 악취물질 항목은 암모니아(NH3), 황화수소(H2S), 메틸머켑탄(CH3SH) 및 복합악취이고, 그 측정법은 표 13에 나타내었다.After stabilizing the microorganisms of the biofilter, the concentration of the tower stay in the biofilter was adjusted to 5 seconds, and the concentration of the malodorous gas generated in the livestock manure public treatment plant collection tank was measured at the inlet and the outlet, respectively. Malodorous items are ammonia (NH 3 ), hydrogen sulfide (H 2 S), methylmerethane (CH 3 SH), and complex odor, and the measurement method is shown in Table 13.
표 13
구 분 측정방법 분석방법
암모니아 검지관법 UV/VIS
황화수소 테들러백 GC/FPD
메틸머켑탄 테들러백 GC/FPD
복합악취 테들러백 공기희석관능법
Table 13
division How to measure Analysis method
ammonia The detective law UV / VIS
Hydrogen sulfide Tedlar Bag GC / FPD
Methylmerethane Tedlar Bag GC / FPD
Compound odor Tedlar Bag Air dilution sensory method
각 악취물질에 대하여 1일째, 31일째, 91일째에 유입농도와 유출농도를 측정하여 오염물질 제거결과를 표 14에 나타내었다.Table 14 shows the results of removing pollutants by measuring the inflow and outflow concentrations on each of the malodorous substances on the 1st, 31st and 91st days.
표 14
구 분 실시예7 실시예8 실시예9 비교예4
1일 31일 91일 1일 31일 91일 1일 31일 91일 1일 31일 91일
암모니아(ppm) 유입 23 24 24 25 25 26 26 25 26 25 26 25
유출 1.5 1.0 ND 1.5 0.5 ND 1.0 1.0 ND 4.0 2.0 1.5
황화수소(ppm) 유입 3.5 3.0 3.0 3.5 4.0 4.0 3.0 3.5 4.0 3.5 3.0 3.0
유출 1.0 0.5 0.2 0.5 0.2 0.2 0.5 ND ND 2.0 1.0 0.6
메틸머켑탄(ppm) 유입 1.5 1.0 1.3 1.5 1.0 1.0 1.0 1.5 1.0 1.0 1.0 1.0
유출 1.0 0.3 0.2 0.5 0.2 ND 0.3 ND ND 0.5 0.5 0.3
복합악취(희석배수) 유입 5000 6000 6000 6000 6000 7000 6000 5000 7000 6000 6000 6000
유출 1000이하 500이하 300이하 1000이하 500이하 300이하 1000이하 300이하 300이하 2000이하 500이하 300이하
Table 14
division Example 7 Example 8 Example 9 Comparative Example 4
1 day 31 days 91 days 1 day 31 days 91 days 1 day 31 days 91 days 1 day 31 days 91 days
Ammonia (ppm) inflow 23 24 24 25 25 26 26 25 26 25 26 25
outflow 1.5 1.0 ND 1.5 0.5 ND 1.0 1.0 ND 4.0 2.0 1.5
Hydrogen sulfide (ppm) inflow 3.5 3.0 3.0 3.5 4.0 4.0 3.0 3.5 4.0 3.5 3.0 3.0
outflow 1.0 0.5 0.2 0.5 0.2 0.2 0.5 ND ND 2.0 1.0 0.6
Methylmerethane (ppm) inflow 1.5 1.0 1.3 1.5 1.0 1.0 1.0 1.5 1.0 1.0 1.0 1.0
outflow 1.0 0.3 0.2 0.5 0.2 ND 0.3 ND ND 0.5 0.5 0.3
Compound Odor (Dilution Drainage) inflow 5000 6000 6000 6000 6000 7000 6000 5000 7000 6000 6000 6000
outflow Less than 1000 500 or less 300 or less Less than 1000 500 or less 300 or less Less than 1000 300 or less 300 or less Less than 2000 500 or less 300 or less
실험예 7: 파일롯 바이오필터 장치에서의 악취물질 제거 효과Experimental Example 7: Removal of odorous substances in a pilot biofilter device
본 발명의 파일롯 바이오필터 장치를 구성하기 위해서 바이오필터 장치, 바이오필터 장치의 가습장치로 이용되는 세정식 스크라버, 세정식 스크라버 앞에 설치되는 산성가스 제거용 약액 세정장치를 각각 파일롯 스케일로 제조하여 연결하였다.In order to construct the pilot biofilter device of the present invention, a biofilter device, a cleaning scrubber used as a humidifier of the biofilter device, and an acid gas removal chemical cleaning device installed in front of the cleaning scrubber are prepared on a pilot scale, respectively. Connected.
실시예 10의 바이오필터 장치는 규격은 1,800W × 1,400L × 2,600H (6,550 L)이며, 내부에 실시예 6의 미생물이 부착된 담체를 단층으로 유효부피 1,400 L로 충진하고, 운전기간 내 영양배지 또는 산, 알카리 등의 pH 조정제는 투입하지 않고, 바이오필터 장치 내부 온도는 15 ℃이상을 유지하도록 조정되었으며, 공탑체류시간을 16초, 공기의 공간속도(SV)를 0.16m/s로 하여 운전하였고, 가습장치로는 다음의 세정식 스크라버에 물을 순환시켜 사용하였다.The biofilter device of Example 10 is 1,800W × 1,400L × 2,600H (6,550 L), and the carrier with the microorganism of Example 6 attached therein is filled with an effective volume of 1,400 L in a single layer, Without adjusting the pH adjusting agent such as medium, acid, or alkali, the internal temperature of the biofilter device was adjusted to be maintained at 15 ° C or higher, and the air column residence time was 16 seconds and the air velocity (SV) was 0.16 m / s. The water was circulated in the following scrubber as a humidifier.
세정식 스크라버의 본체의 규격은 1,600W × 1,000L × 1,600H (2,500 L)이며, 본체 하단부에서 송풍기(용량 25 m3/분)를 설치하여 체류시간이 6초가 되도록 하였으며, 본체 최하부에는 저수조(용량 1,000 L)에는 물을 순환수 공급펌프(용량 50 L/분)에 의해서 2개의 나선형 노즐로 연속 분사하도록 제조되었다.The size of the main body of the cleaning scrubber is 1,600W × 1,000L × 1,600H (2,500L), and a blower (capacity 25 m 3 / min) is installed at the bottom of the main body so that the residence time is 6 seconds. (Capacity 1,000 L) was made to continuously spray water into two spiral nozzles by a circulating water supply pump (capacity 50 L / min).
실시예 11의 바이오필터 장치는 실시예 10의 장치를 이용하되 세정식 스크라버에 물대신 죽초액이 0.5중량%로 희석된 죽초액희석수를 사용한 것이다.The biofilter apparatus of Example 11 uses the apparatus of Example 10, but uses bamboo vinegar dilution water diluted with 0.5% by weight of bamboo vinegar in place of water in a scrubber.
실시예 12의 바이오필터 장치는 실시예 10의 장치를 이용하되 세정식 스크라버의 물대신 죽초액이 0.5중량% 희석된 죽초액희석수에 바실러스 서브틸리스 GU1 균주 1.00E+05 cfu/ml 농도로 접종한 GU1-죽초액희석수를 사용한 것이다.The biofilter device of Example 12 was inoculated at the concentration of 1.00E + 05 cfu / ml of Bacillus subtilis GU1 strain by using the device of Example 10, but diluted with 0.5% by weight of bamboo vinegar diluted with bamboo vinegar instead of water of the scrubber. One GU1- bamboo liquor dilution water was used.
실시예 13의 바이오필터 장치는 실시예 11의 바이오필터 장치의 죽초액 세정식 스크라버 앞에 산성가스 제거용 약액 세정장치를 부가한 것으로, 약액 세정장치는 규격은 1,600W × 1,000L × 1,600H (2,500 L)이며, 본체 하단부에서 송풍기(용량 25 m3/분)를 설치하여 체류시간이 6초가 되도록 하였으며, 본체 최하부에는 저수조(용량 1,000 L)에는 NaOH용액을 순환수 공급펌프(용량 50 L/분)에 의해서 2개의 나선형 노즐로 연속 분사하도록 제조되었다.The biofilter device of Example 13 is an acid gas removal chemical cleaning device in front of the bamboo vinegar cleaning scrubber of the biofilter device of Example 11, the chemical cleaning device is 1,600W × 1,000L × 1,600H (2,500 L), and a blower (capacity 25 m 3 / min) was installed at the bottom of the main body so that the residence time was 6 seconds, and the bottom of the main body was supplied with a circulating water supply pump (capacity 50 L / min) ) To continuously spray into two spiral nozzles.
각 악취물질에 대하여 1일째, 31일째, 91일째에 유입농도와 유출농도를 측정하여 오염물질 제거효율을 표 15에 나타내었다.Table 15 shows the removal efficiency of pollutants by measuring the inflow and outflow concentrations for each odorous substance at 1st, 31st and 91st day.
표 15
구 분 실시예10 실시예11 실시예12 실시예13
1일 31일 91일 1일 31일 91일 1일 31일 91일 1일 31일 91일
암모니아(ppm) 유입 45 45 50 35 40 40 35 40 35 32 36 37
유출 0.5 0.3 ND 0.5 ND ND 0.2 ND ND 0.3 ND ND
황화수소(ppm) 유입 3.5 3.0 3.0 5.0 6.0 6.0 6.5 6.0 5.5 5.5 6.5 5.0
유출 0.3 0.2 ND 0.2 ND ND 0.2 ND ND ND ND ND
메틸머켑탄(ppm) 유입 1.5 1.0 1.3 1.5 2.0 1.5 2.0 1.0 1.5 1.5 2.0 1.5
유출 0.3 ND ND 0.2 ND ND 0.2 ND ND ND ND ND
복합악취(희석배수) 유입 5000 6000 6000 4000 5000 5000 5000 5000 5000 5000 6000 5000
유출 500이하 500이하 300이하 500이하 300이하 300이하 500이하 300이하 300이하 500이하 300이하 300이하
Table 15
division Example 10 Example 11 Example 12 Example 13
1 day 31 days 91 days 1 day 31 days 91 days 1 day 31 days 91 days 1 day 31 days 91 days
Ammonia (ppm) inflow 45 45 50 35 40 40 35 40 35 32 36 37
outflow 0.5 0.3 ND 0.5 ND ND 0.2 ND ND 0.3 ND ND
Hydrogen sulfide (ppm) inflow 3.5 3.0 3.0 5.0 6.0 6.0 6.5 6.0 5.5 5.5 6.5 5.0
outflow 0.3 0.2 ND 0.2 ND ND 0.2 ND ND ND ND ND
Methylmerethane (ppm) inflow 1.5 1.0 1.3 1.5 2.0 1.5 2.0 1.0 1.5 1.5 2.0 1.5
outflow 0.3 ND ND 0.2 ND ND 0.2 ND ND ND ND ND
Compound Odor (Dilution Drainage) inflow 5000 6000 6000 4000 5000 5000 5000 5000 5000 5000 6000 5000
outflow 500 or less 500 or less 300 or less 500 or less 300 or less 300 or less 500 or less 300 or less 300 or less 500 or less 300 or less 300 or less
표 15는 파일럿 프랜트를 이용한 탈취효율 시험으로 표 14의 실험실 규모의 시험장치를 이용한 시험 결과보다 탈취효율이 높게 나타났다. 실시예13의 경우 유출구에서 황화수소와 메틸머캅탄의 농도가 비교예9 보다 크게 낮게 나타난 것은 실시예 11의 바이오필터 장치의 죽초액 세정식 스크라버 앞에 산성가스 제거용 약액 세정장치를 부가한 결과로 판단된다. 또한 실시예12의 경우 유출구에서 암모니아, 황화수소, 메틸머캅탄 및 복합악취의 농도가 실시예11 보다 낮게 나타난 것은 실시예 11의 바이오필터 장치의 죽초액 세정식 스크라버 순환수에 바실러스 서브틸리스 GU1 균주를 접종한 GU1-죽초액희석수를 사용한 결과로 판단된다. Table 15 shows the deodorization efficiency test using the pilot plant. The deodorization efficiency was higher than the test results using the laboratory scale test apparatus shown in Table 14. In the case of Example 13, the concentration of hydrogen sulfide and methyl mercaptan at the outlet was significantly lower than that of Comparative Example 9, which was determined by the addition of an acid gas removal chemical cleaning device in front of the bamboo vinegar cleaning scrubber of the biofilter device of Example 11. do. In addition, in the case of Example 12, the concentration of ammonia, hydrogen sulfide, methylmercaptan, and complex odor at the outlet was lower than that of Example 11. The Bacillus subtilis GU1 strain in the bamboo vinegar-cleaning scrubber circulating water of the biofilter device of Example 11 It is judged to be the result of using GU1- bamboo vinegar dilution water.
Figure PCTKR2010003803-appb-I000001
Figure PCTKR2010003803-appb-I000001
Figure PCTKR2010003803-appb-I000002
Figure PCTKR2010003803-appb-I000002
Figure PCTKR2010003803-appb-I000003
Figure PCTKR2010003803-appb-I000003
Figure PCTKR2010003803-appb-I000004
Figure PCTKR2010003803-appb-I000004

Claims (7)

  1. 죽초액에서 분리되고 목초액을 0.1 ~ 50 중량% 포함하는 배지에서 생육가능한 것을 특징으로 하는 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P]. Bacillus subtilis GU1 [Accession No. KCCM 10890P], characterized in that it is isolated from bamboo vinegar and growable in a medium containing 0.1 to 50% by weight of wood vinegar.
  2. 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주를 목초액을 0.5 ~ 10 중량% 포함하는 배지에서 발효시킨 배양물. Bacillus subtilis ( Bacillus subtilis ) GU1 [Accession No. KCCM 10890P] A culture in which the strain was fermented in a medium containing 0.5 to 10% by weight of wood vinegar.
  3. 제2항에 있어서, 상기 배지는 고체배지인 것을 특징으로 하는 배양물.The culture according to claim 2, wherein the medium is a solid medium.
  4. 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주를 목초액을 0.5 ~ 10 중량% 포함하는 배지에서 발효시킨 배양물을 포함하는 사료첨가제. Bacillus subtilis ( Bacillus subtilis ) GU1 [Accession No. KCCM 10890P] feed additive comprising a culture fermented in a medium containing 0.5 to 10% by weight of wood vinegar.
  5. 악취물질을 바이오필터 장치 내부로 유입시키는 송풍기와, 바이오필터 장치 내부로 수분을 공급하는 가습장치와, 미생물이 부착된 담체를 포함하는 바이오필터 장치에 있어서, 상기 가습장치는 목초액 조성물이 분사되는 세정식 목초액 스크라버이고, 상기 담체에 부착된 미생물은 죽초액에서 분리되고 죽초액을 0.5 ~ 50 중량% 포함하는 배지에서 생육가능한 것을 특징으로 하는 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P]인 것을 특징으로 하는 악취물질 제거용 바이오필터 장치.In the biofilter apparatus comprising a blower for introducing a malodorous substance into the biofilter device, a humidifier for supplying moisture into the biofilter device, and a carrier to which microorganisms are attached, the humidifier comprises: Bacillus subtilis GU1 [Accession No. KCCM 10890P], which is a formal wood vinegar scrubber, and the microorganisms attached to the carrier are separated from the bamboo vinegar solution and are capable of growing in a medium containing 0.5 to 50% by weight of bamboo vinegar solution. Biofilter device for removing odorous substances, characterized in that.
  6. 제 5 항에 있어서, 상기 미생물은 니트로소모나스 속(Nitrosomonas sp.) 균주, 바실러스 속(Bacillus sp.) 균주, 슈도모나스 속(Pseudomonas sp.) 균주, 니트로소모나스 속(Nitrosomonas sp.) 균주, 니트로박터 속(Nitrobacter sp.) 균주, 치오바실러스 속(Thiobacillus sp.) 균주 중에서 어느 하나 이상의 균주가 더 포함된 것을 특징으로 하는 악취물질 제거용 바이오필터 장치.The method of claim 5, wherein the microorganism is Nitrosomonas sp., Bacillus sp., Pseudomonas sp., Nitrosomonas sp., Nitro Bacterial genus ( Nitrobacter sp.) Strain, Genus Bacillus (Thiobacill us sp.) Strain of any one or more biofilter device for removing the odorous substance, characterized in that it further comprises.
  7. 제 5 항에 있어서, 상기 세정식 목초액 스크라버에서는 목초액 조성물과 함께 목초액에서 유래된 바실러스 서브틸리스(Bacillus subtilis) GU1 [기탁번호 KCCM 10890P] 균주 및 바실러스 서브틸리스(Bacillus subtilis) GU2 [기탁번호 KCCM 10891P] 균주 중에서 선택된 어느 하나 이상의 균주가 함께 분사되는 것을 특징으로 하는 악취물질 제거용 바이오필터 장치.The method according to claim 5, wherein in the washed wood-vinegar scrubber Bacillus subtilis GU1 [Accession No. KCCM 10890P] strain and Bacillus subtilis GU2 [Accession No. KCCM 10891P] Biofilter device for removing odorous substances, characterized in that any one or more strains selected from among the strains are sprayed together.
PCT/KR2010/003803 2009-06-15 2010-06-14 Bacillus subtilis gu1 and use thereof WO2010147345A2 (en)

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