JPS6319150B2 - - Google Patents
Info
- Publication number
- JPS6319150B2 JPS6319150B2 JP6392780A JP6392780A JPS6319150B2 JP S6319150 B2 JPS6319150 B2 JP S6319150B2 JP 6392780 A JP6392780 A JP 6392780A JP 6392780 A JP6392780 A JP 6392780A JP S6319150 B2 JPS6319150 B2 JP S6319150B2
- Authority
- JP
- Japan
- Prior art keywords
- cellulose
- ozone
- degrading bacteria
- amount
- cellulosic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 66
- 241000894006 Bacteria Species 0.000 claims description 42
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 239000000126 substance Substances 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 238000012258 culturing Methods 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 239000001913 cellulose Substances 0.000 description 30
- 229920002678 cellulose Polymers 0.000 description 30
- 239000010902 straw Substances 0.000 description 25
- 241000209094 Oryza Species 0.000 description 23
- 235000007164 Oryza sativa Nutrition 0.000 description 23
- 235000009566 rice Nutrition 0.000 description 23
- 239000002994 raw material Substances 0.000 description 13
- 229920005610 lignin Polymers 0.000 description 12
- 230000001580 bacterial effect Effects 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000002609 medium Substances 0.000 description 7
- 108010059892 Cellulase Proteins 0.000 description 6
- 229940106157 cellulase Drugs 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000001954 sterilising effect Effects 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 241000186220 Cellulomonas flavigena Species 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 4
- 241000223261 Trichoderma viride Species 0.000 description 4
- 238000007664 blowing Methods 0.000 description 4
- 238000012136 culture method Methods 0.000 description 4
- 229940088598 enzyme Drugs 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- GUBGYTABKSRVRQ-CUHNMECISA-N D-Cellobiose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-CUHNMECISA-N 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- 108090000604 Hydrolases Proteins 0.000 description 3
- 102000004157 Hydrolases Human genes 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- 241000609240 Ambelania acida Species 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 239000010905 bagasse Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 238000006385 ozonation reaction Methods 0.000 description 2
- 239000010893 paper waste Substances 0.000 description 2
- 230000002085 persistent effect Effects 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 235000013343 vitamin Nutrition 0.000 description 2
- 229940088594 vitamin Drugs 0.000 description 2
- 229930003231 vitamin Natural products 0.000 description 2
- 239000011782 vitamin Substances 0.000 description 2
- 241000186046 Actinomyces Species 0.000 description 1
- 241000228212 Aspergillus Species 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 108010056771 Glucosidases Proteins 0.000 description 1
- 102000004366 Glucosidases Human genes 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 241000228143 Penicillium Species 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241000223259 Trichoderma Species 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 1
- 235000019797 dipotassium phosphate Nutrition 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000013028 medium composition Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 1
- 235000019796 monopotassium phosphate Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 1
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Landscapes
- Enzymes And Modification Thereof (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
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ã«é¢ãããã®ã§ãããDETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for culturing cellulose-degrading bacteria using cellulosic materials such as rice straw, wheat straw, bagasse, waste paper, and wood chips as a carbon source. This invention relates to a method for culturing cellulose-degrading bacteria to enable cellulose assimilation.
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æ¬ ç¹ãããã When cellulose-degrading bacteria are allowed to act on cellulosic substances and the cellulase (cellulose hydrolase) and organic acids secreted by the cellulose-degrading bacteria are grown, or the cellulose-degrading bacteria themselves are grown to produce microbial proteins, the culture of cellulose-degrading bacteria is used. In addition, it must be possible for cellulose-degrading bacteria to efficiently utilize cellulose in cellulosic substances. However, cellulose in cellulosic materials such as rice straw, wheat straw, bagasse, waste paper, and wood chips has a chemical structure that makes it difficult for cellulose-degrading bacteria to act on it. Cellulose is
It is a homopolymer in which glucose is linearly arranged with β-1,-4 bonds, but the cellulose in the above substance has a structure in which the linear homopolymers are coordinated in parallel to each other, that is, a crystal structure, and furthermore, It is covered with persistent lignin. By the way, the ability of cellulose-degrading bacteria to use cellulose as a nutrient source is due to the action of cellulase (cellulose hydrolase) secreted by the same bacteria. Cellulase is
C1 enzyme that amorphizes crystalline cellulose, Cx enzyme that decomposes amorphous cellulose into cellobiose, and β- enzyme that decomposes cellobiose into glucose.
It is a complex enzyme composed of glucosidase.
Cellulose-degrading bacteria convert cellulose into cellobiose and glucose using the cellulase. However, Cerase is C 1
It has weak activity and no lignin decomposition ability. Therefore, cellulose-degrading bacteria cannot directly assimilate cellulose contained in cellulosic substances having the above-mentioned structure. Therefore, in order to cultivate cellulose-degrading bacteria using cellulosic materials as a substrate,
When preparing the substrate, it is necessary to decompose lignin and destroy the crystal structure of cellulose. Chemical or physical treatment is used as a method for this purpose. Chemical methods include alkaline treatment with sodium hydroxide or the like and acid treatment with phosphoric acid, etc., but a common method is to add a cellulosic substance to an aqueous sodium hydroxide solution and heat it.
This has the effect of extracting and removing lignin and swelling the crystal structure of cellulose. However, this method consumes large amounts of water and there is a loss of active ingredients such as cellulose, hemicellulose and protein. Additionally, it is necessary to treat wastewater containing persistent lignin. On the other hand, as a physical treatment, pulverization using a ball mill, vibration mill, etc. is common. This method crushes cellulosic materials into approximately 400 meshes and directly destroys the crystalline structure of cellulose. However, this method has disadvantages, such as the need to thoroughly dry the cellulosic material and the significant power costs.
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ããŒã¹åè§£èå¹é€æ³ãæäŸãããã®ã§ããã An object of the present invention is to provide a method for culturing cellulose-degrading bacteria that eliminates the drawbacks of the conventional methods described above and allows cellulose-degrading bacteria to efficiently utilize cellulose in cellulose materials. It is something to do.
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ã§ããã To summarize the present invention, the method for culturing cellulose-degrading bacteria of the present invention involves mixing a cellulosic material with an aqueous solution containing inorganic nitrogen, inorganic salts, etc. so that the water content becomes 90% or less, and then adding ozone and gas-solidified material. By contacting it, the ability of cellulose-degrading bacteria to assimilate cellulose in cellulose substances is improved.
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ãã It has been reported that lignin is decomposed by ozone treatment of the lignin waste liquid discharged from the wood pulping process in the paper industry (1975 Ministry of Education specific research, Takamasa Higuchi, âReducing waste liquid lignin by ozone and microbial treatmentâ). "Decomposition": see research report on environmental purification using microorganisms). Therefore, the inventors thought that this method could be applied to a substrate preparation method for culturing cellulose-degrading bacteria, and carried out ozone treatment by suspending a cellulosic substance in water and blowing ozone into it. However, cellulose-degrading bacteria hardly utilized cellulose in cellulosic substances. This is because the lignin in cellulosic substances has a three-dimensional tertiary structure, unlike soluble lignin such as waste liquid lignin, so it is assumed that the lignin in cellulosic substances is difficult to be decomposed by ozone using the method reported above. Ta. Therefore, as a result of further studies on ozone treatment of cellulosic materials, the inventors discovered that cellulose decomposition can be prevented by immersing cellulosic materials in water, bringing them into gas-solid contact with ozone, and reacting with more than a specific amount of ozone. The present invention was achieved by discovering that cellulose in cellulosic substances can be effectively decomposed.
以äžã宿œäŸã«åŸã€ãŠæ¬çºæã説æããã The present invention will be described below with reference to Examples.
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ããŠå€è§çã«æ€èšããã The present inventors conducted a multifaceted study on ozone treatment of cellulosic materials and assimilation of the ozonated cellulosic materials by cellulose-degrading bacteria using the following apparatus.
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ãè¯ãã In this apparatus, first, as shown in the figure, a raw material 1 which is a cellulosic substance and a medium 2 containing no carbon source are mixed in a mixer 3, and then reacted with ozone in an ozone treatment tank 4. Here, the medium 2 is an aqueous solution containing inorganic nitrogen such as ammonium sulfate and ammonium chloride, and inorganic salts such as phosphate, magnesium salt, and potassium salt. Further, the medium 2 may be simply water, but in this case, the above-mentioned medium composition may be added again at a later stage. Note that if cellulose-degrading bacteria require organic nitrogen or vitamins, they may be added after the ozone reaction. In the mixer 3, the moisture content of the cellulosic substance raw material 1 is
Prepared to 90% or less. This raw material 1 comes into contact with ozone supplied from an ozone blowing port 6 at the bottom of the tank in the ozone treatment tank 4 . Note that ozone is prepared by an ozone generator 7 using air 8 as a raw material. The inlet ozone concentration at this time is 0.1 to 20g/
m 3 is sufficient, but there is no particular limitation.
The raw material 5 in the ozone reaction tank 4 is extracted by a discharge feeder 9 provided at the bottom of the tank, and thus becomes a moving tank 5 and descends. At this time, it comes into countercurrent contact with the rising ozone. Note that the ozone treatment tank 4 may be a device that mechanically stirs the raw material 5 and brings it into contact with ozone.
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ãã The raw material 5 that has been ozonated in the ozone treatment tank 4 is
It is extracted by the discharge feeder 9 and enters the sterilization tube 10. The sterilization tube 10 is heated to about 100° C. by the steam 11. Then, the raw material 5 passed through the sterilization pipe 10
is sterilized and at the same time unreacted ozone is decomposed. Note that the sterilization method is not particularly limited.
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ãããŸããã»ã«ããŒã¹åè§£èã¯ãCellulomans
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ãã The sterilized raw material 5 is supplied to the culture tank 12. In the culture tank 12, the raw material 5 and cellulose-degrading bacteria are mixed. The cellulose in the raw material 5 is reduced in molecular weight by cellulase (cellulose hydrolase) secreted by cellulose-degrading bacteria.
The culture method may be either a solid culture method or a submerged culture method. At this time, conditions in the culture tank 12 that are suitable for the growth of cellulose-degrading bacteria, such as temperature and pH, must be controlled to optimal values. In addition, cellulose-degrading bacteria are Cellulomans
Genus, Cellribrio, Pseudomonas, Clostrdium
Genus, Actinomyces, Aspergillus,
Bacteria capable of decomposing cellulose, such as those of the genus Penicillium, cannot be used, and there are no particular limitations.
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æ··åç©ã¯ãæåºå£ïŒïŒããåãåºãããã A mixture of decomposition products, decomposition residues, and cellulose-degrading bacteria is taken out from the outlet 13.
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ã¯ãããã«ãããªããéå®ããããã®ã§ã¯ãªãã Next, the present invention will be explained with reference to Examples, but the present invention is not limited thereto.
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ã®ééã§ãããExample 1 Sun-dried rice straw was cut into 5-10 mm pieces and mixed with a culture medium to prepare rice straw with a moisture content of 5-85% by weight. The medium contains 6.0g of sodium chloride/
, ammonium sulfate 1.0g/, monopotassium phosphate 0.5g/, dipotassium phosphate 0.5g/, magnesium sulfate 0.2g/, calcium chloride 0.3
g/aqueous solution. This rice straw was placed in the ozone treatment tank and subjected to gas-solid contact reaction with ozone. Note that the ozone concentration blown was 12 g/m 3 . Moreover, the reaction temperature was room temperature. The amount of ozone reaction was calculated from the difference in ozone concentration between the inlet and the outlet, the ozone blowing rate, and the contact time. The unit of ozone reaction amount is the weight of ozone reacted per 1 g of dry rice straw.
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ãããã§ããã Figure 2 shows the measurement results. Plot A is the result of this example. Even when a water-soluble medium containing inorganic nitrogen and inorganic salts was added to rice straw, the rice straw reacted with ozone, and the amount of ozone reaction increased as the water content increased. As a comparative example, rice straw soaked with water was subjected to the same treatment. The results are also shown in Figure 2. Plot B is the result of a comparative example. From the results of the comparative example and the above example,
It was found that almost the same results as with water can be obtained using a water-soluble medium. The reason why the amount of ozone reaction decreased when the water content was 70% by weight or more was because the rice straws adhered to each other, reducing the efficiency of contact with ozone.
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質ãšããŠã»ã«ããŒã¹åè§£èã®èå¹ãè¡ã€ããExample 2 Cellulose-degrading bacteria were cultured using the ozonated rice straw obtained in Example 1 as a substrate.
ã»ã«ããŒã¹åè§£èãšããŠã¯ãTrichoderma
virideïŒã¢ã¡ãªã«ã³ã»ã¿ã€ãã»ã«ã«ããŠã¢ãŒã»ã³
ã¬ã¯ã·ãšã³ïŒATCCNo.13631ïŒåã³ã³ã³ãã¹ã
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226æ ªïŒãçšãããå¹é€ã¯ãåºäœå¹é€æ¹åŒãšãã
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Trichoderma virideã¯30âïŒCNYâ266æ ªã¯50
âãšããã Trichoderma is a cellulose-degrading bacterium.
viride (American Type Culture Collection: ATCC No. 13631) and a bacterial strain isolated from compost (final identification, tentative name CNY-
226 strains) were used. Cultivation is done using a solid culture method.
That is, ozonated rice straw and cellulose-degrading bacteria were mixed aerobically in a moist state. In addition, both strains are
Since the yeast requires vitamins, a previously sterilized yeast extract solution was added to the ozone-treated rice straw for cultivation. In addition, the culture temperature is
30â for Trichoderma viride, 50â for CNY-266 strain
â.
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ã€ããšæšå®ããã FIG. 3 shows the moisture content and the amount of bacterial cells produced. The culture time was 8 days. C is for Trichoderma
viride, D shows the case of CNY-226 strain. In addition,
The plot with a moisture content of 0% by weight is the case without ozone treatment. From the figure, as the water content increases,
The amount of bacterial cells produced increased, and the same results as in Example 1 were obtained. From this point of view, the amount of ozone reaction is considered to be a factor that influences the amount of bacterial cell production. In other words, it is thought that as the amount of ozone reaction increases, the cellulose in rice straw becomes more easily assimilated by cellulose-degrading bacteria, and when the water content is 70% by weight or more, the amount of ozone reaction is greater than the water content of 10% by weight. Regardless, the amount of bacteria produced is small. In particular, when the water content was around 90% by weight, the amount of bacterial cells produced was almost the same as that of the untreated sample. The reason for this is thought to be as follows. When rice straw with a moisture content of 70% by weight or more was prepared, there was a large amount of free water, and the free water contained soluble substances and had a color. However, when treated with ozone, most of the color was removed. From this, the above cause is that ozone does not react directly with rice straw,
It is assumed that this is because the ozonation reacts with the eluate of the rice straw, and as a result, the effect of ozonation treatment is virtually ineffective.
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ã§ããã Judging from the above results, in order to substantially obtain the effect of ozone treatment, the water content should be 90% by weight or less.
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ããã®çš²ããã調補ããTrichoderma virideïŒ
CNYâ226æ ªãåã³Cellulomonas flavigena
ïŒATCCNo.484ïŒã®å¹é€ãè¡ã€ãããªãã
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é€ã§ãCellulomonas flavigenaã®å¹é€ã¯æ¶²äœå¹
é€ãšãããExample 3 Rice straw with an ozone reaction amount of 0 to 0.04-ozone/g-dried rice straw was prepared, and Trichoderma viride,
CNY-226 strain and Cellulomonas flavigena
(ATCC No. 484) was cultured. In addition,
Tichoderma viride and CNY-226 strains were cultured in solid state, and Cellulomonas flavigena was cultured in liquid culture.
ãªããCellulomonas flavigenaã®å¹é€ã§ã¯ã
枩床30âã§PHã6.8ã«ã³ã³ãããŒã«ããã In addition, in the culture of Cellulomonas flavigena,
The temperature was 30°C and the pH was controlled at 6.8.
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Cellulomonas flavigenaã®å Žåã瀺ãã When the results on the 10th day of culture were organized by the amount of ozone reaction, the results were as shown in Figure 4. E is for Trichoderma
viride, F is CNY-226 stock, and G is
The case of Cellulomonas flavigena is shown.
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ã§ãèäœçæéãèããå¢å ããã From Figure 4, as the amount of ozone reaction increases,
It can be seen that the amount of bacterial cells produced is increasing. In other words, it was found that as the amount of ozone reaction increased, cellulose in rice straw became more easily decomposed by cellulose-degrading bacteria. In particular, the amount of ozone reaction
The amount of bacteria produced increased significantly with rice straw containing 0.005g-ozone/g-dry rice straw or higher.
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ãã以äžãšããã°è¯ããšçµè«ããã From the above examples, in order to substantially obtain the effect of ozone treatment, the water content of the cellulosic material should be 90% or less, and a gas-solid contact reaction with ozone should be carried out.
It was also concluded that the amount of ozone reaction should be set to 0.005 g/g of dry rice straw or more.
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广ãåŸãããŠããããšãããçµæžçã§ããã If the present invention is applied, for example, when cellulose substances are used as a carbon source and cellulose-degrading bacteria are cultured to produce microbial proteins from the bacterial cells, or when cellulase or organic acids secreted by cellulose-degrading bacteria are produced, etc. The cellulose in the cellulosic material is efficiently decomposed by cellulose-degrading bacteria, improving the production rate. Furthermore, since the present invention involves a gas-solid contact reaction between a cellulosic substance and ozone, there is no problem in waste liquid treatment such as in caustic soda treatment. Furthermore, since the treatment effect is obtained with a small amount of consumed ozone reaction, it is economical.
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Figure 1 is a schematic diagram of the culture apparatus used in the present invention, Figure 2 is a graph showing the relationship between ozone reaction amount and water content, Figure 3 is a graph showing the relationship between water content and bacterial cell production, and Figure 4 is a graph showing the relationship between water content and bacterial cell production. The figure is a graph showing the relationship between the amount of ozone reaction and the amount of bacterial cell production. 1... Raw material, 2... Culture medium, 3... Mixer, 4...
... Ozone treatment tank, 5 ... Mobile tank, 6 ... Ozone blowing port, 7 ... Ozone generator, 8 ... Air,
9... Discharge feeder, 10... Sterilization tube, 11...
Steam, 12...Culture tank, 13...Outlet.
Claims (1)
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第ïŒé èšèŒã®ã»ã«ããŒã¹åè§£èå¹é€æ¹æ³ã[Claims] 1. When culturing cellulose-degrading bacteria using a cellulosic substance as a carbon source, the cellulosic substance is mixed with an aqueous solution containing inorganic nitrogen and inorganic salts so that the water content is 90% or less, and then A method for culturing cellulose-degrading bacteria, which is characterized by bringing the cellulose-degrading bacteria into gas-solid contact with ozone. 2 Cellulosic material and ozone are mixed in an amount of ozone reaction per 1 g of dry weight of the cellulosic material.
The method for culturing cellulose-degrading bacteria according to claim 1, wherein the cellulose-degrading bacteria are brought into contact at a rate of 0.005 g or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6392780A JPS56160989A (en) | 1980-05-16 | 1980-05-16 | Cultivating method for microorganism capable of hydrolyzing cellulose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6392780A JPS56160989A (en) | 1980-05-16 | 1980-05-16 | Cultivating method for microorganism capable of hydrolyzing cellulose |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56160989A JPS56160989A (en) | 1981-12-11 |
| JPS6319150B2 true JPS6319150B2 (en) | 1988-04-21 |
Family
ID=13243458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6392780A Granted JPS56160989A (en) | 1980-05-16 | 1980-05-16 | Cultivating method for microorganism capable of hydrolyzing cellulose |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56160989A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0244159A (en) * | 1988-08-05 | 1990-02-14 | Mitsubishi Electric Corp | Refrigerator |
-
1980
- 1980-05-16 JP JP6392780A patent/JPS56160989A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0244159A (en) * | 1988-08-05 | 1990-02-14 | Mitsubishi Electric Corp | Refrigerator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56160989A (en) | 1981-12-11 |
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