JPH03200A - Treatment of waste liquid after production of shochu by distillation - Google Patents
Treatment of waste liquid after production of shochu by distillationInfo
- Publication number
- JPH03200A JPH03200A JP1132801A JP13280189A JPH03200A JP H03200 A JPH03200 A JP H03200A JP 1132801 A JP1132801 A JP 1132801A JP 13280189 A JP13280189 A JP 13280189A JP H03200 A JPH03200 A JP H03200A
- Authority
- JP
- Japan
- Prior art keywords
- shochu
- distillation
- enzyme
- liq
- waste liq
- 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.)
- Granted
Links
- 238000004821 distillation Methods 0.000 title claims abstract description 37
- 235000020083 shōchū Nutrition 0.000 title claims abstract description 24
- 239000002699 waste material Substances 0.000 title abstract description 26
- 238000004519 manufacturing process Methods 0.000 title abstract description 8
- 239000007788 liquid Substances 0.000 title description 24
- 102000004190 Enzymes Human genes 0.000 claims abstract description 24
- 108090000790 Enzymes Proteins 0.000 claims abstract description 24
- 241000187747 Streptomyces Species 0.000 claims abstract description 10
- 241000894006 Bacteria Species 0.000 claims abstract description 3
- 239000002351 wastewater Substances 0.000 claims description 8
- 150000004676 glycans Chemical class 0.000 abstract description 18
- 229920001282 polysaccharide Polymers 0.000 abstract description 18
- 239000005017 polysaccharide Substances 0.000 abstract description 18
- 239000007787 solid Substances 0.000 abstract description 9
- 238000006911 enzymatic reaction Methods 0.000 abstract description 4
- 230000000593 degrading effect Effects 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000000704 physical effect Effects 0.000 abstract description 2
- 102000002568 Multienzyme Complexes Human genes 0.000 abstract 1
- 108010093369 Multienzyme Complexes Proteins 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 15
- 238000001914 filtration Methods 0.000 description 14
- 239000000049 pigment Substances 0.000 description 13
- 238000000354 decomposition reaction Methods 0.000 description 9
- 229920001817 Agar Polymers 0.000 description 8
- 239000008272 agar Substances 0.000 description 8
- 239000006228 supernatant Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 210000002421 cell wall Anatomy 0.000 description 6
- 239000000706 filtrate Substances 0.000 description 6
- 230000001580 bacterial effect Effects 0.000 description 5
- 238000004065 wastewater treatment Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
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- 235000002595 Solanum tuberosum Nutrition 0.000 description 3
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- 229940041514 candida albicans extract Drugs 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 3
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- 238000005516 engineering process Methods 0.000 description 3
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- 239000010802 sludge Substances 0.000 description 3
- 241001446247 uncultured actinomycete Species 0.000 description 3
- 239000012138 yeast extract Substances 0.000 description 3
- GMKMEZVLHJARHF-UHFFFAOYSA-N (2R,6R)-form-2.6-Diaminoheptanedioic acid Natural products OC(=O)C(N)CCCC(N)C(O)=O GMKMEZVLHJARHF-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 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 2
- 240000005979 Hordeum vulgare Species 0.000 description 2
- 235000007340 Hordeum vulgare Nutrition 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 2
- 238000012258 culturing Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- GMKMEZVLHJARHF-SYDPRGILSA-N meso-2,6-diaminopimelic acid Chemical compound [O-]C(=O)[C@@H]([NH3+])CCC[C@@H]([NH3+])C([O-])=O GMKMEZVLHJARHF-SYDPRGILSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000001814 pectin Substances 0.000 description 2
- 229920001277 pectin Polymers 0.000 description 2
- 235000010987 pectin Nutrition 0.000 description 2
- 230000001766 physiological effect Effects 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000005720 sucrose Substances 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- BBBFYZOJHSYQMW-LGDQNDJISA-N (2s)-2,4-diamino-4-oxobutanoic acid;(2r,3s,4r,5r)-2,3,4,5,6-pentahydroxyhexanal Chemical compound OC(=O)[C@@H](N)CC(N)=O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O BBBFYZOJHSYQMW-LGDQNDJISA-N 0.000 description 1
- 241000186361 Actinobacteria <class> Species 0.000 description 1
- DCXYFEDJOCDNAF-UHFFFAOYSA-N Asparagine Natural products OC(=O)C(N)CC(N)=O DCXYFEDJOCDNAF-UHFFFAOYSA-N 0.000 description 1
- 244000056139 Brassica cretica Species 0.000 description 1
- 235000003351 Brassica cretica Nutrition 0.000 description 1
- 235000003343 Brassica rupestris Nutrition 0.000 description 1
- 241000282836 Camelus dromedarius Species 0.000 description 1
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 1
- SHZGCJCMOBCMKK-UHFFFAOYSA-N D-mannomethylose Natural products CC1OC(O)C(O)C(O)C1O SHZGCJCMOBCMKK-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 1
- 244000000626 Daucus carota Species 0.000 description 1
- 235000002767 Daucus carota Nutrition 0.000 description 1
- 244000239348 Echinochloa crus galli var. praticola Species 0.000 description 1
- 239000005715 Fructose Substances 0.000 description 1
- 229930091371 Fructose Natural products 0.000 description 1
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- SRBFZHDQGSBBOR-HWQSCIPKSA-N L-arabinopyranose Chemical compound O[C@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-HWQSCIPKSA-N 0.000 description 1
- DCXYFEDJOCDNAF-REOHCLBHSA-N L-asparagine Chemical compound OC(=O)[C@@H](N)CC(N)=O DCXYFEDJOCDNAF-REOHCLBHSA-N 0.000 description 1
- PNNNRSAQSRJVSB-UHFFFAOYSA-N L-rhamnose Natural products CC(O)C(O)C(O)C(O)C=O PNNNRSAQSRJVSB-UHFFFAOYSA-N 0.000 description 1
- OUYCCCASQSFEME-QMMMGPOBSA-N L-tyrosine Chemical compound OC(=O)[C@@H](N)CC1=CC=C(O)C=C1 OUYCCCASQSFEME-QMMMGPOBSA-N 0.000 description 1
- 229930195725 Mannitol Natural products 0.000 description 1
- 241000544912 Melanoides Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000002834 Paulownia tomentosa Species 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- MUPFEKGTMRGPLJ-RMMQSMQOSA-N Raffinose Natural products O(C[C@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@@H](O[C@@]2(CO)[C@H](O)[C@@H](O)[C@@H](CO)O2)O1)[C@@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 MUPFEKGTMRGPLJ-RMMQSMQOSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241000576755 Sclerotia Species 0.000 description 1
- 244000062793 Sorghum vulgare Species 0.000 description 1
- 102000003425 Tyrosinase Human genes 0.000 description 1
- 108060008724 Tyrosinase Proteins 0.000 description 1
- MUPFEKGTMRGPLJ-UHFFFAOYSA-N UNPD196149 Natural products OC1C(O)C(CO)OC1(CO)OC1C(O)C(O)C(O)C(COC2C(C(O)C(O)C(CO)O2)O)O1 MUPFEKGTMRGPLJ-UHFFFAOYSA-N 0.000 description 1
- 235000013334 alcoholic beverage Nutrition 0.000 description 1
- PNNNRSAQSRJVSB-BXKVDMCESA-N aldehydo-L-rhamnose Chemical compound C[C@H](O)[C@H](O)[C@@H](O)[C@@H](O)C=O PNNNRSAQSRJVSB-BXKVDMCESA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229960001230 asparagine Drugs 0.000 description 1
- 235000009582 asparagine Nutrition 0.000 description 1
- 235000020054 awamori 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
- 230000015572 biosynthetic process Effects 0.000 description 1
- QKSKPIVNLNLAAV-UHFFFAOYSA-N bis(2-chloroethyl) sulfide Chemical compound ClCCSCCCl QKSKPIVNLNLAAV-UHFFFAOYSA-N 0.000 description 1
- 235000013532 brandy Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 210000003495 flagella Anatomy 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 229960000367 inositol Drugs 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- -1 j-inositol Chemical compound 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000019713 millet Nutrition 0.000 description 1
- 235000010460 mustard Nutrition 0.000 description 1
- 239000006916 nutrient agar Substances 0.000 description 1
- 239000006877 oatmeal agar Substances 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000035479 physiological effects, processes and functions Effects 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- MUPFEKGTMRGPLJ-ZQSKZDJDSA-N raffinose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO[C@@H]2[C@@H]([C@@H](O)[C@@H](O)[C@@H](CO)O2)O)O1 MUPFEKGTMRGPLJ-ZQSKZDJDSA-N 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- OUYCCCASQSFEME-UHFFFAOYSA-N tyrosine Natural products OC(=O)C(N)CC1=CC=C(O)C=C1 OUYCCCASQSFEME-UHFFFAOYSA-N 0.000 description 1
- 235000015041 whisky Nutrition 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Fodder In General (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は排液の処理方法に関するものであり、更に詳細
には、焼酎の蒸留工程より排出される蒸留排液を処分す
るにあたり、その処分上の技術的な障害である蒸留排液
の菫ろ過性を改善するための、焼酎蒸留排液のろ過性改
善法に関するものである。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for treating waste liquid, and more specifically, a method for disposing of distillation waste liquid discharged from a shochu distillation process. The present invention relates to a method for improving the filtration performance of shochu distillation effluent in order to improve the violet filtration performance of distillation effluent, which is the technical obstacle mentioned above.
したがって本発明は、醸造工業のみならず、排水処理等
公害防止工業においても重用され、また、濾過分離され
た固形分は飼肥料としても有効利用されることから、本
発明は肥料工業や桐料工業においても重用されるもので
ある。Therefore, the present invention is useful not only in the brewing industry but also in the pollution prevention industry such as wastewater treatment, and since the solid content separated by filtration can be effectively used as feed fertilizer, the present invention is applicable to the fertilizer industry and the paulownia material industry. It is also used heavily in industry.
(従来の技術及び問題点)
焼酎の製造工程の中でも、蒸留工程は欠かすことのでき
ない重要な工程であるが、その際排出される蒸留残液に
ついては適切な処分方法が見出されておらず、その最大
の問題点としてこの蒸留排液のろ過性の悪さがあげられ
ている。たとえば、蒸留排液を活性汚泥処理法で処理す
る場合でも、BOD負荷率の高い固形分をあらかじめ除
く処理をしておけば効率的な活性汚染処理が可能となる
が。(Prior art and problems) Distillation is an indispensable and important step in the shochu manufacturing process, but no appropriate method has been found to dispose of the distillation residue discharged during this process. The biggest problem is the poor filterability of this distillation waste liquid. For example, even when distillation waste liquid is treated by an activated sludge treatment method, efficient active pollution treatment is possible if solids with a high BOD loading rate are removed in advance.
現在は、蒸留排液自身の難ろ過性ゆえに、このような処
分方法をとることはできない。また、焼酎製造業者の中
には、圧ろ圧搾型のいわゆる絞り機により蒸留排液の固
液分離をこころみている者もあるが、しかしこの方法で
ほろ材の目つまりが早い等の問題点が多く、工業的処理
には不適であり、実用上の困難に直面している。したが
って、焼酎蒸留排液は今のところ海洋投棄等の投棄処分
に頼らざるをえない現状であるが、このような投棄処分
による方法は環境保全上好ましい方法でないことは明ら
かであるし、法規制により禁止となる動きもある。この
ため、焼酎蒸留排液の適切なろ過性改善法を確立するこ
とが急務となっている。At present, such a disposal method is not possible due to the difficulty of filtering the distillation waste liquid itself. In addition, some shochu manufacturers are attempting to separate solid-liquid distillation waste using a so-called compressor, but this method has problems such as the guinea wood becoming clogged quickly. are unsuitable for industrial processing, and face practical difficulties. Therefore, currently we have no choice but to dispose of shochu distillation waste by dumping it into the ocean, etc. However, it is clear that such a method of disposal is not a preferable method in terms of environmental conservation, and laws and regulations There are also moves to ban it. Therefore, there is an urgent need to establish an appropriate method for improving the filterability of shochu distillation waste liquid.
(問題点を解決するための手段)
本発明はこのような当業界のニーズに応える目的でなさ
れたものであって、各方面から検討した結果、焼酎蒸留
廃液の薙濾過性の主原因が、廃液中の不溶性固形分、特
に細胞壁多糖類による濾材の目詰まりにあることを見出
した。(Means for Solving the Problems) The present invention was made to meet the needs of this industry, and as a result of examination from various aspects, it was found that the main cause of the filterability of shochu distillation waste liquid is: It was discovered that the filter media was clogged by insoluble solids in the wastewater, especially cell wall polysaccharides.
そこでこの細胞壁多糖類による濾材の目詰りを阻止ない
し軽減する方法であって、単に効率が高いだけでなく、
公害を発生することがなく、しかもマイルドな条件で実
施することができ、コストの低い工業的な方法を開発す
るに当って1本発明者らは微生物に着目した。Therefore, there is a method to prevent or reduce clogging of filter media caused by cell wall polysaccharides, and it is not only highly efficient, but also
In developing a low-cost industrial method that does not cause pollution and can be carried out under mild conditions, the present inventors focused on microorganisms.
そして、これら細胞壁多糖類の分解に関与し。It is also involved in the decomposition of these cell wall polysaccharides.
焼酎蒸留排液のろ過性を改善する酵素を生産する菌の検
索を行ったところ、ストレプトマイセス属に属する放線
菌−株(20−3−A株)が長崎県下の土壌から分離さ
れた。When searching for bacteria that produce an enzyme that improves the filterability of shochu distillation effluent, an actinomycete strain (strain 20-3-A) belonging to the genus Streptomyces was isolated from soil in Nagasaki Prefecture.
そこで本菌株を培養し、生産された多糖類分解系複合酵
素を焼酎蒸留排液に直接作用させたところ、蒸留排液に
よって酵素活性が阻害されることもなく、焼酎蒸留排液
のろ過性を著しく改善できることが判明した。Therefore, when this strain was cultured and the produced polysaccharide decomposition complex enzyme was applied directly to the shochu distillation waste water, the enzyme activity was not inhibited by the distillation waste water and the filterability of the shochu distillation waste water was improved. It turns out that it can be significantly improved.
この有用な新知見を基礎として更に研究を続けた結果1
本発明者らは長崎糸の付近の土壌より新たに分離したス
トレプトマイセスに属する放線菌2O−3−A株が焼酎
廃液の処理に有効であることをはじめて見いだした。As a result of further research based on this useful new knowledge 1
The present inventors discovered for the first time that the actinomycete strain 2O-3-A, which belongs to Streptomyces and was newly isolated from the soil near Nagasaki Ito, is effective in treating shochu waste liquid.
上記の放線菌2O−3−A株の形態、培養、生理におけ
る特徴は次のとおりである。The characteristics of the above-mentioned actinomycete strain 2O-3-A in terms of morphology, culture, and physiology are as follows.
1、形態
2O−3−A株は、一般に使用されている寒天培地で、
隔壁を有し、分岐する気中菌糸及び基生菌糸を形成する
。なお、基生菌糸の特徴的な分断はみられない、又、胞
子のう及び菌核の形成は見いだされない。1. Form 2O-3-A strain is a commonly used agar medium,
It has septa and forms branching aerial hyphae and basal hyphae. Note that no characteristic division of basal hyphae was observed, and no formation of sporangia or sclerotia was found.
胞子は気中菌糸より単純分枝した胞子柄に10個以上の
長い鎖状に形成され、その形態は直状又は僅かに屈曲状
である。成熟した胞子の大きさは0.5〜0.7μsX
1.0〜1.4μmであり、卵形又ハ柱状を示し、その
表面は平滑で鞭毛を持たない。Spores are formed in long chains of 10 or more on sporophores that are simply branched from aerial hyphae, and their morphology is straight or slightly curved. The size of mature spores is 0.5-0.7 μs
It is 1.0 to 1.4 μm, has an oval or columnar shape, and has a smooth surface without flagella.
■、各種培地上での生育状態
2O−3−A株は、一般に使用されている合成および天
然培地で普通もしくは旺盛な成育を示し、灰色の気中菌
糸を形成する。一方、基生菌糸は一般に薄黄色を示す、
可溶性色素は殆ど産生されない。(2) Growth status on various media The 2O-3-A strain shows normal or vigorous growth on commonly used synthetic and natural media, and forms gray aerial hyphae. On the other hand, basal hyphae generally exhibit a pale yellow color.
Very little soluble pigment is produced.
各種培地上での28℃、2週間培養した時の生育及び色
の特徴を下記に示す。なお、色の表示はC,olor
Harmony Manual(Container
Corporationof America)による
色の分類に従った。The characteristics of growth and color when cultured on various media at 28°C for 2 weeks are shown below. In addition, the color display is C, color
Harmony Manual (Container
The color classification according to the Corporation of America was followed.
1、グルコース・アスパラギン寒天培地生育、裏面の色
:普通、ライトアイポリ−(2ca)気中菌糸:普通、
ホワイト(a)−ナチュラル(3dc)可溶性色素:無
し
2、 グリセロール・アスパラギン寒天培−生育、裏面
の色:良好、ライトフィート(2aa)気中菌糸:豊富
、アッシュ(5fa)
可溶性色素:無し
3、 シュクロース・硝酸塩寒天培地
生育、裏面の色:普通、ライトアイポリ−(2ca)気
中菌糸:貧弱、ホワイト(a)
可溶性色素:無し
4、 スターチ・無機塩寒天培地
生育、裏面の色:良好、キャメル(3ie)気中菌糸:
豊富、ホワイト(a)−アッシュ(5fe)可溶性色素
:無し
5、チロシン寒天培地
生育、裏面の色:良好、ライトマスタードタン(2ie
)気中菌糸二豊富、ナチュラル(3dc)可溶性色素ニ
ブラウン
6、栄養寒天培地
生育、裏面の色:普通、ライトフィート(2ea)気中
菌糸:貧弱、ホワイト(a)
可溶性色素:無し
7、麦芽エキス・酵母エキス寒天培地
生育、裏面の色:良好、ライトフィート(2ea )気
中菌糸:豊富、ホワイト(a)
可溶性色素:無し
8、オートミール寒天培地
生育、裏面の色:良好、ライトアイポリ−(2ca)気
中菌糸:豊富、ホワイト(a)−アッシュ(5fs)可
溶性色素:無し
9、ペプトン・酵母・鉄寒天培地
生育、裏面の色:普通、ライトベージュ(3ec)気中
菌糸:無し
可溶性色素ニブラウン
■、生理的性質
2O−3−A株の生理的諸性質を以下に示す。温度は6
日間、その他は2週間後の結果を記述する。1. Growth on glucose-asparagine agar medium, back color: normal, light eye poly-(2ca) aerial mycelium: normal,
White (a) - Natural (3dc) Soluble pigment: None 2, Glycerol/Asparagine agar - Growth, back color: Good, Light feet (2aa) Aerial mycelium: Abundant, Ash (5fa) Soluble pigment: None 3, Growth on sucrose/nitrate agar medium, back color: normal, light eye poly-(2ca) aerial hyphae: poor, white (a), soluble pigment: none 4, growth on starch/inorganic salt agar medium, back color: good , camel (3ie) aerial mycelium:
Abundant, white (a) - ash (5fe) Soluble pigment: none 5, grown on tyrosine agar medium, back color: good, light mustard tan (2ie
) Aerial hyphae abundant, natural (3dc) soluble pigment nibrown 6, grown on nutrient agar medium, back color: normal, light foot (2ea) aerial hyphae: poor, white (a) soluble pigment: none 7, malt extract・Yeast extract agar medium growth, back color: good, light feet (2ea) aerial hyphae: abundant, white (a) soluble pigment: none 8, oatmeal agar medium growth, back color: good, light eye poly( 2ca) Aerial mycelium: Abundant, white (a) - ash (5fs) Soluble pigment: None 9, Peptone/yeast/iron agar medium growth, Underside color: Normal, light beige (3ec) Aerial mycelium: None Soluble pigment Physiological Properties The physiological properties of the 2O-3-A strain are shown below. The temperature is 6
For other cases, the results are described after 2 weeks.
(1)炭素源の利用性フ基礎培地としてプリドハム・ゴ
ツトリーブ無機培地(工SP9号)に、酵母エキス0.
1%を添加したものを使用した。(1) Utilization of carbon source - Pridham-Gottlieb inorganic medium (Engineering SP No. 9) was used as a basic medium with 0.0% yeast extract.
The one containing 1% was used.
2O−3−A株は、叶グルコース、D−キシロース、マ
ンニトール、フラクトース、L−ラムノース、L−アラ
ビノース、j−イノシトール及びシュクロースを資化す
るが、ラフィノースを資化しない。The 2O-3-A strain assimilates glucose, D-xylose, mannitol, fructose, L-rhamnose, L-arabinose, j-inositol, and sucrose, but does not assimilate raffinose.
(2)ゲラチンの液化作用:なし
く3)ミルクに対する作用:凝固、液化あり(4)澱粉
の加水分解作用:あり
(5)生育温度範囲:21℃〜34.5℃(6)チロシ
ナーゼの生成:あり
(7)メラノイド色素の生成:あり
■、細胞壁組成
全菌体加水分解によるジアミノピメリン酸の分析では、
LL−ジアミノピメリン酸のみが検出された。(2) Liquefaction of gelatin: None 3) Effect on milk: Coagulation and liquefaction (4) Hydrolysis of starch: Yes (5) Growth temperature range: 21°C to 34.5°C (6) Production of tyrosinase : Yes (7) Production of melanoid pigment: Yes ■, Cell wall composition Analysis of diaminopimelic acid by whole bacterial cell hydrolysis:
Only LL-diaminopimelic acid was detected.
以上気中菌糸上に形成される胞子鎖及びジアミノピメリ
ン酸の立体型などから、本菌株は放線菌の中でストレプ
トマイセス属に分類される。Based on the spore chains formed on the aerial hyphae and the steric type of diaminopimelic acid, this strain is classified as a member of the genus Streptomyces among actinomycetes.
ストレプトマイセス属における本菌株の種の同定にあた
って1本菌株の特徴であるの灰色系の気中菌糸、■直状
の胞子鎖、■平滑な胞子表面、■メラニン様色素の生成
、■可溶性色素の生成無し、■炭素源の利用性等を考慮
し、細菌学名承認リスト(Int、 J、 5yst、
Bacteriol、 30 : 225゜1980
))において承認され、又Int、 J、 5yst。In order to identify the species of this strain in the genus Streptomyces, the characteristics of this strain are: gray aerial hyphae, ■ straight spore chains, ■ smooth spore surface, ■ production of melanin-like pigment, and ■ soluble pigment. In consideration of the fact that no carbon is produced, ■ the availability of carbon sources, etc., an approved list of bacterial scientific names (Int, J, 5yst,
Bacteriol, 30: 225°1980
)) and also Int, J, 5yst.
Bactariol、誌に公表された既知菌株の中から
検索した結果、もっとも近縁の菌種として、ストレプト
マイセス・アンテバイオテッカ(Streptomyc
esantibioticus)及びストレプトマイセ
ス・ブシュウドベネズエラエ(Streptomyca
speudovanezuelaa)が挙げられる。し
かし、ウィリアム(S、 T、 Wiiliams)
らの数値分類(J、 Gen。As a result of searching among known bacterial strains published in the journal Bactariol, Streptomyces antebiotica was found to be the most closely related bacterial strain.
esantibioticus) and Streptomyces bushoud venezuelae (Streptomyca
speudovanezuelaa). However, William (S, T, Williams)
Numerical classification of et al. (J, Gen.
Microbiol、 129 : 1743−181
3.1983)では、この両種は異なるグループに属す
ると報告されている。Microbiol, 129: 1743-181
3.1983) reported that these two species belong to different groups.
従って、本菌株をストレプトマイセス・エスピー2O−
3−A (Streptomyces sp、 2O−
3−A)と命名し、工業技術院微生物工業技術研究所に
微工研菌寄第10690号として寄託した。Therefore, this strain was used as Streptomyces sp.
3-A (Streptomyces sp, 2O-
It was named 3-A) and deposited with the National Institute of Microbial Technology, Agency of Industrial Science and Technology as Microbiological Laboratories No. 10690.
本発明方法を実施するには、本菌株に係る多糖類分解系
複合酵素を、単離し又は単離することなく、使用して好
適条件下で酵素反応を行わせればよい6例えば1本菌株
を培養して得た多糖類分解系複合酵素を含有する培養物
及び/又はその処理物、例えば培養液上澄を、そのまま
又は必要に応じて濃縮、或は精製して焼酎蒸留排液に加
え、−定の条件下で酵素反応を行わせることにより、焼
酎蒸留排液のろ過性が著しく改善されるのである。To carry out the method of the present invention, the polysaccharide decomposition complex enzyme related to the present strain may be isolated or used without isolation, and the enzymatic reaction may be carried out under suitable conditions6. A culture containing a polysaccharide decomposition complex enzyme obtained by culturing and/or a processed product thereof, such as a culture liquid supernatant, is added to the shochu distillation waste liquid as it is or after being concentrated or purified as necessary, - By carrying out the enzymatic reaction under certain conditions, the filterability of the shochu distillation effluent is significantly improved.
工業的に処理するには、本菌株の培養物及び/又はその
処理物を排液に添加し、必要あればpHの調整を行った
後、攪拌しながら一定時間加温保持すればよい、その間
に目的とする酵素反応が進行し、特に多糖類が分解して
排液の物性が改善され、濾過性が大巾に向上するのであ
る。For industrial treatment, it is sufficient to add a culture of this strain and/or its treated product to the wastewater, adjust the pH if necessary, and then maintain the temperature while stirring for a certain period of time. The desired enzymatic reaction progresses, particularly polysaccharides are decomposed, the physical properties of the waste liquid are improved, and the filterability is greatly improved.
本発明において培養物とは、本菌株の菌体、菌体抽出物
、培養液、培養液濾液、上澄液、これらの混合物をいう
、また、その処理物とは、上記培養物の濃縮物、ペース
ト、乾燥物、希釈物のほか、精製及び/又は粗製の多糖
類分解系複合酵素自体、その含有物、その濃縮物、その
希釈物等を広く指す。In the present invention, the culture refers to the cells of the present strain, cell extract, culture solution, culture solution filtrate, supernatant, and mixtures thereof, and the processed product refers to the concentrate of the above-mentioned culture. , pastes, dried products, diluted products, as well as purified and/or crude polysaccharide decomposition complex enzymes themselves, their contents, their concentrates, their diluted products, etc.
つまり本発明における培養物及び/又はその処理物とは
5本菌株に係る多糖類分解系複合酵素自体のほか、該酵
素を含有するもの、該酵素を産生ずるものをすべて広範
に包含するものである。なお、本菌株を培養するに当っ
ては、処理対象排液及び/又はペクチンその他の植物細
胞壁多糖類を含む培地を用いて培養すると、本菌株によ
る多糖類分解系複合酵素の生産が促進される。In other words, the culture and/or its processed product in the present invention broadly includes not only the polysaccharide decomposition complex enzyme itself related to the five bacterial strains, but also those containing the enzyme and those that produce the enzyme. be. In addition, when culturing this strain, using a medium containing the wastewater to be treated and/or pectin and other plant cell wall polysaccharides will promote the production of polysaccharide degrading complex enzymes by this strain. .
このような酵素処理を行うことによって蒸留廃液の濾過
処理が容易となるため、BOD負荷率の高い固形分を予
じめ簡単に除くことができる。その結果、濾材の目詰り
等を生じることなく、濾液が容易に分離されるので、濾
液のみとなれば既知の廃水処理がいずれも自由に使用す
ることが可能となる。したがって例えば、この濾液を活
性汚泥処理法によっても充分に処理することができ、そ
の結果、全体として廃液の処理がきわめて効率よ〈実施
できるのである。また他方、この方法によれば、有害な
添加物を使用することなくしかも固液の分離がうまく行
えるため、固形分は回収して有用資源として再利用が可
能となり、この点でも本発明の波及効果は大きいものが
ある。By performing such an enzyme treatment, the filtration treatment of the distillation waste liquid becomes easy, so that solids with a high BOD loading rate can be easily removed in advance. As a result, the filtrate can be easily separated without clogging the filter medium, so that any known wastewater treatment can be used freely as long as the filtrate is left alone. Therefore, for example, this filtrate can be sufficiently treated by the activated sludge treatment method, and as a result, the waste liquid can be treated very efficiently as a whole. On the other hand, according to this method, solid-liquid separation can be performed successfully without using harmful additives, so the solid content can be recovered and reused as a useful resource. The effects are significant.
本発明は上記のように焼酎蒸留排液の処理にきわめて有
効に利用されるのであるが1本発明はこのような麦、米
、芋、ヒエ、アワ、人参等各種焼酎の蒸留排液のみなら
ず、他の酒類の蒸留排液にも有利に利用できる。他の蒸
留排液としては、例えば、ブランデー、ウィスキー、カ
ルバトス、ラム、泡盛その他各種の蒸留排液が広く使用
できるが、その場合、本菌株を目的とする蒸留排液を加
えた培地により培養することが好ましい。As mentioned above, the present invention can be used very effectively for the treatment of shochu distillation effluent; however, the present invention can be used only for the treatment of shochu distillation effluent such as barley, rice, potatoes, barnyard millet, millet, carrots, etc. In addition, it can also be advantageously used as distillation effluent from other alcoholic beverages. Other distillation effluents, such as brandy, whiskey, carbatos, rum, awamori, and various other distillation effluents, can be widely used, but in that case, the strain should be cultured in a medium to which the distillation effluent is added. It is preferable.
以下1本発明を実施例について更に詳しく説明する6
実施例−1゜
ストレプトマイセス・エスピー2O−3−Aを芋焼酎蒸
留排液を含む液体培地(pH5)に接種し、30℃で7
日間振どう培養したのち遠心分離をし、上澄液を採取し
た。この上澄液を、分画分子量10,000の限外ろ過
膜で30倍に濃縮処理し、多糖類分解系酵素を含む濃縮
粗酵素液を得た。この濃縮粗酵素液20社を芋焼酎蒸留
排液500mQに添加し、50℃で20時間攪拌したの
ち、ろ過圧力差500+mHgの下でろ過した結果、粗
酵素液を添加しなかった対照区に比し、ろ過速度が約3
倍向上した。The present invention will be described in more detail with reference to Examples 6. Example 1 Streptomyces sp.
After shaking culture for 1 day, centrifugation was performed and the supernatant was collected. This supernatant was concentrated 30 times using an ultrafiltration membrane with a molecular weight cutoff of 10,000 to obtain a concentrated crude enzyme solution containing polysaccharide decomposition enzymes. These 20 concentrated crude enzyme solutions were added to 500 mQ of potato shochu distillation waste liquid, stirred at 50°C for 20 hours, and then filtered under a filtration pressure difference of 500 + mHg. and the filtration rate is about 3
Improved twice.
実施例−2゜
ストレプトマイセス・エスピー2O−3−Aを、酵母エ
キス、ぶどう糖、及びペクチンその他の植物細胞壁多糖
類を含む液体培地(pH5)に接種し、30℃で7日間
振どう培養したのち培養物を遠心分離し多糖類分解系諸
酵素を含む上澄液を採取した。Example-2 Streptomyces sp. 2O-3-A was inoculated into a liquid medium (pH 5) containing yeast extract, glucose, pectin and other plant cell wall polysaccharides, and cultured with shaking at 30°C for 7 days. Thereafter, the culture was centrifuged and a supernatant containing polysaccharide degrading enzymes was collected.
次に、水で4倍に希釈した芋焼酎蒸留排液500m12
に上記の上澄液100m12を添加し、50℃で20時
間攪拌したのち、ろ過圧力差500+omHgの下でろ
過した結果、上澄液を添加しなかった対照区に比し、ろ
過速度が約5倍向上した。Next, 500ml of potato shochu distillation waste water diluted 4 times with water
100ml of the above supernatant liquid was added to the water, stirred at 50°C for 20 hours, and then filtered under a filtration pressure difference of 500+omHg. As a result, the filtration rate was about 5% compared to the control group to which no supernatant liquid was added. Improved twice.
実施例−3゜
実施例−2で得た多糖類分解系諸酵素を含む上澄液を、
分画分子量10,000の限外ろ過膜で30倍に濃縮処
理し濃縮粗酵素液とした6次に、この濃縮粗酵素液50
m12を麦焼酎蒸留排液500m12に添加し、50℃
で20時間攪拌したのち、ろ過圧力差500mmHgの
下でろ過した結果、粗酵素液を添加しなかった対照区に
比し、ろ過速度が約2倍向上した。Example-3゜The supernatant containing polysaccharide decomposition enzymes obtained in Example-2 was
Concentrate 30 times with an ultrafiltration membrane with a molecular weight cutoff of 10,000 to obtain a concentrated crude enzyme solution.6 Next, 50% of this concentrated crude enzyme solution
Add m12 to 500 m12 of barley shochu distillation waste liquid and heat to 50°C.
After stirring for 20 hours, filtration was performed under a filtration pressure difference of 500 mmHg. As a result, the filtration rate was approximately twice as high as in the control group in which no crude enzyme solution was added.
(発明の効果)
本発明によれば多糖類分解系酵素群及び/又はその含有
物を用いて蒸留廃液を処理するという非常にシンプルな
構成を採用することにより、従来濾過処理が困難であっ
た蒸留廃液の濾過処理が非常に容易に行えるという著効
が奏される。(Effects of the Invention) According to the present invention, by adopting a very simple configuration in which distillation waste liquid is treated using polysaccharide decomposition enzymes and/or their contents, filtration treatment was difficult in the past. The remarkable effect is that the filtration treatment of distillation waste liquid can be carried out very easily.
その結果、濾液と固形物とが工業的規模で且つ迅速に分
離される。As a result, filtrate and solids are rapidly separated on an industrial scale.
そして、このようにして分離された濾液は、固形物含量
もきねめで低いので、どのようなタイプの廃水処理技術
も適用することができ、例えば活性汚泥処理技術も充分
に利用することができる。Since the filtrate separated in this way has a very low solids content, any type of wastewater treatment technology can be applied, such as activated sludge treatment technology. .
したがって、前記酵素処理と上記した既知の廃水処理と
を結合すれば、従来きわめて困難であった蒸留廃液の処
理が簡単に且つ工業的規模で実施できることとなり、公
害防止上の効果もはかりしれないものがある。Therefore, if the enzyme treatment and the known wastewater treatment described above are combined, the treatment of distillation waste liquid, which has been extremely difficult in the past, can be easily carried out on an industrial scale, and the effect on pollution prevention will be immeasurable. There is.
また上記により分離された固形分は、有害な添加物や凝
集剤等を含んでいないために、これを回収して飼料や肥
料としても利用することができ、この点においても本発
明の効果には卓越したものがある。Furthermore, since the solid content separated in the above manner does not contain harmful additives or coagulants, it can be recovered and used as feed or fertilizer, and in this respect, the effects of the present invention are also enhanced. is outstanding.
代理人 弁理士 戸 1)親 男Agent Patent Attorney 1) Parent Male
Claims (1)
生産菌の培養物及び/又はその処理物を焼酎蒸留排液に
添加して、焼酎蒸留排液のろ過性を改善することを特徴
とする焼酎蒸留排液の処理法。Shochu distillation characterized by adding a culture of a polysaccharide-degrading complex enzyme-producing bacterium belonging to the genus Streptomyces and/or a treated product thereof to the shochu distillation effluent to improve the filterability of the shochu distillation effluent. How to treat wastewater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1132801A JPH03200A (en) | 1989-05-29 | 1989-05-29 | Treatment of waste liquid after production of shochu by distillation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1132801A JPH03200A (en) | 1989-05-29 | 1989-05-29 | Treatment of waste liquid after production of shochu by distillation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03200A true JPH03200A (en) | 1991-01-07 |
JPH0529519B2 JPH0529519B2 (en) | 1993-04-30 |
Family
ID=15089888
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1132801A Granted JPH03200A (en) | 1989-05-29 | 1989-05-29 | Treatment of waste liquid after production of shochu by distillation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03200A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000043489A1 (en) * | 1999-01-20 | 2000-07-27 | Takara Shuzo Co., Ltd. | Method and additive for reducing solid distillation residue |
EP1273561A4 (en) * | 2000-03-15 | 2005-01-26 | Japan Noble Systems Inc | Method and apparatus for producing organic fertilizer |
-
1989
- 1989-05-29 JP JP1132801A patent/JPH03200A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000043489A1 (en) * | 1999-01-20 | 2000-07-27 | Takara Shuzo Co., Ltd. | Method and additive for reducing solid distillation residue |
EP1273561A4 (en) * | 2000-03-15 | 2005-01-26 | Japan Noble Systems Inc | Method and apparatus for producing organic fertilizer |
Also Published As
Publication number | Publication date |
---|---|
JPH0529519B2 (en) | 1993-04-30 |
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