JP2592399B2 - Treatment method of liquor distillation waste liquid - Google Patents

Treatment method of liquor distillation waste liquid

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Publication number
JP2592399B2
JP2592399B2 JP5300764A JP30076493A JP2592399B2 JP 2592399 B2 JP2592399 B2 JP 2592399B2 JP 5300764 A JP5300764 A JP 5300764A JP 30076493 A JP30076493 A JP 30076493A JP 2592399 B2 JP2592399 B2 JP 2592399B2
Authority
JP
Japan
Prior art keywords
waste liquid
distillation waste
treatment
plant
liquid
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 - Lifetime
Application number
JP5300764A
Other languages
Japanese (ja)
Other versions
JPH07148497A (en
Inventor
孝之 小幡
修 秋田
治幸 家藤
仁 下飯
義知 長森
宣英 樋田
真治 瀬戸口
和則 高峯
雅徳 柏田
哲三 工藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MYAZAKIKEN
NIPPON SHUZO KUMIAI CHUOKAI
OOITAKEN
Kagoshima-Ken Kagoshima-Shi Kagoshima-Ken
Original Assignee
MYAZAKIKEN
NIPPON SHUZO KUMIAI CHUOKAI
OOITAKEN
Kagoshima-Ken Kagoshima-Shi Kagoshima-Ken
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Filing date
Publication date
Application filed by MYAZAKIKEN, NIPPON SHUZO KUMIAI CHUOKAI, OOITAKEN, Kagoshima-Ken Kagoshima-Shi Kagoshima-Ken filed Critical MYAZAKIKEN
Priority to JP5300764A priority Critical patent/JP2592399B2/en
Publication of JPH07148497A publication Critical patent/JPH07148497A/en
Application granted granted Critical
Publication of JP2592399B2 publication Critical patent/JP2592399B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • 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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、廃液の処理方法に関す
るものであり、更に詳細には、高濃度の有機物を含み、
かつ難ろ過性の蒸留廃液等の食品工場廃水を植物性繊維
あるいはそれを主成分とする混合物と酵母で処理をし
て、廃水中の固形分を凝集させ、これを回収除去するこ
とを特徴とする廃液の処理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating a waste liquid, and more particularly to a method for treating a waste liquid containing a high concentration of organic matter.
It is characterized by treating food factory wastewater such as distillation wastewater with poor filtration with vegetable fiber or a mixture containing it as a main component and yeast to aggregate solids in the wastewater and collect and remove this. The present invention relates to a method for treating waste liquid.

【0002】[0002]

【従来の技術】麦、米、ソバ等を原料とした焼酎蒸留廃
液は高濃度の固形分を含み、かつ粘度が高いために固液
分離が非常に困難となっている。そして一般に使用され
ているカチオン系化学凝集材、たとえばポリ塩化アルミ
ニウム、塩化第二鉄塩等とアニオン系化学凝集材を併用
しても、固液分離を容易にする程度までの凝集が見られ
ない。このために広く実施されている微生物を用いた浄
化処理へ進むことができない状態にある。従って、その
処理は海洋投棄、土壌還元、家畜飼料への混合といった
方法に依存してきた。
2. Description of the Related Art Shochu distillation liquor made from wheat, rice, buckwheat or the like contains a high concentration of solids and has a high viscosity, which makes solid-liquid separation extremely difficult. Even when a commonly used cationic chemical flocculant such as polyaluminum chloride or ferric chloride is used in combination with an anionic chemical flocculant, no flocculation to the extent of facilitating solid-liquid separation is observed. . For this reason, it is in a state where it is not possible to proceed to the purification treatment using microorganisms which is widely performed. Therefore, their treatment has relied on methods such as ocean dumping, soil reduction, and mixing with livestock feed.

【0003】しかし、これら廃液は約90%の水分を含
んでいるため、土壌還元には地下水汚染、飼料としては
水分が多すぎる等の問題点があって処理方法として限界
があり、海洋投棄については地球環境保全の上から今後
とも継続していけるとの見通しは立てがたい。
However, since these waste liquids contain about 90% of water, there are problems such as contamination of groundwater in soil reduction and too much water as feed, so that there is a limit as a treatment method. It is difficult to predict that we can continue from the viewpoint of global environmental protection.

【0004】[0004]

【発明が解決しようとする課題】酒類の蒸留廃液のよう
に高濃度の有機物とともに固形分を含む溶液を浄化処理
するには、まず固形分の除去が必須の前処理工程となっ
ているが、この前処理に関して実用的な方法はいまだ開
発されていない。そこで、本発明者らは、蒸留廃液等に
含まれる固形分を速やかに凝集させ、固液分離を容易に
実施できる方法の開発を課題とした。
In order to purify a solution containing solid matter together with high-concentration organic matter such as alcoholic liquor waste liquid, first, the removal of solid matter is an essential pretreatment step. No practical method has been developed for this pretreatment. Then, the present inventors made it a subject to develop the method which can coagulate the solid content contained in distillation waste liquid etc. quickly and can perform solid-liquid separation easily.

【0005】[0005]

【課題を解決するための手段】本発明は、上記目的を達
成するためになされたものであって、各方面から鋭意研
究を行った結果、固形分を除去する技術において、固形
分含量の高い蒸留廃液に更に植物繊維という固形分を添
加するという全く技術常識に逆行する処理を行い、更に
トリコスポロン属による微生物処理を併用したところ、
全く予期せざることに、高濃度廃液の固形分離がきわめ
て効率的に行われるという新規にしてきわめて有用な知
見を得た。
DISCLOSURE OF THE INVENTION The present invention has been made to achieve the above-mentioned object, and as a result of intensive studies from various fields, it has been found that the technique for removing solids has a high solids content. When a treatment contrary to the common technical knowledge of adding a solid content called plant fiber to the distillation waste liquid was further performed, and a microorganism treatment with Trichosporon was further used in combination,
Quite unexpectedly, a new and extremely useful finding was obtained that the solids separation of highly concentrated effluents is very efficient.

【0006】本発明は、このような新知見に基づきなさ
れたものであって、その基本的技術思想は、植物繊維ま
たは植物繊維を主成分とする混合物とともにトリコスポ
ロン属菌を、固形分を含む食品廃水に添加して速やかに
固形分を凝集させ、容易に固形分を分離除去する点であ
る。以下、本発明について詳しく説明する。
The present invention has been made on the basis of such new findings, and its basic technical idea is to use Trichosporon spp. Together with a plant fiber or a mixture containing a plant fiber as a main component, and a food containing solids. The point is that the solid content is added to the wastewater to quickly aggregate the solid content, and the solid content is easily separated and removed. Hereinafter, the present invention will be described in detail.

【0007】本発明においては、トリコスポロン属に属
する酵母を広く使用するものであるが、例えば本発明者
らが自然界から分離取得したトリコスポロン スピーシ
ーズM111株(Trichosporon sp.M
111)(FERM P−11960)が有利に使用で
きる。本菌は、分裂と出芽によって増殖する、真菌糸及
び分裂子を形成するが、子のう胞子を形成しないことか
ら、不完全菌類であるTrichosporon属酵母
と同定された。本菌は、グルコースの発酵性が微弱なが
ら認められ、培地から果実様の芳香が感じられた。本菌
は、pH3〜9、35℃まで生育し、至適pH及び温度
はそれぞれ5及び28℃であった。なお、ウレアーゼ、
DBB及びDNaseテストはいずれも陰性であった。
In the present invention, yeast belonging to the genus Trichosporon is widely used. For example, Trichosporon sp. M111 strain (Trichosporon sp. M) isolated and obtained from nature by the present inventors.
111) (FERM P-11960) can be used to advantage. This fungus forms a mycelium and spores but proliferates by division and budding, but does not form ascospores. Thus, the fungus was identified as a Trichosporon yeast, which is an incomplete fungus. In this bacterium, the fermentability of glucose was recognized although it was weak, and fruit-like aroma was felt from the medium. This bacterium grew to pH 3-9 and 35 ° C., and the optimum pH and temperature were 5 and 28 ° C., respectively. In addition, urease,
Both the DBB and DNase tests were negative.

【0008】トリコスポロン属酵母は、分離した菌体や
胞子のほか、ウェットケーキ、培養液、培養物、その濃
縮ないしペースト化物、希釈物等酵母含有物もすべて使
用することができ、また、廃液を処理した後に得られる
酵母含有物を少なくとも一部返送使用することも可能で
ある。
The yeast belonging to the genus Trichosporon can use not only isolated cells and spores, but also all yeast-containing materials such as wet cakes, culture solutions, cultures, concentrated or pasted products, and dilute products. It is also possible to return and use at least part of the yeast-containing material obtained after the treatment.

【0009】本発明においては、微生物処理に当り、処
理対象廃液に植物繊維及び/又はその含有物を添加して
おくことが必要である。その添加量は、使用する植物繊
維や処理対象廃液の種類等によって異なるが、廃液量に
対して乾燥固形分として少なくとも0.1%程度は必要
である。好適には0.1〜30%、更に好適には0.5
〜20%程度である。
In the present invention, it is necessary to add plant fibers and / or their contents to the waste liquid to be treated in the treatment of microorganisms. The amount of addition varies depending on the type of plant fiber used, the type of waste liquid to be treated, and the like, but at least about 0.1% of dry solid content relative to the amount of waste liquid is required. Preferably 0.1 to 30%, more preferably 0.5
About 20%.

【0010】植物繊維としては、KC−フロックW−5
0(武田薬品工業株式会社製品)といった植物繊維製
品;オカラ、バガス、ビート粕、ヌカ類、フスマ類、脱
穀粕、澱粉製造粕等の農産製造粕;クエン酸等有機酸発
酵粕、醤油粕、アルコール製造粕等の発酵粕;木材ない
し果実パルプ類;こ(れら)の工場の排水汚泥その他が
例示される。
[0010] As the plant fiber, KC-Floc W-5
0 (products of Takeda Pharmaceutical Co., Ltd.); okara, bagasse, beet lees, brassica, bran, threshing lees, starch production lees, and other agricultural production lees; citric acid and other organic acid fermented lees, soy sauce lees, Fermented lees such as alcohol-produced lees; wood or fruit pulp; drainage sludge from this plant, and the like.

【0011】上記のような植物繊維(その含有物)を蒸
留廃液に添加混合しておき、これにトリコスポロン属菌
(その培養物、含有物及び/又はその処理物)を接種し
てインキュベートすると、添加直後から固形物が凝集、
沈澱してくる。
[0011] The above-mentioned plant fiber (the content thereof) is added to the distillation waste liquid, mixed, and inoculated with Trichosporon spp. (The culture, the content and / or the processed product thereof) and incubated. Solid matter aggregates immediately after addition,
Settles.

【0012】このようにして固液分離して分離された液
状部は、汚染度が低い場合にはそのまま河川等に放流
し、それができない場合には、常用される廃液処理、例
えば活性汚泥や各種の微生物を用いる処理、物理的処
理、化学的処理又はこれらの結合によって処理すれば良
く、きわめて効率的に処理が行われる。
[0012] The liquid portion separated by solid-liquid separation in this way is discharged to a river or the like as it is when the degree of contamination is low. The treatment may be carried out using various microorganisms, physical treatment, chemical treatment or a combination thereof, and the treatment is carried out very efficiently.

【0013】他方、液体と分離された固形部は、そのま
ま、あるいは脱水してペースト状とし、あるいは更に乾
燥せしめて、飼料、肥料、土壌改良材、人工土壌等とし
て有効に利用することができるし、必要あれば植物繊維
として本発明において再利用することも可能である。ま
た、希望するのであれば、焼却したり、土壌還元したり
することも可能である。該固形部は安全性に間題がない
ため、この処理をしても二次公害をひき起すおそれはな
い。
On the other hand, the solid part separated from the liquid can be effectively used as feed, fertilizer, soil improving material, artificial soil, etc. as it is, or after dehydration to form a paste, or further drying. If necessary, it can be reused in the present invention as a plant fiber. If desired, it can be incinerated or returned to the soil. Since the solid portion has no problem in safety, there is no possibility of causing secondary pollution even if this treatment is performed.

【0014】以下、本発明の実施例について述べる。Hereinafter, embodiments of the present invention will be described.

【0015】[0015]

【実施例1】麦焼酎及びソバ焼酎の蒸留廃液それぞれ7
5mlに植物性繊維、菌体懸濁液の順に添加して、固液
分離のための濾過性の改善の評価を行った。植物性繊維
としてKC−フロックW−50(武田薬品工業株式会社
製品)を1.0g添加し攪拌後、Trichospor
on sp. M111(FERM P−11960)
(以下、M111と略称する)菌体懸濁液を最終濃度が
3×107cells/mlとなるよう添加し、総量1
00mlとした。
Example 1 Distilled waste liquid of wheat shochu and buckwheat shochu was 7 each
5 ml of the plant fiber and the bacterial cell suspension were added in this order, and the improvement of filterability for solid-liquid separation was evaluated. 1.0 g of KC-Floc W-50 (a product of Takeda Pharmaceutical Co., Ltd.) was added as a vegetable fiber, and after stirring, Trichospor was added.
on sp. M111 (FERM P-11960)
A cell suspension (hereinafter abbreviated as M111) was added to a final concentration of 3 × 10 7 cells / ml, and the total amount was 1 × 10 7 cells / ml.
00 ml.

【0016】(濾過条件)桐山ロートS−60(有限会
社 桐山製作所製品)(直径6cm)の底面にステンレ
ス製網(330mesh、45μm)を敷き、その上に
凝集させた廃液を注ぎ、500mmHgで吸引濾過し
た。試験は室温(20℃)で行い、所定時間に得られた
濾過液を測定して、その結果を図1及び図2に示した。
(Filtration conditions) A stainless steel net (330 mesh, 45 μm) is spread on the bottom of a Kiriyama funnel S-60 (product of Kiriyama Seisakusho) (diameter 6 cm), and the coagulated waste liquid is poured thereon, and suction is performed at 500 mmHg. Filtered. The test was performed at room temperature (20 ° C.), and the filtrate obtained during a predetermined time was measured, and the results are shown in FIGS. 1 and 2.

【0017】[0017]

【実施例2】麦焼酎蒸留廃液100gに所定量のクエン
酸発酵粕(タピオカと甘ショのデンプン粕の混合物にク
エン酸生産菌を培養してクエン酸を生産させ、抽出回収
した後に得られる残渣で、約80%の水分を含んでい
る)と5×108cells/mlのM111菌体溶液
10mlを加え、実施例1と同様の方法で濾過性改善の
評価を行った。試験は室温で行い、結果を図3に示し
た。
Example 2 A predetermined amount of citric acid fermented lees (a mixture of tapioca and sweet sho starch cultivated with citric acid-producing bacteria to produce citric acid in 100 g of barley shochu distillation effluent, and the residue obtained after extraction and recovery) , Containing about 80% of water) and 10 ml of 5 × 10 8 cells / ml M111 bacterial cell solution, and the improvement of filterability was evaluated in the same manner as in Example 1. The test was performed at room temperature, and the results are shown in FIG.

【0018】[0018]

【実施例3】クエン酸発酵粕添加処理における温度の影
響を調べる目的で、所定温度の麦焼酎蒸留廃液100g
にクエン酸粕10gと5×108cells/mlのM
111菌体溶液10mlを加え、実施例1の方法と同様
に濾過性の改善の評価を行い、結果を図4に示した。
Example 3 For the purpose of investigating the effect of temperature in the treatment of adding citric acid fermented cake, 100 g of a distilled liquor of barley shochu at a predetermined temperature was used.
10g of citric acid lees and 5 × 10 8 cells / ml of M
10 ml of the 111-cell solution was added, and the improvement of the filterability was evaluated in the same manner as in Example 1. The results are shown in FIG.

【0019】[0019]

【実施例4】麦焼酎蒸留廃液75mlに製紙工場の総合
排水脱水汚泥を1%添加し、3×108cells/m
lのM111菌体溶液10mlを加え、必要があれば水
を加えて、全量100mlとして、実施例1の方法と同
様に濾過性の改善の評価を行った。試験は室温で行い結
果を図5に示した。
[Example 4] 1% of the wastewater from a paper mill was added to 75 ml of a barley shochu distillation waste liquid, and 3 × 10 8 cells / m 3 were added.
1 ml of the M111 bacterial cell solution was added, and if necessary, water was added to make the total amount 100 ml, and the improvement of the filterability was evaluated in the same manner as in Example 1. The test was performed at room temperature and the results are shown in FIG.

【0020】[0020]

【実施例5】麦焼酎蒸留廃液75mlに醤油粕(水分2
5%)、乾燥オカラをそれぞれ乾物重で1%となるよう
添加し、3×108cells/mlのM111菌体溶
液10mlを加え、必要があれば水を加えて、全量10
0mlとして、実施例1の方法と同様に濾過性の改善の
評価を行った。試験は室温で行い結果を図6に示した。
Example 5 Soy sauce cake (moisture 2
5%) and dried okara were added so that the dry weight was 1%, and 10 ml of a 3 × 10 8 cells / ml M111 cell solution was added, and if necessary, water was added to make a total amount of 10%.
With the volume set to 0 ml, the improvement of the filterability was evaluated in the same manner as in Example 1. The test was performed at room temperature and the results are shown in FIG.

【0021】[0021]

【実施例6】米焼酎蒸留廃液75mlに所定量のクエン
酸発酵粕(実施例2で用いたもの)と5×108cel
ls/mlのM111菌体溶液10mlを加え、必要が
あれば水を加えて、全量100mlとして、実施例1の
方法と同様に濾過性の改善の評価を行った。試験は室温
で行い結果を図7に示した。
Example 6 A predetermined amount of citric acid fermented lees (used in Example 2) was added to 75 ml of rice shochu distillation waste liquid and 5 × 10 8 cells.
10 ml of the ls / ml M111 bacterial cell solution was added, and if necessary, water was added to make the total amount 100 ml, and evaluation of improvement in filterability was performed in the same manner as in Example 1. The test was performed at room temperature and the results are shown in FIG.

【0022】[0022]

【実施例7】ツインクロス式脱水機(図8に示す)を用
いて麦焼酎蒸留廃液の脱水試験を行った。M111株培
養液添加後の廃液菌濃度を2×107cells/m
l、脱水機へのフィード量500 liter/hr、
濾布走行速度1.0m/min、布巾50cmの条件で
処理した。
Example 7 A dehydration test of barley shochu distillation waste liquid was performed using a twin-cross type dehydrator (shown in FIG. 8). The concentration of the waste bacterium after addition of the culture solution of the M111 strain was 2 × 10 7 cells / m 2.
l, feed amount to the dehydrator 500 liter / hr,
The treatment was performed under the conditions of a filter cloth traveling speed of 1.0 m / min and a cloth width of 50 cm.

【0023】蒸留廃液、M111株及び下記表1に示す
植物繊維を混合回転ドラムで混合攪拌し、これを上濾布
及び下濾布の間を上記条件にて通過せしめ、濾液を分離
した。そして濾液を分離した後の固形分は脱水ケークと
して脱水機から回収した。得られた結果を下記表1に示
す。
The distillation waste liquid, the M111 strain, and the plant fibers shown in Table 1 below were mixed and stirred by a mixing rotary drum, and passed through an upper filter cloth and a lower filter cloth under the above conditions to separate the filtrate. The solid content after separating the filtrate was recovered from the dehydrator as a dehydrated cake. The results obtained are shown in Table 1 below.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【発明の効果】本発明によれば、植物繊維処理と微生物
処理とを併用するという全く新規な構成を採用すること
により、高濃度の固形分を含み、且つ粘度が高いために
固液分離が非常に困難であるため廃液処理がきわめて困
難な蒸留廃液等の廃液について、固液分離を単に可能に
しただけでなく、きわめて短時間にそれを可能にするこ
とにはじめて成功したものである。
According to the present invention, by adopting a completely novel structure in which plant fiber treatment and microbial treatment are used in combination, solid-liquid separation is contained due to high solid content and high viscosity. For waste liquids such as distillation waste liquids, which are extremely difficult to treat because they are very difficult, solid-liquid separation has not only been made possible but also made possible in a very short time.

【0026】その結果、麦、米、ソバ等を原料とした各
種焼酎蒸留廃液やアルコール製造廃液等の酒類蒸留廃液
といった高濃度の固形分を含み、且つ粘度の高い廃液を
きわめて短時間に効率的に固液分離することができ、従
来長時間を要していたこれらの廃液処理が短時間で可能
となった。
As a result, waste liquid having high concentration of solids and high viscosity, such as waste liquid of shochu distilled from various sources such as wheat, rice and buckwheat, and waste liquid of alcohol such as alcohol production waste liquid can be efficiently removed in a very short time. The solid-liquid separation can be performed in a short time, and the waste liquid treatment, which conventionally required a long time, can be performed in a short time.

【図面の簡単な説明】[Brief description of the drawings]

【図1】麦焼酎廃液のM111菌による凝集処理を示
す。
FIG. 1 shows a flocculation treatment of barley shochu waste liquid by M111 bacteria.

【図2】ソバ焼酎廃液のM111菌による凝集処理を示
す。
FIG. 2 shows coagulation treatment of buckwheat shochu waste liquid by M111 bacteria.

【図3】麦焼酎廃液のクエン酸発酵粕使用による(添加
量)凝集処理を示す。
FIG. 3 shows the coagulation treatment (addition amount) of barley shochu waste liquid by using citric acid fermented cake.

【図4】同じくクエン酸発酵粕使用による(温度)凝集
処理を示す。
FIG. 4 shows a (temperature) flocculation treatment also using citric acid fermented cake.

【図5】麦焼酎廃液の製紙工場脱水汚泥使用による凝集
処理を示す。
FIG. 5 shows coagulation treatment of barley shochu waste liquid by using dewatered sludge of a paper mill.

【図6】同じく食品工業副産物使用による凝集処理を示
す。
FIG. 6 shows a coagulation treatment using a food industry by-product.

【図7】米焼酎廃液のクエン酸発酵粕使用による凝集処
理を示す。
FIG. 7 shows the flocculation treatment of rice shochu waste liquid by using citric acid fermented cake.

【図8】ツインクロス式脱水機を用いる廃液の固液分
離、脱水システムを示す。
FIG. 8 shows a waste liquid solid-liquid separation and dehydration system using a twin-cross type dehydrator.

───────────────────────────────────────────────────── フロントページの続き (73)特許権者 391011700 宮崎県 宮崎県宮崎市橘通東2丁目10番1号 (72)発明者 小幡 孝之 東京都北区滝野川2丁目6番30号 国税 庁醸造試験所内 (72)発明者 秋田 修 東京都北区滝野川2丁目6番30号 国税 庁醸造試験所内 (72)発明者 家藤 治幸 東京都北区滝野川2丁目6番30号 国税 庁醸造試験所内 (72)発明者 下飯 仁 東京都北区滝野川2丁目6番30号 国税 庁醸造試験所内 (72)発明者 長森 義知 大分県大分市大字下群3239−4 大分県 工業試験場内 (72)発明者 樋田 宣英 大分県大分市大字下群3239−4 大分県 工業試験場内 (72)発明者 瀬戸口 真治 鹿児島県姶良郡隼人町小田1445−1 鹿 児島県工業技術センター内 (72)発明者 高峯 和則 鹿児島県姶良郡隼人町小田1445−1 鹿 児島県工業技術センター内 (72)発明者 柏田 雅徳 宮崎県宮崎市恒久1丁目7−14 宮崎県 食品加工研究開発センター内 (72)発明者 工藤 哲三 宮崎県宮崎市恒久1丁目7−14 宮崎県 食品加工研究開発センター内 (56)参考文献 特開 平4−271776(JP,A) ──────────────────────────────────────────────────続 き Continued on the front page (73) Patent holder 391011700 2-10-1 Tachibana-dori Higashi, Miyazaki City, Miyazaki Prefecture, Miyazaki Prefecture (72) Inventor Takayuki Obata 2-6-30 Takinogawa, Kita-ku, Tokyo National Tax Agency Brewing Test In-house (72) Inventor Osamu Akita 2-6-30 Takinogawa, Kita-ku, Tokyo National Tax Agency brewing laboratory (72) Inventor Haruyuki Ito 2-6-30 Takinogawa, Kita-ku, Tokyo National Tax Agency brewing laboratory (72 Inventor Jin Shimoi 2-6-30 Takinogawa, Kita-ku, Tokyo National Tax Agency Brewing Laboratory (72) Inventor Yoshitomo Nagamori 3239-4 Ogata, Oita-shi, Oita Pref. Oita Industrial Testing Laboratory (72) Inventor Hida 3239-4 Oita, Oita, Oita, Oita Pref.Industrial Research Laboratory (72) Inventor Shinji Setoguchi 145-1 Oda, Hayato-cho, Aira-gun, Kagoshima Pref. Kagoshima Prefectural Industrial Technology Center (72) Akita Kazunori Takamine 1445-1 Oda, Hayato-cho, Aira-gun, Kagoshima Prefecture Kagoshima Prefectural Industrial Technology Center Tetsuzo Kudo 1-7-14 Tsunehisa Tsunehisa, Miyazaki City, Miyazaki Prefecture Inside the Food Processing Research and Development Center, Miyazaki Prefecture (56) References JP-A-4-271776 (JP, A)

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 酒類蒸留廃液に、更に植物性繊維及び/
又はその含有物を0.1〜30%添加し、トリコスポロ
ン属酵母を用いて処理すること、を特徴とする酒類蒸留
廃液の処理方法。
1. The method according to claim 1, wherein the liquor distillation waste liquid further comprises vegetable fiber and / or
Alternatively, a method for treating a liquor distillation waste liquid, comprising adding 0.1 to 30% of the content thereof and treating with a Trichosporon yeast.
【請求項2】 トリコスポロン属酵母がトリコスポロ
ン スピーシーズM111(FERM P−1196
0)であることを特徴とする請求項1に記載の方法。
2. The yeast of the genus Trichosporon is Trichosporone species M111 (FERM P-1196).
The method of claim 1, wherein 0).
【請求項3】 酒類蒸留廃液が、麦、米、ソバ等を原料
とした焼酎蒸留廃液及び/又はアルコール蒸留廃液であ
ること、を特徴とする請求項1又は請求項2に記載の方
法。
3. The method according to claim 1, wherein the liquor distillation waste liquid is a shochu distillation waste liquid and / or an alcohol distillation waste liquid using wheat, rice, buckwheat or the like as a raw material.
【請求項4】 植物性繊維が、植物繊維製品、農産製造
粕、発酵粕、木材ないし果実パルプ、及び/又はこ(れ
ら)の工場の排水汚泥であること、を特徴とする請求項
1〜請求項3のいずれかに記載の方法。
4. The plant fiber according to claim 1, wherein the plant fiber is a plant fiber product, an agricultural production lees, a fermented lees, wood or fruit pulp, and / or a wastewater sludge from a plant of the plant. The method according to claim 3.
【請求項5】 請求項1〜請求項4のいずれかに記載の
方法で固液分離した後、液状部を更に微生物処理、物理
処理及び/又は化学処理すること、を特徴とする酒類蒸
留廃液の処理方法。
5. A liquor distillation waste liquid, wherein the liquid part is further subjected to a microorganism treatment, a physical treatment and / or a chemical treatment after solid-liquid separation by the method according to any one of claims 1 to 4. Processing method.
JP5300764A 1993-11-08 1993-11-08 Treatment method of liquor distillation waste liquid Expired - Lifetime JP2592399B2 (en)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5300764A JP2592399B2 (en) 1993-11-08 1993-11-08 Treatment method of liquor distillation waste liquid

Publications (2)

Publication Number Publication Date
JPH07148497A JPH07148497A (en) 1995-06-13
JP2592399B2 true JP2592399B2 (en) 1997-03-19

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ID=17888820

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Country Link
JP (1) JP2592399B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0732700B2 (en) * 1991-02-27 1995-04-12 国税庁長官 Aggregation method of vegetable fiber solids

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