JPH08267051A - Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom - Google Patents

Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom

Info

Publication number
JPH08267051A
JPH08267051A JP7078501A JP7850195A JPH08267051A JP H08267051 A JPH08267051 A JP H08267051A JP 7078501 A JP7078501 A JP 7078501A JP 7850195 A JP7850195 A JP 7850195A JP H08267051 A JPH08267051 A JP H08267051A
Authority
JP
Japan
Prior art keywords
rice
bran
washing
waste water
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.)
Pending
Application number
JP7078501A
Other languages
Japanese (ja)
Inventor
Shin Akamatsu
伸 赤松
Takuya Atari
卓也 當
Akira Nishimura
顕 西村
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.)
AZUMI FILTER PAPER
Azumi Filter Paper Co Ltd
Original Assignee
AZUMI FILTER PAPER
Azumi Filter Paper Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by AZUMI FILTER PAPER, Azumi Filter Paper Co Ltd filed Critical AZUMI FILTER PAPER
Priority to JP7078501A priority Critical patent/JPH08267051A/en
Publication of JPH08267051A publication Critical patent/JPH08267051A/en
Pending legal-status Critical Current

Links

Landscapes

  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE: To recover a bran-component which is reusable from waste water of rise washing and to efficiently purify the waste water of rice washing. CONSTITUTION: While flocs are formed by mixing a flocculating agent with the waste water of washing rice in a flocculating tank 1, the high-pressure water dissolved with air in a high concn. by pressurization in a fine air bubble forming device 2 is reduced in pressure and fine air bubbles are generated in a dissolving liquid to form fine air bubbles. These two liquids are mixed to adsorb the fine air bubbles in the flocs. The flocs are floated in a flotation vessel 3. Scum 30 formed by sepn. of solid from the liquid without modification is recovered. The release of the cleaned waste water is made possible.

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、日本酒醸造や無洗米製
造等に伴って発生する洗米作業の廃液、即ち洗米排水か
ら再利用可能な糠と呼ばれる米粉成分を回収するととも
に、洗米排水を浄化する洗米排水からの糠分回収方法及
びその実施に使用する糠分回収装置に関するものであ
る。
[Field of Industrial Application] The present invention collects a waste liquid of rice washing work, which is generated in association with sake brewing and non-washed rice production, that is, a rice powder component called reusable rice bran drainage, and purifies the rice wash drainage. The present invention relates to a method for recovering bran content from waste water of washing rice and a bran content recovery apparatus used for the implementation.

【0002】[0002]

【従来の技術】従来、洗米排水は、例えば図3に示され
る曝気槽40と沈澱槽50とから成る排水処理装置で浄化さ
れ、公共下水道等に放流されている。即ち、洗米作業場
からの洗米排水は、微生物混合培養体を活性汚泥として
保持している曝気槽40へ送られ、ここで、洗米排水中の
有機物は、活性汚泥中の微生物の食物連鎖反応により、
凝集、吸着、酸化分解され、減量されるとともに、沈澱
しやすい汚泥に変性される。続いて、曝気槽11で微生物
処理された排水は、沈澱槽50に送られ、ここで汚泥が沈
澱除去され、その後、浄化処理水として公共下水道等に
放流される。なお、沈澱した汚泥は、連続的もしくは定
期的に収集、脱水され、廃棄される。
2. Description of the Related Art Conventionally, waste water for washing rice has been purified by a waste water treatment apparatus comprising an aeration tank 40 and a sedimentation tank 50 shown in FIG. 3, and discharged to a public sewer or the like. That is, the rice washing wastewater from the rice washing workshop is sent to the aeration tank 40 which holds the microorganism mixed culture as activated sludge, where the organic matter in the rice washing wastewater is due to the food chain reaction of the microorganisms in the activated sludge,
It is coagulated, adsorbed, oxidatively decomposed, reduced in weight, and modified into sludge that easily precipitates. Subsequently, the wastewater treated with microorganisms in the aeration tank 11 is sent to a settling tank 50, where sludge is precipitated and removed, and then discharged to a public sewer or the like as purified treated water. The sludge that has settled is continuously or regularly collected, dehydrated, and discarded.

【0003】[0003]

【発明が解決しようとする課題】このように、上記の排
水処理装置は、洗米排水の浄化のみを目的とし、本来利
用可能な洗米排水中の糠分を回収し、再利用することは
行われていなかった。このため、有用な資源が無駄に廃
棄されていた。
As described above, the above wastewater treatment device is intended only for purifying the wastewater for washing rice, and the originally usable bran in the wastewater for washing rice is recovered and reused. Didn't. Therefore, useful resources were wasted.

【0004】また、この排水処理装置は、微生物の食物
連鎖といった生物反応を利用しているため、浄化処理に
時間を要するとともに、処理装置が大型となり広大な設
置スペースを要するという問題があった。
Further, since this wastewater treatment equipment utilizes biological reaction such as food chain of microorganisms, there is a problem that the purification treatment requires a long time and the treatment equipment becomes large and requires a vast installation space.

【0005】さらには、装置の維持のため微生物の生存
に必要な量の有機物を定期的に補給しなければならない
という煩わしさもあった。
Furthermore, in order to maintain the apparatus, it is troublesome that the amount of organic matter necessary for the survival of the microorganisms has to be periodically replenished.

【0006】本発明は、上記従来技術の問題点を解消
し、洗米排水から再利用可能な糠分を回収するととも
に、洗米排水を効率よく浄化できる洗米排水からの糠分
回収方法及び糠分回収装置を提供することを目的とす
る。
[0006] The present invention solves the above-mentioned problems of the prior art, recovers reusable bran content from rice rinsing wastewater, and efficiently recovers the rice rinsing wastewater from the rice rinsing wastewater and recovers the bran content. The purpose is to provide a device.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明の糠分回収方法は、洗米排水に凝集剤を混
合して凝集物を生成する工程と、加圧による高濃度空気
溶解液を減圧し、溶解液中に微細な気泡を発生させる工
程と、凝集物が生成された洗米排水と微細な気泡が発生
した溶解液を混合し、凝集物を浮上させて固液分離させ
る工程と、浮上した凝集物を回収する工程とを含むこと
を特徴としている。また、本発明の糠分回収装置は、洗
米排水に凝集剤を混合して凝集物を生成する凝集槽と、
加圧による高濃度空気溶解液を減圧し、溶解液中に微細
な気泡を発生させる微細気泡液生成装置と、凝集槽及び
微細気泡液生成装置から供給される2液の混合液から、
凝集物を浮上させて固液分離する浮上分離槽とを具備す
ることを特徴としている。凝集剤としては、キトサンが
好ましい。
In order to solve the above problems, the method for collecting bran fraction of the present invention comprises a step of mixing an aggregating agent with waste water of washing rice to produce an agglomerate, and a high concentration air by pressurization. The process of decompressing the solution to generate fine bubbles in the solution, mixing the washing water from which the agglomerate was generated with the solution in which the fine bubbles were generated, and floating the agglomerates for solid-liquid separation It is characterized by including a step and a step of collecting the floated aggregate. Further, the bran fraction recovery device of the present invention, a coagulation tank that mixes a flocculant in the rice rinsing wastewater to generate coagulates,
From the mixture of two liquids supplied from the fine bubble liquid generator that decompresses the high-concentration air dissolved liquid by pressurization to generate fine bubbles in the dissolved liquid, and the aggregation tank and the fine bubble liquid generator,
The present invention is characterized by comprising a flotation separation tank that floats aggregates to perform solid-liquid separation. Chitosan is preferable as the aggregating agent.

【0008】[0008]

【作用】微細な気泡が発生している溶解液と凝集物が凝
集している洗米排水を混合すると、凝集物に気泡が吸着
する。このため、凝集物には浮力が作用するので、浮上
分離層内で凝集物が浮上して固液分離が行われる。即
ち、浮上分離層内の混合液の表層部に凝集物が集められ
る。このため、凝集物の回収が容易に行える。しかも、
この固液分離によれば、生物反応を起こして凝集物中の
糠分が変成することもない。従って、糠分を利用可能な
状態で回収することができる。このため、有機肥料や生
分解性・生崩壊性プラスチックなどの原料として利用で
きる。また、固液分離された排水は自動的に清浄化され
る。従って、そのまま公共下水等に放流しても環境問題
を引き起こすことがない。また、凝集剤として、キトサ
ンを用いると、キトサンは食用可能であるため、回収さ
れた糠分は、食器などの高い安全性が要求される生分解
性・生崩壊性プラスチックの原料や飼料、和菓子などの
食品原料などに利用が可能となる。さらに、キトサンの
機能食品性を活用し、付加価値の高い健康食品原料とし
て使用することもできる。
[Function] When the solution containing fine bubbles is mixed with the rice washing water in which the aggregates are aggregated, the bubbles are adsorbed to the aggregates. Therefore, since buoyancy acts on the aggregate, the aggregate floats in the floating separation layer and solid-liquid separation is performed. That is, aggregates are collected in the surface layer portion of the mixed liquid in the floating separation layer. Therefore, the aggregates can be easily collected. Moreover,
According to this solid-liquid separation, there is no possibility that the bran fraction in the agglomerate is denatured due to a biological reaction. Therefore, the bran can be collected in a usable state. Therefore, it can be used as a raw material for organic fertilizers and biodegradable / biodegradable plastics. In addition, the wastewater that has been solid-liquid separated is automatically cleaned. Therefore, it will not cause environmental problems even if it is directly discharged to public sewers. When chitosan is used as the coagulant, chitosan is edible, so the collected bran is a raw material for biodegradable / biodegradable plastics such as tableware, feed, and Japanese sweets. It can be used for food materials such as. Furthermore, by utilizing the functional food properties of chitosan, it can also be used as a high value-added health food material.

【0009】[0009]

【実施例】本発明の実施例を図面に基づいて説明する。
図1は、本発明方法の実施に使用する糠分回収装置の一
実施例を示す模式的正面図である。この糠分回収装置
は、凝集槽1、微細気泡液生成装置2及び浮上分離槽3
を備えている。
An embodiment of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic front view showing an example of a bran fraction collecting apparatus used for carrying out the method of the present invention. This bran content recovery device includes a flocculation tank 1, a fine bubble liquid generation device 2 and a floating separation tank 3.
It has.

【0010】凝集槽1には、攪拌装置10が配設されてい
る。凝集槽1の底面には洗米排水送給用の配管11の一端
が接続されている。配管11の他端は2液混合用の配管20
の途中に接続されている。配管20の一端は微細気泡液生
成装置2に接続され、他端は浮上分離槽3の底面に接続
されている。また、浮上分離槽3は配管31を介して公共
下水等に接続されている。なお、各配管の途中には、流
量制御用のバルブが設けられている。
A stirring device 10 is arranged in the flocculation tank 1. To the bottom surface of the flocculation tank 1 is connected one end of a pipe 11 for feeding and washing rice drainage. The other end of the pipe 11 is the pipe 20 for mixing two liquids.
Connected in the middle of. One end of the pipe 20 is connected to the fine bubble liquid generation device 2, and the other end is connected to the bottom surface of the floating separation tank 3. The floating separation tank 3 is connected to public sewage or the like via a pipe 31. A valve for controlling the flow rate is provided in the middle of each pipe.

【0011】次に、各部の処理を説明する。洗米作業現
場から流出する廃液、即ち洗米排水は、凝集槽1に流入
し、攪拌装置10により流入量に応じて投入される凝集剤
と攪拌混合される。凝集剤としては、例えばキトサンが
用いられる。洗米排水中に浮遊物質(以下、SSと示
す。)として存在する糠分は、この操作により凝集し、
フロック(凝集物)を形成する。
Next, the processing of each unit will be described. The waste liquid flowing out from the rice washing work site, that is, the rice washing waste water, flows into the flocculation tank 1 and is agitated and mixed by the agitation device 10 with the aggregating agent charged according to the inflow amount. As the coagulant, for example, chitosan is used. The bran components present as suspended matter (hereinafter referred to as SS) in the rice rinsing waste water are aggregated by this operation,
Form flocs.

【0012】微細気泡液生成装置2においては、空気を
混入した水を加圧ポンプで加圧し、水中に高濃度で空気
を溶解させ、この高濃度空気溶解高圧水を減圧すること
により液中に微細な気泡が発生し、微細気泡液となる。
上記の微細気泡液生成装置2としては、他に、例えば特
開平5-317847号公報や特開平6-285344号公報等に示され
るような装置を用いることができる。
In the fine bubble liquid generator 2, water containing air is pressurized by a pressure pump to dissolve air in water at a high concentration, and the high-concentration air-dissolved high-pressure water is decompressed into the liquid. Fine bubbles are generated and become fine bubble liquid.
As the above-mentioned fine bubble liquid generation device 2, other devices such as those disclosed in, for example, JP-A-5-317847 and JP-A-6-285344 can be used.

【0013】フロックが形成された洗米排水には、微細
気泡液生成装置2からの微細気泡液が配管20内で混合さ
れる。これにより、洗米排水中のフロックに気泡が吸着
し、浮上分離槽3内に流入する。浮上分離槽3内では、
気泡の浮力によってフロックが浮上し、液中から分離し
て、液面にスカム(固液分離された凝集物)30を形成す
る。このスカム30は、スクレーバー等により容易に回収
でき、糠分として再利用が可能となる。
In the pipe 20, the fine bubble liquid from the fine bubble liquid generating device 2 is mixed with the rice rinsing wastewater in which the flocs are formed. As a result, air bubbles are adsorbed on the flocs in the waste water after washing and flow into the flotation separation tank 3. In the flotation tank 3,
The flocs are floated by the buoyancy of the bubbles and separated from the liquid to form scum (aggregate solid-liquid separated) 30 on the liquid surface. The scum 30 can be easily collected by a scraper or the like and can be reused as bran.

【0014】次に、上記の糠分回収装置を使用して洗米
排水中の糠分を回収した実施結果について説明する。な
お、処理される原水としては、日本酒醸造工程中で生ず
る洗米排水(SS濃度900ppm)を使用した。その
他、処理の条件は次のとおりである。実施例A 原 水 量 :5リットル 凝 集 剤 :な し 凝集剤濃度(原水比): − 原水/気泡液 混合比:1/1実施例B 原 水 量 :5リットル 凝 集 剤 :硫酸バンド(1%水溶液として
使用) 凝集剤濃度(原水比):30ppm 原水/気泡液 混合比:1/2実施例C 原 水 量 :5リットル 凝 集 剤 :キトサン(キトサン0.1%,
酢酸0.2%の水溶液として使用) 凝集剤濃度(原水比):30ppm 原水/気泡液 混合比:1/2実施例D 原 水 量 :5リットル 凝 集 剤 :キトサン(キトサン0.1
%,酢酸0.2%の水溶液として使用) アルギン酸 凝集剤濃度(原水比):20ppm 20ppm 原水/気泡液 混合比:1/2
Next, a description will be given of the results of the implementation of collecting the bran content in the waste water of washing rice by using the above-mentioned bran content recovery device. As the raw water to be treated, rice washing wastewater (SS concentration 900 ppm) generated in the sake brewing process was used. In addition, the processing conditions are as follows. Example A Raw water amount: 5 liters Coagulant: None Coagulant concentration (raw water ratio):-Raw water / bubble liquid mixing ratio: 1/1 Example B Raw water amount: 5 liters Coagulant: Sulfate band ( Flocculant concentration (raw water ratio): 30 ppm Raw water / bubble liquid mixing ratio: 1/2 Example C Raw water amount: 5 liters Coagulant: chitosan (chitosan 0.1%,
Used as an aqueous solution of 0.2% acetic acid) Flocculant concentration (raw water ratio): 30 ppm Raw water / bubble liquid mixing ratio: 1/2 Example D Raw water amount: 5 liter Coagulant: chitosan (chitosan 0.1
%, Used as an aqueous solution of 0.2% acetic acid) Alginic acid Flocculant concentration (raw water ratio): 20 ppm 20 ppm Raw water / bubble liquid mixing ratio: 1/2

【0015】上記の処理条件により、それぞれ以下に示
す値の糠分を回収できた。 実施例A:0.2g 実施例B:3.2g 実施例C:4.2g 実施例D:4.2g
Under the above-mentioned processing conditions, the bran content having the values shown below could be collected. Example A: 0.2 g Example B: 3.2 g Example C: 4.2 g Example D: 4.2 g

【0016】上記の実施例B、C、Dの実施結果より、
本発明によれば、従来回収できなかった糠分を効率よく
回収できることがわかる。
From the results of the above-mentioned Examples B, C and D,
According to the present invention, it can be seen that the bran content, which could not be collected conventionally, can be collected efficiently.

【0017】また、洗米排水に凝集剤を混合しない実施
例Aの場合は、糠分の回収量が0.2gであるのに対
し、凝集剤を混合する実施例Bの場合は、3.2gとな
っており、回収量が16倍になっている。同様に、実施
例C、Dの場合の回収量は共に4.2gであり、実施例
Aの場合の21倍になっている。このように、凝集剤を
洗米排水に混合して凝集物を生成し、この凝集物に気泡
を吸着して浮上させることにより固液分離を行う本発明
方法によれば、洗米排水中の糠分の回収率を格段に向上
できることがわかる。
Further, in the case of Example A in which the coagulant is not mixed with the rice rinsing waste water, the recovered amount of bran is 0.2 g, whereas in the case of Example B in which the coagulant is mixed, 3.2 g is obtained. And the recovery amount is 16 times. Similarly, the recovery amount in each of Examples C and D is 4.2 g, which is 21 times that in Example A. In this way, according to the method of the present invention in which the coagulant is mixed with the rice sewage wastewater to form an agglomerate, and the agglomerates are adsorbed by air bubbles to cause solid-liquid separation, the bran content in the rice sewage wastewater is increased. It can be seen that the recovery rate of can be significantly improved.

【0018】図2は、上記の処理による洗米排水のSS
濃度の変化を示す。図中点線は、制約なしに公共下水に
放流できる一般排水上限値であり、実施例C及び実施例
Dではこの値以下に、実施例Bでもこの値に近いレベル
まで、洗米排水を浄化できることがわかる。
FIG. 2 shows the SS of the rice sewage discharged by the above treatment.
The change in concentration is shown. The dotted line in the figure is the upper limit value of general wastewater that can be discharged into public sewage without restriction, and it is possible to purify the rice washing wastewater to below this value in Example C and Example D and to a level close to this value in Example B as well. Recognize.

【0019】実施例C及び実施例Dにおいて使用してい
る酢酸は、キトサンを水溶化する作用を有する。また、
実施例Dは、キトサンの凝集作用を調整するアルギン酸
(フロックの大きさを制御する。)の使用が、本発明の
作用の妨げにならず、凝集作用の調整が必要な他の洗米
排水への対応が可能であることを示したものである。
The acetic acid used in Examples C and D has the effect of solubilizing chitosan. Also,
Example D shows that the use of alginic acid (which controls the size of flocs) to regulate the flocculating action of chitosan does not interfere with the action of the present invention, and to other rice washing effluents requiring adjustment of the flocculating action. This shows that it is possible to cope.

【0020】ここで、キトサンは食用可能な凝集剤であ
り、酢酸及びアルギン酸は食用可能な凝集補助剤であ
る。また、キトサン及びアルギン酸は健康食品等に添加
されている。そこで、実施例C及び実施例Dによる回収
糠分を少量試食したところ、口中刺激もなく、身体的異
常も発生しないことが確認できた。従って、このような
凝集剤及び凝集補助剤を使用すると、回収糠分を高い安
全性が要求される生分解性・生崩壊性プラスチックの原
料や飼料、食品原料、さらに付加価値の高い健康食品原
料として利用することが可能になる。
Here, chitosan is an edible flocculant, and acetic acid and alginic acid are edible flocculants. Further, chitosan and alginic acid are added to health foods and the like. Then, when a small amount of the collected bran in Example C and Example D was sampled, it was confirmed that there was no oral irritation and no physical abnormality occurred. Therefore, when such flocculants and coagulant aids are used, the recovered bran is required to be highly safe, as raw materials for biodegradable / biodegradable plastics, feeds, food ingredients, and health food ingredients with high added value. Can be used as.

【0021】[0021]

【発明の効果】以上述べたように、本発明によれば、従
来利用されていなかった洗米排水中の糠分を回収し、例
えば有機肥料に再利用することができる。特に、凝集剤
として、キトサンを使用すると、食器等の高い安全性が
要求される生分解性・生崩壊性プラスチックの原料や飼
料、和菓子等の食品原料に利用することが可能になる。
さらには、キトサンの機能食品性を活用し、付加価値の
高い健康食品原料として使用することもできる。しか
も、本発明では、物理化学的に処理して洗米排水中の糠
分を回収するものであるため、生物反応を利用するもの
に比べて、処理時間を格段に短縮できる。また、微生物
を定期的に補給するといった煩わしさもない。さらに
は、洗米排水を長時間滞留させる曝気槽や沈澱層を必要
としないので、装置構成が小型で済むという利点もあ
る。
As described above, according to the present invention, it is possible to recover the bran content in the waste water for washing rice, which has not been used conventionally, and reuse it for organic fertilizer, for example. In particular, when chitosan is used as the coagulant, it can be used as a raw material for biodegradable / biodegradable plastics that require high safety for tableware and the like, and as a raw material for foods such as feed and Japanese sweets.
Furthermore, by utilizing the functional food properties of chitosan, it can also be used as a high value-added health food raw material. Moreover, in the present invention, since the bran content in the rice rinsing wastewater is recovered by physicochemical treatment, the treatment time can be markedly shortened as compared with the one utilizing a biological reaction. Moreover, there is no need to bother with the regular supply of microorganisms. Furthermore, since there is no need for an aeration tank or a settling layer for retaining the waste water for washing rice for a long time, there is an advantage that the device configuration can be small.

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

【図1】本発明方法の実施に使用される糠分回収装置の
一実施例を示す模式的正面図である。
FIG. 1 is a schematic front view showing an example of a bran fraction recovery device used for carrying out the method of the present invention.

【図2】洗米排水のSS濃度の変化例を示すグラフであ
る。
FIG. 2 is a graph showing an example of changes in the SS concentration of rice washing wastewater.

【図3】洗米排水処理装置の従来例を示す模式的正面図
である。
FIG. 3 is a schematic front view showing a conventional example of a rice washing wastewater treatment device.

【符号の説明】[Explanation of symbols]

1 凝集槽 2 微細気泡液生成装置 3 浮上分離槽 20 2液混合用の配管 30 スカム 1 Coagulation tank 2 Micro bubble liquid generator 3 Floating separation tank 20 2 Liquid mixing pipe 30 Scum

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 9/00 502 C02F 9/00 502P 502Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C02F 9/00 502 C02F 9/00 502P 502Z

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 洗米排水に凝集剤を混合して凝集物を生
成する工程と、 加圧による高濃度空気溶解液を減圧し、溶解液中に微細
な気泡を発生させる工程と、 凝集物が生成された洗米排水と微細な気泡が発生した溶
解液を混合し、凝集物を浮上させて固液分離させる工程
と、 浮上した凝集物30を回収する工程とを含むことを特徴と
する洗米排水からの糠分回収方法。
1. A step of mixing an aggregating agent with the washing rice effluent to form an agglomerate; a step of depressurizing a high-concentration air-dissolved solution by pressurization to generate fine bubbles in the solution; A rice washing wastewater characterized by including a step of mixing the generated washing rice drainage and a solution in which fine air bubbles are generated, floating the aggregates to perform solid-liquid separation, and a step of collecting the floated aggregates 30. Bran recovery method from.
【請求項2】 凝集剤としてキトサンを用いる請求項1
記載の洗米排水からの糠分回収方法。
2. A chitosan is used as a flocculant.
The method for collecting bran from the drained rice water.
【請求項3】 洗米排水に凝集剤を混合して凝集物を生
成する凝集槽1と、 加圧による高濃度空気溶解液を減圧し、溶解液中に微細
な気泡を発生させる微細気泡液生成装置2と、 凝集槽1及び微細気泡液生成装置2から供給される2液
の混合液から、凝集物を浮上させて固液分離する浮上分
離槽3とを具備することを特徴とする糠分回収装置。
3. A flocculation tank 1 for producing a flocculate by mixing a flocculant in the washed rice sewage, and depressurizing a high-concentration air-dissolved solution by pressurization to generate fine bubble liquid in the solution. A bran fraction comprising an apparatus 2 and a flotation separation tank 3 that floats an aggregate and separates it into solid and liquid from a mixed liquid of two liquids supplied from the flocculation tank 1 and the fine bubble liquid generation apparatus 2. Recovery device.
【請求項4】 凝集剤としてキトサンを用いる請求項3
記載の糠分回収装置。
4. Chitosan is used as the flocculant.
The bran recovery device described.
JP7078501A 1995-04-04 1995-04-04 Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom Pending JPH08267051A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7078501A JPH08267051A (en) 1995-04-04 1995-04-04 Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7078501A JPH08267051A (en) 1995-04-04 1995-04-04 Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom

Publications (1)

Publication Number Publication Date
JPH08267051A true JPH08267051A (en) 1996-10-15

Family

ID=13663714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7078501A Pending JPH08267051A (en) 1995-04-04 1995-04-04 Method for recovering bran component from waste water of rice washing and device for recovering bran component therefrom

Country Status (1)

Country Link
JP (1) JPH08267051A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008126168A (en) * 2006-11-22 2008-06-05 Fuji Eng Kk Coagulating sedimentation method of waste water
JP2010029756A (en) * 2008-07-25 2010-02-12 Kameda Seika Co Ltd Method for subjecting rice washing drainage to solid-liquid separation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008126168A (en) * 2006-11-22 2008-06-05 Fuji Eng Kk Coagulating sedimentation method of waste water
JP2010029756A (en) * 2008-07-25 2010-02-12 Kameda Seika Co Ltd Method for subjecting rice washing drainage to solid-liquid separation

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