JPS60150884A - Method for recovering valuable material from organic waste liquid - Google Patents

Method for recovering valuable material from organic waste liquid

Info

Publication number
JPS60150884A
JPS60150884A JP684984A JP684984A JPS60150884A JP S60150884 A JPS60150884 A JP S60150884A JP 684984 A JP684984 A JP 684984A JP 684984 A JP684984 A JP 684984A JP S60150884 A JPS60150884 A JP S60150884A
Authority
JP
Japan
Prior art keywords
waste liquid
organic
organic waste
acid
bioreactor
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
JP684984A
Other languages
Japanese (ja)
Inventor
Yasuo Kuwamoto
桑元 康雄
Tadaaki Kawasugi
河杉 忠昭
Haruki Morikawa
森川 治記
Akio Toriyama
明夫 鳥山
Eisuke Hakubun
栢分 英助
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP684984A priority Critical patent/JPS60150884A/en
Publication of JPS60150884A publication Critical patent/JPS60150884A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the time and equipment, and to treat practically the organic waste liquid by acid-fermenting the organic waste liquid in a bioreactor, and recovering organic acids with membrane separation. CONSTITUTION:The high-concn. organic waste liquid such as the waste liquid from food is supplied into an immobilized bioreactor 2 from a supply passage 1, and the organic acids such as acetic acid, propionic acid, and butyric acid are formed in the bioreactor 2 from the organic materials in the waste liquid with the acid fermentation by bacteria immobilized on a carrier. The liquid is then sent through a pipeline 3 equipped with a pump into a membrane separator 4 wherein the organic acids are recovered, and the recovered organic acids are sent to a recovery passage 5. The membrane separation is sufficiently carried out, and the organic acids are recovered.

Description

【発明の詳細な説明】 本発明は、何+1に廃液から有価物全回収する方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention primarily relates to a method for recovering all valuable materials from waste liquid.

従来、有機廃液をバイオリアクターで酸発酵させた後メ
タン発酵槽に供給し、廃液中の有機酸のほぼ全量をメタ
ン菌に工り有価物としてのメタンガスに変えていたが、
メタン発酵に極めて長時間會要すると共に広大な敷地?
要する欠点があった。
Conventionally, organic waste liquid was subjected to acid fermentation in a bioreactor and then supplied to a methane fermentation tank, and almost all of the organic acid in the waste liquid was converted into methane bacteria and converted into methane gas as a valuable product.
Does methane fermentation take an extremely long time and a vast area?
There were some drawbacks.

本第1発明の目的は、有価物回収に要する時間及び敷地
全従来に比して大巾に少くできるようにする点にある。
An object of the first invention is to greatly reduce the time and site required for collecting valuables compared to the conventional method.

本第1発明による有機廃液からの有価物回収方法の特徴
手段は、バイオリアクターで酸発酵させた有機廃液から
、膜分離によって有機酸を回収することにあり、数十日
間を要していたメタン発酵に代えて、有機酸をそのまま
有価物として膜分離にエリ回収すると、グルj時間程度
で処理できるようになった。
The characteristic means of the method for recovering valuables from organic waste liquid according to the first invention is that organic acids are recovered by membrane separation from the organic waste liquid that has been subjected to acid fermentation in a bioreactor. Instead of fermentation, organic acids can be recovered as valuable substances through membrane separation, making it possible to process them in about 1 hour.

その結果、有機廃液処理に要する時間及び敷地を大巾に
少くでき、地価高騰の都市部等の敷地確保面で問題を生
じやすい地域においても、実用的に有機廃液処理を行え
るようになった。
As a result, the time and site required for organic waste liquid treatment can be greatly reduced, and organic waste liquid treatment can now be practically carried out even in areas where land prices tend to be difficult to secure, such as in urban areas where land prices are soaring.

本第2発明の目的は、本第1発明による有機廃液からの
有価物回収方法に改良を加えて、有価物の回収効率を一
層同上できるようにする点にある。
An object of the second invention is to improve the method for recovering valuables from organic waste liquid according to the first invention, so that the efficiency of recovering valuables can be further improved.

本第2発明による有機廃液からの荷価物回収方法の特徴
手段は、バイオリアクターで酸発酵させた有機廃液から
、膜分離によって有機酸を回収し、膜分離処理後の有機
廃液を前記バイオリアクターに循環供給することにあり
、その作用効果は次の通りである。
The characteristic means of the method for recovering cargo from organic waste liquid according to the second aspect of the present invention is to recover organic acid by membrane separation from the organic waste liquid acid-fermented in a bioreactor, and to transfer the organic waste liquid after the membrane separation treatment to the bioreactor. Its functions and effects are as follows.

つ捷り、膜分離による有機酸回収によって処理に要する
時間及び敷地を大中に少くできる上に、膜分離における
有機酸回収を、膜分離処理後の有機廃液のバイオリアク
ターへの循環供給VcJ:t)9gJ率良く行えるので
ある。 さらに詳述すると、膜分離において、有機、廃
液の有機酸濃度がある程度低下すると、時間当りの有機
酸の膜透過量が極めて少くなり、7回の膜分離処理で有
機酸を十分に回収するためには膜分離処理に長時間を要
する。 しかし、膜分離処理後の何機廃液をバイオリア
クターに循環供給すtl、ば、未分解の有機物が分解さ
れ、有機酸濃度が高い状態で常に膜分離を行えると共に
、未回収の有機酸を再度膜分離処理して回収でき、した
がって、膜分離を極めて能率良く、かつ、有機酸回収を
十分に行えるのである。
In addition to reducing the time and site required for treatment by collecting organic acids through thinning and membrane separation, organic acid recovery during membrane separation can also be used to circulate and supply organic waste liquid to the bioreactor after membrane separation treatment VcJ: t) It can be done at a high rate of 9gJ. More specifically, in membrane separation, when the organic acid concentration of the organic waste liquid decreases to a certain extent, the amount of organic acid that permeates through the membrane per hour becomes extremely small, and it is necessary to sufficiently recover the organic acid with seven membrane separation treatments. The membrane separation process takes a long time. However, if the waste liquid after membrane separation treatment is circulated and supplied to the bioreactor, undecomposed organic matter is decomposed and membrane separation can be performed at all times with a high concentration of organic acids, and unrecovered organic acids can be recycled again. It can be recovered by membrane separation treatment, and therefore membrane separation can be extremely efficient and organic acids can be recovered sufficiently.

次に、図面にエリ実施例を示す。Next, an embodiment is shown in the drawings.

食料廃液、その他の高濃度有機廃eを、供給路(1)か
ら固定化バイオリアクター(2)に供ML、バイオリア
クター(2)において、担体に固定させた函体による酸
発酵で、廃液中の有機物から酢酸、プロピオン酸、酪酸
等の有機酸を生成させる。
Food waste liquid and other high-concentration organic waste e are supplied from the supply path (1) to the immobilization bioreactor (2). Organic acids such as acetic acid, propionic acid, and butyric acid are produced from organic matter.

バイオリアクター(2)で酸発酵させた有機廃液を、ポ
ンプ付管路(3)で膜分離装置(4)に供給し、膜分離
装置(4)において、逆浸透膜やイオン交換膜等の分離
膜(4@)による(図は逆浸透膜の場合)有機酸選択透
過作用で有機酸を回収し、その有機酸を回収路(5)に
送る。
The organic waste liquid subjected to acid fermentation in the bioreactor (2) is supplied to the membrane separation device (4) through a pipe with a pump (3), and in the membrane separation device (4), it is separated using a reverse osmosis membrane, an ion exchange membrane, etc. The organic acid is recovered by the organic acid selective permeation effect by the membrane (4@) (the diagram shows the case of a reverse osmosis membrane), and the organic acid is sent to the recovery channel (5).

膜分離処理した何機廃液の大部分を循環路(6)でバイ
オリアクター(2)に供給し、残NSを排出路(7)で
廃液処理設備(8)に送る。
Most of the membrane-separated waste liquid is supplied to the bioreactor (2) through the circulation path (6), and the remaining NS is sent to the waste liquid treatment equipment (8) through the discharge path (7).

次に、別の実施例を説明する。Next, another example will be described.

本第1発明の場合、膜分離装置(4)からの有機廃液の
全量を廃液処理設備(8)に送る。
In the case of the first invention, the entire amount of organic waste liquid from the membrane separation device (4) is sent to the waste liquid treatment facility (8).

本¥J1及び第2発明の場合、有機廃液から有機酸全回
収するに、有機廃液から抽出液に有機酸を抽出した後、
抽出液に対する膜分離で有機酸を回収する間接方式を利
用しても工い。
In the case of this J1 and the second invention, in order to completely recover the organic acid from the organic waste liquid, after extracting the organic acid from the organic waste liquid into an extract liquid,
An indirect method of recovering organic acids through membrane separation of the extract can also be used.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明方法全例示する70−シートである。 代理人 弁理士 北 村 修 第1頁の続き ■発明者鳥山 防去 [相]発明者栢分 英助 大阪市浪速区敷津東1丁目2番47号 久保田鉄工株式
会社内 内
The drawing is a 70-sheet illustrating the entire method of the invention. Agent Patent Attorney Osamu Kitamura Continuation of page 1 ■Inventor Toriyama Inventor Toriyama Eisuke 1-2-47 Shikitsu Higashi, Naniwa-ku, Osaka Inside Kubota Tekko Co., Ltd.

Claims (1)

【特許請求の範囲】 ■ バイオリアクターで酸発酵させた有機廃液から、膜
分離によって有機酸を回収する有機廃液からの有価物回
収方法。 ■ バイオリアクターで酸発酵させた有機廃液から、膜
分離に1って有機酸を回収し、膜分離処理後の有機廃液
を前記パイオリアククーに循環供給する有機廃液からの
有価物回収方法。
[Scope of Claims] ■ A method for recovering valuables from organic waste liquid, which recovers organic acids by membrane separation from organic waste liquid subjected to acid fermentation in a bioreactor. (2) A method for recovering valuables from an organic waste solution, which involves recovering an organic acid from an organic waste solution subjected to acid fermentation in a bioreactor through membrane separation, and circulating and supplying the organic waste solution after the membrane separation treatment to the bioreactor.
JP684984A 1984-01-17 1984-01-17 Method for recovering valuable material from organic waste liquid Pending JPS60150884A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP684984A JPS60150884A (en) 1984-01-17 1984-01-17 Method for recovering valuable material from organic waste liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP684984A JPS60150884A (en) 1984-01-17 1984-01-17 Method for recovering valuable material from organic waste liquid

Publications (1)

Publication Number Publication Date
JPS60150884A true JPS60150884A (en) 1985-08-08

Family

ID=11649683

Family Applications (1)

Application Number Title Priority Date Filing Date
JP684984A Pending JPS60150884A (en) 1984-01-17 1984-01-17 Method for recovering valuable material from organic waste liquid

Country Status (1)

Country Link
JP (1) JPS60150884A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998041478A1 (en) * 1997-03-14 1998-09-24 E.I. Du Pont De Nemours And Company Treatment of effluent streams containing organic acids
KR100471963B1 (en) * 2001-08-29 2005-02-21 이원바이오텍주식회사 Method for Manufacturing Anaerobic Fermentation Broth from Organic Wastes for Using in Nutrient Removal

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998041478A1 (en) * 1997-03-14 1998-09-24 E.I. Du Pont De Nemours And Company Treatment of effluent streams containing organic acids
KR100471963B1 (en) * 2001-08-29 2005-02-21 이원바이오텍주식회사 Method for Manufacturing Anaerobic Fermentation Broth from Organic Wastes for Using in Nutrient Removal

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