JPS60150885A - Method for recovering valuable material from organic waste liquid - Google Patents
Method for recovering valuable material from organic waste liquidInfo
- Publication number
- JPS60150885A JPS60150885A JP59008191A JP819184A JPS60150885A JP S60150885 A JPS60150885 A JP S60150885A JP 59008191 A JP59008191 A JP 59008191A JP 819184 A JP819184 A JP 819184A JP S60150885 A JPS60150885 A JP S60150885A
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- organic
- acid
- organic waste
- flow passage
- 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
Links
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
本発明け、有機廃液から有価物を回収する方法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recovering valuable materials from organic waste liquid.
従来、有機廃液をバイオリアクターにおいて嫌気雰囲気
で酸発酵させた後、メタン発酵−[程で、廃液中の有機
酸のほぼ全量をメタン菌により有価物としてのメタンガ
スに変えていたが、酸発酵及びメタン発酵に極めて長時
間を嬰すると共に広大な敷地を要する欠点があった。Conventionally, organic waste liquid was subjected to acid fermentation in an anaerobic atmosphere in a bioreactor, and then almost all of the organic acid in the waste liquid was converted into methane gas as a valuable product by methane bacteria. The drawbacks were that methane fermentation took an extremely long time and required a vast area.
本発明の目的は、有価物回収に要する時間及び敷地を従
来に比して大巾に少くできるように、かつ、動力面でも
有利vc%理できるようにする点にある。An object of the present invention is to make it possible to greatly reduce the time and site required for collecting valuables compared to the conventional method, and to make it possible to manage the amount of time and space advantageously in terms of power.
本発明による有機廃液からの有価物回収方法)4I&手
段は、有機廃液のバイオリアクターによる酸発酵を、高
液圧下で酸素含有ガスを供給しながら行い、酸発酵させ
た有機廃液中の有機酸を、選択性透過膜によって、かつ
、その暎に前記バイオリアクター内の高液圧を付与しな
がら回収することにあり、その作用効果は次の通シであ
る。Method for recovering valuables from organic waste liquid according to the present invention) 4I & means performs acid fermentation of organic waste liquid in a bioreactor under high liquid pressure while supplying oxygen-containing gas, and collects organic acids in the acid-fermented organic waste liquid. The purpose is to recover the liquid using a selectively permeable membrane and applying high liquid pressure inside the bioreactor, and its effects are as follows.
つまり、従来嫌気性雰囲気でないと行えないと考えられ
ていた菌体による酸発酵を、各種実験の結果、好気性雰
囲気でも十分に、むしろ嫌気性雰囲気よりも活発に行え
ることを見出したのである。 そこで、バイオリアクタ
ーを探検酸素濃度を十分高くして、酸発酵を行わせるこ
とによって、酸発酵能力を大巾に向上できた。In other words, as a result of various experiments, it was discovered that acid fermentation by bacterial cells, which was previously thought to be possible only in an anaerobic atmosphere, can be carried out satisfactorily in an aerobic atmosphere, and in fact more actively than in an anaerobic atmosphere. Therefore, by exploring the bioreactor and increasing the oxygen concentration sufficiently to carry out acid fermentation, we were able to greatly improve the acid fermentation capacity.
その上、数十日間を翳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喚分離により回収すると、
4〜5時間程度で処理できるようになった。Furthermore, instead of methane fermentation, which takes several tens of days, organic acids can be recovered as valuable products through dialysis separation.
Now it can be processed in about 4 to 5 hours.
その結果、全体として、有機廃液匙理Vc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
酸回収を行えるようVCなった。As a result, the time and site required to process organic waste liquid can be greatly reduced, making organic acid recovery practical even in areas where land prices tend to be difficult to secure, such as in urban areas where land prices are soaring. I became a VC.
さらには、嘆分離に要する加圧力を、酸発酵全効率良く
するだめのバイオリアクターの高液圧を有効利用して得
ることによって、前方効率をも向上でき、ランニングコ
スト面で有利に処理を行えるようになった。Furthermore, by effectively utilizing the high hydraulic pressure of the bioreactor, which increases the overall efficiency of acid fermentation, to obtain the pressurizing force required for separation, forward efficiency can also be improved, making the process advantageous in terms of running costs. It became so.
次に、第1図により実施例を示す。Next, an example will be shown with reference to FIG.
水処理等により発生する各種汚泥、熱処理した汚泥から
の脱離液、食品廃液、その他の高濃度有機廃液を、供給
路fl+から探検式/(イオリアクク−(2)に供給し
、バイオリアクター(2)において、下降流路(2a)
、上昇流路(2b)、ポンプ流路(2c)の順に有機廃
液を循環させ、空気等の酸素含有ガスをプロワ−181
及びノズル(2d )Kより下降流路(2a)に吹込み
、高液圧下で酸素含有ガスを供給しながら菌体によって
有機廃液を酸発酵させて、廃液中の有機物から酢酸、プ
ロピオン酸、醋酸等の有機酸を生成させる。Various types of sludge generated from water treatment, etc., desorbed liquid from heat-treated sludge, food waste liquid, and other high-concentration organic waste liquids are supplied from the supply path fl+ to the exploration type / ), in the descending flow path (2a)
, the ascending flow path (2b), and the pump flow path (2c) in this order, and oxygen-containing gas such as air is passed through the blower 181.
Then, the organic waste liquid is blown into the descending flow path (2a) from the nozzle (2d) K, and the organic waste liquid is acid-fermented by the bacterial cells while supplying oxygen-containing gas under high liquid pressure, and acetic acid, propionic acid, and acetic acid are extracted from the organic matter in the waste liquid. generates organic acids such as
バイオリアクター(2)で酸発酵させた有機廃液を、バ
イオリアクター(2)の底部側に付設した第1膜分離装
置(3)に供給し、第1嘆分離装置(3)において、逆
浸透III(!3a)による有機酸選択透過作用で、か
つ、その透過に要する加圧力をバイオリアクター(2)
内の高液圧によって付与して、有機酸を回収する。The organic waste liquid subjected to acid fermentation in the bioreactor (2) is supplied to the first membrane separation device (3) attached to the bottom side of the bioreactor (2), and in the first membrane separation device (3), it is subjected to reverse osmosis III. The organic acid selective permeation effect by (!3a) and the pressurizing force required for its permeation are applied to the bioreactor (2).
The organic acid is recovered by applying high liquid pressure within the tank.
回収した有機酸を第2嘆分離装置+4)VC送り、第2
模分離装置(4)で有機酸を二種類に暎分離し、低分子
の有機酸を第1回収路(611/C,かつ、高分子の有
機酸を¥J2回収F@f15) l’l:送る。The recovered organic acid is sent to the second separator +4) VC, and the second
The organic acid is separated into two types using the simulated separation device (4), and the low-molecular organic acid is collected in the first recovery path (611/C, and the high-molecular organic acid is recovered at ¥J2 F@f15). :send.
第1竪分離装置(3)からの有機廃水を水処理設備i7
1 VC送る。The organic wastewater from the first vertical separator (3) is collected in the water treatment facility i7.
1 Send VC.
次に、別の実施例を説明する。Next, another example will be described.
バイオリアクター(2)において高液圧を得るに、第2
図に示すように、バイオリアクター(2)ヲ攪拌機(8
)付密閉槽に形成しておいて、有機廃液をポンプ「ンで
かつ酸素含有ガスをコンプレッサーfc)で加圧供給し
、排ガスを絞り弁■)付排気路(9)から排出し、バイ
オリアクター(2)内のiFEを高く維持してもよい。To obtain high fluid pressure in the bioreactor (2), the second
As shown in the figure, the bioreactor (2) is equipped with a stirrer (8).
), the organic waste liquid is supplied with a pump and oxygen-containing gas is supplied under pressure with a compressor fc), and the exhaust gas is discharged from an exhaust passage (9) with a throttle valve (), and the bioreactor is The iFE in (2) may be kept high.
第1図は本発明の実施例を示す70−シート、第2図は
、本発明の別実施例を示す70−シートである。
代理人 弁理士 」ヒ 村 條FIG. 1 shows a 70-sheet showing an embodiment of the invention, and FIG. 2 shows a 70-sheet showing another embodiment of the invention. Agent Patent Attorney: Jo Himura
Claims (1)
で酸素含有ガスを供給しながら行い、酸発酵させた有機
廃液中の有機酸を、選択性透過膜によって、かつ、その
膜に前記バイオリアクター内の高液圧を付与しながら回
収する有機廃液からの有価物回収方決。Acid fermentation of the organic waste liquid is carried out in a pipe reactor under high hydraulic pressure while supplying oxygen-containing gas, and the organic acids in the acid-fermented organic waste liquid are passed through a selectively permeable membrane, and the organic acid in the organic waste liquid is transferred to the membrane through a selective permeable membrane. A method for recovering valuables from organic waste liquid while applying high liquid pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59008191A JPS60150885A (en) | 1984-01-18 | 1984-01-18 | Method for recovering valuable material from organic waste liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59008191A JPS60150885A (en) | 1984-01-18 | 1984-01-18 | Method for recovering valuable material from organic waste liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60150885A true JPS60150885A (en) | 1985-08-08 |
Family
ID=11686391
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59008191A Pending JPS60150885A (en) | 1984-01-18 | 1984-01-18 | Method for recovering valuable material from organic waste liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60150885A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1317207C (en) * | 2003-10-21 | 2007-05-23 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
-
1984
- 1984-01-18 JP JP59008191A patent/JPS60150885A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1317207C (en) * | 2003-10-21 | 2007-05-23 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
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