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JPS5874192A - Treatment for waste of processed marine products - Google Patents

Treatment for waste of processed marine products

Info

Publication number
JPS5874192A
JPS5874192A JP56172404A JP17240481A JPS5874192A JP S5874192 A JPS5874192 A JP S5874192A JP 56172404 A JP56172404 A JP 56172404A JP 17240481 A JP17240481 A JP 17240481A JP S5874192 A JPS5874192 A JP S5874192A
Authority
JP
Japan
Prior art keywords
treatment
digesting
tank
produced
mixture
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
JP56172404A
Other languages
Japanese (ja)
Inventor
Hirohide Kinoshita
木下 浩秀
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.)
OOSHINOTSU SHOKUHIN KOGYO KK
Original Assignee
OOSHINOTSU SHOKUHIN KOGYO KK
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 OOSHINOTSU SHOKUHIN KOGYO KK filed Critical OOSHINOTSU SHOKUHIN KOGYO KK
Priority to JP56172404A priority Critical patent/JPS5874192A/en
Publication of JPS5874192A publication Critical patent/JPS5874192A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To prevent the generation of malodors and to obtain dry bacterial fertilizers by subjecting a mixture of the blood juice produced in the stage of cooking raw material fishes in processing of marine products and the floating froth produced in treatment of waste liquid to anaerobic treatments thereby generating gaseous methane. CONSTITUTION:The mixture (a) of the blood juice produced in the stage of cooking of raw material fishes stored temporarily in a receiving tank 1 and the floating froth produced in treatment of waste liquid is transferred into the hesinetically closed 1st digesting tank 2, and is further transferred into the 2nd digesting tank 3. In the respective digesting tanks, the mixture is anaerobically digested. If in this case, the anaerobic digesting treatment is performed by maintaining the respective digesting tanks at 30-40 deg.C, org. materials are decomposed and digested in the tanks 2, 3 and digesting gases contg. 60-70% gaseous methane which is an essential component are produced. The desorbing liquid discharged from the upper part of the tank 3 is fed to an activaged sludge aerating tank 8, where the liquid is subjected to a biological oxidation treatment. The excess sludge thereof is dried under reduced pressure in a dryer 9 and is made into dry bacterial fertilizers 10.

Description

【発明の詳細な説明】 この発明は水産加工廃物の処理方法に関し、更に詳しく
は、公害防止と省エネルギーの点で極めて有効な処理方
法忙関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating marine product processing waste, and more specifically to a treatment method that is extremely effective in terms of pollution prevention and energy conservation.

従来、水産かん詰等の加工工場に於ては、原料魚の調理
工程で生じる血汁や、廃液処理で生じる浮上フロス等の
廃物は、有効な処理方法がなかったため、議縮処理を行
なうか又は廃棄処理参ていた。しかしながら、淡縮処理
の場合は、昨今の重油価格の高騰により処理費用がかさ
む一方であり、又廃棄処理の場合は、悪臭公害の原因と
なるなど、種々の問題があった。
Conventionally, in processing plants such as seafood canning, there was no effective treatment method for waste such as blood juice generated during the cooking process of raw fish and floating floss generated from waste liquid treatment, so they either carried out condensation treatment or I was in the process of disposing of it. However, in the case of thinning treatment, the treatment cost continues to increase due to the recent rise in the price of heavy oil, and in the case of disposal treatment, there are various problems such as causing foul odor and pollution.

ところで、これまで下水汚泥処理、a取りし尿処理、畜
産糞尿処理に於ては、燃料として使用できるメタンガス
を発生させるメタン醗酵処理方法が実用化されているが
、前述の浮上フロス等の水産加工廃物の処理の場合は、
油脂分を多量に含むものであるため、そのようなメタン
醗酵処理が困難と考えられていた。しかしながら、水産
加工廃物をメタン醗酵処理によって充分に分解しメタン
ガスを発生させることが出来るならば、省エネルギーや
悪臭公害防止の点でこれほど望ましいことはない0 この発明は、上記事情に鑑みてなされたもので、水産加
工の原料魚調理工程で生じる血汁と、廃液処理で生じる
浮上クロスとの混合物を嫌気性消化処理することKより
メタンガス化を可能とし、もって省エネルギーと悪臭公
害防止を図ると共K。
By the way, methane fermentation treatment methods that generate methane gas that can be used as fuel have been put to practical use in the treatment of sewage sludge, human waste, and livestock manure. In the case of processing,
Since it contains a large amount of oil and fat, it was thought that such methane fermentation treatment would be difficult. However, if marine product processing waste could be sufficiently decomposed by methane fermentation treatment to generate methane gas, it would be more desirable in terms of energy saving and prevention of odor pollution.This invention was made in view of the above circumstances. By anaerobically digesting the mixture of blood juice produced during the raw material fish cooking process and floating cloth produced during waste liquid treatment, it is possible to convert the mixture into methane gas, thereby saving energy and preventing odor pollution. K.

曳質の乾燥函体肥料も得られるよう忙したものである0
       ゛ 以下を望ましい一実施例を示す第1図を参照しなから、
この発明の処理方法を詳細に説明する。
I've been busy trying to get some dry boxed fertilizer.
``With reference to FIG. 1, which shows a preferred embodiment,
The processing method of this invention will be explained in detail.

第1図に於て、lは受槽であり、血汁と浮上70スは最
初この受槽l中に一時的Kfi合貯留されるO 血汁は、前述のように、原料魚調理工程で生じる廃物で
あって、原料魚から取り出された内臓が多量に含まれて
いる0又、浮上フロスは、水産加工廃液処理に於て、粗
大固形物と粗油を分離した廃液を更に加圧浮上分離装置
で処理するときに浮上してくるもので、微細固形物と油
脂分とよりなるものである。
In Fig. 1, l is a receiving tank, and the blood juice and floating liquid are initially temporarily combined and stored in this receiving tank l.As mentioned above, the blood juice is a waste product generated in the raw fish cooking process. Floating floss, which contains a large amount of internal organs extracted from raw fish, is used in the treatment of waste liquid from seafood processing to separate waste liquid from coarse solids and crude oil into a pressurized flotation separator. It comes to the surface during processing and consists of fine solids and fats and oils.

このように、受槽l中に一時的に混合貯部された血汁と
浮上フロスの混合物aは、次に密閉された第1消化槽2
に移送され、更に第2消化槽3に移送されて、夫々の消
化槽内で嫌気性消化処理される。この嫌気性消化処理は
、第1及び第2の消化槽2.3内で発生、増殖するメタ
ン醒と酸性菌の作用によって行なわ五るものであるが、
油脂分音多量に含む浮上フロスのみを嫌気性消化処理す
る場合は、油脂分がこれらの菌の作用では分解・消化さ
れK<rものであるため、満足な処理が行なえないので
ある。けれども、この発明のように、浮上フロスに血汁
が混合されていると、血汁に含まれる原料魚の内臓酵素
が油脂分の分解を促進するため、鉋が活発に働き、血汁
及び浮上フロス中の有機物を速やかに消化してメタンガ
スを主成分とする消化ガスを発生するのである。従って
、この嫌気性処理は、血汁と浮上フロスの混合物を、内
臓酵llKよる分解促進作用が大で劇の働きが活発に行
なわれる3Q、’〜40°Cの温度に維持するのが望ま
しい。そのため、第1図の実施例では、第1及び第2の
消化槽2,3にスチーム管21.31を通し、混合物a
i30°〜400Cの温度域に保温している。
In this way, the mixture a of blood juice and floating floss temporarily mixed and stored in the receiving tank l is then transferred to the sealed first digestion tank 2.
and further transferred to the second digestion tank 3, where they are subjected to anaerobic digestion treatment. This anaerobic digestion treatment is carried out by the action of methane atomization and acid bacteria that are generated and proliferated in the first and second digestion tanks 2.3.
When only floating floss containing a large amount of oil and fat is subjected to anaerobic digestion, the oil and fat are decomposed and digested by the action of these bacteria, and K<r, so that a satisfactory treatment cannot be achieved. However, when blood juice is mixed in the flotation floss as in this invention, the internal enzymes of the fish contained in the blood juice promote the decomposition of oil and fat, so the plane works actively, and the blood juice and flotation floss are mixed. It quickly digests the organic matter inside and generates digestive gas, the main component of which is methane gas. Therefore, in this anaerobic treatment, it is desirable to maintain the mixture of blood juice and floating floss at a temperature between 3Q and 40°C, where the decomposition promoting effect by visceral enzyme llK is large and the action is active. . Therefore, in the embodiment shown in FIG.
It is kept warm in the temperature range of 30° to 400C.

このような温度域で嫌気性消化処理すると、混合物を双
方の、消化槽2,3内で合計25〜40日程度・滞留さ
11.せるだけで、混合物中のほとんどす■、。
When anaerobic digestion is performed in such a temperature range, the mixture remains in both the digestion tanks 2 and 3 for a total of about 25 to 40 days. ■Just add most of the liquid to the mixture.

べての有機物が分解・消化され、主成分のメタンガスを
約60〜75%含んだ消化ガス(メタンガスを除く残り
の大部分は炭酸ガスンとなる0この消化ガスの発生量は
、例えば12m’の混合物(V機物含量800kg)を
上記条件で嫌気性処理する場合、約800m”である。
All organic matter is decomposed and digested, and the digestive gas contains approximately 60-75% of the main component, methane gas (excluding the methane gas, most of the remainder is carbon dioxide).The amount of this digestive gas generated is, for example, 12 m' When a mixture (V material content: 800 kg) is subjected to anaerobic treatment under the above conditions, the length is approximately 800 m''.

特に原料魚がイワシやサバである場合、この嫌気性消化
処理が効率よく行なわれる。
This anaerobic digestion process is particularly efficient when the raw fish is sardines or mackerel.

消化槽内で発生した消化ガスbは5、すべて取出しても
よいが、第1図の実施例では、この消化ガスの一部をブ
ロワ−4,4で消化槽2,3に戻し、混合物中でバブリ
ングさせて該□混合・物の攪拌に利用している。消化槽
2,3へ戻されずに途中で取出された消化ガスは、脱硫
器5,5に通され、そこでボイラー腐蝕等の原因となる
イオウ化合物か除去された後、ガスホルダー6に留めら
れる。このガスホルダー6に留められたメタンガス含有
率60〜75%程度の消化ガスは、ボイラー7の加熱に
使用され、発生したスチームは、前述した消化槽”2.
3の保温、或は”工場内で使用するボイラー用水の予熱
等に利用される0   一方、第2消化槽3の上部よシ取出された離脱液は、活
性汚泥曝気槽8へ送られ、前述の浮上フロスを浮上分離
除去したあとの廃液と共に生物学的酸化処理される。こ
の活性汚泥曝気槽8から取出された余剰汚泥は、沈降分
離したのち脱水されて汚泥乾燥機9に送られ、前述のボ
イラー7から供給されるスチームの熱を利用して減圧下
に乾燥同化され、乾燥菌体肥料lOとなる。
All of the digestion gas b generated in the digestion tank 5 may be taken out, but in the embodiment shown in FIG. It is used for bubbling and mixing and stirring of materials. Digestion gas taken out midway without being returned to the digestion tanks 2, 3 is passed through desulfurizers 5, 5, where sulfur compounds that cause boiler corrosion etc. are removed, and then retained in a gas holder 6. The digestion gas with a methane gas content of about 60 to 75% retained in the gas holder 6 is used to heat the boiler 7, and the generated steam is transferred to the aforementioned digestion tank "2.
On the other hand, the separated liquid taken out from the upper part of the second digestion tank 3 is sent to the activated sludge aeration tank 8, and is used for preheating boiler water used in the factory. The floating floss is subjected to biological oxidation treatment together with the waste liquid after flotation separation.The excess sludge taken out from the activated sludge aeration tank 8 is separated by sedimentation, dehydrated and sent to the sludge dryer 9, and then Using the heat of the steam supplied from the boiler 7, it is dried and assimilated under reduced pressure to become dry bacterial fertilizer lO.

又、第2消化槽3の下部よシ取出される消化汚泥は、有
機物含量が極めて少なく且つ脱水性が良いものであるの
で、脱水機11に送られて真空脱水された後、埋立処分
される。このように埋立処分しても、有機物が殆んど含
まれていないため悪臭公害を生じる惧れはない。
In addition, the digested sludge taken out from the lower part of the second digestion tank 3 has extremely low organic matter content and has good dewatering properties, so it is sent to the dehydrator 11 and vacuum dehydrated before being disposed of in a landfill. . Even if it is disposed of in a landfill, there is no risk of causing odor pollution because it contains almost no organic matter.

以上の説明から明らかなように、この発明の水産加工廃
物の処理方法は、嫌気性消化処理が困難な油脂分の多い
浮上フロスに対し、油脂分の分解を促進する内臓酵素管
含む血汁を混合することに−よって、メタン園及び酸性
菌の働きを活発にし、嫌気性消化処理を可能となしたも
のであり、それによって発生するメタンガスを主灰分と
する消化ガスを熱エネルギーとして利用し、重油節減に
よる省エネルギーと悪臭公害防止全実現すると共に1良
質の乾燥菌体肥料も得ることか出来る等、−石三鳥の効
果を奏するものである。
As is clear from the above explanation, the method for treating seafood processing waste of the present invention uses blood juice containing visceral enzyme tubes that promote the decomposition of fats and oils for floating floss containing a lot of fats and oils, which is difficult to anaerobically digest. By mixing, the methane garden and acid bacteria are activated, making anaerobic digestion possible, and the resulting digestion gas, whose main ash is methane gas, is used as thermal energy. It achieves the following effects: it saves energy by saving heavy oil, prevents bad odor pollution, and also provides high-quality dried bacterial fertilizer.

尚、第1図の実施例では、第1消化槽2と第2消化槽3
全併設した二段式消化槽を使用した場合を示したが、単
−消化槽を使用してもよく、又場合によっては、水産加
工の蒸煮工程で生じる煮汁を混合物に更に加えて同様に
処理してもよい0
In the embodiment shown in FIG. 1, the first digestion tank 2 and the second digestion tank 3 are
Although we have shown the case where a two-stage digester with all attached tanks is used, a single-stage digester may also be used, and in some cases, the broth produced in the steaming process of seafood processing may be further added to the mixture and treated in the same way. OK to do 0

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

第1図はこの発明の一実施例の模式説明図であるO 1・・・受槽、2・・・第1消化檀、3・・・第2消化
檜、4・・・ブロワ−15・・・脱硫器、6・・・ガス
ホルダー、7・・・ボイラー、8・・・活性汚泥曝気槽
、9・・・汚泥乾燥機、lO・・・乾燥菌体肥料、ll
・・・脱水機、a・・・混合物、b・・・消化ガス。 特許出願人   大篠津食品工□業株式会社同代理人 
 渡  辺  三  彦
FIG. 1 is a schematic explanatory diagram of an embodiment of the present invention.・Desulfurizer, 6... Gas holder, 7... Boiler, 8... Activated sludge aeration tank, 9... Sludge dryer, lO... Dry bacterial fertilizer, ll
... Dehydrator, a... Mixture, b... Digestion gas. Patent applicant: Oshinozu Food Industry Co., Ltd. Agent
Mihiko Watanabe

Claims (1)

【特許請求の範囲】[Claims] 水産加工の原料魚調理工程で生じる血汁と、廃液処理で
生じる浮上フロスとの混合物を嫌気性消化処理してメタ
ンガスを主成分とする消化ガスを発生させることを特徴
とする水産加工廃物の処理方法0
Processing of seafood processing waste characterized by anaerobically digesting a mixture of blood juice produced in the fish cooking process and floating floss produced in waste liquid treatment to generate digestive gas mainly composed of methane gas. Method 0
JP56172404A 1981-10-27 1981-10-27 Treatment for waste of processed marine products Pending JPS5874192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56172404A JPS5874192A (en) 1981-10-27 1981-10-27 Treatment for waste of processed marine products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56172404A JPS5874192A (en) 1981-10-27 1981-10-27 Treatment for waste of processed marine products

Publications (1)

Publication Number Publication Date
JPS5874192A true JPS5874192A (en) 1983-05-04

Family

ID=15941315

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56172404A Pending JPS5874192A (en) 1981-10-27 1981-10-27 Treatment for waste of processed marine products

Country Status (1)

Country Link
JP (1) JPS5874192A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4521310A (en) * 1982-08-31 1985-06-04 Casey Thomas J Apparatus and method for the treatment of organic wastes
JPS63185499A (en) * 1987-01-28 1988-08-01 Osaka Pref Gov Methane fermentation method
JPS6451187A (en) * 1987-08-21 1989-02-27 Sapporo Sanki Kk Clarifying method of bloody water

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4521310A (en) * 1982-08-31 1985-06-04 Casey Thomas J Apparatus and method for the treatment of organic wastes
JPS63185499A (en) * 1987-01-28 1988-08-01 Osaka Pref Gov Methane fermentation method
JPS6451187A (en) * 1987-08-21 1989-02-27 Sapporo Sanki Kk Clarifying method of bloody water

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