JPS6330388A - Recycling treatment of kitchen waste - Google Patents

Recycling treatment of kitchen waste

Info

Publication number
JPS6330388A
JPS6330388A JP61175120A JP17512086A JPS6330388A JP S6330388 A JPS6330388 A JP S6330388A JP 61175120 A JP61175120 A JP 61175120A JP 17512086 A JP17512086 A JP 17512086A JP S6330388 A JPS6330388 A JP S6330388A
Authority
JP
Japan
Prior art keywords
waste
treatment
oil
dehydration treatment
methane fermentation
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.)
Granted
Application number
JP61175120A
Other languages
Japanese (ja)
Other versions
JPH0788268B2 (en
Inventor
宮内 修平
俊則 亀岡
因野 要一
崎元 道男
中園 修三
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.)
Osaka Prefecture
Original Assignee
Osaka Prefecture
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 Osaka Prefecture filed Critical Osaka Prefecture
Priority to JP61175120A priority Critical patent/JPH0788268B2/en
Publication of JPS6330388A publication Critical patent/JPS6330388A/en
Publication of JPH0788268B2 publication Critical patent/JPH0788268B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Landscapes

  • Fodder In General (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 この発明は、厨房廃棄物の資源化処理法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application This invention relates to a method for recycling kitchen waste into resources.

(ロ) 従来の技術 従来、都市において、レストラン、ホテル、食堂、病院
、学校給食等の食品事業所から排出される残飯等の厨房
廃棄物は、もともと家畜の飼料になりうるちのであるが
、ごく一部が都市近郊の養豚場で利用されているだけで
、大部分は焼却処理、又は下水処理等によって処分され
ている。
(b) Conventional technology Conventionally, in cities, kitchen waste such as leftover food discharged from food establishments such as restaurants, hotels, cafeterias, hospitals, and school cafeterias could originally be used as feed for livestock. Only a small portion is used in pig farms near cities, and the majority is disposed of by incineration or sewage treatment.

(ハ) 発明が解決しようとする問題点このように上記
廃棄物は飼料として利用されているのはごく一部であり
、さらに最近では、悪臭公害や、調理給飼上の取扱いの
問題、軟脂豚の発生等によって利用する養豚場が少なく
なる傾向にある。
(c) Problems to be solved by the invention As described above, only a small portion of the above-mentioned waste is used as feed, and more recently, problems such as odor pollution, handling problems in cooking and feeding, and soft The number of pig farms in use is decreasing due to the occurrence of fatty pigs.

一方、廃棄物処理の面からみると、含水率の高い厨房廃
棄物は焼却処理のために多量の石油を消費しており、い
わば、飼料として資源化の可能性のある素材を、燃r1
を用いて焼却するという二重の無駄が行われていること
になる。
On the other hand, from the perspective of waste treatment, kitchen waste with a high moisture content consumes a large amount of oil to be incinerated.
This means that there is double waste in incinerating the waste.

なお、厨房廃棄物の加工法として蒸気等の熱源を用いた
直接加熱法による乾燥が試みられたが、脂肪の酸化が急
速に進む等、品質の劣化、及び燃料を多量に消費するな
どの難点があり実用には至らなかった。
Drying by direct heating using a heat source such as steam has been attempted as a processing method for kitchen waste, but it has problems such as rapid oxidation of fat, deterioration of quality, and consumption of a large amount of fuel. However, it was not put into practical use.

(ニ) 問題点を解決するための手段 本発明では、厨房より産出される残飯等の廃棄物を、油
温脱水処理用の廃棄物とメタン発酵用の廃棄物とに選別
処理し、油温脱水処理用の廃棄物は、初期は軽度の減圧
、終期には強度の減圧の二段階減圧条件下において所定
温度の加熱油中に浸漬して、同廃棄物の脱水乾燥を行っ
て家畜等の飼料とし、メタン発酵用の廃棄物は、嫌気条
件下でメタン発酵処理を行い、発生したメタンガスを油
温脱水処理用等のエネルギー源として用い、消化汚泥は
脱水処理して堆肥とすることを特徴とする厨房廃棄物の
資源化処理法を提供せんとするものである。
(d) Means for Solving the Problems In the present invention, waste such as leftover food produced in the kitchen is sorted into waste for oil temperature dehydration treatment and waste for methane fermentation. Waste for dehydration treatment is immersed in heated oil at a predetermined temperature under two-step depressurization conditions: mild depressurization at the beginning and strong decompression at the end, and dehydration and drying of the waste is performed. The waste for methane fermentation is used as feed, and the waste is subjected to methane fermentation treatment under anaerobic conditions, and the generated methane gas is used as an energy source for oil temperature dehydration treatment, etc., and the digested sludge is dehydrated and made into compost. The aim is to provide a method for recycling kitchen waste.

(ホ) 作用・効果 この発明によれば、厨房廃棄物を選別処理により、鮮度
の良好なものを飼料の原料としての油温脱水処理用の廃
棄物とすることで、飼料原料の品質を保持し、二段階の
減圧条件下で加熱油を熱媒体とした油温脱水処理により
、原料の口;2水乾燥を行うことで高品位かつ長期保存
可能の飼料を製造でき、一方鮮度不良の厨房廃棄物をメ
タン発酵させて1りだメタンガスを、上記油温脱水処理
等のエネルギー源として用いることにより、他からのエ
ネルギー補給を不要とし、更に、メタン発酵の消化汚泥
を脱水処理して堆肥化することによって、上記厨房廃棄
物を余すことなく資源として利用することができ、しか
も、他からのエネルギー補給い を要しないとう効果を奏するものである。
(E) Function/Effect According to the present invention, the quality of feed raw materials is maintained by sorting kitchen waste and using waste with good freshness as waste for oil temperature dehydration treatment as feed raw materials. By applying oil-temperature dehydration treatment using heated oil as a heating medium under two-step depressurization conditions, high-quality feed that can be stored for a long time can be produced by drying the raw materials. By methane fermentation of waste and using the methane gas as an energy source for the above-mentioned oil-temperature dehydration treatment, there is no need to supply energy from other sources.Furthermore, the digested sludge from methane fermentation can be dehydrated and composted. By doing so, the above-mentioned kitchen waste can be fully utilized as a resource, and moreover, there is an effect that energy supply from other sources is not required.

△ (へ) 実施例 この発明の実施例を詳説すれば、第1図は、本発明によ
る厨房廃棄物資源化処理法のフローを示しており、以下
このフローに従って説明する。なお、円形枠内の符号は
物質等を、方形枠内の符号は処理等を示す。
Δ (f) Example To explain in detail an example of the present invention, FIG. 1 shows the flow of the kitchen waste resource recycling method according to the present invention, and the following description will be made according to this flow. Note that the symbols in the circular frame indicate substances, etc., and the symbols in the square frame indicate processes, etc.

まず、収集されたIig房廃棄物(1)を選別処理(2
)して、鮮度が良好なものを、飼料原料としての油温脱
水処理用の廃棄物(3)とし、鮮度が低いものをメタン
発酵用の廃棄物(4)とする。
First, the collected Iig cell waste (1) is subjected to sorting treatment (2).
), those with good freshness are used as waste (3) for oil temperature dehydration treatment as feed raw materials, and those with low freshness are used as waste (4) for methane fermentation.

なお、この選別処理の際、包装用プラスチックフィルム
等の夾雑物(5)などを除去する。
Note that during this sorting process, impurities (5) such as plastic packaging films are removed.

次いで、油温脱水処理用の廃棄物(3)を油温脱水処理
(6)する。
Next, the waste (3) for oil temperature dehydration treatment is subjected to oil temperature dehydration treatment (6).

この油温脱水処1!l (6)は、上記廃棄物〈3〉を
、密閉可能のクツカー中の加熱油(7)に浸漬して、二
段階減圧条件下で水分を蒸散させ脱水乾燥等を行うもの
であり、加熱油(7)は、動物又は植物油、又はこれら
の混合油を予め60〜110℃に加熱して熱媒体とし、
二段階減圧条件は同処理(6)の初期的30分根は軽度
の減圧(8)を行って、同廃棄物(3)中の蛋白質及び
栄養素等を熱凝固させ、しかるのち強度の減圧(9)を
行って、同廃棄物(3)中の水分の蒸散を活発化し、約
1時間程で含水率を約10%以下になるまで脱水乾燥す
る。
This oil temperature dehydration place 1! l (6) is to immerse the above waste <3> in heated oil (7) in a sealable container to evaporate water under two-step reduced pressure conditions to perform dehydration and drying. The oil (7) is an animal or vegetable oil, or a mixture thereof, which is heated in advance to 60 to 110°C to serve as a heat medium;
The two-stage depressurization conditions are as follows: In the initial 30 minutes of the same treatment (6), mild depressurization (8) is performed to thermally coagulate the proteins and nutrients in the waste (3), and then strong depressurization ( 9) to activate the evaporation of water in the waste (3) and dehydrate and dry it in about 1 hour until the water content becomes about 10% or less.

また、油温脱水処理(6)にて、発生する脱水液(13
)は、生化学的汚水処理(21)により浄化する。
In addition, the dehydration liquid (13) generated in the oil temperature dehydration treatment (6)
) is purified by biochemical wastewater treatment (21).

次いで、脱水乾燥された廃棄物(3)をクツカーから取
出し、プレス等によって脱油処理(10)し、脱油され
た澗は、加熱油(7)として再利用し、更に、粒状等の
飼料としての適正な形態に成形すると共に、ビタミン及
びミネラル添加等の成分調整(11)を行って、製品の
飼料(12)とする。
Next, the dehydrated and dried waste (3) is taken out of the cutter and subjected to oil removal treatment (10) using a press or the like, and the oil-removed waste is reused as heated oil (7), and further processed into feed such as granules. The product is molded into an appropriate form, and the ingredients are adjusted (11) such as adding vitamins and minerals to make the product feed (12).

一方、メタン発酵用の廃棄物(4)は、嫌気条件下で中
温のメタン発酵処理<17!りを行い、発生したメタン
ガス(15)を、前記油温脱水処理(6)用等のエネル
ギー源(E)として用い、消化汚泥〈16)は脱水処理
(17)して、固形分(18)を再発酵させて堆肥(1
9)どして農地に還元し、脱水水分(20)は生化学的
汚水処理(21)により浄化して、汚泥(22)は前記
消化汚泥く16)と共に脱水処理(17)して堆肥(1
9)とし、浄化水(23)にてクロレラ培養(24)を
゛行って、得たクロレラ(25)を前記の成分調整(1
1)に用いると共に、放流される浄化水(23)中の無
機塩類を回収して環境の富栄養化を防止する。なお、浄
化水(23)の一部はメタン発酵処理(14)の希釈水
にも用いている。
On the other hand, waste material for methane fermentation (4) is subjected to methane fermentation treatment at medium temperature under anaerobic conditions <17! The methane gas (15) generated is used as an energy source (E) for the oil temperature dehydration treatment (6), etc., and the digested sludge (16) is dehydrated (17) to reduce the solid content (18). re-ferment and compost (1
9) The dehydrated water (20) is purified by biochemical sewage treatment (21), and the sludge (22) is dehydrated (17) together with the digested sludge (16) and composted ( 1
9), cultured chlorella (24) in purified water (23), and added the obtained chlorella (25) to the above component adjustment (1).
In addition to being used for 1), the inorganic salts in the purified water (23) that is discharged are recovered to prevent eutrophication of the environment. Note that a part of the purified water (23) is also used as dilution water for the methane fermentation treatment (14).

なお、油温脱水処理(6)に用いる加熱油(7)は繰返
し使用されるものであるが、酸化等により次第に層化す
るので、限度を超えて劣化した加熱油は、前記のメタン
ガス(15)と共にエネルギー源(E)として利用する
Although the heated oil (7) used in the oil temperature dehydration treatment (6) is used repeatedly, it gradually becomes stratified due to oxidation, etc. Therefore, the heated oil that has deteriorated beyond the limit is treated with the methane gas (15 ) is used as an energy source (E).

このようにして得た飼料(12)は、性状的には完全に
乾燥されているため長期保存ができ、悪臭がなく、給飼
時の取扱いが容易であり、成分的には、油温脱水処理(
6)によって脂肪の酸化が抑制されて品質の劣化が少な
く、また廃棄物(3)中の過剰の脂肪が加熱油(7)中
に溶出して脂肪の旦が一定し、また、加熱油(7)に飽
和脂肪酸の天ぷら油を用いることで、製品の飼料(12
)の脂肪を飽和化することにより、流通性、安全性、給
飼効果の改善、軟脂豚発生防止等の効果を奏するもので
ある。
Feed (12) obtained in this way can be stored for a long time because it is completely dry, has no bad odor, and is easy to handle during feeding. process(
6) suppresses fat oxidation and reduces quality deterioration, and excess fat in waste (3) is eluted into heated oil (7) to maintain a constant fat content. By using tempura oil with saturated fatty acids in 7), the feed of the product (12
) By saturating the fat of the pig, it is possible to improve distribution efficiency, safety, feeding effectiveness, and prevent the occurrence of soft fat pigs.

なお、この飼料(12)は豚ばかりでなく、牛、鶏等の
家畜の飼料とすることもできる。
Note that this feed (12) can be used not only for pigs but also for livestock such as cows and chickens.

また、上記のように厨房廃棄物(1)は、余すところな
く利用されて、飼料(12)と堆肥(18)という有価
物に変換され、しかも他からのエルギーの補給を必要と
しないので、資源の有効利用の面だけでなく、従来、焼
却処分に多量の石油を消費して地方自治体の負担となっ
ていた厨房廃棄物が有価物として対価を得ることができ
るようになり自治体の財政に貢献することができる。
In addition, as mentioned above, kitchen waste (1) is fully utilized and converted into valuable materials such as feed (12) and compost (18), and does not require energy supply from other sources. In addition to the effective use of resources, kitchen waste, which used to be a burden on local governments by consuming a large amount of oil for incineration, can now be treated as valuable material and benefit local governments' finances. can contribute.

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

第1図は、本発明による厨房廃棄物の資源化処理法のフ
ローを示すブロックダイヤグラム(E):エネルギー源 (1):gJ房廃棄物 (2):選別処理 (3):油温脱水処理用の廃棄物 (4):メタン発酵用の廃棄物 (7):加熱油 (8):軽度の減圧 くっ)二強度の減圧 (12):飼料 (14):メタン発酵処理 (16):消化汚泥 (17):脱水処理 (19):堆肥
Figure 1 is a block diagram (E) showing the flow of the kitchen waste resource recycling treatment method according to the present invention: Energy source (1): gJ waste (2): Sorting treatment (3): Oil temperature dehydration treatment Waste for methane fermentation (4): Waste for methane fermentation (7): Heated oil (8): Mild vacuum) Double-strength vacuum (12): Feed (14): Methane fermentation treatment (16): Digestion Sludge (17): Dewatering treatment (19): Compost

Claims (1)

【特許請求の範囲】[Claims] 1)厨房より産出される残飯等の廃棄物(1)を、油温
脱水処理用の廃棄物(3)とメタン発酵用の廃棄物(4
)とに選別処理(2)し、油温脱水処理用の廃棄物(3
)は、初期は軽度の減圧(8)、終期には強度の減圧(
9)の二段階減圧条件下において所定温度の加熱油(7
)中に浸漬して、同廃棄物(3)の脱水乾燥を行って家
畜等の飼料(12)とし、メタン発酵用の廃棄物(4)
は、嫌気条件下でメタン発酵処理(14)を行い、発生
したメタンガス(15)を油温脱水処理用等のエネルギ
ー源(E)として用い、消化汚泥(16)は脱水処理(
17)して堆肥(19)とすることを特徴とする厨房廃
棄物の資源化処理法。
1) Waste such as leftover food produced in the kitchen (1) is divided into waste for oil temperature dehydration treatment (3) and waste for methane fermentation (4).
) and waste for oil temperature dehydration treatment (3).
) is a mild decompression at the beginning (8) and a strong decompression at the end (8).
Heated oil (7) at a predetermined temperature under the two-step reduced pressure conditions of (9)
), the waste (3) is dehydrated and dried to be used as feed for livestock (12), and the waste (4) is used for methane fermentation.
is subjected to methane fermentation treatment (14) under anaerobic conditions, the generated methane gas (15) is used as an energy source (E) for oil temperature dehydration treatment, etc., and the digested sludge (16) is subjected to dehydration treatment (
17) A method for recycling kitchen waste into resources, characterized by turning it into compost (19).
JP61175120A 1986-07-24 1986-07-24 Recycling method of kitchen waste Expired - Lifetime JPH0788268B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61175120A JPH0788268B2 (en) 1986-07-24 1986-07-24 Recycling method of kitchen waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61175120A JPH0788268B2 (en) 1986-07-24 1986-07-24 Recycling method of kitchen waste

Publications (2)

Publication Number Publication Date
JPS6330388A true JPS6330388A (en) 1988-02-09
JPH0788268B2 JPH0788268B2 (en) 1995-09-27

Family

ID=15990626

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61175120A Expired - Lifetime JPH0788268B2 (en) 1986-07-24 1986-07-24 Recycling method of kitchen waste

Country Status (1)

Country Link
JP (1) JPH0788268B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02295473A (en) * 1989-05-09 1990-12-06 Shuzo Nakazono Apparatus for producing feed and fertilizer
CN102030456A (en) * 2010-11-09 2011-04-27 同济大学 Method for enhancing dry-process fermentation stability of sludge by adding kitchen waste
CN103819240A (en) * 2014-03-12 2014-05-28 郑小兵 Biological treatment equipment and method for kitchen wastes
JP2016203103A (en) * 2015-04-23 2016-12-08 三井造船環境エンジニアリング株式会社 Processing method of organic waste
JP2017042726A (en) * 2015-08-27 2017-03-02 三井造船株式会社 Livestock feed production recycle system, and livestock feed production recycle method
JP2017113728A (en) * 2015-12-25 2017-06-29 三井造船環境エンジニアリング株式会社 Hybrid valuable object manufacturing equipment

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55158190A (en) * 1979-05-24 1980-12-09 Fuji Electric Co Ltd Waste composting method and device
JPS57140391A (en) * 1981-02-24 1982-08-30 Nakazono Shuzo Manufacture of feed and fertilizer from garbage

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55158190A (en) * 1979-05-24 1980-12-09 Fuji Electric Co Ltd Waste composting method and device
JPS57140391A (en) * 1981-02-24 1982-08-30 Nakazono Shuzo Manufacture of feed and fertilizer from garbage

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02295473A (en) * 1989-05-09 1990-12-06 Shuzo Nakazono Apparatus for producing feed and fertilizer
CN102030456A (en) * 2010-11-09 2011-04-27 同济大学 Method for enhancing dry-process fermentation stability of sludge by adding kitchen waste
CN103819240A (en) * 2014-03-12 2014-05-28 郑小兵 Biological treatment equipment and method for kitchen wastes
JP2016203103A (en) * 2015-04-23 2016-12-08 三井造船環境エンジニアリング株式会社 Processing method of organic waste
JP2017042726A (en) * 2015-08-27 2017-03-02 三井造船株式会社 Livestock feed production recycle system, and livestock feed production recycle method
JP2017113728A (en) * 2015-12-25 2017-06-29 三井造船環境エンジニアリング株式会社 Hybrid valuable object manufacturing equipment

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