JPH01164787A - Method for manufacturing powder manure or feed from organic waste material and appratus therefor - Google Patents
Method for manufacturing powder manure or feed from organic waste material and appratus thereforInfo
- Publication number
- JPH01164787A JPH01164787A JP62324870A JP32487087A JPH01164787A JP H01164787 A JPH01164787 A JP H01164787A JP 62324870 A JP62324870 A JP 62324870A JP 32487087 A JP32487087 A JP 32487087A JP H01164787 A JPH01164787 A JP H01164787A
- Authority
- JP
- Japan
- Prior art keywords
- cooking
- organic waste
- wastes
- tank
- spray
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 8
- 239000010815 organic waste Substances 0.000 title claims description 25
- 238000000034 method Methods 0.000 title claims description 15
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 239000000463 material Substances 0.000 title description 4
- 210000003608 fece Anatomy 0.000 title 1
- 239000010871 livestock manure Substances 0.000 title 1
- 238000010411 cooking Methods 0.000 claims abstract description 38
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 239000003337 fertilizer Substances 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 3
- 238000007790 scraping Methods 0.000 claims description 3
- 238000013517 stratification Methods 0.000 claims description 2
- 239000010419 fine particle Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 210000000988 bone and bone Anatomy 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 7
- 239000007921 spray Substances 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 4
- 238000001694 spray drying Methods 0.000 abstract description 2
- 238000013019 agitation Methods 0.000 abstract 2
- 235000021190 leftovers Nutrition 0.000 abstract 1
- 244000144972 livestock Species 0.000 abstract 1
- 210000001835 viscera Anatomy 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 13
- 238000010586 diagram Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 241000251468 Actinopterygii Species 0.000 description 4
- 241000283690 Bos taurus Species 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 3
- 239000010828 animal waste Substances 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 235000019698 starch Nutrition 0.000 description 3
- 241000282472 Canis lupus familiaris Species 0.000 description 2
- 241000283086 Equidae Species 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 2
- 241000287828 Gallus gallus Species 0.000 description 2
- 108010010803 Gelatin Proteins 0.000 description 2
- 241000282887 Suidae Species 0.000 description 2
- 235000013330 chicken meat Nutrition 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 229920000159 gelatin Polymers 0.000 description 2
- 239000008273 gelatin Substances 0.000 description 2
- 235000019322 gelatine Nutrition 0.000 description 2
- 235000011852 gelatine desserts Nutrition 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 235000015170 shellfish Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 241000271566 Aves Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000011437 continuous method Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 238000009372 pisciculture Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Fodder In General (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、動物性廃棄物や調理残滓等の有機性廃棄物を
処理して粉体飼料又は肥料を製造する方法及びそれに用
いる装置に関するものである。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for producing powdered feed or fertilizer by processing organic waste such as animal waste and cooking residue, and an apparatus used therefor. It is.
(従来技術)
動物性廃棄物、すなわち牛、馬、豚、鶏、魚、貝等の内
蔵、肉、頭、骨等の廃棄物やレストラン、ホテル、飲食
店、料亭等で発生する油、澱粉、ゼラチン、蛋白質等を
含む調理残滓等の有機性廃棄物は、そのほとんどが焼却
場で焼却又は埋設処分されている。(Prior art) Animal wastes, such as offal, meat, heads, and bones of cows, horses, pigs, chickens, fish, and shellfish, as well as oils and starches generated in restaurants, hotels, eateries, restaurants, etc. Most organic wastes such as cooking residues containing food, gelatin, protein, etc. are incinerated at incinerators or buried.
(発明が解決しよう表する問題点)
ところで、これらの有機性廃棄物は油、澱粉、蛋白質等
の有用成分を含んでいるので、焼却又は埋設することは
有用資源の大きな損失であるが、手軽で安価な再生法が
なくその開発が望まれていた。(Problems to be solved by the invention) By the way, these organic wastes contain useful components such as oil, starch, and protein, so incinerating or burying them would be a major loss of useful resources, but it is easy to There was no inexpensive regeneration method available, and the development of one was desired.
(問題点を解決するための手段)
そこで、本発明者等は有機性廃棄物の有効な再生方法に
ついて鋭意検討を重ねた結果、有機性廃棄物を撹拌、す
りつぶし、破砕しながら加圧水蒸気と接触させて蒸解し
たのち噴霧乾燥を行う方法が好ましいことを見出し、こ
の知見に基づき本発明を完成した。(Means for Solving the Problems) Therefore, as a result of extensive research into an effective method for recycling organic waste, the inventors of the present invention brought the organic waste into contact with pressurized steam while stirring, grinding, and crushing the organic waste. It was discovered that a method of boiling and cooking followed by spray drying was preferable, and based on this knowledge, the present invention was completed.
以下、本発明を図面に基づいて詳細に説明する。Hereinafter, the present invention will be explained in detail based on the drawings.
第1図は本発明方法の実施に用いる装置の一例のフロー
シート、第2図は竪型蒸解装置の一例の説明図、第3図
は横型蒸解装置の一例の説明図、第4図は第3図のA−
A矢視図、第5図は第3図の分岐板部の拡大斜視図であ
る。Fig. 1 is a flow sheet of an example of an apparatus used to implement the method of the present invention, Fig. 2 is an explanatory diagram of an example of a vertical digester, Fig. 3 is an explanatory diagram of an example of a horizontal digester, and Fig. 4 is an explanatory diagram of an example of a horizontal digester. A- in Figure 3
A view taken along arrow A, and FIG. 5 is an enlarged perspective view of the branch plate portion in FIG. 3.
図中、3は蒸解装置、5は油分離タンク、12はクラッ
シャータンク、14は蒸解液タンク、17は噴霧乾燥機
、22.34は密閉容器、29は多孔板、36は回転能
である。In the figure, 3 is a cooking device, 5 is an oil separation tank, 12 is a crusher tank, 14 is a cooking liquid tank, 17 is a spray dryer, 22, 34 is a closed container, 29 is a perforated plate, and 36 is a rotation capacity.
蒸解装置3は、有機性廃棄物を加圧水蒸気と接触させて
蒸解させるためのもので、竪型蒸解装置、横型蒸解装置
又は通常の加圧缶等が用いられる。The digester 3 is for bringing organic waste into contact with pressurized steam to cook it, and may be a vertical digester, a horizontal digester, or a normal pressurized can.
竪型蒸解装置としては例えば第2図に示すように、竪方
向に設置された円筒形の密閉容器22と、その下部を上
下方向に区画するように設けられた截頭逆円錐状の多孔
板29と−3=
、該多孔板29の上面に沿って回動するように設けられ
た渦巻式の撹拌翼31と、多孔板29の下方に設けられ
多数の蒸気噴出孔が削孔されたリング状の蒸気供給管3
0より構成されたものが用いられ−る。多孔板29は水
蒸気の均一な流入を助ける分散板の役目をすると共に蒸
解液の濾過の役目も果たしている。For example, as shown in FIG. 2, a vertical digester includes a cylindrical sealed container 22 installed vertically, and a truncated inverted conical perforated plate provided to vertically divide the lower part of the container 22. 29 and -3=, a spiral stirring blade 31 provided to rotate along the upper surface of the perforated plate 29, and a ring provided below the perforated plate 29 with a large number of steam ejection holes drilled therein. shaped steam supply pipe 3
A configuration consisting of 0 is used. The perforated plate 29 serves as a dispersion plate that helps uniform inflow of water vapor, and also serves as a filter for cooking liquor.
横型蒸解装置としては、例えば第3図、第4図及び第5
図に示すように、横方向に設置された円筒形の密閉容器
34と、該容器34内に同軸に設けられた回転能36と
、回転能36の内壁に軸心方向に突き出し軸方向に延び
るかき上げ板40と、密閉容器34に設けられた蒸気供
給管35より構成されたものが用いられる。回転能36
は水蒸気の均一な流入を助ける分散板の役目をすると共
に蒸解液の濾過の役目も果たしている。Examples of horizontal digesters include those shown in Figs. 3, 4, and 5.
As shown in the figure, there is a cylindrical sealed container 34 installed laterally, a rotary shaft 36 provided coaxially within the container 34, and a rotary shaft 36 that protrudes in the axial direction from the inner wall of the rotary shaft 36 and extends in the axial direction. A device consisting of a scraping plate 40 and a steam supply pipe 35 provided in a closed container 34 is used. Rotation ability 36
serves as a dispersion plate that helps the uniform flow of water vapor, and also serves as a filter for cooking liquor.
゛ 油分離タンク5は、蒸解液中に含まれる油分を成
層分離するためのもので、通常のタンクが用いられるが
、加熱、加圧下で撹拌するものが望ましい。゛ The oil separation tank 5 is for stratified separation of the oil contained in the cooking liquor, and a normal tank is used, but one that stirs under heating and pressure is preferable.
噴霧乾燥機17は、蒸解液を象、速に乾燥するためのも
ので、通常の旋回ガス気流中に蒸解液を噴霧する形式の
ものが用いられる。The spray dryer 17 is used to quickly dry the cooking liquor, and is of a type that sprays the cooking liquor into a normal swirling gas stream.
クラッシャータンク12は、蒸解装置3で溶解されなか
った骨等の固形物を含む蒸解残渣を破砕するためのもの
で、ホモミキサー、カッターミル、ボールミル又はロー
タリークラッシャー等の破砕作用を有するものが用いら
れるが、第3図、第4図及び第5図に示す蒸解装置で目
開きの小さい網目の回転能を用いる場合は省略すること
ができる。The crusher tank 12 is for crushing the cooking residue containing solids such as bones that have not been dissolved in the digester 3, and a crusher such as a homo mixer, a cutter mill, a ball mill, or a rotary crusher is used. However, this can be omitted when using the rotation ability of a mesh with a small opening in the digester shown in FIGS. 3, 4, and 5.
なお、回転能36としては、鋼線を籠状に編んだものや
種々の形状のパンチングメタルを筒状にしたもの等が用
いられる。Note that, as the rotary force 36, a cage-like steel wire knitted material, a cylindrical material made of punched metal of various shapes, etc. are used.
(作用)
次に、このように構成された装置を用いて本発明方法を
実施する場合について説明する先ず、本発明に用いられ
る有機性廃棄物としては、動物性廃棄物、すなわち牛、
馬、膜部、魚、貝等の内蔵、肉、頭、骨等の廃棄物やレ
ストラン、ホテル、飲食店、料亭等で発生する油、澱粉
、ゼラチン、蛋白質、野菜屑等を含んでいる調理残滓、
残飯等が挙げられる。(Function) Next, the case where the method of the present invention is carried out using the apparatus configured as described above will be explained. First, the organic waste used in the present invention is animal waste, that is, cow,
Waste products such as offal, meat, heads, bones, etc. of horses, membranes, fish, shellfish, etc., and cooked food containing oil, starch, gelatin, protein, vegetable scraps, etc. generated in restaurants, hotels, eateries, restaurants, etc. residue,
Examples include leftover food.
第1図に於いて、有機性廃棄物は、好ましくは適度の大
きさに切断又は破砕した後、導管1から蒸解装置3へ供
給される。供給された有機性廃棄物は導管2から供給さ
れる1〜10kg/crMG、好ましくは3−10kg
/cnGの加圧水蒸気の熱と圧力により加水分解(蒸解
)され液状となる。得られた蒸解液は導管4から油分離
タンク5へ導出され油分が成層分離される。分離された
油層は導管7から系外へ取り出され再利用される。水層
は導管8からクンジョンタンク9へ導出され一時貯留さ
れる。骨等の蒸解残渣は導管11からクラノシャ−クン
ク12へ導出され、導管10から導入されるクツション
タンク9内の溶液と混合され破砕される。破砕物を含む
液はポンプ13で蒸解液タンク14へ移送され、導管1
0から供給される溶液と混合される。混合液はスクリー
ン15を経て導管16より噴霧乾燥機17へ供給され、
熱風発生装置18から供給される熱ガス気流中へ噴霧さ
れ乾燥される。得られた乾燥粉体は熱ガスと共に製品捕
集装置19へ導入され固気分離される。分離された粉体
は導管21より排出され製品ホッパー等へ移送され、そ
のまま又は添加物を加えた後飼料又は肥料として提供さ
れる。製品捕集装置19で分離されたガスは、ブロワ−
20で吸引され脱臭装置等の排ガス処理装置(図示せず
)へ送られ処理される。In FIG. 1, organic waste is fed to a digester 3 through a conduit 1, preferably after being cut or crushed to an appropriate size. The organic waste fed is from 1 to 10 kg/crMG, preferably from 3 to 10 kg fed through conduit 2.
It is hydrolyzed (cooked) and becomes liquid by the heat and pressure of pressurized steam of /cnG. The obtained cooking liquor is led to an oil separation tank 5 through a conduit 4, and the oil component is separated by stratification. The separated oil layer is taken out of the system through conduit 7 and reused. The water layer is led out from the conduit 8 to the Kunjeong tank 9 and temporarily stored therein. Cooking residues such as bones are led out from a conduit 11 to a cranoshank 12, mixed with a solution in a cushion tank 9 introduced from a conduit 10, and crushed. The liquid containing the crushed material is transferred to a cooking liquid tank 14 by a pump 13, and is transferred to a cooking liquid tank 14 through a conduit 1.
mixed with the solution supplied from 0. The mixed liquid passes through a screen 15 and is supplied to a spray dryer 17 from a conduit 16.
It is sprayed into a hot gas stream supplied from the hot air generator 18 and dried. The obtained dry powder is introduced into the product collection device 19 together with hot gas and separated into solids and gases. The separated powder is discharged from the conduit 21 and transferred to a product hopper or the like, and is provided as feed or fertilizer as it is or after adding additives. The gas separated by the product collection device 19 is
20 and sent to an exhaust gas treatment device (not shown) such as a deodorization device for treatment.
一方、蒸解残渣を排出した蒸解装W3には、必要に応じ
て導管6より油分離タンク5の水層が導入され、再び有
機性廃棄物が供給され、上述した方法に従って第2回目
の蒸解操作が開始される。以下このような操作が繰り返
し行われる。On the other hand, the water layer of the oil separation tank 5 is introduced from the conduit 6 to the digester W3 from which the cooking residue has been discharged, as necessary, and organic waste is supplied again, and a second cooking operation is carried out according to the method described above. is started. Thereafter, such operations are repeated.
次に、第2図に示す竪型蒸解装置を用いる場合について
説明する。先ず、有機性廃棄物が密閉容器22の上部の
ポールバルブ32より密閉容器22内へ投入される。次
いでパドル式撹拌翼24及び渦巻式撹拌翼31を有する
撹拌機23で撹拌し、好ましくはすりつぶし、破砕しな
がら、蒸気供給管30より加圧水蒸気が供給され系内が
所定の圧力に保持される。供給された水蒸気は、多孔板
29の下方の位置に開口する蒸気供給管30の噴出孔よ
り噴出し、多孔板29の開口部を通って密閉容器22内
の有機性廃棄物と接触する。得られた蒸解液は導管25
及び26より次工程へ導出される。骨等の蒸解残渣は、
スクリュー270回転によりポールバルブ28より次工
程へ導出される。蒸解装置3内の状態は、密閉容器22
の側面に設けた覗き窓(図示せず)より観察し確認され
る。以上の操作で第1回目の蒸解操作が終わる。Next, a case where the vertical digester shown in FIG. 2 is used will be described. First, organic waste is introduced into the closed container 22 through the pole valve 32 at the top of the closed container 22. Next, the mixture is stirred by a stirrer 23 having paddle-type stirring blades 24 and spiral-type stirring blades 31, preferably grinding and crushing, while pressurized steam is supplied from a steam supply pipe 30 to maintain the inside of the system at a predetermined pressure. The supplied water vapor is ejected from the ejection hole of the steam supply pipe 30 that opens at a position below the perforated plate 29, passes through the opening of the perforated plate 29, and comes into contact with the organic waste in the closed container 22. The obtained cooking liquor is passed through the conduit 25
and 26 to the next step. Cooking residue such as bones, etc.
By rotating the screw 270 times, it is led out from the Paul valve 28 to the next process. The state inside the digester 3 is that of the closed container 22.
It is observed and confirmed through a viewing window (not shown) provided on the side of the machine. With the above operations, the first cooking operation is completed.
内容物の排出を終えた蒸解装置には、必要に応じて、油
分離タンク5内の水層が導入され、再び有機性廃棄物が
投入され、上述した方法に従りて第2回目の蒸解操作が
開始される。After the contents have been discharged, the aqueous layer in the oil separation tank 5 is introduced into the digester as necessary, and organic waste is again fed into the digester for the second cooking process according to the method described above. The operation is started.
次いで、第3図、第4図及び第5図に示す横型蒸解装置
を用いる場合について説明する。先ず、有機性廃棄物が
密閉容器34の上部のポールバルブ33より回転中の回
転能36内へ投入される。投入された有機性廃棄物は、
回転方向に突出した分岐板39により左右の回転能36
内に分配される。次いで蒸気供給管35より加圧水蒸気
を供給し、密閉容器34内を所定の圧力に保つ。供給さ
れた水蒸気は回転能36の開口部を通って回転能36内
に入り有機性廃棄物と接触する。有機性廃棄物は回転能
36の内側に設置されているかき上げ板40により上部
までかき上げられた後落とされるので、撹拌と共に破砕
作用を受けることになる。従って蒸解によってもろくな
った骨等の蒸解残渣は逐次破砕されるので蒸解残渣はほ
とんど残らない。得られた蒸解液は導管38より次工程
へ導出される。蒸解液の導出を終えた蒸解装置3には、
必要に応じて油分離タンク5内の水層が導入され、再び
有機性廃棄物が投入され、上述した方法に従って第2回
目の蒸解操作が開始される。以上回分法で行う場合につ
いて説明したが本発明は連続法によって実施することも
出来る。Next, the case of using the horizontal digester shown in FIGS. 3, 4, and 5 will be described. First, organic waste is introduced into the rotating rotary unit 36 from the pole valve 33 at the top of the closed container 34. The input organic waste is
Left and right rotational ability 36 is achieved by the branch plate 39 protruding in the rotational direction.
distributed within. Next, pressurized steam is supplied from the steam supply pipe 35 to maintain the inside of the closed container 34 at a predetermined pressure. The supplied water vapor enters the rotary chamber 36 through the opening in the rotary chamber 36 and comes into contact with the organic waste. The organic waste is scraped up to the top by a scraping plate 40 installed inside the rotating capacity 36 and then dropped, so that it is subjected to a crushing action as well as stirring. Therefore, the cooking residue such as bones that have become brittle due to cooking is sequentially crushed, so that almost no cooking residue remains. The obtained cooking liquor is led out to the next step through a conduit 38. After the cooking liquid has been discharged, the cooking device 3 includes:
If necessary, the aqueous layer in the oil separation tank 5 is introduced, organic waste is again introduced, and the second cooking operation is started according to the method described above. Although the case where a batch method is used has been described above, the present invention can also be carried out by a continuous method.
本発明で得られた粉体飼料又は肥料の組成は、原料とな
る有機性廃棄物の種類によって異なるが、平均的には蛋
白質38〜B’ OW t%、炭水化物10〜50wt
%、灰分1〜35wt%、油脂分0.5〜5wt%、カ
ルシウム5〜12wt%、水分2〜10wt%程度の粉
体で、そのまま又は添加物を加えた後、粉体のままある
いは任意の形状に整形して、魚、犬、猫、鶏、豚、牛等
の飼料として、あるいは有機質肥料として用いられる。The composition of the powdered feed or fertilizer obtained in the present invention varies depending on the type of organic waste used as a raw material, but on average it contains 38-B' OW t% protein and 10-50 wt% carbohydrates.
%, ash content 1 to 35 wt%, fat and oil content 0.5 to 5 wt%, calcium 5 to 12 wt%, and moisture content of about 2 to 10 wt%. It is shaped into a shape and used as feed for fish, dogs, cats, chickens, pigs, cows, etc., or as organic fertilizer.
特に犬、猫、小鳥、魚等のペット用及び養魚用飼料とし
て適している。It is particularly suitable as feed for pets such as dogs, cats, small birds, and fish, and for fish farming.
(発明の効果)
以上説明したように、本発明は有機性廃棄物を、撹拌下
、加圧水蒸気と直接接触させて蒸解し、次いで噴霧乾燥
を行うという簡単な操作により、従来焼却又は埋設処分
されていた物を飼料又は肥料として利用できるので、未
利用資源の活用という点で産業上価値がある。(Effects of the Invention) As explained above, the present invention enables organic waste to be digested by directly contacting it with pressurized steam under stirring, and then spray-dried. It is industrially valuable in terms of utilizing unused resources, as the waste can be used as feed or fertilizer.
第1図は本発明方法の実施に用いる装置の一例のフロー
シート、第2図は竪型蒸解装置の一例の説明図、第3図
は横型蒸解装置の一例の説明図、第4図は第3図のA−
A矢視図、第5図は第3図に示す分岐板部の拡大斜視図
である。Fig. 1 is a flow sheet of an example of an apparatus used to implement the method of the present invention, Fig. 2 is an explanatory diagram of an example of a vertical digester, Fig. 3 is an explanatory diagram of an example of a horizontal digester, and Fig. 4 is an explanatory diagram of an example of a horizontal digester. A- in Figure 3
The A arrow view and FIG. 5 are enlarged perspective views of the branch plate portion shown in FIG. 3.
Claims (6)
気と接触させて蒸解し、得られた 液層を噴霧乾燥して粉体とすることを特徴 とする有機性廃棄物よりの粉体飼料又は肥 料の製造方法。(1) Organic waste is digested by contacting it with pressurized steam in a closed container with stirring, and the resulting liquid layer is spray-dried to form a powder. A method for producing powdered feed or fertilizer.
とを特徴とする特許請求の範囲第1項記載 の方法。(2) The method according to claim 1, wherein the pressurized steam is 1 to 10 kg/cm^2G.
去したものであることを特徴とす る特許請求の範囲第1項又は第2項記載の 方法。(3) The method according to claim 1 or 2, wherein the liquid layer to be spray-dried is obtained by removing an oil layer by stratification separation.
れた微粒子を含むことを特徴とす る特許請求の範囲第1項又は第2項記載の 方法。(4) The method according to claim 1 or 2, wherein the liquid layer to be spray-dried contains fine particles obtained by crushing the cooking residue.
出口を有する竪型円筒状密閉容器 と、該容器内下部を上下方向に区画する截 頭逆円錐状の多孔板と、多孔板の下方に開 口する水蒸気導入口と、多孔板の上方に設 けられた撹拌翼とを有することを特徴とす る有機性廃棄物の蒸解装置。(5) A vertical cylindrical sealed container having a raw material inlet in the upper part and a cooking liquid outlet and a cooking residue outlet in the lower part, a truncated inverted conical perforated plate that vertically divides the lower part of the container, and a perforated plate. 1. An organic waste digester characterized by having a steam inlet opening downward and a stirring blade provided above a perforated plate.
置に水蒸気導入口を有する横型円 筒状密閉容器と、該容器内に同軸に設けら れた円筒状回転籠と、該籠内壁の軸方向に 沿って設けられたかき上げ板とを有するこ とを特徴とする有機性廃棄物の蒸解装置。(6) A horizontal cylindrical sealed container having a raw material inlet at the top, a cooking liquid outlet at the bottom, and a steam inlet at an arbitrary position, a cylindrical rotating cage provided coaxially within the container, and an axis of the inner wall of the cage. 1. An apparatus for digesting organic waste, comprising a scraping plate provided along the direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62324870A JPH01164787A (en) | 1987-12-21 | 1987-12-21 | Method for manufacturing powder manure or feed from organic waste material and appratus therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62324870A JPH01164787A (en) | 1987-12-21 | 1987-12-21 | Method for manufacturing powder manure or feed from organic waste material and appratus therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01164787A true JPH01164787A (en) | 1989-06-28 |
Family
ID=18170560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62324870A Pending JPH01164787A (en) | 1987-12-21 | 1987-12-21 | Method for manufacturing powder manure or feed from organic waste material and appratus therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01164787A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009172597A (en) * | 2002-11-01 | 2009-08-06 | Comprehensive Resources Recovery & Reuse Inc | Apparatus for treating waste material, system, and method |
JP2012080825A (en) * | 2010-10-12 | 2012-04-26 | Ns Foods:Kk | Apparatus and method for producing pet food, using unused bird and beast |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57196784A (en) * | 1981-05-29 | 1982-12-02 | Seibu Kagaku Kogyo Kk | Manufacture of compost |
JPS6284007A (en) * | 1985-10-08 | 1987-04-17 | Nippon Ham Kk | Plant growth regulator |
-
1987
- 1987-12-21 JP JP62324870A patent/JPH01164787A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57196784A (en) * | 1981-05-29 | 1982-12-02 | Seibu Kagaku Kogyo Kk | Manufacture of compost |
JPS6284007A (en) * | 1985-10-08 | 1987-04-17 | Nippon Ham Kk | Plant growth regulator |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009172597A (en) * | 2002-11-01 | 2009-08-06 | Comprehensive Resources Recovery & Reuse Inc | Apparatus for treating waste material, system, and method |
JP2012080825A (en) * | 2010-10-12 | 2012-04-26 | Ns Foods:Kk | Apparatus and method for producing pet food, using unused bird and beast |
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