JPH0335762A - Preparation of feed-fertilizer - Google Patents
Preparation of feed-fertilizerInfo
- Publication number
- JPH0335762A JPH0335762A JP1116787A JP11678789A JPH0335762A JP H0335762 A JPH0335762 A JP H0335762A JP 1116787 A JP1116787 A JP 1116787A JP 11678789 A JP11678789 A JP 11678789A JP H0335762 A JPH0335762 A JP H0335762A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- cooker
- feed
- raw material
- fertilizer
- 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
Links
- 239000003337 fertilizer Substances 0.000 title claims abstract description 17
- 239000002994 raw material Substances 0.000 claims abstract description 44
- 239000003921 oil Substances 0.000 claims abstract description 29
- 235000019198 oils Nutrition 0.000 claims abstract description 29
- 239000000463 material Substances 0.000 claims abstract description 17
- 241001465754 Metazoa Species 0.000 claims abstract description 12
- 241000251468 Actinopterygii Species 0.000 claims abstract description 10
- 235000015170 shellfish Nutrition 0.000 claims abstract description 10
- 235000021323 fish oil Nutrition 0.000 claims abstract description 4
- 239000010775 animal oil Substances 0.000 claims abstract description 3
- 235000015112 vegetable and seed oil Nutrition 0.000 claims abstract description 3
- 239000008158 vegetable oil Substances 0.000 claims abstract description 3
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 abstract description 10
- 238000007599 discharging Methods 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 210000001519 tissue Anatomy 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 108090000623 proteins and genes Proteins 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 230000003247 decreasing effect Effects 0.000 description 3
- 239000000618 nitrogen fertilizer Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 108010010803 Gelatin Proteins 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- -1 and at the same time Substances 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 150000001728 carbonyl compounds Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000005068 transpiration Effects 0.000 description 1
- 238000009489 vacuum treatment Methods 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
Landscapes
- Fertilizers (AREA)
- Fodder In General (AREA)
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
Description
【発明の詳細な説明】 （イ） 産業上の利用分野 この発明は、飼料・肥料の製造方法に関する。[Detailed description of the invention] (b) Industrial application field The present invention relates to a method for producing feed and fertilizer.
（ロ） 従来の技術
従来、飼料・肥料を製造する方法として、例えば、油温
脱水方法が用いられており、同油温脱水方法は、予め加
熱された油を熱媒体として、クツカー内に投入した動物
、魚介類等の原料を加熱し、さらに、同クツカー内の減
圧処理を行うことにより、原料の脱水処理を行うととも
に、異臭成分をも取り去っていた。(b) Conventional technology Conventionally, as a method for producing feed and fertilizer, for example, an oil temperature dehydration method has been used. By heating raw materials such as animals, seafood, etc., and then applying a vacuum treatment inside the same courier, the raw materials were dehydrated and odor components were also removed.
その後、圧搾機等で処理物を油分と固形物とに分離し、
同固形物より飼料や肥料等を製造していた。After that, the processed material is separated into oil and solids using a compressor, etc.
Feed, fertilizer, etc. were manufactured from the solids.
しかも、その操作は、クツカー内に大量の原料を投入し
て加熱、減圧処理を行い、大量の飼料・肥料を製造して
いた。Moreover, this operation involved putting a large amount of raw materials into the feeder, heating and depressurizing them, and producing large amounts of feed and fertilizer.
（ハ） 発明が対決しようとする課題
ところが、かかる油温脱水方法でもって飼料・肥料を製
造する場合、大量の原料をクツカー内へ投入するため、
大量の原料によってクツカー内の熱媒体としての油の温
度が低下し、その為に、原料から含水分の分離蒸散がし
にくくなって、処理時間をも非常に長くかかっていた。(c) The problem that the invention attempts to confront is that when producing feed and fertilizer using the oil temperature dehydration method, a large amount of raw materials are put into the feeder.
The large amount of raw materials lowers the temperature of the oil, which serves as a heat medium in the courier, making it difficult to separate and evaporate moisture from the raw materials, and the processing time is extremely long.
（ニ） 課題を対決するための手段
本発明では、クツカー内に収容した動物、魚貝類等の原
料を、予め加熱された魚油、植物油、動物油等の熱媒体
によって加熱して、上記加工残滓物を蒸散すると共に、
同クツカーの減圧処理により脱水した後、圧搾機等によ
って油分と処理物とに分離させてなる飼料・肥料製造方
法において、同クッカーの投入口及び排出口に開閉弁を
設けて、同開閉弁によって、原料を少量ずつクツカーに
供給すると共に、同クッカーより処理物を少量ずつ取出
すことを特徴とする飼料・肥料製造方法を提供せんとす
るものである。(d) Means for Confronting the Problems In the present invention, raw materials such as animals, fish and shellfish housed in a cutter are heated with a heat medium such as fish oil, vegetable oil, or animal oil that has been heated in advance, and the processing residues described above are heated. Along with transpiring,
In the feed/fertilizer manufacturing method in which the water is dehydrated by the reduced pressure treatment of the cooker and then the oil and the processed material are separated using a press or the like, an on-off valve is provided at the inlet and the outlet of the cooker, and the on-off valve is It is an object of the present invention to provide a method for producing feed and fertilizer, which is characterized in that raw materials are fed into a cooker in small quantities and processed materials are taken out in small quantities from the cooker.
（ホ） 作用及び効果
この発明では、クツカーの投入口の開閉弁を開閉させる
ことによって、投入口より、少量づつ動物、魚貝類等の
原料をクツカー内へ投入し、そして、クツカー内へ予め
供給された熱媒体たる油の温度の低下を防止することが
できる。(E) Functions and Effects In this invention, by opening and closing the opening/closing valve of the input port of the bagger, raw materials such as animals, fish and shellfish are introduced into the bagger little by little from the input port, and then supplied into the bagger in advance. It is possible to prevent the temperature of oil, which is a heat medium, from decreasing.
そのために、クツカー内にて処理される動物、魚貝類等
の原料から常に一定量の水分を分離蒸散させることがで
き、さらにこの発明では、クツカーの投入口の開閉弁を
開閉させることによって、投入口より、少量づつ動物、
魚貝類等の原料をクツカー内へ投入し、そして、クツカ
ー内へ予め供給された熱媒体たる油の温度の低下を防止
することができる。Therefore, it is possible to always separate and evaporate a certain amount of water from the raw materials such as animals, fish and shellfish that are processed in the cutter. Animals, taken by mouth in small quantities,
Raw materials such as fish and shellfish can be put into the cooker, and the temperature of oil, which is a heat medium, supplied into the cooker in advance can be prevented from decreasing.
そのために、クツカー内にて処理される動物、魚貝類等
の原料から常に一定量の水分を分離蒸散させることがで
き、さらに１、原料の処理時間を短くすると共に、処理
された蛋白飼料・窒素肥料を含水分の少ない高品質なも
のにすることができまた、クツカーの排出口の開閉弁を
開閉させて、少量づつ処理物を取り出すことにより、連
続的に処理物をクツカー内より回収できる。Therefore, it is possible to always separate and evaporate a certain amount of moisture from the raw materials such as animals, fish and shellfish processed in the Kutsuka. The fertilizer can be made into a high-quality fertilizer with low moisture content, and the treated material can be continuously collected from the inside of the picker by opening and closing the on-off valve at the outlet of the picker and taking out the processed material little by little.
（へ） 実施例
本考案の実施例を図面にもとづき詳説すれば、第１図及
び第２図は、本発明の飼料、肥料製造方法を実施する製
造装置を示したものであり、同製造装置（＾）は、原料
コンテナとクツカーと圧搾機等よりなり、（１）は、原
料コンテナで、食品工場、料理店、家庭等のから排出さ
れる原料としての魚貝類、動物肉等を収納している。(f) Example An example of the present invention will be described in detail based on the drawings. Figures 1 and 2 show a manufacturing apparatus for carrying out the method for manufacturing feed and fertilizer of the present invention. (^) consists of a raw material container, a squeezer, a compressor, etc., and (1) is a raw material container that stores raw materials such as fish, shellfish, and animal meat discharged from food factories, restaurants, homes, etc. ing.
この原料コンテナ（１）は、スキップホイスト（２）で
もって上方向へ引き揚げられ、原料ホッパー（３）の真
上で反転させ、原料を原料ホッパー（３）へ収納する。This raw material container (1) is lifted upward by a skip hoist (2), is turned over right above the raw material hopper (3), and the raw material is stored in the raw material hopper (3).
次に、原料ホッパー（３）に設けた投入口（３ａ）には
、クツカーの投入パイプ（４〉を介してクツカーを連通
しており、同パイプ〈４）の上下部に、開閉弁としての
プレートバルブ（５ａ） （５ｂ）を一定の間隔をあけ
て取付けている。Next, the feed port (3a) provided in the raw material hopper (3) is connected to the feeder via the feeder pipe (4). Plate valves (5a) and (5b) are installed at regular intervals.
第３ａ図及び第３ｂ図は、このプレートバルブ（５ａ）
（５ｂ）の操作を示したものであり、第３ａ図に示す
ように、まず、下部のプレートバルブ（５ｂ）を閉じ、
上部のプレートバルブ（５ａ）を開き、投入パイプ（４
）内へ原料（Ａ）を落下し、さらに、第３ｂ図に示した
ように、上部のプレートバルブ（５ａ）を閉じ、下部の
プレートバルブ〈５ｂ〉を開き、投入パイプ（４）へ落
し込まれたＦＡ料をクツカー内に投入する。Figures 3a and 3b show this plate valve (5a)
(5b), as shown in Figure 3a, first close the lower plate valve (5b),
Open the upper plate valve (5a) and insert the input pipe (4).
), and as shown in Figure 3b, close the upper plate valve (5a), open the lower plate valve <5b>, and drop the raw material (A) into the input pipe (4). Insert the FA fee received into the cutter.
また、第３ａ図に示すように、下部のプレートバルブ（
５ｂ）を閉じ、上部のプレートバルブ（５ａ）を開き、
原料ホッパー（３）より投入パイプ（４〉内へ原料を落
下させる。In addition, as shown in Figure 3a, the lower plate valve (
5b) and open the upper plate valve (5a).
The raw material is dropped from the raw material hopper (3) into the input pipe (4>).
このように、上記のバルブ操作を繰り返して、クツカー
内へ少量づつ、定量の原料をクツカー内に投入するよう
に構成している。In this way, the above-mentioned valve operation is repeated to feed a fixed amount of raw material into the picker little by little.
さらに、投入量を設定する場合、上下部のプレートバル
ブ（５ａ）及び（５ｂ〉の間隔を変え、また投入バイブ
（４）の径等を変えることによりその調節を行うことが
できる。Furthermore, when setting the injection amount, it can be adjusted by changing the interval between the upper and lower plate valves (5a) and (5b>), and by changing the diameter of the injection vibrator (4).
また、投入バイブ（４）に取り付けるバルブもプレート
バルブに制限する必要もなく、ロータリーバルブや電磁
弁等各種のバルブを使用できる。Further, the valve attached to the input vibrator (4) does not need to be limited to a plate valve, and various valves such as a rotary valve and a solenoid valve can be used.
次に、クツカーの構造について説明すると、第２図に示
すように、本実施例は、クツカーを第１クツカー（６）
と第２クツカー〈７）とより形成しており、第１クツカ
ー（６〉内で油温減圧処理した原料を連結管（８）より
第２クツカー（７）に搬送し、同クツカー（７）で再び
油温・減圧処理を行うように構成している。Next, to explain the structure of the puller, as shown in FIG.
and a second extractor (7), and the raw material subjected to oil temperature and pressure reduction treatment in the first extractor (6) is conveyed to the second extractor (7) through the connecting pipe (8), and then transferred to the second extractor (7). The structure is such that the oil temperature and pressure reduction process is performed again.
本実施例では、第１クツカー（６）及び第２クツカー（
７）を、直径５００叩、長さ４０００ ｎｖ＋に形成し
ており、しかも、支持台（Ｍ）を介【２てそれぞれ後方
に向けて上り勾配とした傾斜状に配置すると共に、第１
クツカー（６）の後部に設けた排出口の真下に第２クツ
カー〈７）の投入口を配設し、搬送連結管（８）に連通
連結している。In this embodiment, the first picker (6) and the second picker (
7) is formed to have a diameter of 500 nv+ and a length of 4000 nv+, and is arranged in an upward slope toward the rear via the support stand (M).
The input port of the second picker (7) is provided directly below the outlet provided at the rear of the picker (6), and is connected to the conveying connecting pipe (8).
そして、第１クツカー（６）と第２クツカー（７）との
後部には、熱媒体としての加熱油を収納するための給油
口（６ａ） （７ａ）を設け、同給油口（６ａ） （７
ａ）にオイルポンプ（Ｐ）を介してオイルタンク（Ｔ）
を接続している。At the rear of the first puller (6) and the second puller (7), oil filler ports (6a) (7a) for storing heating oil as a heat medium are provided. 7
a) Oil tank (T) via oil pump (P)
are connected.
かかる第１クツカー（６〉には、真空ポンプ（Ｓ）を連
結しており、オイルタンク（Ｔ）より予め９５℃以上に
加熱された加熱油を入れて、原料（ａ）を加熱しながら
同クツカー（６）内を１０〜２０ｍｍ１１ｇに減圧して
原料（ａ）の油温処理を行う。A vacuum pump (S) is connected to the first picker (6), and heating oil preheated to 95°C or higher is poured from an oil tank (T) to the same while heating the raw material (a). The pressure inside the cutter (6) is reduced to 10 to 20 mm and 11 g, and the raw material (a) is subjected to oil temperature treatment.
さらに、第１クツカー（６）内には、回転自在とした撹
拌羽根（９）を収納しており、同羽根（９）によって油
と原料（ａ）とを撹拌し菟しかも処理された原料（ａ）
を同クツカー（６）内の後部方向へ輸送し、排出口に取
付けた搬送連結管（８）より第２クツカー（７〉へ搬送
される。Furthermore, a rotatable stirring blade (9) is housed in the first extractor (6), and the blade (9) stirs the oil and the raw material (a). a)
is transported toward the rear of the same picker (6), and is conveyed to the second picker (7>) through a transport connecting pipe (8) attached to the discharge port.
本実施例では、撹拌羽根（９）を第１クツカー内に回転
軸（９ａ〉を回転自在に架設し、同回転輔（９ａ）に螺
旋状に多数の羽根（９ｂ）を取付けている。In this embodiment, a stirring blade (9) is rotatably installed on a rotating shaft (9a) in a first picker, and a large number of blades (9b) are spirally attached to the rotating shaft (9a).
また、かかる回転軸（９ａ）の一端には、モーター（ｍ
）を取付け、同モーター（ａ）によって回転羽根を回転
させ、原料（ａ）の撹拌と搬送を行うように構成してい
る。Further, at one end of the rotating shaft (9a), a motor (m
) is attached, and the rotating blade is rotated by the motor (a) to stir and transport the raw material (a).
また、かかる第２クツカー（７）は、上記の第１クツカ
ー（６〉と同様に形成されており、オイルタンク（Ｔ）
より予め９５℃以上に加熱された加熱油を入れて、原料
（ａ）を加熱しながら真空ポンプ（Ｓ）によって７４０
〜７６０ ｍ＋１１１ｇに減圧するように構成している
。さらに、第２クツカー（７）に設けた撹拌羽根（９）
によって同クツカーの原料（ａ）をクツカー（７）の後
部に搬送するようにしている。Further, the second puller (7) is formed in the same manner as the first puller (6>), and the oil tank (T)
740°C using a vacuum pump (S) while heating the raw material (a) by adding heated oil preheated to 95°C or higher.
It is configured to reduce the pressure to ~760 m + 111 g. Furthermore, the stirring blade (9) provided on the second puller (7)
The raw material (a) of the picker is conveyed to the rear of the picker (7).
そして、かかるクツカー（８）（７）内の原料（ａ）は
、加熱油が組織中に浸透し、組織内部を均一に加熱して
、組織自体は、約９０〜１００℃に保持され、しかも、
組織内部が加熱されていくと、自己保有水分は脱水され
ていき、含水率が６％以下となる。The heating oil penetrates into the tissue of the raw material (a) in the cutter (8) (7), uniformly heating the inside of the tissue, and maintaining the tissue itself at about 90 to 100°C. ,
As the inside of the tissue is heated, the self-retained water is dehydrated, and the water content becomes 6% or less.
さらに、組織そのものが熱変性により破壊されて、水分
と共に揮発性化合物、例えば、カルボニル化合物、トリ
メチルアミン、アンモニア等を蒸散分離し、同時に組織
中のゼラチン、水溶性蛋白質は熱変性を生じて凝固して
、その流出を防止す゛る。Furthermore, the tissue itself is destroyed by thermal denaturation, and volatile compounds such as carbonyl compounds, trimethylamine, ammonia, etc. are evaporated and separated along with water, and at the same time, gelatin and water-soluble proteins in the tissue are thermally denatured and coagulated. , prevent its leakage.
本実施例では、第２クツカー（７）内を、上記のように
高い減圧状態に調整しているため、原料（ａ）の内部ま
で圧力が作用し、同時に含水骨の分離、蒸散が円滑に行
われるようになって、原料中の含水率を均一分布で低率
な状態に調整できるものである。In this example, the inside of the second extractor (7) is adjusted to a highly reduced pressure state as described above, so that the pressure is applied to the inside of the raw material (a), and at the same time, the separation and transpiration of the hydrated bones are facilitated. By doing so, it is possible to adjust the moisture content in the raw materials to a uniformly distributed and low level state.
このように、第１クツカー（８）と第２クツカー（７〉
とを連結管〈８）でもって連通連結し、原料（ａ）を投
入口（３ａ〉より少量づつ定量に調整しながら投入する
ことにより、連続的に油温減圧処理を行うようにしてい
る。In this way, the first kutskar (8) and the second kutskah (7)
They are connected to each other by a connecting pipe (8), and the raw material (a) is fed into the feed port (3a) in small amounts at a constant rate, thereby continuously performing oil temperature and pressure reduction treatment.
次に、第２クツカー（７）の後部には、排出口を設け、
同排出口に排出バイブ（１０）を介してスクリューコン
ベア（１２）の基端部（１２ａ）に連結し、上記排出バ
イブ（ＬＯ〉には、その上下部に、それぞれ開閉弁とし
てのプレートバルブ（Ｌｌａ）及び（ｆｌｂ）を設けて
いる。Next, a discharge port is provided at the rear of the second puller (7),
The discharge port is connected to the proximal end (12a) of the screw conveyor (12) via a discharge vibrator (10), and the discharge vibrator (LO) has plate valves (12a) as opening/closing valves at the upper and lower portions thereof, respectively. Lla) and (flb) are provided.
かかるプレートバルブ（ｌｌａ）（ｌｌｂ）は、前記し
た第１クツカー（６）の投入バイブ（４）に設けたブレ
−トバルブ（５ａ） （５ｂ）と同じ作用をさせるもの
であり、第２クツカー（７）内の処理物をプレートバル
ブ（ｌｌａ）（ｌｌｂ）を交互に開閉させて、少量づつ
抜き取り、スクリューコンベア（１２）へ落下させるも
のである。These plate valves (lla) (llb) have the same effect as the plate valves (5a) (5b) provided on the input vibrator (4) of the first puller (6) described above, and are used in the second puller (6). By alternately opening and closing the plate valves (lla) and (llb), the processed material in 7) is taken out little by little and dropped onto the screw conveyor (12).
スクリューコンベア（１２）は、第２図に示すように、
急傾斜に設置し、この傾斜角度を利用して回収物から油
を分散流下させるように構成している。As shown in Fig. 2, the screw conveyor (12)
It is installed on a steep slope and is configured to use this angle of inclination to disperse and flow down the oil from the recovered material.
そして、スクリューコンベア（１２）の先端部（１２ｂ
）には、連結シュート（１３）を垂設して中間ホッパー
（１４）を連結し、更に、この中間ホッパー（１４）よ
りスクリューコンベア（１５） （１６）を介設して遠
心分離機（１７）に連結させ、ここで処理物中の油分を
分離するものである。Then, the tip (12b) of the screw conveyor (12)
), a connecting chute (13) is installed vertically to connect the intermediate hopper (14), and screw conveyors (15) and (16) are interposed from the intermediate hopper (14) to connect the centrifuge (17). ), where the oil in the processed material is separated.
そして、遠心分離機（１７）からのスクリューコンベア
（１８）より固形分を取出して、蛋白飼料・窒素肥料を
製造する。Then, the solid content is taken out from the centrifuge (17) through the screw conveyor (18) to produce protein feed and nitrogen fertilizer.
上記のような構造の製造装置（Ａ）を利用して製造した
蛋白飼料及び窒素肥料中には、蛋白７０〜８０％程度が
含まれ、含水分も４〜６％、含油性６〜８％と高品質の
製品として回収することができる。The protein feed and nitrogen fertilizer produced using the production equipment (A) with the above structure contain approximately 70 to 80% protein, have a water content of 4 to 6%, and an oil content of 6 to 8%. and can be recovered as high-quality products.
以上、本発明によれば、第１クツカー（６）と第２クツ
カー（７〉とを連結し、投入パイプ（４）及び排出バイ
ブ（ｌＯ）へそれぞれ二重のバルブを取り付け、このバ
ルブの開閉操作によって原料（ａ）の投入を連続的に少
量づつ調整できるようにし、同時に、処理物の排出量も
同様に連続的に少量ずつ調整できるようにしている。As described above, according to the present invention, the first puller (6) and the second puller (7>) are connected, double valves are attached to the input pipe (4) and the discharge vibe (lO), and the valves are opened and closed. The input of raw material (a) can be continuously adjusted in small amounts by operation, and at the same time, the amount of discharged material to be treated can also be adjusted continuously in small amounts.
かかる方法により、第１クツカー（６）の投入口（３ａ
〉の開閉弁を開閉させることによって、投入口（３ａ）
より、少量づつ動物、魚貝類等の原料を第１クツカー（
６）内へ投入し、また、第２クツカー（７）に搬送し、
そして、各クツカー（６） （７）内へ予め供給された
熱媒体たる油の温度の低下を防止することができる。By this method, the input port (3a) of the first picker (6)
> By opening and closing the on-off valve, the inlet (3a)
Then, raw materials such as animals, fish and shellfish are added in small quantities to the first cutter (
6) into the container and transport it to the second picker (7),
In addition, it is possible to prevent the temperature of the oil, which is a heat medium, supplied in advance into each shoemaker (6) and (7) from decreasing.
そのために、各クツカー（６）（７）内にて処理される
動物、魚貝類等の原料から常に一定量の水分を分離蒸散
させることができ、さらに、原料の処理時間を短くする
と共に、処理された蛋白飼料・窒素肥料を含水分の少な
い高品質なものにすることができる
また、第２クツカー（７）の排出口の開閉弁を開閉させ
て、少量づつ処理物を取り出すことにより、連続的に処
理物を同クツカー（７）内より回収できる。Therefore, it is possible to always separate and evaporate a certain amount of water from the raw materials such as animals, fish and shellfish that are processed in each cutter (6) and (7). The processed protein feed and nitrogen fertilizer can be made into high-quality products with low moisture content.In addition, by opening and closing the opening/closing valve of the outlet of the second feeder (7) and taking out the processed material in small quantities, it is possible to continuously The processed material can be recovered from the same picker (7).
第１図及び第２図は、それぞれ本発明の飼料・肥料製造
方法の装置を示した平面図及び側面図。
第３ａ図及び第３ｂ図は、本発明方法の要部を示した開
閉弁の操作説明図。
（＾）：製造装置
（６）：第１クツカー
（７）：第２クツカーFIG. 1 and FIG. 2 are a plan view and a side view, respectively, showing an apparatus for the feed/fertilizer manufacturing method of the present invention. Figures 3a and 3b are explanatory diagrams for explaining the operation of the on-off valve, showing the main parts of the method of the present invention. (^): Manufacturing equipment (6): 1st shoemaker (7): 2nd shoemaker
Claims (1)
め加熱された魚油、植物油、動物油等の熱媒体によって
加熱して、上記加工残滓物を蒸散すると共に、同クッカ
ーの減圧処理により脱水した後、圧搾機等によって油分
と処理物とに分離させてなる飼料・肥料製造方法におい
て、同クッカーの投入口及び排出口に開閉弁を設けて、
同開閉弁によって、原料を少量ずつクッカーに供給する
と共に、同クッカーより処理物を少量ずつ取出すことを
特徴とする飼料・肥料製造方法。1) Raw materials such as animals, fish and shellfish housed in a cooker are heated with a heat medium such as fish oil, vegetable oil, or animal oil that has been heated in advance to evaporate the processing residues and dehydrated by depressurization treatment in the same cooker. After that, in the feed/fertilizer production method in which the oil and the processed material are separated using a press or the like, an on-off valve is provided at the input and output ports of the cooker,
A feed/fertilizer manufacturing method characterized by supplying raw materials to a cooker in small quantities and taking out processed materials from the cooker in small quantities using the same on-off valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1116787A JP2799349B2 (en) | 1989-05-09 | 1989-05-09 | Feed production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1116787A JP2799349B2 (en) | 1989-05-09 | 1989-05-09 | Feed production method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0335762A true JPH0335762A (en) | 1991-02-15 |
| JP2799349B2 JP2799349B2 (en) | 1998-09-17 |
Family
ID=14695692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1116787A Expired - Fee Related JP2799349B2 (en) | 1989-05-09 | 1989-05-09 | Feed production method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2799349B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61137312A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Electrode paste |
| JPS61137310A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Electrode material |
| JPS61137311A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Conductive paste |
| JPS61139017A (en) * | 1984-12-11 | 1986-06-26 | 松下電器産業株式会社 | Electrode material |
| JP2008285589A (en) * | 2007-05-17 | 2008-11-27 | Sekisui Chem Co Ltd | Resin composition, conductive paste, and ceramic paste |
| US7569166B2 (en) | 2003-06-26 | 2009-08-04 | Sekisui Chemical Co., Ltd. | Binder resin for coating paste |
| KR20110087209A (en) | 2008-11-13 | 2011-08-02 | 세키스이가가쿠 고교가부시키가이샤 | Polyvinyl acetal resin composition |
| US8701359B2 (en) | 2006-04-27 | 2014-04-22 | Jeffrey Alan Packer | Cast structural connectors |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6066943A (en) * | 1983-09-19 | 1985-04-17 | Kazuo Ukimura | Preparation of feed for animal, fish and shellfish |
| JPS61239846A (en) * | 1985-04-12 | 1986-10-25 | Shuzo Nakazono | Treatment for fat meat |
| JPS63126463A (en) * | 1986-11-14 | 1988-05-30 | Shuzo Nakazono | Production of feed for pisciculture |
-
1989
- 1989-05-09 JP JP1116787A patent/JP2799349B2/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6066943A (en) * | 1983-09-19 | 1985-04-17 | Kazuo Ukimura | Preparation of feed for animal, fish and shellfish |
| JPS61239846A (en) * | 1985-04-12 | 1986-10-25 | Shuzo Nakazono | Treatment for fat meat |
| JPS63126463A (en) * | 1986-11-14 | 1988-05-30 | Shuzo Nakazono | Production of feed for pisciculture |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61137312A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Electrode paste |
| JPS61137310A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Electrode material |
| JPS61137311A (en) * | 1984-12-10 | 1986-06-25 | 松下電器産業株式会社 | Conductive paste |
| JPH0449766B2 (en) * | 1984-12-10 | 1992-08-12 | Matsushita Electric Ind Co Ltd | |
| JPH0449768B2 (en) * | 1984-12-10 | 1992-08-12 | Matsushita Electric Ind Co Ltd | |
| JPH0449767B2 (en) * | 1984-12-10 | 1992-08-12 | Matsushita Electric Ind Co Ltd | |
| JPH0449769B2 (en) * | 1984-12-11 | 1992-08-12 | Matsushita Electric Ind Co Ltd | |
| JPS61139017A (en) * | 1984-12-11 | 1986-06-26 | 松下電器産業株式会社 | Electrode material |
| US7569166B2 (en) | 2003-06-26 | 2009-08-04 | Sekisui Chemical Co., Ltd. | Binder resin for coating paste |
| US8701359B2 (en) | 2006-04-27 | 2014-04-22 | Jeffrey Alan Packer | Cast structural connectors |
| JP2008285589A (en) * | 2007-05-17 | 2008-11-27 | Sekisui Chem Co Ltd | Resin composition, conductive paste, and ceramic paste |
| KR20110087209A (en) | 2008-11-13 | 2011-08-02 | 세키스이가가쿠 고교가부시키가이샤 | Polyvinyl acetal resin composition |
| US8431047B2 (en) | 2008-11-13 | 2013-04-30 | Sekisui Chemical Co., Ltd. | Polyvinyl acetal resin composition |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2799349B2 (en) | 1998-09-17 |
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