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JP4911750B2 - Active ingredient extraction method and waste reduction method from food waste, active ingredient extraction device and waste reduction device - Google Patents

Active ingredient extraction method and waste reduction method from food waste, active ingredient extraction device and waste reduction device Download PDF

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JP4911750B2
JP4911750B2 JP2005285782A JP2005285782A JP4911750B2 JP 4911750 B2 JP4911750 B2 JP 4911750B2 JP 2005285782 A JP2005285782 A JP 2005285782A JP 2005285782 A JP2005285782 A JP 2005285782A JP 4911750 B2 JP4911750 B2 JP 4911750B2
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栄一 岩本
正人 笠森
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Description

本発明は食品廃棄物(例えば、おから、酒かすなどの製品精製後の残物)中に含まれているアミノ酸などの有効成分を抽出する為の方法及び廃棄物の減量方法であり、又有効成分抽出装置及び廃棄物の減量装置に関するものである。   The present invention is a method for extracting active ingredients such as amino acids contained in food waste (for example, residue after product purification such as okara and sake lees) and a method for reducing waste. The present invention relates to an active ingredient extraction device and a waste reduction device.

食品メーカーなどからは多くの廃棄物が排出され、これの処理方法に関して色々な技術が提案されている。例えば、特開2005−111385号に係る「食品廃棄物の処理方法」は、食品廃棄物の処理時間を短縮することが出来るもので、固体状の食品廃棄物と液体状の食品廃棄物とが混在する食品廃棄物に澱粉質を添加した後、発酵菌を含有する菌床に混入して食品廃棄物を発酵させ、発酵の際に発生する発酵熱で澱粉質をアルファー化させると共に、発酵熱で食品廃棄物に残存する水分を蒸発させる技術である。   A lot of waste is discharged from food manufacturers, and various techniques have been proposed for the processing method. For example, “Food waste processing method” according to Japanese Patent Application Laid-Open No. 2005-111385 can shorten the processing time of food waste, and solid food waste and liquid food waste After adding starch to the mixed food waste, it is mixed with the bacterial bed containing the fermenting bacteria to ferment the food waste, and the starch is alphatized by the fermentation heat generated during fermentation, and the fermentation heat In this technology, the water remaining in food waste is evaporated.

特開2001−334245号に係る「食品廃棄物の処理方法及び装置」は、非可食部分の分解精度及び可食部分の回収率を向上し、回収可食分を肥料として利用可能とする。このように、食品廃棄物(例えば、おから、酒かすなど製品精製後の残物)を産業廃棄物として処理していたが、これらの廃棄物の中にもアミノ酸などの有効成分が相当量含まれており、単一食品中からの抽出は安定した組成の有効成分を取り出すことができ為に有益とされている。   “Food waste processing method and apparatus” according to Japanese Patent Application Laid-Open No. 2001-334245 improves the decomposition accuracy of the non-edible part and the recovery rate of the edible part, and makes the recovered edible part available as a fertilizer. In this way, food waste (for example, residue from refined products such as okara and sake lees) was treated as industrial waste, but there are considerable amounts of active ingredients such as amino acids in these wastes. It is included, and extraction from a single food is beneficial because it can extract an active ingredient having a stable composition.

ところで、密閉容器に食品廃棄物と水を適量入れ常温の状態から一定温度に触媒中で昇温し、高圧高温水下で一定時間保持後冷却し、常温に到達後開封して有効成分の抽出を行っており、温度帯による抽出物の判断がつかないと同時に、廃棄物と水は常に接触しており多量の溶液の中からの必要な成分を抽出しなくてはならない。   By the way, we put food waste and water in appropriate quantities in a sealed container, raised the temperature in the catalyst from room temperature to a certain temperature, held it under high pressure and high temperature water for a certain period of time, cooled it, and opened it after reaching room temperature to extract the active ingredients. At the same time, the extract cannot be judged by the temperature zone, and at the same time, the waste and water are always in contact with each other, and necessary components must be extracted from a large amount of solution.

又、蒸気発生器からの高温蒸気を食品廃棄物に直接散布し、該蒸気の凝縮液を採集して抽出物を取り出す方法も知られている。しかし、この方法は廃棄物の試料温度が目的温度に到達する間、高温蒸気を照射しなければならず、抽出物は参考成分にしかなかった。   A method is also known in which high-temperature steam from a steam generator is directly sprayed on food waste, and a condensate of the steam is collected to extract an extract. However, this method had to irradiate high temperature steam while the waste sample temperature reached the target temperature, and the extract was only a reference component.

さらに、食品廃棄物と水を高圧圧入できる粘度に調整した混合物を、高圧ポンプで細長いチューブに圧入し、その道中にヒーターと冷却装置を取り付け連続的に混合物として加工し、最後に遠心分離器で有効成分を抽出する方法がある。しかし、この方法では試料に対する有効成分抽出比率が低く、又熱エネルギー消費が高いため、有効成分抽出装置としては不向きである。   Furthermore, the mixture adjusted to a viscosity that allows high pressure injection of food waste and water is pressed into a long and narrow tube with a high-pressure pump, a heater and a cooling device are installed in the path, and the mixture is continuously processed. Finally, a centrifuge is used. There are methods for extracting active ingredients. However, this method is not suitable as an active ingredient extraction apparatus because the active ingredient extraction ratio with respect to the sample is low and the heat energy consumption is high.

特開2004−65184号に係る「食品廃棄物利用の良質タンパク回収方法」は、廃棄パンなどの食品廃棄物を効率的に処理することが出来、上水や酵素の必要量を低減でき、食品廃棄物以外の余分な原料を必要とせず、均質かつ良質のタンパクを回収することが出来る食品廃棄物利用の良質タンパク回収方法である。
特開2005−111385号に係る「食品廃棄物の処理方法」 特開2001−334245号に係る「食品廃棄物の処理方法及び装置」 特開2004−65184号に係る「食品廃棄物利用の良質タンパク回収方法」
Japanese Patent Application Laid-Open No. 2004-65184, “High quality protein recovery method using food waste” can efficiently process food waste such as waste bread, can reduce the necessary amount of water and enzymes, It is a high quality protein recovery method using food waste that can recover homogeneous and high quality protein without requiring extra raw materials other than waste.
“Method for treating food waste” according to JP-A-2005-111385 "Method and apparatus for treating food waste" according to JP 2001-334245 A “High quality protein recovery method using food waste” according to Japanese Patent Application Laid-Open No. 2004-65184

このように従来の有効成分抽出装置には上記のごとき問題がある。本発明が解決しようとする課題はこれら問題点であり、高温高圧下で目的温度での有効成分を浪費なく、効率よく抽出することが出来る方法及び装置を提供する。一方、この装置で処理された後の廃棄物の重量が大幅に減量する方法及び装置を提供する。   As described above, the conventional active ingredient extraction apparatus has the above-described problems. The problems to be solved by the present invention are these problems, and provide a method and apparatus capable of efficiently extracting an active ingredient at a target temperature under high temperature and high pressure without wasting. On the other hand, the present invention provides a method and an apparatus in which the weight of waste after being processed by this apparatus is greatly reduced.

本発明に係る食品廃棄物からの有効成分抽出装置は、蒸気発生容器(高温高圧容器)中に食品廃棄物を特殊容器に充填して蓋をし、ボルト等で封止した後、食品廃棄物が浸水しない水位まで容器に高圧ポンプで給水を行う。その後容器外壁よりヒーターで加熱を行う。目的温度に達した後、水蒸気を廃棄物に当てながら抽出弁を解放する場合と、徐々に水位を上昇させて蒸気発生容器内に配置した上記特殊容器の上部開口から流入して廃棄物に高温高圧水を当てて排出する場合とが有り、目的に応じて選択出来る。
The apparatus for extracting an active ingredient from food waste according to the present invention fills a special container with the food waste in a steam generation container (high temperature and high pressure container) , covers it, seals it with bolts, etc. Water is supplied to the container with a high-pressure pump until the water level is not submerged. Thereafter, heating is performed from the outer wall of the container with a heater. After reaching the target temperature, the extraction valve is released while water vapor is applied to the waste, and when the water level is gradually raised and flows from the upper opening of the special container placed in the steam generation container, the waste becomes hot. There are cases where high pressure water is applied and discharged, and it can be selected according to the purpose.

特に水蒸気を照射する場合は廃棄物の減量に効果が有り、高温高圧水を経由する場合は有効成分を抽出する場合に効果がある。試料内部の有効成分が期待できる廃棄物は高温高圧水で処理し、有効成分がさほど期待できない廃棄物は水蒸気で減量するように目的に応じて処理が可能となる。有効成分を含んだ高温高圧水は間接冷却管で冷却されて採集される。また容器から放出された水蒸気は、間接冷却管内を経由し凝縮液となり採集される。   In particular, irradiation with water vapor is effective in reducing the amount of waste, and when passing through high-temperature and high-pressure water, it is effective in extracting active ingredients. Waste that can be expected to have an active ingredient in the sample is treated with high-temperature and high-pressure water, and waste that cannot be expected to have so much active ingredient can be treated according to the purpose so as to be reduced with water vapor. The high-temperature and high-pressure water containing the active ingredient is cooled and collected by an indirect cooling pipe. The water vapor released from the container is collected as a condensate via the indirect cooling pipe.

ヒーターは2段構造に配置され、容器の下層部と上層部を別々に加熱する構造となっている。熱量負荷や液量に応じて、加熱方法は下層部と上層部のヒーターを使い分けることが可能である。そこで容器に給水された水は発生蒸気と共に容器外に放出され、容器内の水位は低下する。本装置では水位センサーで水位を検知し高圧ポンプで容器内に給水でき温度低下が極力少なくなるように配管中に予熱ヒーターを取付け、高圧ポンプの吐出量を加減することができる。   The heater is arranged in a two-stage structure, and has a structure in which the lower layer part and the upper layer part of the container are heated separately. Depending on the heat load and the amount of liquid, the heating method can use different heaters for the lower layer and the upper layer. Therefore, the water supplied to the container is released out of the container together with the generated steam, and the water level in the container is lowered. In this device, the water level can be detected by a water level sensor, and water can be supplied into the container with a high pressure pump, so that a preheating heater can be attached in the pipe so that the temperature drop is minimized, and the discharge amount of the high pressure pump can be adjusted.

また水蒸気として容器外にバルブによって放出された気体又は高温水は、取り出し口手前で冷却装置により凝縮又は冷却され、低い温度の液体として取り出し、抽出物の蒸発及び昇華を防止することができる。抽出物輸送管は冷却による凝結により、抽出物の堆積、スケール化で抽出中の有効成分の混入や輸送管の冷却効果低下などにより、定期的に洗浄する必要がある。本装置では高圧ポンプからの吐出液を利用し、抽出途中でも輸送管内を洗浄することができる。   Further, the gas or high-temperature water released as water vapor by the valve outside the container is condensed or cooled by the cooling device before the take-out port and taken out as a low-temperature liquid to prevent evaporation and sublimation of the extract. It is necessary to clean the extract transport pipe periodically by condensation due to cooling, accumulation of the extract, mixing of active ingredients during extraction by scaling, and a decrease in the cooling effect of the transport pipe. In this apparatus, the discharge pipe from the high-pressure pump can be used to clean the inside of the transport pipe even during extraction.

食品廃棄物を高温高圧容器に充填し、制御された温度の水蒸気を定時間照射することにより、目的とするアミノ酸、有機酸等の有効抽出が可能である。
又、食品廃棄物を高温高圧容器に充填し、処理条件で有効成分を抽出した後の食品廃棄物は重量が減少し、処理前の約4割に減量されたことからも、廃棄物処理にかかる負担を軽減することが出来る。
By filling food waste into a high-temperature and high-pressure container and irradiating water vapor at a controlled temperature for a certain period of time, it is possible to effectively extract target amino acids, organic acids, and the like.
In addition, food waste after filling food waste into high-temperature and high-pressure containers and extracting active ingredients under the processing conditions is reduced in weight and reduced to about 40% before processing. This burden can be reduced.

図1は本発明に係る有効成分抽出装置の構成を示す実施例であり、主に1の蒸気発生容器、9の蓋及びボルト、3の給水タンク、4の高圧ポンプ、6の冷却管で構成されており、それに計測器、止め弁、附属機器、安全弁18などが付随する装置である。   FIG. 1 is an embodiment showing a configuration of an active ingredient extraction apparatus according to the present invention, which is mainly composed of 1 steam generating container, 9 lid and bolt, 3 water supply tank, 4 high-pressure pump, and 6 cooling pipe. It is a device accompanied by a measuring instrument, a stop valve, an attached device, a safety valve 18 and the like.

蒸気発生容器1には、試料及び試料ポット2を装着できる固定枠が装着してあり、その固定枠上部には開口部を設けてあり、蒸気発生容器1内で発生した蒸気が試料及び試料ポット2を通過し、有効成分を含んだ蒸気が固定枠底部より凝固することなく容器外部に排出される様に形成されている。   The steam generation container 1 is provided with a fixed frame on which a sample and a sample pot 2 can be mounted, and an opening is provided on the upper part of the fixed frame, so that the steam generated in the steam generation container 1 is transferred to the sample and sample pot. It is formed so that the vapor | steam containing an active ingredient passes through 2 and is discharged | emitted from the container, without solidifying from the bottom of a fixed frame.

蒸気発生容器1での給水量管理は、液面計5に附属する水位センサー12a,12b,12c,12d・・・の間で行われている。同給水は容器内部が高圧の条件下でも可能な様に、給水元弁13を介して、給水タンク3の水を高圧ポンプ4で加圧し、ヒーター11で加熱した温水が容器給水弁22を開くことにより、蒸気発生容器1に送り込まれる。高圧ポンプ4の吐出量はヒーター11の昇温状況で加減することが出来、容器内温度の急変を防止出来る。またヒーター11の出力制御も可能である。    The water supply amount management in the steam generation container 1 is performed among the water level sensors 12a, 12b, 12c, 12d. The water supply is pressurized by the high-pressure pump 4 through the water supply source valve 13 with the high-pressure pump 4 and the hot water heated by the heater 11 opens the container water supply valve 22 so that the inside of the container is possible even under high pressure conditions. As a result, it is fed into the steam generation container 1. The discharge amount of the high-pressure pump 4 can be adjusted depending on the temperature rise of the heater 11, and a sudden change in the container temperature can be prevented. Moreover, the output control of the heater 11 is also possible.

蒸気発生容器1の胴外周側にヒーター8a,8bが配置されており、電気又は熱媒等を熱源とする。このヒーター8a,8bは、温度センサー10a,10bで容器内温度変化をPID制御しており、昇温に必要な熱量を微積分し過昇温にならないように制御している。また圧力計17の計測値からの制御も可能である。容器冷却弁15は容器内部液温度の冷却用に間接冷却コイルを容器内液相部に配置してあり、仮に過昇温の場合でもこの容器冷却弁15を開き、コイル内部に冷却水が通ることにより過昇温を防止することが出来る。この容器冷却弁15は容器の通常冷却用としても使用される。   Heaters 8a and 8b are disposed on the outer peripheral side of the body of the steam generating container 1, and electricity or a heat medium is used as a heat source. The heaters 8a and 8b perform temperature control 10a and 10b to perform PID control of the temperature change in the container, and control so that the amount of heat necessary for temperature rise is integrated to prevent overheating. Control from the measured value of the pressure gauge 17 is also possible. The container cooling valve 15 has an indirect cooling coil arranged in the liquid phase part in the container for cooling the liquid temperature inside the container. Even if the temperature rises excessively, the container cooling valve 15 is opened and the cooling water passes inside the coil. Therefore, excessive temperature rise can be prevented. The container cooling valve 15 is also used for normal cooling of the container.

所定温度に容器内水温が到達すると、冷却水弁16を開き、冷却管6を冷却する。その後容器温度と圧力が急激に降下しない容量の有効成分を含んだ水蒸気は、採集流量調整弁14と圧力調整弁24を開くならば、その採集流量調整弁14を通過後、有効成分を含んだ水蒸気は冷却管6を流れ、凝縮水となり圧力調整弁24を通過して採集容器7で有効成分を含む水溶液となる。   When the water temperature in the container reaches the predetermined temperature, the cooling water valve 16 is opened and the cooling pipe 6 is cooled. After that, the steam containing the active ingredient having a capacity that does not cause the container temperature and pressure to drop suddenly contains the active ingredient after passing through the collecting flow regulating valve 14 if the collecting flow regulating valve 14 and the pressure regulating valve 24 are opened. The steam flows through the cooling pipe 6, becomes condensed water, passes through the pressure regulating valve 24, and becomes an aqueous solution containing the active ingredient in the collection container 7.

抽出物輸送管内部の洗浄は、採集流量調整弁14、容器給水弁22を閉めた後、洗浄弁23と圧力調整弁24を開け、高圧ポンプ4を運転することで可能となる。このような工程で有効成分の抽出が行われ、蒸気発生容器1内の水位が低水位位置12dを超えて低下すると高圧ポンプ4が作動し所定水位位置12aまで給水し、所定温度までヒーター8a,8bで加熱して水温を温度調節する。この動作を繰り返すことにより長時間有効成分の抽出が可能である。   The inside of the extract transport pipe can be cleaned by opening the cleaning valve 23 and the pressure adjusting valve 24 and operating the high-pressure pump 4 after closing the collection flow rate adjusting valve 14 and the container water supply valve 22. In this process, the active ingredient is extracted, and when the water level in the steam generation container 1 falls below the low water level position 12d, the high pressure pump 4 is activated to supply water to the predetermined water level position 12a, and the heaters 8a, 8a, Heat at 8b to adjust water temperature. By repeating this operation, it is possible to extract an effective component for a long time.

抽出完了後はヒーター8a,8bの電源を切り、排水弁19を開くならば蒸気発生容器1内の温水は給水タンク3へ導かれ、水と混じり低い温度の温水となる。排水完了後は排水弁19を閉め、この温水を再び高圧ポンプ4を経由し蒸気発生容器1に送り込んで該蒸気発生容器1の冷却を行う。さらに排水弁19を開いて給水タンク3へ高温水を送り込む。給水タンク3の温度上昇が見られれば、給水タンク3の排水弁21を開き低温度の水に取り替える。給水タンク3への給水は、給水弁20の自動水位調整器又はボールタップ弁を使用する。
(高温水による減量化)
上記装置で水蒸気による各条件での連続抽出後、装置内の液を冷却しながら排出し、圧力を大気圧になるまで開放した後、試料ポットごと残ったおからを取り出し、湿潤重量と乾燥重量から算出した場合のそれぞれの減量率を図2に示す。
食品廃棄物を高温高圧容器に充填し、処理条件で有効成分を抽出した後の食品廃棄物は重量が減少し、テストでは処理前の約4割に減量されたことからも、廃棄物処理に掛かる負担を軽減することが出来る。
オカラは処理温度が180℃、200℃では1時間で約40%に減量され、150℃では3時間〜4時間ほどで同様の減量に達する。
このような有機物の減量には限界があるが、食品リサイクル法が求める20%以上の減量化は十分に達成される。
After the extraction is completed, if the heaters 8a and 8b are turned off and the drain valve 19 is opened, the hot water in the steam generation container 1 is guided to the water supply tank 3 and becomes hot water having a low temperature mixed with water. After the drainage is completed, the drain valve 19 is closed, and this warm water is again sent to the steam generation container 1 via the high-pressure pump 4 to cool the steam generation container 1. Further, the drain valve 19 is opened to feed hot water into the water supply tank 3. If the temperature increase of the water supply tank 3 is observed, the drain valve 21 of the water supply tank 3 is opened and replaced with low temperature water. For supplying water to the water supply tank 3, an automatic water level regulator or a ball tap valve of the water supply valve 20 is used.
(Weight reduction with hot water)
After continuous extraction with water vapor in each of the above conditions, discharge the liquid in the apparatus while cooling it, release the pressure to atmospheric pressure, take out the remaining okara together with the sample pot, wet weight and dry weight FIG. 2 shows the respective weight loss rates when calculated from the above.
Food waste after filling it into a high-temperature and high-pressure container and extracting active ingredients under the processing conditions is reduced in weight, and in tests it was reduced to about 40% before processing. It is possible to reduce the burden.
Okara is reduced to about 40% in 1 hour at processing temperatures of 180 ° C. and 200 ° C., and reaches the same weight loss in about 3 to 4 hours at 150 ° C.
Although there is a limit to the weight reduction of such organic substances, the weight reduction of 20% or more required by the Food Recycling Law is sufficiently achieved.

(高温水による有効成分の抽出)
本発明の装置を用いてオカラの有効成分を抽出した結果が図3である。同図は200℃で処理時間が1時間と4時間での高温水処理により検出される主なアミノ酸であり、常温の水で処理した場合も示している。このように、加熱時間が長くなるとアミノ酸の種類により分解が進行すると考えられ、抽出されるアミノ酸の種類及びその量は変化する。従って、最適な温度及び時間を設定することで、抽出したいアミノ酸を効率よく得ることが可能と成る。
(Extraction of active ingredients with hot water)
FIG. 3 shows the result of extracting the active ingredient of okara using the apparatus of the present invention. The figure shows the main amino acids detected by high-temperature water treatment at 200 ° C. with treatment times of 1 hour and 4 hours, and also shows the case of treatment with water at room temperature. Thus, it is thought that decomposition | disassembly advances with the kind of amino acid when heating time becomes long, and the kind of amino acid extracted and its quantity change. Therefore, the amino acid to be extracted can be efficiently obtained by setting the optimum temperature and time.

(水蒸気による減量化)
図4は水蒸気によるオカラの減量化を表している。最初に処理量100g
で試験した場合、160℃以下では水蒸気の水分を吸収して湿潤重量は増加しているが、乾燥すると10〜50%の減量となる。200℃では湿潤でも30%の減量、乾燥状態では60%近くの減量となる。さらに、処理量を400gに増加させると、処理温度が120℃から160℃に上昇するに従い湿潤重量は10%〜30%近くに減量すると共に、乾燥重量も25%〜45%へと減量している。これは、装置の大きさと処理量に最適な関係があることを示している。
(Weight reduction with water vapor)
FIG. 4 shows the reduction of okara by water vapor. First 100g throughput
When the test is conducted at a temperature of 160 ° C. or lower, the moisture content of water vapor is absorbed and the wet weight is increased. However, when it is dried, the weight is reduced by 10 to 50%. At 200 ° C., the weight loss is 30% even when wet, and the weight loss is close to 60% when dry. Further, when the treatment amount is increased to 400 g, the wet weight is reduced from 10% to 30% and the dry weight is reduced from 25% to 45% as the treatment temperature is increased from 120 ° C to 160 ° C. Yes. This indicates that there is an optimum relationship between the size of the apparatus and the processing amount.

(水蒸気による有効成分の分析)
本装置の試料ポット2にオカラを入れて水蒸気による連続抽出を行い、成分分析を行った。
分析試料は水蒸気温度変化による抽出物の量を図5で示す。抽出時間変化による抽出物の量は図6に示す。
120℃で5時間抽出することで、カルノシン(アミノ酸)だけが際だって多く抽出出来ることが分かる。又、アスパラギン酸は160℃で抽出することで、その他の温度条件より際だって多く抽出出来ることも明らかである。
その他の食品廃棄物に関しても処理温度による抽出割合に特性があると考えられ、適切な処理温度が判明すれば、効率的な有効成分の抽出が可能となる。
(Analysis of active ingredients with water vapor)
Okara was placed in the sample pot 2 of this apparatus, and continuous extraction with water vapor was performed to perform component analysis.
The analysis sample shows the amount of the extract due to the change in water vapor temperature in FIG. The amount of the extract due to the change in extraction time is shown in FIG.
It can be seen that by extracting at 120 ° C. for 5 hours, only carnosine (amino acid) can be significantly extracted. It is also clear that aspartic acid can be extracted significantly more at 160 ° C. than at other temperature conditions.
Regarding other food wastes, it is considered that there is a characteristic in the extraction ratio depending on the processing temperature, and if an appropriate processing temperature is found, it is possible to efficiently extract active ingredients.

本発明に係る有効成分抽出装置の概略図。1 is a schematic diagram of an active ingredient extraction apparatus according to the present invention. オカラの高温水処理による残量の変化。Changes in remaining amount due to high temperature water treatment of Okara. 高温水及び水により抽出された主なアミノ酸。Main amino acids extracted with hot water and water. オカラの処理温度と処理量による減量率に変化。Changes in weight loss rate due to processing temperature and processing amount of okara. オカラの処理温度によるアミノ酸と有機酸の生成量。Amounts of amino acids and organic acids generated by the processing temperature of okara. オカラの処理時間によるアミノ酸と有機酸の生成量。Amount of amino acid and organic acid produced by okara treatment time.

符号の説明Explanation of symbols

1 蒸気発生容器
2 試料及び試料ポット
3 給水タンク
4 高圧ポンプ
5 液面計
6 冷却管
7 採集容器
8 ヒーター(蒸発器用)
9 蓋
10 温度センサー
11 ヒーター(給水用)
12 水位センサー
13 給水元
14 採集流量調整弁
15 容器冷却弁
16 冷却水弁
17 圧力計
18 安全弁
19 排水弁
20 給水弁
21 給水タンク排水弁
22 容器給水弁
23 洗浄弁
24 圧力調整弁









DESCRIPTION OF SYMBOLS 1 Steam generation container 2 Sample and sample pot 3 Water supply tank 4 High pressure pump 5 Liquid level gauge 6 Cooling pipe 7 Collection container 8 Heater (for evaporator)
9 Lid
10 Temperature sensor
11 Heater (for water supply)
12 Water level sensor
13 Water supply source
14 Collecting flow rate adjustment valve
15 Container cooling valve
16 Cooling water valve
17 Pressure gauge
18 Safety valve
19 Drain valve
20 Water supply valve
21 Water tank drain valve
22 Container water supply valve
23 Cleaning valve
24 Pressure regulating valve









Claims (6)

食品廃棄物からアミノ酸などの有効成分を抽出する為の方法において、水位センサーにて水位を検知して高温高圧容器内に水を給水し、その内部に上部を開口した特殊容器を配置し、この特殊容器に食品廃棄物を収容し、そして上記高温高圧容器をヒーターで加熱し、制御された温度と圧力の水蒸気又は高温高圧水を上記特殊容器内の食品廃棄物に当て、特殊容器内の水蒸気又は高温高圧水を取り出し冷却するもので、目的温度に達するまでは食品廃棄物が浸水しない水位までの給水を行い、目的温度に達した後は、水蒸気を食品廃棄物に当てながら抽出弁を開放したり、徐々に水位を上昇させて高温高圧容器内に配置した上記特殊容器の上部開口から流入して食品廃棄物に高温高圧水を当てて排出することを特徴とする食品廃棄物からの有効成分抽出方法。 In a method for extracting active ingredients such as amino acids from food waste, the water level is detected by a water level sensor, water is supplied into a high-temperature and high-pressure container, and a special container with an open top is placed inside this container. Food waste is stored in a special container, and the high-temperature and high-pressure container is heated with a heater, steam of controlled temperature and pressure or high-temperature and high-pressure water is applied to the food waste in the special container, and the water vapor in the special container Or, take out and cool high-temperature high-pressure water, and supply water to the water level where food waste does not immerse until the target temperature is reached, and after reaching the target temperature, open the extraction valve while applying water vapor to the food waste Yes from or gradually food waste, characterized in that the discharge by applying a high-temperature high-pressure water to raise the water level and flows from the upper opening of the special container disposed in high-temperature high-pressure vessel food waste Component extraction method. 食品廃棄物の重量を軽減する為の方法において、水位センサーにて水位を検知して高温高圧容器内に水を給水し、その内部に上部を開口した特殊容器を配置し、この特殊容器に食品廃棄物を収容し、そして上記高温高圧容器をヒーターで加熱し、制御された温度と圧力の水蒸気を上記特殊容器内の食品廃棄物に当て、特殊容器内の水蒸気を取り出し冷却するもので、目的温度に達するまでは食品廃棄物が浸水しない水位までの給水を行い、目的温度に達した後は、水蒸気を食品廃棄物に当てながら抽出弁を開放することを特徴とする食品廃棄物の重量軽減方法。 In a method for reducing the weight of food waste, a water level sensor detects the water level, water is supplied into a high-temperature and high-pressure container, a special container with an open top is placed inside, and food is placed in this special container. It contains waste, heats the high-temperature and high-pressure container with a heater, applies steam at a controlled temperature and pressure to food waste in the special container, takes out the water vapor in the special container, and cools it. Reduces the weight of food waste by supplying water to a level where food waste does not soak until the temperature is reached, and opening the extraction valve while applying water vapor to the food waste after reaching the target temperature Method. 食品廃棄物からアミノ酸などの有効成分を抽出する為の装置において、水を入れて加熱することで蒸気を発生する高温高圧容器内には食品廃棄物を収容する特殊容器をその上部を開口した状態で配置し、該高温高圧容器にはヒーターを取付けると共に水位を検知する為の水位センサーを備え、上記特殊容器の底には抽出管を接続すると共に該抽出管の途中には冷却装置、採集流量調整弁及び圧力調整弁を設け、そして抽出管の先端には有効成分を含む液が収容される採集容器を有し、又、上記高温高圧容器へ給水するための給水管を接続していることを特徴とする食品廃棄物からの有効成分抽出装置。 In a device for extracting active ingredients such as amino acids from food waste, a special container containing food waste is opened in the high-temperature and high-pressure container that generates steam by adding water and heating. The high-temperature and high-pressure vessel is equipped with a water level sensor for detecting the water level and a water level sensor for detecting the water level. An extraction pipe is connected to the bottom of the special vessel and a cooling device and a collection flow rate are provided in the middle of the extraction pipe. A regulating valve and a pressure regulating valve are provided, and the extraction pipe has a collection container for storing a liquid containing an active ingredient at the tip, and is connected to a water supply pipe for supplying water to the high-temperature and high-pressure container. A device for extracting active ingredients from food waste. 給水タンクに給水管を接続し、該給水管の途中には高圧ポンプと内部を流れる水を加熱するヒーターを設けた請求項3記載の食品廃棄物からの有効成分抽出装置。 The apparatus for extracting an active ingredient from food waste according to claim 3, wherein a water supply pipe is connected to the water supply tank, and a heater for heating water flowing in the high pressure pump and the inside is provided in the middle of the water supply pipe. 食品廃棄物の重量を軽減する為の装置において、水を入れて加熱することで蒸気を発生する高温高圧容器内には食品廃棄物を収容する特殊容器をその上部を開口した状態で配置し、該高温高圧容器にはヒーターを取付けると共に水位を検知する為の水位センサーを備え、上記特殊容器の底には抽出管を接続すると共に該抽出管の途中には冷却装置、採集流量調整弁及び圧力調整弁を設け、そして抽出管の先端には有効成分を含む液が収容される採集容器を有し、又、上記高温高圧容器へ給水するための給水管を接続していることを特徴とする食品廃棄物の重量軽減装置。 In a device for reducing the weight of food waste, a special container that contains food waste is placed in an open state in a high-temperature and high-pressure container that generates steam by adding water and heating it. The high-temperature and high-pressure vessel is equipped with a water level sensor for detecting the water level and a heater is connected. An extraction pipe is connected to the bottom of the special vessel, and a cooling device, a collection flow rate adjusting valve and a pressure are provided in the middle of the extraction pipe. A regulating valve is provided, and a tip of the extraction pipe has a collection container for storing a liquid containing an active ingredient, and is connected to a water supply pipe for supplying water to the high-temperature and high-pressure container. Weight reduction device for food waste. 給水タンクに給水管を接続し、該給水管の途中には高圧ポンプと内部を流れる水を加熱するヒーターを設けた請求項5記載の食品廃棄物の重量軽減装置。 6. The food waste weight reducing device according to claim 5, wherein a water supply pipe is connected to the water supply tank, and a heater for heating water flowing in the high pressure pump is provided in the middle of the water supply pipe.
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