JP7651108B2 - How to recycle food waste - Google Patents
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- 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
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特許法第30条第2項適用 (1)開催日:令和 3年 3月 1日 (2)集会名、開催場所:令和二年度 国立大学法人山梨大学 工学部 応用化学科卒業論文発表会、国立大学法人山梨大学 工学部A2-21教室(山梨県甲府市武田四丁目4番37号)(1) Date: March 1, 2021 (2) Name and location of the meeting: 2020 National University Corporation Yamanashi University, Faculty of Engineering, Department of Applied Chemistry Graduation Thesis Presentation, Room A2-21, Faculty of Engineering, Yamanashi University (4-4-37 Takeda, Kofu, Yamanashi Prefecture)
本発明は、食品廃棄物のリサイクル方法に関するものであり、例えばコーヒー殻や緑茶殻などから高級脂肪酸を抽出したり、さらにその残滓物の有効利用を可能とするものである。 The present invention relates to a method for recycling food waste, for example by extracting higher fatty acids from coffee grounds and green tea leaves, and by making effective use of the residue.
都市ごみの処理は、コストや環境問題の観点から重要な課題となっており、バイオマス利用技術の一分野として、各種のリサイクル技術の開発が望まれている。 The treatment of municipal waste has become an important issue from the standpoint of cost and environmental concerns, and there is a need for the development of various recycling technologies as part of biomass utilization technology.
コーヒー殻の処理に関する従来技術としては、例えば以下の特許文献1~3記載の発明がある。 Conventional techniques relating to the processing of coffee husks include the inventions described in the following Patent Documents 1 to 3, for example.
特許文献1には、コーヒー殻を含む植物性原料をイオン交換水中で150~350℃の温度において水熱炭化することにより、炭化物を比較的低い温度において高い回収率で製造する方法が開示されている。 Patent Document 1 discloses a method for producing carbonized material at a relatively low temperature with a high recovery rate by hydrothermally carbonizing plant-based raw materials including coffee husks in ion-exchanged water at a temperature of 150 to 350°C.
特許文献2には、コーヒー粕等のバイオマスを効率よくメタン発酵させるバイオマス処理方法が開示されている。 Patent Document 2 discloses a biomass processing method that efficiently ferments biomass such as coffee grounds into methane.
特許文献3には、60℃以上で加熱処理することにより、コーヒー粕の可溶化処理とコーヒー粕の乾燥重量の5~10倍相当量の希釈媒体を添加するコーヒー粕を利用したメタン発酵方法が開示されている。 Patent Document 3 discloses a methane fermentation method using coffee grounds, which involves solubilizing the coffee grounds by heating them at 60°C or higher and adding a dilution medium in an amount equivalent to 5 to 10 times the dry weight of the coffee grounds.
上述した特許文献1~3に記載されるコーヒー殻の処理技術は、基本的には炭化物を製造して燃料としての有効利用を図ったものである。 The coffee grounds processing technologies described in the above-mentioned Patent Documents 1 to 3 are basically aimed at producing carbonized material and using it effectively as fuel.
しかしながら、炭化物の製造コストと燃料として価値や有効性、環境への影響などを総合的に判断した場合、必ずしも効率的なリサイクル技術とは言えない。 However, when taking into consideration the manufacturing costs of the carbonized material, its value and effectiveness as a fuel, and its impact on the environment, it cannot necessarily be said to be an efficient recycling technology.
本発明は、コーヒー殻や緑茶殻などの食品廃棄物の処理および処理物の有効利用において、より効率的なリサイクル方法を提供することを目的としたものである。 The present invention aims to provide a more efficient recycling method for the treatment of food waste such as coffee grounds and green tea leaves and for the effective use of the treated materials.
本発明の食品廃棄物のリサイクル方法は、食品廃棄物を水熱処理することにより高級脂肪酸を含有する水熱チャーを生成させることを特徴とするものである。 The food waste recycling method of the present invention is characterized by producing hydrothermal char containing higher fatty acids by hydrothermal treatment of food waste.
本発明における食品廃棄物としては、例えばコーヒーの抽出殻や緑茶、紅茶、麦茶などのお茶の抽出殻を用いることができる。 In the present invention, food waste that can be used includes, for example, coffee grounds and grounds from tea extracts such as green tea, black tea, and barley tea.
本発明により得られる水熱チャーから高級脂肪酸を抽出することで、高級脂肪酸の種類に応じて、化粧品や、洗剤、塗料、合成樹脂などの原料として有効利用することができる。また、高級脂肪酸を抽出した残渣物は燃料リサイクルおよび活性炭などの炭化物としての利用が可能である。 By extracting higher fatty acids from the hydrothermal char obtained by the present invention, depending on the type of higher fatty acid, it can be effectively used as a raw material for cosmetics, detergents, paints, synthetic resins, etc. In addition, the residue from which the higher fatty acids are extracted can be used for fuel recycling and as carbonized materials such as activated carbon.
水熱処理は、150~220℃程度の加熱、好ましくは150~200℃の加熱で行われる。水熱処理の温度は180℃前後で水熱チャーの収率が高く、220℃を超えると収率が低くなる傾向がある。 Hydrothermal treatment is carried out at heating at about 150 to 220°C, preferably 150 to 200°C. The yield of hydrothermal char is high when the hydrothermal treatment temperature is around 180°C, but the yield tends to decrease when the temperature exceeds 220°C.
また、水熱処理時間は、食品廃棄物の種類によっても異なるが、3時間から48時間程度、より好ましくは3時間~24時間程度が望ましい。水熱処理時間が長いほど水熱チャーの収率が高くなる傾向があるが、食品廃棄物の種類によっては収率の増加率が低いか明確でなく、長時間の処理は効率的でない。また、残留液の有機酸を例えばスラグの溶解、金属溶出などで酸利用を図る場合、水熱処理時間が長くなるほど酸性度が低くなる(pHが高くなる)傾向があるため、水熱処理時間が24時間以内、あるいは12時間以内が好ましい。 The hydrothermal treatment time varies depending on the type of food waste, but is preferably about 3 to 48 hours, more preferably about 3 to 24 hours. The longer the hydrothermal treatment time, the higher the yield of hydrothermal char tends to be, but depending on the type of food waste, the rate of increase in yield is low or unclear, and long treatment times are not efficient. In addition, when attempting to utilize the organic acid in the residual liquid, for example, for dissolving slag or eluting metals, the longer the hydrothermal treatment time, the lower the acidity (the higher the pH), so the hydrothermal treatment time is preferably within 24 hours, or within 12 hours.
本発明によれば、コーヒー殻や緑茶殻などの食品廃棄物を水熱処理することによって、パルミチン酸などの高級脂肪酸を含有する水熱チャーを生成させることができ、高級脂肪酸を得ることができ、この水熱チャーから高級脂肪酸を抽出することで、高級脂肪酸の種類に応じて、化粧品や、洗剤、塗料、合成樹脂などの原料として有効利用することができる。また、高級脂肪酸を抽出した残渣物は燃料化するなどしての利用が可能である。 According to the present invention, by subjecting food waste such as coffee grounds and green tea grounds to hydrothermal treatment, it is possible to produce hydrothermal char containing higher fatty acids such as palmitic acid, and higher fatty acids can be obtained. By extracting higher fatty acids from this hydrothermal char, they can be effectively used as raw materials for cosmetics, detergents, paints, synthetic resins, etc., depending on the type of higher fatty acid. In addition, the residue from which the higher fatty acids have been extracted can be used as fuel, etc.
以下、本発明の効果を確認するために行った試験について説明する。
原料殻:コーヒー、緑茶、麦茶殻、紅茶殻
水熱処理条件:180℃、220℃、3~24時間
溶媒:H2O
Tests conducted to confirm the effects of the present invention will now be described.
Raw material husks: coffee, green tea, barley tea husks, black tea husks Hydrothermal treatment conditions: 180°C, 220°C, 3 to 24 hours Solvent: H 2 O
合成後、固液分離して黒色残留物(水熱チャー)を回収した。
試験結果を図1~図5に示す。
After the synthesis, the black residue (hydrothermal char) was recovered by solid-liquid separation.
The test results are shown in Figures 1 to 5.
図1はコーヒー殻、緑茶殻、麦茶殻、紅茶殻について、水熱処理温度が180℃の場合と220℃の場合での水熱チャーの収率をグラフに示したものであり、図2は水熱処理後の残留液のpHをグラフとして示したものである。 Figure 1 is a graph showing the hydrothermal char yields for coffee grounds, green tea grounds, barley tea grounds, and black tea grounds when the hydrothermal treatment temperatures are 180°C and 220°C, and Figure 2 is a graph showing the pH of the residual liquid after hydrothermal treatment.
これらのグラフにおいて、コーヒー殻を180℃で水熱処理した場合を●、220℃で水熱処理した場合を〇、緑茶を180℃で水熱処理した場合を▲、220℃で水熱処理した場合を△、麦茶殻を180℃で水熱処理した場合を■、220℃で水熱処理した場合を□、紅茶殻を180℃で水熱処理した場合を▼、220℃で水熱処理した場合を▽で示している。 In these graphs, coffee grounds are marked with a ● when hydrothermally treated at 180°C, a ◯ when hydrothermally treated at 220°C, green tea grounds are marked with a ▲ when hydrothermally treated at 180°C, a △ when hydrothermally treated at 220°C, barley tea grounds are marked with a ■ when hydrothermally treated at 180°C, a □ when hydrothermally treated at 220°C, black tea grounds are marked with a ▼ when hydrothermally treated at 180°C, and a ▽ when hydrothermally treated at 220°C.
コーヒー殻を180℃で水熱処理した場合(●)と、220℃で水熱処理した場合(〇)では、180℃で水熱処理した場合の方が水熱チャーの収率が高かった。 When coffee grounds were hydrothermally treated at 180°C (●) versus 220°C (◯), the yield of hydrothermal char was higher when hydrothermally treated at 180°C.
コーヒー殻を180℃で水熱処理した場合は、24時間水熱処理した場合の水熱チャーの収率が最も高かった。コーヒー殻を220℃で水熱処理した場合は、12時間水熱処理した場合の水熱チャーの収率が高かったが、処理時間の違いによる差はあまり明確ではなかった。 When coffee grounds were hydrothermally treated at 180°C, the yield of hydrothermal char was highest when hydrothermally treated for 24 hours. When coffee grounds were hydrothermally treated at 220°C, the yield of hydrothermal char was highest when hydrothermally treated for 12 hours, but the difference due to the difference in treatment time was not very clear.
コーヒー殻の残留液の有機酸のpHは、220℃の方が180℃よりも若干高い傾向が見られたが、水熱処理の時間との関係でも大きな差は見られなかった。 The pH of the organic acids in the residual liquid from the coffee grounds tended to be slightly higher at 220°C than at 180°C, but no significant difference was observed in relation to the hydrothermal treatment time.
緑茶殻を180℃で水熱処理した場合(▲)と、220℃で水熱処理した場合(△)についても、180℃で水熱処理した場合の方が水熱チャーの収率が高かった。 When green tea leaves were hydrothermally treated at 180°C (▲) and 220°C (△), the yield of hydrothermal char was higher when hydrothermally treated at 180°C.
緑茶殻は180℃、220℃ともに水熱処理を長時間行うと収率が低くなる傾向が見られた。緑茶殻の残留液の有機酸のpHは、長時間の方が高い傾向(短時間の方が酸性が強い)見られた。このことから緑茶殻については、水熱処理の時間は24時間行うより、3~12時間が好ましいと考えられる。 For green tea leaves, the yield tended to decrease when hydrothermal treatment was performed for a long period of time at both 180°C and 220°C. The pH of the organic acids in the residual liquid from green tea leaves tended to be higher the longer the treatment (shorter treatment was more acidic). From this, it is believed that for green tea leaves, hydrothermal treatment for a period of 3 to 12 hours is preferable rather than 24 hours.
また、図2から、コーヒー殻と緑茶殻の比較では、コーヒー殻由来の有機酸のpHが小さいという結果が得られた。 Figure 2 also shows that when comparing coffee grounds and green tea grounds, the pH of the organic acids derived from coffee grounds is lower.
麦茶殻と紅茶殻については、データ数が必ずしも十分ではないが、紅茶殻については緑茶殻と近い結果が得られ、麦茶殻についてはコーヒー殻と緑茶殻の中間的な結果が得られた。 Although the amount of data for barley tea leaves and black tea leaves was not necessarily sufficient, results for black tea leaves were similar to those for green tea leaves, and results for barley tea leaves were intermediate between those for coffee leaves and green tea leaves.
図3は、コーヒー殻(CF)、紅茶殻(ET)、緑茶殻(GT)、麦茶殻(BT)をそれぞれ220℃で24時間水熱処理した水熱チャーをX線回析により構造解析したグラフを示したものである。また、エタノールにより洗浄したものをEで表している。 Figure 3 shows a graph of the structure analysis by X-ray diffraction of hydrothermal chars obtained by hydrothermal treatment of coffee grounds (CF), black tea grounds (ET), green tea grounds (GT), and barley tea grounds (BT) at 220°C for 24 hours. E represents those washed with ethanol.
コーヒー殻から水熱チャーを得たCF220/24では、21.4°および23.7°付近に強度の高い2本の回析ピーク(図3の点線で示した箇所)が認められた。 In CF220/24, which is a hydrothermal char obtained from coffee husks, two highly intense diffraction peaks (shown by dotted lines in Figure 3) were observed at around 21.4° and 23.7°.
なお、パルミチン酸の特徴的な強度の高いピークは、2.7°、7.22°、21.5°、24.1°であり、ガスクロマトグラフィーの測定で、パルミチン酸が検出された。その他、高級脂肪酸については、パルミチン酸の他にステアリン酸が検出されている。参考まで、図7にパルミチン酸(上側)とセタノール(下側)のX線回析強度のグラフを示す。 The characteristic high intensity peaks of palmitic acid are 2.7°, 7.22°, 21.5°, and 24.1°, and palmitic acid was detected by gas chromatography. As for higher fatty acids, stearic acid was detected in addition to palmitic acid. For reference, the X-ray diffraction intensity graphs of palmitic acid (upper side) and cetanol (lower side) are shown in Figure 7.
緑茶殻から水熱チャーを得たGT220/24についても21.4°および23.7°付近に強度の高い2本の回析ピークが認められた。 Two intense diffraction peaks were observed around 21.4° and 23.7° for GT220/24, which was obtained by hydrothermal char from green tea leaves.
CF220/24EとGT220/24Eは、エタノールによる洗浄により水熱チャーからパルミチン酸などの高級脂肪酸が除去されたため、水熱処理したチャーからパルミチン酸などの回析ピークは消失した。 In the case of CF220/24E and GT220/24E, higher fatty acids such as palmitic acid were removed from the hydrothermal char by washing with ethanol, so the diffraction peaks of palmitic acid, etc. disappeared from the hydrothermally treated char.
図4は、コーヒー殻を220℃で、3、6、24時間水熱処理したものと、180℃で12、24時間水熱処理したものをX線回析して分析したグラフである。220℃で水熱処理したものをCF220/3、CF220/6、CF220/24で示しており、180℃で12、24時間水熱処理したものをCF180/12、CF180/24で示している。 Figure 4 is a graph showing X-ray diffraction analysis of coffee grounds hydrothermally treated at 220°C for 3, 6, and 24 hours, and at 180°C for 12 and 24 hours. The coffee grounds hydrothermally treated at 220°C are shown as CF220/3, CF220/6, and CF220/24, while the coffee grounds hydrothermally treated at 180°C for 12 and 24 hours are shown as CF180/12 and CF180/24.
220℃で水熱処理したチャーは、CF220/3とCF220/6において、2.5°および21.4°付近におけるピークが明瞭であり、CF220/24についてもピークが確認された。 Chars hydrothermally treated at 220°C showed clear peaks at around 2.5° and 21.4° for CF220/3 and CF220/6, and peaks were also observed for CF220/24.
180℃で水熱処理したチャーは、220℃で水熱処理したチャーよりもピークが明瞭であり、2.5°および21.4°付近に加え、23.5°付近にも弱いピークが見られる。CF180/12とCF180/24では、CF180/12の場合がよりピークが明瞭である。 Char hydrothermally treated at 180°C has a clearer peak than char hydrothermally treated at 220°C, and in addition to the peaks near 2.5° and 21.4°, a weak peak is also seen near 23.5°. Between CF180/12 and CF180/24, the peak is clearer in the case of CF180/12.
図5は、緑茶殻を水熱処理したものをX線回析して分析したグラフである。220℃で24時間水熱処理したものをGT220/24、180℃で12、24時間水熱処理したものをGT180/12、CF180/24で示している。 Figure 5 is a graph showing the X-ray diffraction analysis of green tea leaves that were hydrothermally treated. The samples that were hydrothermally treated at 220°C for 24 hours are shown as GT220/24, and the samples that were hydrothermally treated at 180°C for 12 and 24 hours are shown as GT180/12 and CF180/24.
GT220/24では、21.4°付近に比較的明瞭なピークが見られるが、GT180/24、CF180/12ではピークにおけるX線回析強度がより高く、2.5°、21.4°、23.5°付近のピークを確認することができる。 In GT220/24, a relatively clear peak is seen at around 21.4°, but in GT180/24 and CF180/12, the X-ray diffraction intensity at the peak is higher, and peaks can be confirmed at around 2.5°, 21.4°, and 23.5°.
以上の試験結果より、コーヒー殻、緑茶殻などを水熱処理して得られた水熱チャーに、パルミチン酸などの高級脂肪酸が含まれていることが確認された。 From the above test results, it was confirmed that hydrothermal char obtained by hydrothermal treatment of coffee grounds, green tea grounds, etc. contains higher fatty acids such as palmitic acid.
図6は、220℃で24時間水熱処理したコーヒー殻のSEM写真を示したものである。(b)は(a)の拡大写真である。 Figure 6 shows an SEM image of coffee husks hydrothermally treated at 220°C for 24 hours. (b) is an enlarged image of (a).
図6の写真において、球状チャーの生成も認められた。よって、コーヒー由来の炭素体は、例えばエチレン吸着に利用するなどのポーラスカーボンへの活用が期待できる。
The generation of spherical char was also observed in the photograph of Figure 6. Therefore, it is expected that the carbonaceous material derived from coffee can be used as porous carbon, for example, for ethylene adsorption.
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