JPH07278581A - Production of solid fuel from waste - Google Patents

Production of solid fuel from waste

Info

Publication number
JPH07278581A
JPH07278581A JP7114694A JP7114694A JPH07278581A JP H07278581 A JPH07278581 A JP H07278581A JP 7114694 A JP7114694 A JP 7114694A JP 7114694 A JP7114694 A JP 7114694A JP H07278581 A JPH07278581 A JP H07278581A
Authority
JP
Japan
Prior art keywords
oil
cooker
raw material
mmhg
reduced pressure
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
Application number
JP7114694A
Other languages
Japanese (ja)
Inventor
Shuzo Nakazono
修三 中園
Norihisa Matsuoka
範久 松岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP7114694A priority Critical patent/JPH07278581A/en
Publication of JPH07278581A publication Critical patent/JPH07278581A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PURPOSE:To obtain a solid fuel with high combustion efficiency from wastes. CONSTITUTION:A feedstock, a water-rich waste solid containing combustible materials, is immersed in a heated oil such as animal oil, vegetable oil or mineral oil in a cooker; this system is agitated under heating using the heated oil as heating medium while the closed cooker are subjected to pressure reduction in three stages, and treated at normal pressure minus 100 to 300mmHg in the initial reduced pressure process, and at further 100 to 300mmHg reduced pressure in the medium-stage reduced pressure process, and at an absolute pressure of 10 to 60mmHg in the final reduced pressure process, thereby separating and transpirating the water in the feedstock and impregnating the feedstock texture with the oil in the cooker; the resultant feedstock is drawn off the cooker and then squeezed to remove the oil to an oil content of 10-30wt.%, thus obtaining the objective solid fuel.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、廃棄物からの固形燃
料の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing solid fuel from waste.

【0002】[0002]

【従来の技術】従来、有機質汚泥、家畜糞尿、動植物残
渣等のいわゆる利用価値のない廃棄物は、海岸埋立て用
に利用したり、燃焼したりして処理する方法が採用され
ており、一部、本出願の発明者が開発した油温による脱
水処理をして飼料、肥料等の有効利用をするようにして
いる。
2. Description of the Related Art Conventionally, wastes such as organic sludge, livestock excrement, animal and plant residues, and so on that have no utility value have been used for landfilling or burning to treat them. Part, the inventors of the present application have developed a dehydration treatment using oil temperature to effectively use feed, fertilizer and the like.

【0003】[0003]

【発明が解決しようとする課題】しかし、埋立て処理も
環境問題のために従来のように簡単に採用できなくなっ
てきており、燃焼処理するにしても、設備や燃料等に莫
大な費用がかかり、採算上の問題があって採用しにくい
状況にあり、また、従来の減圧条件下における油温によ
る脱水脱油処理も単なる肥料等に用途を限定した処理産
物であれば問題がなかったが、特に燃料に使用しうるよ
うな処理産物にするためには、不十分であり、処理産物
の熱カロリーが低く燃料に供しえない等の欠点を有して
いた。
However, landfill treatment cannot be easily adopted as in the past due to environmental problems, and even if it is burnt, a huge amount of equipment, fuel, etc. are required. However, there is a problem in profitability and it is difficult to adopt, and there was no problem in the conventional dehydration deoiling process with oil temperature under reduced pressure as long as it is a processed product whose purpose is limited to simple fertilizer, etc. In particular, it is insufficient to make a processed product that can be used as a fuel, and has a drawback that the processed product has a low thermal calorie and cannot be used as a fuel.

【0004】[0004]

【課題を解決するための手段】この発明は、可燃性素材
を含有した多水分含有の廃棄固形物を原料として、これ
らの原料をクッカー内の加熱された動物油、植物油、鉱
物油等の油中に浸漬し、密閉されたクッカー内を三段階
に減圧しながら加熱された油を熱媒体として撹拌加熱
し、しかも、初期の減圧過程においては、常圧から10
0mmHg〜300mmHgを減圧した減圧条件下で処理し、次
いで、中期減圧過程においては、更に100mmHg〜30
0mmHgを減圧した減圧条件下で処理し、最後に後期減圧
過程においては、絶対圧の10mmHg〜60mmHgの減圧条
件下で処理を行うことにより原料中の含水分を分離蒸散
すると共にクッカー内の油を原料組織中に含浸させ、次
いで、原料をクッカーから取出して含油率10〜30%
にまで搾油或は脱油して固形物を得ることを特徴とした
廃棄物からの固形燃料の製造方法を提供せんとするもの
である。
The present invention uses, as raw materials, waste solids containing a high moisture content containing a flammable raw material, and these raw materials are used in heated oils such as animal oils, vegetable oils and mineral oils in a cooker. The heated oil is stirred and heated using the heated oil as a heat medium while reducing the pressure in the closed cooker in three steps.
0mmHg ~ 300mmHg under reduced pressure condition, then in the intermediate pressure reduction process, 100mmHg ~ 30
0mmHg is decompressed under reduced pressure conditions, and finally, in the latter stage decompression process, absolute moisture pressure of 10mmHg-60mmHg is applied under reduced pressure conditions to separate and evaporate the water content in the raw material and to remove the oil in the cooker. Impregnate the raw material structure and then take out the raw material from the cooker to obtain an oil content of 10 to 30%.
It is intended to provide a method for producing a solid fuel from waste, which is characterized by obtaining a solid matter by squeezing or deoiling up to 1.

【0005】[0005]

【実施例】この発明の実施例を詳説すると、まず、原料
としては可燃性素材を有した多水分含有の廃棄固形物を
使用する。具体的には、有機質汚泥や、余剰汚泥や、家
畜糞尿や、植物残渣や、動物残渣等があり、これ以外に
も可燃性の廃棄物で含水分が多いために燃焼処理が困難
なものを原料として使用する。
EXAMPLES To explain the examples of the present invention in detail, first, as a raw material, a waste solid having a high moisture content and having a combustible material is used. Specifically, there are organic sludge, surplus sludge, livestock excrement, plant residues, animal residues, etc. Other than this, flammable waste that is difficult to burn due to its high water content. Used as a raw material.

【0006】また、クッカー内の加熱された油として
は、動物油、植物油、鉱物油等を使用するものであり、
具体的には、鉱物廃油や、一般に使用不可能な動植物油
脂や油泥やタンクスラッジやタンカースラッジ等を一種
類或は混合して使用する。
As the heated oil in the cooker, animal oil, vegetable oil, mineral oil, etc. are used.
Specifically, one or a mixture of mineral waste oil, animal and vegetable oils and fats, oil mud, tank sludge, tanker sludge, etc., which are generally unusable, is used.

【0007】これらの油の加熱温度は一律に70℃〜8
0℃で行う場合と、後述する三段階の減圧条件に対応さ
せた油温で行う場合とがある。
The heating temperature of these oils is uniformly 70 ° C to 8 ° C.
There are cases where it is carried out at 0 ° C. and cases where it is carried out at an oil temperature corresponding to the three-stage depressurization conditions described below.

【0008】そこで、三段階の減圧処理の過程を述べる
と、原料をクッカー内に投入した後から約40分間は、
常圧から100mmHg〜300mmHgの減圧を行い、この減
圧処理条件下では、クッカー内の温度を初期100℃〜
120℃位に保持する。
Then, the process of the three-step depressurization treatment will be described. About 40 minutes after the raw materials were put into the cooker,
A pressure of 100 mmHg to 300 mmHg is depressurized from normal pressure.
Hold at about 120 ° C.

【0009】次いで、その後約40〜50分間は更に1
00mmHg〜200mmHgの減圧を行い、この中期減圧処理
条件下ではクッカー内の温度を60℃〜70℃とし、こ
の温度から徐々に昇温して約100℃〜120℃にまで
する。
Then, for about 40 to 50 minutes thereafter, another 1
The pressure is reduced to 00 mmHg to 200 mmHg, and the temperature in the cooker is set to 60 ° C. to 70 ° C. under this intermediate pressure reduction treatment condition, and the temperature is gradually raised from this temperature to about 100 ° C. to 120 ° C.

【0010】次いで、その後約30分間は、更に減圧し
て絶対圧を約10〜60mmHg(すなわち常圧から700
〜750mmHgの減圧を行う)にまですると共に、この後
期減圧処理条件下では、クッカー内の温度を約110℃
〜120℃とする。
Then, for about 30 minutes thereafter, the pressure is further reduced to an absolute pressure of about 10 to 60 mmHg (that is, from normal pressure to 700 mm).
Up to 750 mmHg), and under the latter decompression condition, the temperature inside the cooker is about 110 ° C.
~ 120 ° C.

【0011】かかる減圧処理は、クッカー中に連通した
真空吸引パイプにリーク弁を介設し、リーク弁の開放、
閉塞を調節しながらクッカー内の圧力を調節する。
In the depressurizing process, a leak valve is provided in a vacuum suction pipe communicating with the cooker, and the leak valve is opened.
Adjust the pressure in the cooker while adjusting the blockage.

【0012】以上のように、クッカー内で油温による減
圧加熱処理した原料は、クッカー中より取出し、搾油或
は脱油する。
As described above, the raw material which has been heated under reduced pressure at the oil temperature in the cooker is taken out from the cooker and crushed or deoiled.

【0013】搾油、脱油は、スクリュープレス機等によ
り物理的に圧搾する場合や、遠心分離機により油を遠心
分離する場合や、ノーマルヘキサン等の脱油剤を散布し
て脱油する場合等があり、特に原料の搾油、脱油に際し
ては原料の残油率が10〜30%の固形物となるように
する。
Oil extraction and deoiling are carried out by physically pressing with a screw press or the like, centrifuging oil with a centrifuge, or deoiling with a deoiling agent such as normal hexane. In particular, when the raw material is squeezed and deoiled, the residual oil rate of the raw material should be 10 to 30% solid.

【0014】かかる固形物は、固形燃料となるものであ
り、1Kg重量に対し約6500Kcalの燃焼効率を有す
る。
Such a solid substance serves as a solid fuel and has a combustion efficiency of about 6500 Kcal per 1 Kg weight.

【0015】また、クッカー内の加熱油としては、油
泥、タンクスラッジ、タンカースラッジ等の20%〜6
0%の水分を含んだものに、原料としては比較的含水率
の低い水分40%〜60%の固形可燃物を投入して上記
の三段階処理をすると、燃焼効率が安定した固形燃料を
得ることができる。
The heating oil in the cooker is 20% to 6% of oil mud, tank sludge, tanker sludge, etc.
When a solid combustible material having a relatively low water content of 40% to 60% is added to a material containing 0% water and the above three-step treatment is performed, a solid fuel with stable combustion efficiency is obtained. be able to.

【0016】また、他の実施例としては、三段階減圧の
条件として、原料をクッカー中に投入した後に約40分
間は、クッカー内温度を約110℃とし、クッカー内圧
力を常圧から10〜20mmHgだけ減圧する。次いで約4
0分間は、更に100〜200mmHgだけ減圧し、これと
共にクッカー内温度を60℃〜70℃にまで一旦低下さ
せた後に更に中途から徐々に昇温して約120℃にまで
上昇させる。
In another embodiment, as a condition of three-stage depressurization, the temperature inside the cooker is set to about 110 ° C. for about 40 minutes after the raw materials are put into the cooker, and the pressure inside the cooker is 10 to 10 from the normal pressure. Reduce the pressure by 20 mmHg. Then about 4
During 0 minutes, the pressure is further reduced by 100 to 200 mmHg, and the temperature inside the cooker is once lowered to 60 to 70 ° C., and then gradually raised from the middle to rise to about 120 ° C.

【0017】次いで、約30分間は、絶対圧の10mmHg
〜20mmHgだけ減圧し、クッカー内温度を約120℃に
保持する。
Next, for about 30 minutes, the absolute pressure is 10 mmHg.
Reduce the pressure by -20 mmHg and keep the temperature inside the cooker at about 120 ° C.

【0018】本発明の実施例は、上記のように構成され
ているものであり、初期の減圧過程において、原料投入
後、原料は、クッカー内の温度により加温されて品温を
上げていき、クッカー内温度と同時の100℃前後とな
り、同時に油中に含まれた或は油に混合された水分を蒸
散する。この時点で中期の減圧過程に入り、更なる減圧
によりクッカー内温度は一旦低下するものの原料の品温
は初期減圧段階の状態を保持しており、これから徐々に
クッカー内温度を昇温していき、かつ減圧を大きくする
と、原料組織表層中の含水分は比重が油より低くなり、
徐々に蒸散していき、原料組織の表層部分に含水された
水分が脱水されていく。
The embodiment of the present invention is configured as described above, and in the initial depressurization process, after the raw material is charged, the raw material is heated by the temperature in the cooker to raise the product temperature. The temperature inside the cooker is about 100 ° C. at the same time, and at the same time, the water contained in the oil or mixed with the oil is evaporated. At this point, the middle-stage depressurization process started, and the temperature inside the cooker once dropped due to further depressurization, but the product temperature of the raw material remained at the initial depressurization stage, and the temperature inside the cooker gradually increased from this point onward. And, if the decompression is increased, the specific gravity of the water content in the surface layer of the raw material tissue becomes lower than that of oil,
The water gradually evaporates, and the water contained in the surface layer of the raw material structure is dehydrated.

【0019】次いで、真空に近い後期段階の減圧を行う
ことにより、先に脱水された原料組織表層部分を通過し
て、原料組織中心部の水分が脱水し、同時にクッカー内
の油が脱水された原料組織中に浸透して、結果的に原料
組織中において水分と油との置換が行われ、油を原料組
織中に含浸させ、水分の除去された状態の一定量の油が
含まれた固形物となる。
Then, by depressurizing in the latter stage close to vacuum, the water in the central portion of the raw material tissue was dehydrated by passing through the surface layer of the raw material tissue that was dehydrated previously, and at the same time, the oil in the cooker was also dehydrated. A solid containing a certain amount of oil that has penetrated into the raw material tissue, resulting in the replacement of water with oil in the raw material tissue, impregnating the raw material tissue with oil, and removing the water content. It becomes a thing.

【0020】従って、このようにして完成した固形燃料
は、原料組織そのものが脱水された可燃物となり、か
つ、原料組織中に含浸された脱水油が燃料の一部ともな
り、燃焼効率のよい固形燃料とすることができる効果が
ある。
Therefore, the solid fuel thus completed becomes a combustible substance in which the raw material structure itself is dehydrated, and the dehydrated oil impregnated in the raw material structure also serves as a part of the fuel, so that the solid fuel having good combustion efficiency is obtained. There is an effect that can be used as fuel.

【0021】[0021]

【発明の効果】この発明によれば、原料を可燃性素材を
含有した多水分含有の廃棄固形物としたために、従来廃
棄処分されていた原料を有効な燃料として利用しうる効
果を有し、また、処理媒体として各種油を熱媒体として
使用しうるためコスト上も安価に処理でき、また、加熱
処理中の減圧条件を三段階としたので、初期減圧段階で
原料の品温を水分が蒸散しやすい温度に上昇し、かつ油
に含まれた、或は油と混合された水分を蒸散し、中期減
圧段階で、油の比重を水より小さくして原料組織の表層
部に含浸された水分を脱水し、後期減圧段階で原料組織
の中心部に含浸された水分を脱水し、油との置換を行う
ことにより、燃料に有効な熱媒体としての油を原料中に
含浸させ、かつ本来の原料としての可燃性素材の特性に
より、燃料として燃焼効率のよい固形燃料にできる効果
を有する。
EFFECTS OF THE INVENTION According to the present invention, since the raw material is the waste solid containing a large amount of water containing the combustible material, the raw material which has been conventionally disposed of can be used as an effective fuel. In addition, since various oils can be used as a heat medium as a heat medium, it can be processed at a low cost, and since the depressurization conditions during the heat treatment are set to three stages, water vaporizes the product temperature of the raw material at the initial depressurization stage. Water that has risen to an easy temperature and evaporates the water contained in the oil or mixed with the oil, and the specific gravity of the oil is made smaller than that of water in the middle decompression stage, and the water impregnated in the surface layer of the raw material structure is impregnated. Is dehydrated, the water impregnated in the center of the raw material structure is dehydrated in the latter stage of decompression, and the oil is replaced to impregnate the raw material with oil as a heat medium effective for fuel, and Due to the characteristics of flammable materials as raw materials, Has the effect of a good solid fuels burn efficiency.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 可燃性素材を含有した多水分含有の廃棄
固形物を原料として、これらの原料をクッカー内の加熱
された動物油、植物油、鉱物油等の油中に浸漬し、密閉
されたクッカー内を三段階に減圧しながら加熱された油
を熱媒体として撹拌加熱し、しかも、初期の減圧過程に
おいては、常圧から100mmHg〜300mmHgを減圧した
減圧条件下で処理し、次いで、中期減圧過程において
は、更に100mmHg〜300mmHgを減圧した減圧条件下
で処理し、最後に後期減圧過程においては、絶対圧の1
0mmHg〜60mmHgの減圧条件下で処理を行うことにより
原料中の含水分を分離蒸散すると共にクッカー内の油を
原料組織中に含浸させ、次いで、原料をクッカーから取
出して含油率10〜30%にまで搾油或は脱油して固形
物を得ることを特徴とした廃棄物からの固形燃料の製造
方法。
1. A cooker in which a waste water-containing waste solid material containing a flammable material is used as a raw material, and these raw materials are immersed in heated animal oil, vegetable oil, mineral oil or the like in a cooker and sealed. The heated oil is stirred and heated as a heat medium while decompressing the inside in three stages, and in the initial decompression process, the pressure is reduced from normal pressure to 100 mmHg to 300 mmHg under reduced pressure conditions, and then the medium-term decompression process. In this case, 100 mmHg to 300 mmHg was further depressurized under the depressurized condition.
The water content in the raw material is separated and evaporated by performing the treatment under a reduced pressure condition of 0 mmHg to 60 mmHg, and the oil in the cooker is impregnated into the raw material structure, and then the raw material is taken out from the cooker to obtain an oil content of 10 to 30%. A method for producing a solid fuel from waste, characterized in that solid matter is obtained by squeezing or deoiling.
JP7114694A 1994-04-08 1994-04-08 Production of solid fuel from waste Pending JPH07278581A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7114694A JPH07278581A (en) 1994-04-08 1994-04-08 Production of solid fuel from waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7114694A JPH07278581A (en) 1994-04-08 1994-04-08 Production of solid fuel from waste

Publications (1)

Publication Number Publication Date
JPH07278581A true JPH07278581A (en) 1995-10-24

Family

ID=13452175

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7114694A Pending JPH07278581A (en) 1994-04-08 1994-04-08 Production of solid fuel from waste

Country Status (1)

Country Link
JP (1) JPH07278581A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004209462A (en) * 2002-12-18 2004-07-29 Kobe Steel Ltd Drying method of plant-derived biomass, and production method of biomass fuel
JP6095836B1 (en) * 2016-08-26 2017-03-15 株式会社テクモア Method for infiltrating waste cooking oil into woody material, infiltration device, and biomass power generation system including the same
WO2017179603A1 (en) * 2016-04-15 2017-10-19 株式会社神戸製鋼所 Method for producing modified biomass
JP2017193696A (en) * 2016-04-15 2017-10-26 株式会社神戸製鋼所 Method for producing modified biomass

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004209462A (en) * 2002-12-18 2004-07-29 Kobe Steel Ltd Drying method of plant-derived biomass, and production method of biomass fuel
US7320715B2 (en) 2002-12-18 2008-01-22 Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) Method for drying plant-derived biomass and method for producing biomass fuel
WO2017179603A1 (en) * 2016-04-15 2017-10-19 株式会社神戸製鋼所 Method for producing modified biomass
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JP6095836B1 (en) * 2016-08-26 2017-03-15 株式会社テクモア Method for infiltrating waste cooking oil into woody material, infiltration device, and biomass power generation system including the same
JP2018030961A (en) * 2016-08-26 2018-03-01 株式会社テクモア Method for infiltrating waste food oil into woody material, infiltration device, and biomass power generation system provided therewith

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