JP2001205243A - Charcoal producing method and charcoal - Google Patents
Charcoal producing method and charcoalInfo
- Publication number
- JP2001205243A JP2001205243A JP2000362200A JP2000362200A JP2001205243A JP 2001205243 A JP2001205243 A JP 2001205243A JP 2000362200 A JP2000362200 A JP 2000362200A JP 2000362200 A JP2000362200 A JP 2000362200A JP 2001205243 A JP2001205243 A JP 2001205243A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- coffee grounds
- charcoal
- raw coal
- raw
- 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
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
Description
【０００１】近年缶コーヒーの消費の増大に伴い、工場
より発生するコーヒー粕の排出量が急増している。この
処理には、現在かなりの経費をかけて燃焼、或は産廃業
者が処理しているのが現状である。In recent years, with the increase in consumption of canned coffee, the amount of coffee grounds generated from factories has been rapidly increasing. At present, this processing is currently being carried out by burning or industrial waste companies with considerable expense.
【０００２】コーヒー粕自体は水分９０％ぐらいの細粒
であるため、脱水乾燥するにも経費がかかり、堆肥にす
るにも異臭及害虫が発生して環境衛生上困難を究める。
この処理について、経費をほとんどかけないで処理し、
環境浄化製品を製造するため考案した装置である。[0002] Since coffee grounds itself is fine granules having a water content of about 90%, it is costly to dehydrate and dry it, and when compost is made, an unpleasant odor and pests are generated, and environmental health is difficult.
This process is done with little expense,
This is a device devised to manufacture environmental purification products.
【０００３】１．先ずコーヒー粕の中に、好気性の発酵
菌を混合し特別に考案した「図１」発酵槽に入れる。そ
のまま１０日間くらい放置すれば３日目位からバクテリ
アすなわち好気性細菌の活動により、７５°Ｃ位の高温
になり、槽の通気機孔により水分が蒸散し、約２０％位
迄乾燥する。この際は異臭は発生せず、むしろ糀のよう
な芳香を発生するこの地点で乾燥は終了したのである。[0003] 1. First, an aerobic fermentation bacterium is mixed with coffee grounds and put into a specially designed fermenter (FIG. 1). If left as it is for about 10 days, the temperature rises to about 75 ° C. due to the activity of bacteria, that is, aerobic bacteria, from about the third day, and the water evaporates through the vent hole of the tank and dries to about 20%. At this time, no off-flavor was generated, but rather drying was completed at this point where aroma such as koji was generated.
【０００４】２．この状態のまま第２段階の炭化に入
る。つまり発酵槽が今度は燃焼槽になるので一切の手間
はかからないのである。この発酵燃焼槽「図１」を図
（４）炭化釜へ入れて（６）炊口より廃材又は、薪を燃
やすことにより少しづつ自燃し始める。この状態は炭焼
と同じであるが、この排煙中より（７）木酢油を抽出す
る装置を取り付けました。「図４」の（５）排煙冷却装
置である。[0004] 2. In this state, the second stage carbonization starts. In other words, the fermenter becomes a combustion tank this time, so no effort is required. This fermentation combustion tank “FIG. 1” is put into a carbonization pot as shown in FIG. (4), and (6) self-combustion is started little by little by burning waste or firewood from the cooking port. This condition is the same as that of charcoal-grilling, but a device to extract (7) wood vinegar oil from the smoke was installed. This is the (5) flue gas cooling device shown in FIG.
【０００５】△活性炭の素である素炭 △病害虫防除及土壌活性剤などによい、木酢油を最小の
経費にて製造する装置である。[0005] (1) Raw carbon, which is a raw material of activated carbon.
【図１】 発酵燃焼槽。（３）パンチングメタルの中に
（１）の通気機を取り付けたもの、左側が断面にしたも
の右側が外部である。FIG. 1 Fermentation combustion tank. (3) Punched metal with the ventilator of (1) attached, left side in cross section, right side outside.
【図２】 発醇燃焼槽の側面である左側半分が断面とな
る。 １．通気樋 ３．パンチングメダルFIG. 2 is a cross section of the left half, which is the side surface of the melting combustion tank. 1. Ventilation gutter 3. Punching medal
【図３】 蒸発水分が４にできた通気孔を通って外部へ
放出される。 １．Ｖ字型に整形した樋FIG. 3 evaporates moisture to the outside through a vent formed in 4; 1. V-shaped gutter
【図４】 炭化釜へ発酵燃焼槽を納め、排煙の先端に煙
の冷却ファンを取り付けたものである。FIG. 4 is a diagram in which a fermentation combustion tank is placed in a carbonization pot and a smoke cooling fan is attached to a tip of the smoke exhaust.
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【手続補正書】[Procedure amendment]
【提出日】平成１２年１２月２６日（２０００．１２．
２６）[Submission date] December 26, 2000 (200.12.
26)
【手続補正１】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】特許請求の範囲[Correction target item name] Claims
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【特許請求の範囲】[Claims]
【手続補正２】[Procedure amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】発明の詳細な説明[Correction target item name] Detailed description of the invention
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【発明の属する技術分野】本発明は素炭製造方法及び素
炭に関し、更に詳しくは、コーヒー粕を発酵及び乾燥さ
せ、次いで燃焼槽を用いて炭化させることにより、活性
炭の素である素炭を製造する方法、及びこうして得られ
る素炭に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing raw coal and a raw coal, and more particularly, to ferment and dry coffee grounds and then carbonize using a combustion tank to produce raw carbon as a raw material of activated carbon. It relates to a method for producing and to the raw coal thus obtained.
【従来の技術】近年、缶コーヒーの消費の増大に伴い、
工場より発生するコーヒー粕の排出量が急増している。
現在、このコーヒー粕の処理には、かなりの経費をかけ
て、燃焼処理したり、産廃業者が処理したりしている。2. Description of the Related Art In recent years, with the increase in consumption of canned coffee,
The amount of coffee lees emitted from factories is increasing rapidly.
At present, the processing of the coffee grounds requires a considerable amount of expense, such as a burning treatment or a waste disposal company.
【発明が解決しようとする課題】しかしながら、コーヒ
ー粕自体が９０％ぐらいの水分を含む細粒であるため、
脱水乾燥処理に経費がかかる。又、コーヒー粕を堆肥に
するにも、異臭や害虫が発生して、環境衛生上好ましく
ない。本発明は、上記問題に鑑み、経費をほとんどかけ
ないでコーヒー粕を処理し、活性炭の素として有用な素
炭を製造することを、解決すべき課題とする。However, since the coffee grounds itself is a fine grain containing about 90% of water,
The dehydration and drying process is expensive. Further, even when composting coffee grounds, unpleasant odors and pests are generated, which is not preferable in terms of environmental hygiene. In view of the above problems, it is an object of the present invention to treat coffee grounds with little expense and to produce raw carbon useful as a raw material of activated carbon.
【課題を解決するための手段】（第１発明の構成）上記
課題を解決するための本願第１発明（請求項１に記載の
発明）の構成は、コーヒー粕を発酵させてその発酵熱に
より乾燥させ、次いで燃焼槽を用いて炭化させて活性炭
の素である素炭を製造する、素炭製造方法である。 （第２発明の構成）上記課題を解決するための本願第２
発明（請求項２に記載の発明）の構成は、前記第１発明
に係る発酵を、コーヒー粕に好気性の発酵菌を混合する
ことにより行う、素炭製造方法である。 （第３発明の構成）上記課題を解決するための本願第３
発明（請求項３に記載の発明）の構成は、前記第１発明
又は第２発明に係る発酵の発酵熱によりコーヒー粕を約
７５°Ｃとして水分を蒸散させ、約２０％位まで乾燥す
る、素炭製造方法である。 （第４発明の構成）上記課題を解決するための本願第４
発明（請求項４に記載の発明）の構成は、前記第１発明
〜第３発明のいずれかの方法により得られたものであ
る、素炭である。Means for Solving the Problems (Structure of the First Invention) The structure of the first invention of the present application (the invention as set forth in claim 1) for solving the above-mentioned problems is to ferment coffee grounds and use the fermentation heat thereof. This is a method for producing raw coal, which is dried and then carbonized using a combustion tank to produce raw coal which is a raw material of activated carbon. (Structure of the second invention) A second invention of the present application for solving the above-mentioned problems.
The structure of the invention (the invention described in claim 2) is a method for producing a raw coal, wherein the fermentation according to the first invention is performed by mixing aerobic fermentative bacteria with coffee grounds. (Structure of the third invention) A third invention of the present application for solving the above problems.
The configuration of the invention (the invention according to claim 3) is that the coffee grounds is evaporated to about 75 ° C. by the fermentation heat of the fermentation according to the first invention or the second invention to evaporate water, and dried to about 20%. It is a raw coal production method. (Structure of the fourth invention) The fourth application of the present invention for solving the above-mentioned problems.
The structure of the invention (invention of claim 4) is a raw coal obtained by the method according to any one of the first to third inventions.
【発明の作用・効果】（第１発明の作用・効果）第１発
明によって、活性炭の素である素炭をコーヒー粕より製
造すると言う新しい素炭製造方法が提供される。 （第２発明の作用・効果）第２発明のように、コーヒー
粕に好気性の発酵菌を混合することにより発行を行う
と、好気性発酵菌の活動により温度が上昇して水分が蒸
散し、乾燥が良好になる。 （第３発明の作用・効果）第３発明のように、発酵の発
酵熱によりコーヒー粕を約７５°Ｃとして水分を蒸散さ
せ、約２０％位まで乾燥することが好ましい。この場
合、異臭は発生せず、むしろ糀のような芳香を発生す
る。 （第４発明の作用・効果）上記第１発明〜第３発明のい
ずれかの方法により得られた素炭は、活性炭の素として
利用できる。Operation and Effect of the Invention (Operation and Effect of the First Invention) According to the first invention, a new raw coal production method for producing raw coal, which is a raw material of activated carbon, from coffee grounds is provided. (Action / Effect of the Second Invention) As in the second invention, when issuance is performed by mixing aerobic fermentation bacteria with coffee grounds, the temperature rises due to the activity of the aerobic fermentation bacteria, and water evaporates. , Drying becomes good. (Function / Effect of Third Invention) As in the third invention, it is preferable to evaporate water by setting coffee grounds to about 75 ° C. by fermentation heat of fermentation and drying to about 20%. In this case, no off-flavor is generated, but rather an aroma like koji. (Action / Effect of the Fourth Invention) The raw coal obtained by any one of the first to third inventions can be used as a raw material of activated carbon.
【実施例】先ずコーヒー粕の中に、好気性の発酵菌を混
合し、例えば図１〜図３に示す発酵槽に入れる。そのま
ま１０日間くらい放置すれば、３日目位からバクテリア
すなわち好気性細菌の活動により、７５°Ｃ位の高温に
なり、槽の通気機孔により水分が蒸散し、約２０％位迄
乾燥する。この際は異臭は発生せず、むしろ糀のような
芳香を発生するこの地点で乾燥は終了したのである。こ
の状態のまま第２段階の炭化に入る。例えば、図１〜図
３に示す発酵槽は今度は燃焼槽として利用できる。この
発酵燃焼槽を例えば図４に示す炭化釜へ入れて、炊口６
より廃材又は薪を燃やすことにより、少しづつ自燃し始
める。この状態は、炭焼と同じである。この排煙中より
木酢油７を抽出する装置を取り付けても良い。５は排煙
冷却装置である。以上の、発酵熱による乾燥工程、及び
燃焼槽を用いた炭化工程により、活性炭の素である素炭
が製造される。上記図１〜図４に示す発酵槽や炭化釜
は、発酵や炭化を行うための通常の構成を備えていれば
良い。DESCRIPTION OF THE PREFERRED EMBODIMENTS First, an aerobic fermentation bacterium is mixed with coffee grounds and put into, for example, a fermenter shown in FIGS. If left as it is for about 10 days, the temperature rises to about 75 ° C. due to the activity of bacteria, that is, aerobic bacteria, from about the third day. At this time, no off-flavor was generated, but rather drying was completed at this point where aroma such as koji was generated. In this state, the second stage carbonization starts. For example, the fermenter shown in FIGS. 1-3 can now be used as a combustion tank. This fermentation combustion tank is put into, for example, a carbonization pot shown in FIG.
By burning more waste wood or firewood, it starts to burn itself little by little. This state is the same as charcoal making. A device for extracting the wood vinegar oil 7 from the exhaust gas may be attached. 5 is a smoke exhaust cooling device. By the above-described drying process using fermentation heat and the carbonization process using a combustion tank, raw coal, which is a raw material of activated carbon, is produced. The fermenter and the carbonization pot shown in FIGS. 1 to 4 may have a normal configuration for performing fermentation and carbonization.
Claims (4)
り乾燥させ、次いで燃焼槽を用いて炭化させて活性炭の
素である素炭を製造することを特徴とする素炭製造方
法。1. A method for producing raw coal, comprising fermenting coffee grounds, drying it by the heat of fermentation, and carbonizing it using a combustion tank to produce raw carbon, which is a raw material of activated carbon.
菌を混合することにより行うことを特徴とする請求項１
に記載の素炭製造方法。2. The fermentation according to claim 1, wherein the fermentation is performed by mixing aerobic fermentation bacteria with coffee grounds.
The method for producing a raw coal described in 1.
７５°Ｃとして水分を蒸散させ、約２０％位まで乾燥す
ることを特徴とする請求項１又は請求項２に記載の素炭
製造方法。3. The method according to claim 1, wherein the coffee grounds is evaporated to about 75 ° C. by the fermentation heat of the fermentation to evaporate water and dried to about 20%. .
炭。4. A raw coal obtained by the method according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000362200A JP3532151B2 (en) | 2000-11-29 | 2000-11-29 | Raw coal production method and raw coal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000362200A JP3532151B2 (en) | 2000-11-29 | 2000-11-29 | Raw coal production method and raw coal |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6313965A Division JPH08132016A (en) | 1994-11-11 | 1994-11-11 | Equipment for producing elemental carbon |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001205243A true JP2001205243A (en) | 2001-07-31 |
| JP3532151B2 JP3532151B2 (en) | 2004-05-31 |
Family
ID=18833518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000362200A Expired - Lifetime JP3532151B2 (en) | 2000-11-29 | 2000-11-29 | Raw coal production method and raw coal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3532151B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263617A (en) * | 2001-03-07 | 2002-09-17 | Ryoichi Okamoto | Waste treatment equipment |
| US11394922B2 (en) | 2020-01-31 | 2022-07-19 | Hyperconnect Inc. | Terminal and operating method thereof |
| US11716424B2 (en) | 2019-05-10 | 2023-08-01 | Hyperconnect Inc. | Video call mediation method |
-
2000
- 2000-11-29 JP JP2000362200A patent/JP3532151B2/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263617A (en) * | 2001-03-07 | 2002-09-17 | Ryoichi Okamoto | Waste treatment equipment |
| US11716424B2 (en) | 2019-05-10 | 2023-08-01 | Hyperconnect Inc. | Video call mediation method |
| US11394922B2 (en) | 2020-01-31 | 2022-07-19 | Hyperconnect Inc. | Terminal and operating method thereof |
| US11825236B2 (en) | 2020-01-31 | 2023-11-21 | Hyperconnect Inc. | Terminal and operating method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3532151B2 (en) | 2004-05-31 |
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