JP2551958B2 - Charcoal manufacturing method and apparatus - Google Patents
Charcoal manufacturing method and apparatusInfo
- Publication number
- JP2551958B2 JP2551958B2 JP62328872A JP32887287A JP2551958B2 JP 2551958 B2 JP2551958 B2 JP 2551958B2 JP 62328872 A JP62328872 A JP 62328872A JP 32887287 A JP32887287 A JP 32887287A JP 2551958 B2 JP2551958 B2 JP 2551958B2
- Authority
- JP
- Japan
- Prior art keywords
- charcoal
- wood
- combustion chamber
- combustible gas
- chamber
- 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.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
-
- 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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Coke Industry (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) この発明は、木炭の製造方法およびその装置に関する
ものである。TECHNICAL FIELD The present invention relates to a method of manufacturing charcoal and an apparatus thereof.
(従来技術) 従来、木炭の製造にあっては燃焼室で発生する熱で炭
化室の木材の一部を燃やし、蒸し焼きにして揮発分、水
分を分離して木材を炭化させて収炭していた。(Prior Art) Conventionally, in the manufacture of charcoal, a part of the wood in the carbonization chamber is burned by the heat generated in the combustion chamber and steamed to separate volatile components and water, and the wood is carbonized to collect coal. It was
そして、この木炭製造過程に於て、生成する水蒸気は
冷却することにより木酢酸及び木タールとして回収され
るが、タールを含む非凝縮性の生成ガスは炭焼き窯の煙
として大気に放出されていた。Then, in this charcoal production process, the steam generated is recovered as wood acetic acid and wood tar by cooling, but the non-condensable product gas containing tar was released to the atmosphere as smoke from a charcoal kiln. .
(発明の解決すべき問題点) しかしながら、製炭に要する時間が掛ることと収炭量
が少ないことのため、木炭の需要はあっても採算が合わ
ず木炭の製造を取り止める人が増え、結果として木炭は
高価となっていた。ところで、先述した生成ガス中には
可燃性ガスが多量に含まれているにもかかわらず、無駄
に放出されてしまっていた。(Problems to be solved by the invention) However, due to the time required for charcoal making and the small amount of charcoal collected, the number of people who withdraw from charcoal production due to an unprofitable increase in charcoal demand As charcoal was expensive. By the way, although the generated gas described above contains a large amount of combustible gas, it has been wasted.
(発明の目的) そこで、この発明は、木炭の価格を低下させるため木
炭の製造時間を短縮しかつ収炭量を増加させることを目
的としている。(Object of the invention) Therefore, an object of the present invention is to shorten the production time of charcoal and increase the amount of charcoal to reduce the price of charcoal.
(発明の構成) この目的を達成するため、第1の発明は燃焼室で発生
する熱で炭化室の木材の一部を燃やし、蒸し焼きにして
揮発分、水分を分離して前記木材を炭化させて収炭する
木炭の製造方法において、 前記炭化室で木材から発生した可燃性ガスを粗木酢液
に触れさせ吸着させて吸着されなかった可燃性ガスを前
記燃焼室に強制循環させて燃焼させることを特徴とする
木炭の製造方法とし、 第2の発明は、点火燃焼可能な燃焼室と、 該燃焼室の熱を受けて入れた木材を炭化燃焼させて木
炭とし、該木炭を取り出すことが可能な炭化室と、 該炭化室において炭化燃焼の過程で発生した可燃ガス
を前記燃焼室へ強制循環させる循環手段とからなり、 該循環手段は、前記炭化室の上部から可燃性ガスを集
める集合ダクトと、該集合ダクトからの可燃性ガスを粗
木酢液中に導き、吸着させるタンクと、該タンクの上部
に粗木酢液に吸着されず集まった可燃性ガスを前記燃焼
室に導く可燃性ガスファンとからなることを特徴とする
木炭の製造装置としている。(Structure of the Invention) In order to achieve this object, the first invention burns a part of the wood in the carbonization chamber with heat generated in the combustion chamber and steams it to separate volatile components and water to carbonize the wood. In the method for producing charcoal to collect coal, the combustible gas generated from wood in the carbonization chamber is contacted with the crude wood vinegar to be adsorbed and the unadsorbed combustible gas is forcibly circulated in the combustion chamber to burn. A second aspect of the present invention is a charcoal manufacturing method, wherein the second invention is a combustion chamber capable of igniting and burning, and the wood received by the heat of the combustion chamber is carbonized and burned to obtain the charcoal. And a circulation means for forcibly circulating the combustible gas generated in the carbonization chamber in the carbonization combustion process to the combustion chamber, the circulation means collecting duct collecting the combustible gas from the upper part of the carbonization chamber. And the gathering duct Of the combustible gas introduced into the crude wood vinegar and adsorbing it, and a combustible gas fan that guides the combustible gas collected in the upper part of the tank without being adsorbed to the crude wood vinegar into the combustion chamber. It is used as a charcoal manufacturing device.
(作用) 炭化室で生成される可燃性ガスを燃焼室へ強制的に循
環させ、燃焼室で燃焼させることにより、供給燃料を少
なくしても炭化室温度を急速上昇でき、省エネルギー化
が可能となり、さらに熱をもった生成ガスを強制循環す
るので熱伝導率の向上が図れる。(Function) Combustible gas generated in the carbonization chamber is forcibly circulated to the combustion chamber and combusted in the combustion chamber, so that the temperature of the carbonization chamber can be rapidly raised even if the supply fuel is reduced, and energy can be saved. Further, since the generated gas with heat is forcedly circulated, the thermal conductivity can be improved.
(実施例) 次にこの発明の一実施例を添付図面に基づいて説明す
る。(Embodiment) Next, an embodiment of the present invention will be described with reference to the accompanying drawings.
図は、この第1発明の木炭の製造方法に使用する第2
発明の木炭の製造装置の概略構成図である。The figure shows the second embodiment of the charcoal production method of the first invention.
It is a schematic block diagram of the charcoal manufacturing apparatus of invention.
図中、1は燃焼室で、そこには必要な空気を供給し点
火燃焼をさせるパイロットバーナ4が水平方向側壁に設
けられ、反対側の側壁に排気ガスを放出する煙室5が設
けられ、天井壁に簀子状に穴のあいたロストル7を介し
て燃焼室1の上部には燃焼室1の熱を受ける炭化室9が
設けられ、ここには木炭となる原材料である木材11が上
方に開閉自在の蓋13部から投入充填されている。In the figure, 1 is a combustion chamber, in which a pilot burner 4 for supplying necessary air to perform ignition combustion is provided on a horizontal side wall, and a smoke chamber 5 for discharging exhaust gas is provided on the opposite side wall, A carbonization chamber 9 that receives the heat of the combustion chamber 1 is provided above the combustion chamber 1 through a rostrut 7 having a hole like a ceiling on the ceiling wall, and a wood 11 which is a raw material for charcoal is opened and closed upwards. It is charged and filled from 13 parts of the free lid.
炭化室9の側壁下部には炭化室9内の燃焼炭化状況を
見る内部検視孔15が設けられ、側壁上部には例えば鉢巻
き状に集合ダクト17が設けられている。この集合ダクト
17と炭化室9とを連通させている孔18が炭化室9の側壁
には多数形成され、そこから炭化室9内で炭化燃焼過程
で生成した生成ガスを集合させ得る。An internal inspection hole 15 for viewing the combustion and carbonization state inside the carbonization chamber 9 is provided at the lower part of the side wall of the carbonization chamber 9, and a collecting duct 17 is provided at the upper part of the side wall, for example, in the shape of a headband. This collecting duct
A large number of holes 18 that communicate 17 with the carbonization chamber 9 are formed in the side wall of the carbonization chamber 9, from which the generated gas generated in the carbonization combustion process can be collected.
集合ダクト17と燃焼室1との間には生成ガス中の少な
くとも可燃ガスを集合ダクト17から燃焼室9へ強制的に
循環させる循環手段が設けられている。この循環手段に
は可燃ガスファン19を中間に備えたパイプで集合ダクト
17の燃焼室1とを連結させればよい。この実施例におい
ては、粗大酢液が上方を一部残して充填されたタンク21
が設けられ、このタンク21の下部から木酢液循環ポンプ
23を介して延び、さらにタンク21の上方から上壁を貫通
して十分液中に没して先端を開放しているパイプ25が設
けられている。Between the collecting duct 17 and the combustion chamber 1, there is provided a circulation means for forcibly circulating at least the combustible gas in the generated gas from the collecting duct 17 to the combustion chamber 9. This circulation means is a pipe with a combustible gas fan 19 in the middle and a collecting duct.
17 combustion chambers 1 may be connected. In this embodiment, a tank 21 filled with a coarse vinegar solution with a part of the upper part left
Is installed and the wood vinegar circulation pump is installed from the bottom of this tank 21.
A pipe 25 is provided which extends through 23 and further penetrates the upper wall from above the tank 21 and is fully immersed in the liquid to open the tip.
このパイプ25の液中に没する側の鉛直部分のタンク21
の上方部分にはジェットスクラバー27が設けられ、この
ジェットスクラバー27には集合ダクト17からのパイプ29
が接続されている。ジェットスクラバー27は集合ダクト
17からの生成ガスを吸引するとともにここにおいて粗木
酢液をシャワー状に噴霧し、生成ガスを吸着させ、タン
ク21内の粗木酢液に入れる。The tank 21 in the vertical portion of the pipe 25 on the side submerged in the liquid
A jet scrubber 27 is provided in the upper part of the pipe, and a pipe 29 from the collecting duct 17 is attached to the jet scrubber 27.
Is connected. Jet scrubber 27 is a collecting duct
The generated gas from 17 is sucked, and at the same time, the crude wood vinegar is sprayed in a shower shape to adsorb the generated gas and put into the crude wood vinegar in the tank 21.
このタンク21の上壁には燃焼室1に接続されるパイプ
31が設けられ、この中間に燃焼室1側へ送る可燃ガスフ
ァン19が設けられている。またタンク21内の増加した粗
木酢液を抜くバルブ33が設けられている。A pipe connected to the combustion chamber 1 on the upper wall of this tank 21.
31 is provided, and in the middle thereof, a combustible gas fan 19 for sending to the combustion chamber 1 side is provided. Further, a valve 33 for removing the increased coarse wood vinegar in the tank 21 is provided.
このような構造の木炭の製造装置を用いて、木炭の製
造方法を説明する。A charcoal manufacturing method will be described using the charcoal manufacturing apparatus having such a structure.
まず、炭化室9の蓋13を開けて、ここに木炭にする原
材料である木材11を充填し、後に蓋13を閉じる。パイロ
ットバーナ4に点火し、燃焼室1の温度を約350℃に上
昇させる。この熱ガスは一部分は煙突5から大気へ、残
りは可燃ガスファン19の吸引により炭化室9内にロスト
ル7を介して送られる。この熱で木材11の一部を燃や
し、自己燃焼の発熱で炭化室9内の温度を炭化温度まで
高くして木材11を蒸し焼きにして木材11から揮発分、水
分を蒸発させて炭化させる。First, the lid 13 of the carbonization chamber 9 is opened, the wood 11 which is a raw material for making charcoal is filled therein, and the lid 13 is closed later. The pilot burner 4 is ignited to raise the temperature of the combustion chamber 1 to about 350 ° C. A part of this hot gas is sent from the chimney 5 to the atmosphere, and the rest is sent to the inside of the carbonization chamber 9 through the roster 7 by suction of the combustible gas fan 19. A part of the wood 11 is burned by this heat, and the temperature in the carbonization chamber 9 is raised to the carbonization temperature by the heat generated by self-combustion, and the wood 11 is steam-baked to evaporate volatile components and moisture from the wood 11 to carbonize it.
木材11から分離蒸発させられたガス、この煙りの中に
は可燃性ガスが含まれている。この生成ガスをパイプ29
を通してジェットスクラバー27へ送り、ここで木酢液循
環ポンプ23で送られた粗木酢液をシャワーし、粗木酢液
に吸着させるとともにパイプ25を通ってタンク21の粗木
酢液中を通過させる。ここで粗木酢液に溶融しない可燃
性ガスは気泡となってタンク21の上部空間に溜まる。こ
の間水蒸気は水や木酢酸や木タールとして回収される。Combustible gas is contained in the smoke, which is the gas separated and evaporated from the wood 11. This generated gas is pipe 29
To the jet scrubber 27 through which the coarse wood vinegar sent by the wood vinegar circulation pump 23 is showered to be adsorbed by the coarse wood vinegar and passed through the pipe 25 through the coarse wood vinegar in the tank 21. Here, the flammable gas that does not melt in the coarse wood vinegar becomes bubbles and collects in the upper space of the tank 21. During this time, steam is recovered as water, wood acetic acid, and wood tar.
タンク21の上部空間に溜まった可燃性ガスは可燃性ガ
スファン19により燃焼室1に送り込まれ、パイロットバ
ーナ4の燃焼圏に入りここで供給される空気を受けて燃
焼発熱する。すなわち可燃性ガス成分の熱量は炭化木材
質の保有する熱量の1/3を占めており、この熱量をリサ
イクルし木材自身の燃焼分すなわち、自燃する木材の量
が減少する。それで製炭時間の短縮と収炭量の増加を図
っている。できた炭は、蓋13を開けて取り出される。The combustible gas accumulated in the upper space of the tank 21 is sent to the combustion chamber 1 by the combustible gas fan 19, enters the combustion zone of the pilot burner 4, and receives the air supplied here to generate heat by combustion. That is, the calorific value of the combustible gas component occupies 1/3 of the calorific value of the carbonized wood material, and by recycling this calorific value, the amount of combustion of the wood itself, that is, the amount of self-combusting wood decreases. Therefore, we are trying to shorten the coal production time and increase the amount of coal collected. The charcoal produced is taken out by opening the lid 13.
この木炭の製造装置における定常運転時における温度
の一例は、燃焼室1の熱ガスの温度を350℃としている
とき、煙突5からの排気ガスの温度は230℃であり、燃
焼室1の350℃の熱ガスが炭化材に伝熱され、炭化材か
らの生成ガスで集合ダクト17の位置の温度が100℃であ
る。また、自然対流では時間当り30m3の熱ガスの通過量
であり、強制対流では時間当り600m3にもなる。したが
って上記のような場合の熱伝達量は、 強制対流の場合(熱伝達率0.45kcal/m2h・k) (350℃−100℃)×600m3/h×0.45kcal/m2h・k =675000kcal/h 自然対流の場合(熱伝達率0.03kcal/m2h・k) (350℃−100℃)×30m3/h×0.03kcal/m2h・k =225kcal/h となり、強制循環させることにより、炭化室9への大量
の熱をパイロットバーナ4でのガスを供給することな
く、可燃性ガスの燃焼で供給することができる。An example of the temperature during steady operation in this charcoal manufacturing device is that when the temperature of the hot gas in the combustion chamber 1 is 350 ° C, the temperature of the exhaust gas from the chimney 5 is 230 ° C, and the temperature of the combustion chamber 1 is 350 ° C. Is transferred to the carbonized material, and the temperature at the position of the collecting duct 17 is 100 ° C. due to the generated gas from the carbonized material. In natural convection, the flow rate of hot gas is 30 m 3 per hour, and in forced convection, it reaches 600 m 3 per hour. Therefore, the amount of heat transfer in the above case is the case of forced convection (heat transfer coefficient 0.45kcal / m 2 h ・ k) (350 ℃ -100 ℃) × 600m 3 / h × 0.45kcal / m 2 h ・ k = 675,000 kcal / h In case of natural convection (heat transfer rate 0.03 kcal / m 2 h ・ k) (350 ℃ -100 ℃) × 30 m 3 / h × 0.03 kcal / m 2 h ・ k = 225 kcal / h, forced circulation By doing so, a large amount of heat to the carbonization chamber 9 can be supplied by burning the combustible gas without supplying the gas in the pilot burner 4.
このように、炭化室9内の温度の伝熱は炭化室9が密
閉され空気の供給を受けないものではなく、高温の燃焼
ガスが直接通過していくようになっており、伝導や放射
よりも高温ガスの強制循環による対流が主であり、顕熱
の伝達を良好とし炭化を促進している。As described above, the heat transfer of the temperature in the carbonization chamber 9 is not such that the carbonization chamber 9 is sealed and does not receive the supply of air, but the high-temperature combustion gas directly passes therethrough. In particular, convection due to forced circulation of high-temperature gas is the main, and it promotes carbonization by making sensible heat transfer good.
なお、生成ガスの温度が集合ダクト17の位置で約90℃
になったときリサイクルされた可燃性ガスに点火すれ
ば、燃焼が安定続行するとともに強制循環の高温ガスに
よる炭化が行なわれ、自燃する木材が減少するため、そ
の収炭量が乾木材の33%を記録した。これは従来の収炭
量が16〜18%であるに比較して大変な増加である。The temperature of the generated gas is about 90 ° C at the position of the collecting duct 17.
If the flammable gas recycled is ignited, the combustion will continue to be stable and carbonization by the hot gas of forced circulation will be carried out, and the self-combusting wood will decrease, so the amount of coal collected will be 33% of the dry wood. Was recorded. This is a huge increase compared to the conventional coal amount of 16-18%.
また、高温ガスの循環による対流の熱伝達の繰り返し
で、炭化温度までの時間が従来の方法に比較して1/10に
短縮することが可能となった。In addition, by repeating convective heat transfer by circulating high-temperature gas, it became possible to reduce the time to carbonization temperature to 1/10 of the conventional method.
(効果) 以上説明したように、この発明によれば、木炭の製造
時間を短縮し、かつ収炭量を増加させることができ、さ
らには燃料使用量も少なくして省資源エネルギの趣旨に
沿った効果を発揮することができる。(Effects) As described above, according to the present invention, it is possible to shorten the production time of charcoal, increase the amount of coal collected, and reduce the amount of fuel used, which is in line with the purpose of resource saving energy. It is possible to exert the effect.
図はこの発明に係る木炭の製造装置の概略構成図であ
る。 1……燃焼室、4……パイロットバーナ 5……煙突、9……炭化室 11……木材、17……集合ダクト 19……可燃性ガスファン、21……タンクFIG. 1 is a schematic configuration diagram of a charcoal manufacturing apparatus according to the present invention. 1 ... Combustion chamber, 4 ... Pilot burner 5 ... Chimney, 9 ... Carbonization chamber 11 ... Wood, 17 ... Collecting duct 19 ... Combustible gas fan, 21 ... Tank
Claims (2)
を燃やし、蒸し焼きにして揮発分、水分を分離して前記
木材を炭化させて収炭する木炭の製造方法において、 前記炭化室で木材から発生した可燃性ガスを粗木酢液に
触れさせ吸着させて、吸着されなかった可燃性ガスを前
記燃焼室に強制循環させて燃焼させることを特徴とする
木炭の製造方法。1. A method for producing charcoal in which a part of wood in a carbonization chamber is burned by heat generated in a combustion chamber and steamed to separate volatile components and moisture to carbonize the wood to collect charcoal. A method for producing charcoal, characterized in that a flammable gas generated from wood in a room is brought into contact with a crude wood vinegar solution to be adsorbed, and the unadsorbed combustible gas is forcedly circulated in the combustion chamber to be burned.
とし、該木炭を取り出すことが可能な炭化室と、 該炭化室において炭化燃焼の過程で発生した可燃ガスを
前記燃焼室へ強制循環させる循環手段とからなり、 該循環手段は、前記炭化室の上部から可燃性ガスを集め
る集合ダクトと、該集合ダクトからの可燃性ガスを粗木
酢液中に導き、吸着させるタンクと、該タンクの上部に
粗木酢液に吸着されず集まった可燃性ガスを前記燃焼室
に導く可燃性ガスファンとからなることを特徴とする木
炭の製造装置。2. A combustion chamber capable of igniting and burning, a charcoal that charcoal-burns wood that has received heat of the combustion chamber, and can take out the charcoal, and charring combustion in the charring chamber. And a circulation means for forcibly circulating the combustible gas generated in the process to the combustion chamber, the circulation means collecting the combustible gas from the upper part of the carbonization chamber and the combustible gas from the collection duct. Manufacture of charcoal, characterized by comprising a tank for introducing and adsorbing in the crude wood vinegar, and a combustible gas fan for guiding the combustible gas collected in the upper part of the tank without being adsorbed by the crude wood vinegar to the combustion chamber. apparatus.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62328872A JP2551958B2 (en) | 1987-12-25 | 1987-12-25 | Charcoal manufacturing method and apparatus |
| KR1019880017478A KR910004937B1 (en) | 1987-12-25 | 1988-12-26 | Charcoal manufacturing method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62328872A JP2551958B2 (en) | 1987-12-25 | 1987-12-25 | Charcoal manufacturing method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01168796A JPH01168796A (en) | 1989-07-04 |
| JP2551958B2 true JP2551958B2 (en) | 1996-11-06 |
Family
ID=18215037
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62328872A Expired - Lifetime JP2551958B2 (en) | 1987-12-25 | 1987-12-25 | Charcoal manufacturing method and apparatus |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP2551958B2 (en) |
| KR (1) | KR910004937B1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101505872B1 (en) * | 2014-09-25 | 2015-03-25 | 백종현 | A charcoal for loess kiln and a method of roasting using the same |
| JP6530036B2 (en) * | 2017-10-30 | 2019-06-12 | 義麟 黄 | Organic matter decomposer |
| JP7029731B2 (en) * | 2019-05-14 | 2022-03-04 | 義麟 黄 | Organic matter decomposer |
-
1987
- 1987-12-25 JP JP62328872A patent/JP2551958B2/en not_active Expired - Lifetime
-
1988
- 1988-12-26 KR KR1019880017478A patent/KR910004937B1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| KR890010162A (en) | 1989-08-07 |
| KR910004937B1 (en) | 1991-07-18 |
| JPH01168796A (en) | 1989-07-04 |
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