JPH03207792A - Continuous wood carbonization device utilizing electric oven - Google Patents
Continuous wood carbonization device utilizing electric ovenInfo
- Publication number
- JPH03207792A JPH03207792A JP2003801A JP380190A JPH03207792A JP H03207792 A JPH03207792 A JP H03207792A JP 2003801 A JP2003801 A JP 2003801A JP 380190 A JP380190 A JP 380190A JP H03207792 A JPH03207792 A JP H03207792A
- Authority
- JP
- Japan
- Prior art keywords
- wood
- zone
- heating
- blower
- container
- 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
- 239000002023 wood Substances 0.000 title claims abstract description 31
- 238000003763 carbonization Methods 0.000 title claims description 9
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 238000001816 cooling Methods 0.000 claims abstract description 17
- 239000000945 filler Substances 0.000 claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 5
- 239000000567 combustion gas Substances 0.000 claims abstract description 3
- 238000011068 loading method Methods 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 abstract 2
- 238000010000 carbonizing Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 230000001590 oxidative effect Effects 0.000 abstract 1
- 239000003610 charcoal Substances 0.000 description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
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
-
- 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
- Coke Industry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、電気炉を利用した連続式木材炭化装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a continuous wood carbonization apparatus using an electric furnace.
従来、木材の炭化には、炭焼窯が利用されている。即ち
、適当な大きさに切断した木材を炭焼窯内に配列し、入
口を塞いで窯に火を入れ、僅かな空気(酸素)が入る状
態を保って一週間ほど不完全燃焼させ、それから火を止
め、窯がある程度冷えるのを待って出炭を行なっている
。Traditionally, charcoal kilns have been used to carbonize wood. That is, the wood cut to an appropriate size is arranged in a charcoal kiln, the entrance is closed, the kiln is turned on, and a small amount of air (oxygen) is allowed to enter to let it burn incompletely for about a week. The kiln is stopped and the coal is extracted after waiting for the kiln to cool down to a certain extent.
上記の炭焼窯による木炭製造においては、一回の作業に
一週間以上の長時間を要する上、木材の配列位置や空気
供給量及び火加減によって木炭の品質が異なる場合があ
った。又炭焼時に生じる亀裂等で窯の状態が毎回微妙に
変化するため、木炭の品質が一定しなくなる恐れがあっ
た。そのため従来の炭焼窯では、上記諸要因の影響につ
いて熟知した熟練者でなければ、安定した品質の木炭を
得にくいという欠点があった。In the production of charcoal using the above-mentioned charcoal kiln, one operation takes a long time of one week or more, and the quality of the charcoal may vary depending on the arrangement position of the wood, the amount of air supplied, and the temperature of the fire. In addition, the condition of the kiln changes slightly each time due to cracks that occur during charcoal firing, so there is a risk that the quality of the charcoal will be inconsistent. Therefore, conventional charcoal kilns have the disadvantage that it is difficult to obtain charcoal of stable quality unless one is an expert who is familiar with the effects of the above factors.
そこで本発明は上記の欠点を解消するために成されたも
のであり、熟練者でなくても、安定した品質の木炭が短
時間で連続的に得られる電気炉を利用した連続式木材炭
化装置を提供することを目的とする。Therefore, the present invention has been made to eliminate the above-mentioned drawbacks, and is a continuous wood carbonization device using an electric furnace that allows stable quality charcoal to be obtained continuously in a short time even without being an expert. The purpose is to provide
前記目的を達或するため、本発明では、加熱帯の前後に
予熱帯と冷却帯を備えた電気炉を用い、予熱帯側搬入口
に扉を付設し、予熱帯にブロワ付き排気口を設け、電気
炉床部に搬入口から冷却帯側搬出口に至るローラコンベ
アを敷設し、ローラコンベア上を搬入口から搬出口へ順
送りに移動させる複数の箱状容器を備え、各容器には木
材と助燃用充填材が収納され、容器に燃焼用気体取込用
の小さな吸気口と加熱生成気体の排出口を設け、ブロワ
の動作により搬出口から排気口への雰囲気の流れを持つ
ことを特徴とする。In order to achieve the above object, the present invention uses an electric furnace equipped with a preheating zone and a cooling zone before and after the heating zone, a door is attached to the entrance on the side of the preheating zone, and an exhaust port with a blower is provided in the preheating zone. , a roller conveyor is installed in the electric hearth section from the loading port to the cooling zone side loading port, and a plurality of box-shaped containers are sequentially moved on the roller conveyor from the loading port to the loading port, and each container is filled with wood and wood. The container contains a filler for auxiliary combustion, and the container has a small intake port for taking in combustion gas and an exhaust port for heated gas, and the atmosphere flows from the outlet to the exhaust port by the operation of a blower. do.
〔作 用〕
本発明による電気炉を利用した連続式木材炭化装置では
、ブロワの動作により常時開口する搬出口から冷却帯、
加熱帯を経て予熱帯の排出口へ向かう雰囲気の流れを生
ずる。箱状容器がローラコンベアに載って予熱帯から加
熱帯、冷却帯と順送りに移動する間に、容器内の木材は
予熱帯で予熱・乾燥され、加熱帯で加熱・炭化され、冷
却帯で冷却され、搬出口から容器ごとに押出される。[Function] In the continuous wood carbonization apparatus using the electric furnace according to the present invention, the cooling zone,
This creates a flow of atmosphere through the heating zone and toward the outlet of the preheating zone. While the box-shaped container is placed on a roller conveyor and sequentially moves from the preheating zone to the heating zone and cooling zone, the wood inside the container is preheated and dried in the preheating zone, heated and carbonized in the heating zone, and cooled in the cooling zone. Each container is then extruded from the outlet.
以下、本発明による電気炉を利用した連続式木材炭化装
置について図面を参照しつつ具体的に説明する。本発明
装置は、加熱帯1の前後に予熱帯2と冷却帯3を備えた
電気炉Fと、この電気炉F内を順送りに移動させる複数
の箱状容器Bとで構成される。Hereinafter, a continuous wood carbonization apparatus using an electric furnace according to the present invention will be specifically described with reference to the drawings. The apparatus of the present invention includes an electric furnace F having a preheating zone 2 and a cooling zone 3 before and after a heating zone 1, and a plurality of box-shaped containers B that are sequentially moved within the electric furnace F.
電気炉Fは各帯域1,2.3が同じ長さで、予熱帯2前
方の搬入口4には扉5と作業台6を設け、冷却帯3後方
の搬出口7に作業台8を付設し、電気炉F内床部と両作
業台6,8上に亘って容器B移送用のローラコンベア9
を敷設し、予熱帯2上部に排気用ブロワ10付排気口1
1を設けてある。In the electric furnace F, each zone 1, 2.3 has the same length, a door 5 and a workbench 6 are installed at the entrance 4 in front of the preheating zone 2, and a workbench 8 is attached to the entrance 7 behind the cooling zone 3. A roller conveyor 9 for transporting the container B is installed over the inner floor of the electric furnace F and both work tables 6 and 8.
Install an exhaust port 1 with an exhaust blower 10 on the top of the preheating zone 2.
1 is provided.
尚、加熱帯1に設ける抵抗発熱体12は加熱帯1内両側
面に配設され、容器Bを両側面から加熱するもので、第
3図の符号13はその電極を示すものである。又、符号
21は電気炉Fの架台を示している。The resistance heating elements 12 provided in the heating zone 1 are disposed on both sides of the heating zone 1 to heat the container B from both sides, and reference numeral 13 in FIG. 3 indicates the electrodes thereof. Further, reference numeral 21 indicates a frame for the electric furnace F.
容器Bは箱状の容器本体14に蓋15を被せるもので、
本体14の先端側下部に容器B内部に通じる一対の筒体
16を設け、筒体16に小さな吸気口17を穿設し、蓋
15の後端側に排出口18を設けてある。容器Bの大き
さと電気炉Fの各帯域1,2.3の大きさとの関係を以
下に示す。Container B is a box-shaped container body 14 covered with a lid 15.
A pair of cylindrical bodies 16 communicating with the inside of the container B are provided at the lower part of the front end side of the main body 14, a small intake port 17 is provided in the cylindrical bodies 16, and an outlet port 18 is provided at the rear end side of the lid 15. The relationship between the size of container B and the size of each zone 1, 2.3 of electric furnace F is shown below.
0.6W≦By≦0.8W
O.6H≦Bh≦0.8H
O.6L≦B1≦0.8L
但し、By,Bh,B1は容器(筒体16は含まない)
の外幅、外高、外長、W, H, Lは各帯域1, 2
. 3の内幅、内高、内長である。0.6W≦By≦0.8W O. 6H≦Bh≦0.8H O. 6L≦B1≦0.8L However, By, Bh, and B1 are containers (does not include cylinder 16)
The outer width, outer height, outer length, W, H, and L are for each band 1 and 2.
.. These are the inner width, inner height, and inner length of 3.
尚、筒体16を含めた容器Bの全長は、各帯域1,2,
3の内長に等しい。The total length of the container B including the cylindrical body 16 is for each zone 1, 2,
Equal to the inner length of 3.
容器B内には木材19と粉状助燃用充填材20が収納さ
れる。充填材20としては、水分が10%程度の乾燥し
たおが屑やもみがら及びその燃えかすが使用され、木材
19を包むようにその隙間を埋めるものである。Inside the container B, wood 19 and powdered combustion auxiliary filler 20 are stored. As the filler 20, dry sawdust, rice husks, and their cinders with a moisture content of about 10% are used, and fill the gaps so as to wrap around the wood 19.
本発明装置は上記の如く構成されており、まず電気炉F
に通電し、ブロワ10を動作させる。ここで、搬入口4
の扉5が通常閉じてあるので、搬出口7から冷却帯3、
加熱帯1、予熱帯2を経て排気口11に至る雰囲気の流
れが生じ、予熱帯2内は加熱帯1からの熱風で温められ
る。そして、木材19と充填材20の収納された容器B
を搬入口4側作業台6上のローラコンベア9に載せ、所
定時間毎に扉5を開けてブッシャ一(図示せず)等で容
器Bを一個分電気炉F内に押込み、扉5を閉じる。この
作業を繰返せば、容器Bは電気炉F内を予熱帯2から加
熱帯1、加熱帯1から冷却帯3へと所定時間毎に順送り
で移動し、ついには搬出口7側の作業台8上に押出され
る。The apparatus of the present invention is constructed as described above.
energizes and operates the blower 10. Here, loading entrance 4
Since the door 5 is normally closed, the cooling zone 3,
An atmosphere flows through the heating zone 1 and the preheating zone 2 to the exhaust port 11, and the inside of the preheating zone 2 is heated by the hot air from the heating zone 1. Container B containing wood 19 and filler 20
is placed on the roller conveyor 9 on the workbench 6 on the side of the loading entrance 4, the door 5 is opened at predetermined intervals, one container B is pushed into the electric furnace F using a busher (not shown), and the door 5 is closed. . By repeating this operation, the container B will be moved in the electric furnace F from the pre-heating zone 2 to the heating zone 1, from the heating zone 1 to the cooling zone 3, at predetermined intervals, and will finally be placed on the workbench on the side of the unloading port 7. Extruded onto 8.
予熱帯2では加熱帯1からの熱風により、容器B内の温
度が約100℃まで上昇し、木材19と充填材20の予
熱及び乾燥が行われる。In the preheating zone 2, the temperature inside the container B rises to about 100° C. by the hot air from the heating zone 1, and the wood 19 and the filler 20 are preheated and dried.
加熱帯1では抵抗発熱体12により約400℃まで加熱
すると、吸気口17から容器B内に入った空気(酸素)
により、充填材20の一部が酸化発熱、即ち焦げるので
、容器B内温度が加熱帯1温度(約400℃)付近まで
上昇し、木材19の熱分解による炭化が促進される。こ
の吸気口17は木材19が完全燃焼することのないよう
、小さくすることが望ましい。熱分解により生ずる二酸
化炭素やタール等の加熱生成気体は排出口18から加熱
帯1、予熱帯2を経て、ブロヮ10により排気口11を
通して吸引排出される。When heated to approximately 400°C by the resistance heating element 12 in the heating zone 1, air (oxygen) enters the container B from the intake port 17.
As a result, part of the filler 20 generates heat of oxidation, that is, burns, and the temperature inside the container B rises to around the temperature of the heating zone 1 (approximately 400° C.), promoting carbonization of the wood 19 due to thermal decomposition. It is desirable that this intake port 17 be made small so that the wood 19 will not be completely burned. Heated gases such as carbon dioxide and tar produced by thermal decomposition pass through the heating zone 1 and the preheating zone 2 from the exhaust port 18, and are sucked and discharged by the blower 10 through the exhaust port 11.
尚、実験の結果、加熱帯1における加熱温度と加熱時間
は、400℃で約1時間が最適の組み合わぜであった。As a result of the experiment, the optimum combination of heating temperature and heating time in heating zone 1 was 400° C. for about 1 hour.
又、380℃乃至400゜Cでは約1時間30分、45
0℃では約40分であった。Also, at 380°C to 400°C, it takes about 1 hour and 30 minutes, 45
At 0°C, it took about 40 minutes.
冷却帯3では、加熱帯1から充分加熱された容器Bが押
出されるが、ブロヮ10により搬出口7から炉外の空気
が流入し、熱くなった容器Bを冷却する。In the cooling zone 3, the sufficiently heated container B is extruded from the heating zone 1, but air from outside the furnace flows in from the outlet 7 by the blower 10 to cool the heated container B.
冷却帯3から搬出口7側作業台8上に押出された容器B
は、蓋15を開け、内部の木材19の炭化物、即ち木炭
を例えばふるいなどで選別する。Container B pushed out from the cooling zone 3 onto the workbench 8 on the side of the outlet 7
Then, the lid 15 is opened and the charcoal, that is, the charcoal of the wood 19 inside, is sorted out using a sieve or the like.
又、燃え残った充填材20及び一部の燃焼物は新たな充
填材20に混合して再使用する。Further, the unburnt filler 20 and some of the combustion materials are mixed with new filler 20 and reused.
この発明は以上述べたように、容器内に木材と一諸に助
燃用充填材を収納し、容器内に少量の酸素を取込む吸気
口と加熱生成気体の吹き出す排出口とを設け、容器ごと
所定温度に加熱して木材を取り囲む充填材の一部を酸化
発熱させるものであるから、木材を短時間で容易にしか
も効率良く炭化できる。As described above, this invention stores a combustion-assisting filler together with wood in a container, and provides an intake port for introducing a small amount of oxygen into the container and an exhaust port for blowing out heated gas. Since it is heated to a predetermined temperature to oxidize and heat a portion of the filler surrounding the wood, the wood can be easily and efficiently carbonized in a short time.
又、加熱帯の前後に予熱帯と冷却帯を備えた電気炉を用
い、その電気炉の床部にローラコンベアを敷設し、木材
と充填材の収納された複数の容器を上記電気炉に順送り
で搬出人するものであるから、加熱温度と加熱時間の制
御が容易に行なえ、従って、均一の炭化条件設定により
品質の安定した木炭の製造を連続的に行なえる。In addition, an electric furnace equipped with a preheating zone and a cooling zone before and after the heating zone is used, and a roller conveyor is installed on the floor of the electric furnace to sequentially transport multiple containers containing wood and filler to the electric furnace. Since the charcoal is carried out by a person, the heating temperature and heating time can be easily controlled, and therefore charcoal of stable quality can be continuously produced by setting uniform carbonization conditions.
第1図は本発明による電気炉を利用した連続式木材炭化
装置の一実施例を示す断面図、第2図は本発明装置の温
度分布図。第3図は第1図A−A線矢視の一部切欠斜視
図、第4図は容器の斜視図、第5図は容器縦断面図であ
る。
B・・・箱状容器、F・・・電気炉、1・・・加熱帯、
2・・・予熱帯、3・・・冷却帯、4・・・搬入口、5
・・・扉、7・・・搬出口、9・・・ローラコンベア、
10・・・ブロワ、11・・・排気口、l7・・・吸気
口、18・・・排出口、19・・・木材、20・・・充
填材10シ多)
手続補正書。
自発)
1
事件の表示
平或2年特許願第3801号
2
発明の名称
5
補正の対象
図面の第2図を別紙の通り,補正する。
第
2
図FIG. 1 is a sectional view showing an embodiment of a continuous wood carbonization apparatus using an electric furnace according to the present invention, and FIG. 2 is a temperature distribution diagram of the apparatus of the present invention. 3 is a partially cutaway perspective view taken along line A--A in FIG. 1, FIG. 4 is a perspective view of the container, and FIG. 5 is a vertical sectional view of the container. B... Box-shaped container, F... Electric furnace, 1... Heating zone,
2... Pre-preparation zone, 3... Cooling zone, 4... Loading entrance, 5
...Door, 7...Exit, 9...Roller conveyor,
10...Blower, 11...Exhaust port, l7...Intake port, 18...Exhaust port, 19...Wood, 20...10 fillers) Procedural amendment. (Spontaneous) 1. Indication of the case: Patent Application No. 3801, filed in 2013. 2. Title of the invention. 5. Figure 2 of the drawing to be amended is amended as shown in the attached sheet. Figure 2
Claims (1)
を備えた電気炉(F)を用い、予熱帯(2)側搬入口4
に扉5を付設し、予熱帯(2)にブロワ(10)付排気
口(11)を設け、電気炉(F)床部に搬入口(4)か
ら冷却帯(3)側搬出口(7)に至るローラコンベア(
9)を敷設し、該ローラコンベア(9)上を順送りに移
動させる複数の箱状容器(B)を備え、容器(B)には
木材(19)と助燃用充填材(20)が収納され、容器
(B)に燃焼用気体を取込む小さな吸気口(17)と加
熱生成気体の排出口(18)を設け、ブロワ(10)の
動作により搬出口(7)から排気口(11)へ至る雰囲
気の流れを持つことを特徴とする電気炉を利用した連続
式木材炭化装置。1. Pre-heating zone (2) and cooling zone (3) before and after heating zone (1)
Using an electric furnace (F) equipped with
A door 5 is attached to the preheating zone (2), an exhaust port (11) with a blower (10) is provided in the preheating zone (2), and an exhaust port (11) with a blower (10) is installed on the floor of the electric furnace (F) from the loading port (4) to the cooling zone (3) side loading port (7). ) to the roller conveyor (
9) and a plurality of box-shaped containers (B) that are sequentially moved on the roller conveyor (9), and the containers (B) contain wood (19) and combustion assisting filler (20). The container (B) is provided with a small intake port (17) for taking in combustion gas and a discharge port (18) for heating generated gas, and is moved from the discharge port (7) to the exhaust port (11) by the operation of the blower (10). A continuous wood carbonization device that uses an electric furnace and is characterized by a continuous flow of atmosphere.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2003801A JPH0699688B2 (en) | 1990-01-10 | 1990-01-10 | Continuous wood carbonizer using electric furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2003801A JPH0699688B2 (en) | 1990-01-10 | 1990-01-10 | Continuous wood carbonizer using electric furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03207792A true JPH03207792A (en) | 1991-09-11 |
JPH0699688B2 JPH0699688B2 (en) | 1994-12-07 |
Family
ID=11567303
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2003801A Expired - Lifetime JPH0699688B2 (en) | 1990-01-10 | 1990-01-10 | Continuous wood carbonizer using electric furnace |
Country Status (1)
Country | Link |
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JP (1) | JPH0699688B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06264078A (en) * | 1993-03-12 | 1994-09-20 | Toru Moriyama | Apparatus for continuously producing charcoal |
JP2008144131A (en) * | 2006-11-17 | 2008-06-26 | Koutaro Tsuchimoto | Method for carbonization treatment of organic waste and continuous heating furnace for carbonization treatment of organic waste |
CN108393993A (en) * | 2018-02-11 | 2018-08-14 | 广西荔浦安吉利木业有限公司 | A kind of preparation method of charing plank |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102586393B1 (en) * | 2021-11-30 | 2023-10-10 | 신근영 | Charcoal production equipment using combustible gas |
KR102586386B1 (en) * | 2021-11-30 | 2023-10-10 | 신근영 | Apparatus for manufacturing charcoal |
-
1990
- 1990-01-10 JP JP2003801A patent/JPH0699688B2/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06264078A (en) * | 1993-03-12 | 1994-09-20 | Toru Moriyama | Apparatus for continuously producing charcoal |
JP2008144131A (en) * | 2006-11-17 | 2008-06-26 | Koutaro Tsuchimoto | Method for carbonization treatment of organic waste and continuous heating furnace for carbonization treatment of organic waste |
JP2013091808A (en) * | 2006-11-17 | 2013-05-16 | Kotaro Tsuchimoto | Heating furnace for carbonizing organic waste |
CN108393993A (en) * | 2018-02-11 | 2018-08-14 | 广西荔浦安吉利木业有限公司 | A kind of preparation method of charing plank |
CN108393993B (en) * | 2018-02-11 | 2020-06-30 | 台州中知英健机械自动化有限公司 | Preparation method of carbonized wood board |
Also Published As
Publication number | Publication date |
---|---|
JPH0699688B2 (en) | 1994-12-07 |
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