JPH1121560A - Carbonization furnace unit - Google Patents
Carbonization furnace unitInfo
- Publication number
- JPH1121560A JPH1121560A JP9208283A JP20828397A JPH1121560A JP H1121560 A JPH1121560 A JP H1121560A JP 9208283 A JP9208283 A JP 9208283A JP 20828397 A JP20828397 A JP 20828397A JP H1121560 A JPH1121560 A JP H1121560A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- ejector
- carbonization
- kiln
- gas
- 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
Links
- 238000003763 carbonization Methods 0.000 title claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 6
- 238000002485 combustion reaction Methods 0.000 claims description 18
- 238000000197 pyrolysis Methods 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 7
- 238000010304 firing Methods 0.000 abstract description 3
- 239000010815 organic waste Substances 0.000 abstract description 2
- 239000002023 wood Substances 0.000 abstract description 2
- 239000000919 ceramic Substances 0.000 abstract 4
- 239000011800 void material Substances 0.000 abstract 3
- 239000007789 gas Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000005539 carbonized material Substances 0.000 description 4
- 238000010000 carbonizing Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000007670 refining Methods 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
Landscapes
- Coke Industry (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は木材等の植物をはじめ
様々な建築廃材や有機廃棄物等を広汎に効率よく炭化さ
せる炭化炉装置において利用される。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used in a carbonizing furnace for widely and efficiently carbonizing various building wastes, organic wastes, etc., including plants such as wood.
【0002】[0002]
【従来の技術】炭類を作るための炭化炉は、昔からよく
知られた黒炭窯や白炭窯の他に、様々な連続又は不連続
窯やロータリーキルンにおいて内部を非酸化的環境にし
たものが広く使われている。2. Description of the Related Art In addition to the well-known black charcoal kiln and white charcoal kiln, various types of continuous or discontinuous kilns and rotary kilns with a non-oxidizing environment are used for making charcoal. Widely used.
【0003】[0003]
【発明が解決しようとする課題】このような従来の炭化
炉に共通して言えることは、窯の内部における温度ムラ
が大きくなりがちで、部分的に高温になりすぎたり燃焼
(灰化)してしまうことが多いために炭の品質を高度に
保つには効率が悪く、廃棄物をも含めた多様な材料を炭
化するには採算や排煙処理等において難点があった。本
発明はかかる難点を解消して、廃棄物等の有機物を有用
な吸着性その他の物性を備えた炭類に効率よく変化させ
ることのできる炭化炉を提供することを課題とする。What can be said in common with such a conventional carbonizing furnace is that the temperature unevenness inside the kiln tends to be large, and the temperature becomes partially too high or burns (ashes). However, it is inefficient to maintain high quality coal, and there are difficulties in carbonizing various materials, including waste, in terms of profitability and flue gas treatment. An object of the present invention is to provide a carbonization furnace capable of solving such difficulties and efficiently converting organic matter such as waste into coal having useful adsorptivity and other physical properties.
【0004】[0004]
【課題を解決するための手段】窯炉(1)における被炭
化物(2)を収容する通気性バケット(3)の上方に着
火バーナー(4)に連なる空隙(5)を設け、該通気性
バケット(3)の下方に位置する隙間部(6)より吸気
管(7)を設けて窯炉(1)の外に導出し、これにエゼ
クター(8)を取り付けてその先の乾留ガス燃焼炉
(9)に連結する。In the kiln (1), an air gap (5) connected to an ignition burner (4) is provided above a gas permeable bucket (3) for accommodating a carbonized material (2). An intake pipe (7) is provided from the gap (6) located below (3) and led out of the kiln (1), and an ejector (8) is attached to the intake pipe (7). Connect to 9).
【0005】また上記の窯炉(1)、吸気管(7)、及
びエゼクター(8)等からなる同様の連なりが図面のよ
うにもう一つ或いは複数、該乾留ガス燃焼炉(9)に連
結されるようにすることが望ましい。[0005] Further, as shown in the drawing, one or more of the same series of the kiln (1), the intake pipe (7), the ejector (8) and the like are connected to the carbonization gas combustion furnace (9). It is desirable to be done.
【0006】さらに乾留ガス燃焼炉(9)の上方に設け
た排気管(10)の少なくとも一部を窯炉(1)の上方
の空隙(5)に連通させることが一層望ましい。これも
図面のように、排気管(10)を分岐させて双方の該空
隙(5)に至るように窯炉(1)を貫通させるものとす
る。[0006] It is further desirable that at least a part of an exhaust pipe (10) provided above the dry distillation gas combustion furnace (9) communicates with a space (5) above the kiln (1). Also in this case, as shown in the drawing, the exhaust pipe (10) is branched and penetrated through the kiln (1) so as to reach both the gaps (5).
【0007】なお充分に炭化が進んだ時点において、バ
ケット(3)内の被炭化物(2)に水を上方より噴射し
て炭の内部の残留物を飛ばし微細空泡化する。その水噴
射装置の図示は省略するが、これば既存の技術・設計に
より容易に達成できる。When the carbonization has sufficiently proceeded, water is sprayed from above onto the carbonized material (2) in the bucket (3) to blow off the residue inside the charcoal and form fine bubbles. Although illustration of the water injection device is omitted, this can be easily achieved by existing technology and design.
【0008】[0008]
【作用】窯炉(1)内の被炭化物(2)は、通常の下か
らの加熱と異なり、上方における着火バーナー(4)の
火炎によってその上部より加熱される。従ってそのまま
では対流現象が起こらず、下部の加熱ができないが、本
発明においては下方に設けられた吸気管(7)よりエゼ
クター(8)の吸引力で窯炉(1)内の気体を吸引する
ので、それに伴い堆積した被炭化物(2)の隙間に存在
する気体も熱とともに下方に移行して通気性バケット
(3)の外に出る。The object to be carbonized (2) in the kiln (1) is heated from above by the flame of the ignition burner (4) at the upper part, unlike ordinary heating from below. Therefore, the convection phenomenon does not occur as it is, and the lower part cannot be heated, but in the present invention, the gas in the kiln (1) is sucked from the suction pipe (7) provided below by the suction force of the ejector (8). Therefore, the gas present in the gaps between the carbonized materials (2) deposited therewith also moves downward with heat and exits the permeable bucket (3).
【0009】その結果、被炭化物(2)の自燃作用も徐
々に下方に移行するが、その際、従来のような自然対流
を伴う場合と異なり過熱化しにくく、焼きムラをおこし
たり白炭化することなくより均一かつ効率的に炭化でき
ることが判明した。As a result, the self-combustion action of the material to be carbonized (2) also gradually shifts downward. At this time, unlike the conventional case involving natural convection, it is difficult to overheat, causing uneven burning and white carbonization. It has been found that carbonization can be performed more uniformly and efficiently.
【0010】炉内の残留酸素量が少ないため自燃作用も
限定されるが、乾留ガスは下方から吸引されて空気と混
合しつつエゼクター(8)を経て前記燃焼炉(9)に到
り、ここで完全燃焼される。これも既存の技術で二重の
燃焼装置を設けるなどして完全燃焼率を一層高めること
ができ、またその燃焼熱を任意に有効利用することもで
きる。Although the amount of residual oxygen in the furnace is small, the self-combustion action is also limited. However, the carbonized gas is sucked from below and mixed with air to reach the combustion furnace (9) via the ejector (8). Is completely burned. In this case as well, the complete combustion rate can be further increased by providing a double combustion device with existing technology, and the combustion heat can be arbitrarily and effectively used.
【0011】その燃焼炉(9)から排出される排気は上
方の排気管(10)に移行するが、これは分岐して再び
窯炉(1)の上部空隙(5)内に少なくとも一部進入す
る。従ってそれのもつ熱は再利用されて再び吸気管
(7)より吸引され、再度、同じ燃焼炉(9)に送り込
まれて完全燃焼することになる。なおこのような気体の
流量の調節や開閉は管の要所に取り付けられたダンパー
(11)で行うことができる。The exhaust gas discharged from the combustion furnace (9) is transferred to an upper exhaust pipe (10), which branches and at least partially enters the upper space (5) of the furnace (1) again. I do. Therefore, the heat of the heat is reused, sucked again from the intake pipe (7), and sent again to the same combustion furnace (9) to be completely burned. Adjustment and opening / closing of such a gas flow rate can be performed by a damper (11) attached to a key point of the pipe.
【0012】更にこのような一連の窯炉(1)等を該燃
焼炉(9)の一方のみでなく、他方からも同様に設けて
連結しておくと、一方の被炭化物(2)が炭化終了して
取り変えるような場合でも、他方の窯炉が稼働しておれ
ば、燃焼炉(9)は消すことなく連続稼働することがで
き、甚だ効率的であると同時に、例えば建築廃材と有機
汚泥ケーキのように組成が著しく異なり昇温特性が大き
く違う場合でも、ダンパー(11)を適宜開閉してそれ
ぞれに合わせた焼成を一度に実現することができる。Further, when such a series of kilns (1) and the like are provided and connected not only from one of the combustion furnaces (9) but also from the other, one carbonized material (2) is carbonized. Even when the furnace is finished and replaced, if the other kiln is operating, the combustion furnace (9) can be operated continuously without erasing, which is extremely efficient, and at the same time, for example, waste of building materials and organic Even in the case where the composition is remarkably different from the sludge cake and the temperature raising characteristics are largely different, the damper (11) can be opened and closed appropriately to realize the firing corresponding to each case at a time.
【0013】[0013]
【実施例】図1に示すような窯炉(1)において、(1
2)はチャンバー開閉装置であり、必要に応じこれに水
噴射装置(図示せず)を接続する。上部の空隙(5)は
着火バーナー(4)の火炎が収まるに充分な広さとし、
下部に多数の小孔を穿った通気性バケット(3)の外側
をキャスタブル(13)、鉄板(14)、及び発泡材
(15)の層で覆って炉の外壁に至る。下部においてそ
れ等を貫通する吸気管(7)にはダンパー(11)及び
空気吸入口(16)と送風機付のエゼクター(8)を設
けて、その先の乾留ガス燃焼炉(9)に導入する。その
内部は一次炉(91)と二次炉(92)とに分けられ、
それぞれバーナー(17)と送風機(18)が収められ
て、超耐熱酸化防止材で覆われる。またその上方に設け
られた排気管(10)の上部には重量式安全弁(19)
を取り付けて、その下で該管を分岐させてその中途にダ
ンパー(11)を2ケ所設け、再び該炉(1)の上部空
隙(5)内に導入させる。また同様の一連の装置を該燃
焼炉(9)にもう一つ左右対称に連設する。DESCRIPTION OF THE PREFERRED EMBODIMENTS In a kiln (1) as shown in FIG.
2) is a chamber opening / closing device to which a water injection device (not shown) is connected if necessary. The upper gap (5) is large enough to contain the flame of the ignition burner (4),
The outside of a breathable bucket (3) with a number of small holes at the bottom is covered with layers of castable (13), iron plate (14) and foam (15) to reach the outer wall of the furnace. A damper (11), an air inlet (16) and an ejector (8) with a blower are provided in an intake pipe (7) penetrating therethrough at a lower portion, and introduced into a carbonization gas combustion furnace (9) ahead. . The interior is divided into a primary furnace (91) and a secondary furnace (92),
Each contains a burner (17) and a blower (18) and is covered with a super heat resistant antioxidant. A weight-type safety valve (19) is provided above the exhaust pipe (10) provided thereabove.
The pipe is branched under the pipe, two dampers (11) are provided on the way, and the pipe is introduced again into the upper space (5) of the furnace (1). Another similar series of devices is connected to the combustion furnace (9) symmetrically.
【0014】なお精煉のために窯炉(1)の下部にブロ
アー(送風器;図示せず)を設け、更に上部に水噴射装
置(図示せず)を設ける。これは所定焼成時間を経た後
に酸素を炉内に送り込んで一時的に高温化させ、そこへ
水を噴射し蒸気爆発させて、炭の内部空隙の残留物を飛
ばすことにより炭の品質向上をはかるためのものであ
る。なお本発明はかかる例に限定されるものではない。For refining, a blower (blower; not shown) is provided at the lower part of the kiln (1), and a water injection device (not shown) is further provided at the upper part. This is to improve the quality of charcoal by sending oxygen into the furnace after a predetermined firing time to temporarily raise the temperature, injecting water into it, causing a steam explosion, and flying off the residue in the internal voids of the charcoal. It is for. The present invention is not limited to such an example.
【0015】[0015]
【発明の効果】このように本発明によれば、炭化に適し
た加熱を均一かつ効率よく、しかも管理された状況のも
とで行うことができるので、通常の木材は勿論のこと、
建築廃材から脱水汚泥や食物カスに至る廃棄物等も甚だ
低コストで高品質な炭類に変えられ、廃棄物公害の防止
と炭のもつ物性による環境改善などに大きく貢献できる
という効果がある。As described above, according to the present invention, heating suitable for carbonization can be performed uniformly and efficiently under a controlled condition.
Waste such as building debris, dewatered sludge and food waste can be converted to high-quality coal at extremely low cost, which has the effect of greatly contributing to the prevention of waste pollution and the improvement of the environment through the properties of coal.
【図1】本発明一例の側・断面図FIG. 1 is a side and sectional view of an example of the present invention.
1 ………窯炉 2 ………被炭化物 3 ………通気性バケット 4 ………着火バーナー 5 ………空隙 6 ………隙間部 7 ………吸気管 8 ………エゼクター 9 ………乾留ガス燃焼炉 91………一次炉 92………二次炉 10………排気管 11………ダンパー 12………チャンバー開閉装置 13………キャスタブル 14………鉄板 15………発泡材 16………空気吸入口 17………バーナー 18………送風機 19………重量式安全弁 DESCRIPTION OF SYMBOLS 1 ... Furnace 2 ... Carburized material 3 ... Breathable bucket 4 ... Ignition burner 5 ... Air gap 6 ... Gap part 7 ... Intake pipe 8 ... Ejector 9 ... … Drying gas combustion furnace 91… Primary furnace 92… Secondary furnace 10… Exhaust pipe 11… Damper 12… Chamber opening and closing device 13 …… Castable 14 …… Iron plate 15 …… Foaming material 16 Air inlet 17 Burner 18 Blower 19 Weight relief valve
Claims (3)
ケットの上方に着火バーナーに連なる空隙を設け、該通
気性バケットの下方に位置する隙間部より吸気管を設け
て窯炉の外に導出し、これにエゼクターを取り付けてそ
の先の乾留ガス燃焼炉に連結したことを特徴とする炭化
炉装置。1. A space connected to an ignition burner is provided above a gas permeable bucket for accommodating a material to be carbonized in a kiln, and an intake pipe is provided from a gap located below the gas permeable bucket to lead out of the kiln. And an ejector attached thereto and connected to a carbonization gas combustion furnace ahead of the ejector.
らなる同様の連なりが複数、乾留ガス燃焼炉に連結され
た請求項1記載の炭化炉装置。2. The carbonization furnace apparatus according to claim 1, wherein a plurality of the same series of the furnace, the intake pipe, the ejector, and the like are connected to the dry distillation gas combustion furnace.
なくとも一部を窯炉の上方の空隙に連通させた請求項
1、請求項2記載の炭化炉装置。3. The carbonization furnace apparatus according to claim 1, wherein at least a part of an exhaust pipe provided above the dry distillation gas combustion furnace is communicated with a space above the kiln.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9208283A JPH1121560A (en) | 1997-06-27 | 1997-06-27 | Carbonization furnace unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9208283A JPH1121560A (en) | 1997-06-27 | 1997-06-27 | Carbonization furnace unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1121560A true JPH1121560A (en) | 1999-01-26 |
Family
ID=16553687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9208283A Pending JPH1121560A (en) | 1997-06-27 | 1997-06-27 | Carbonization furnace unit |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1121560A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013061996A1 (en) * | 2011-10-25 | 2013-05-02 | 有限会社美炭産業 | Process and device for producing palm kernel shell charcoal |
-
1997
- 1997-06-27 JP JP9208283A patent/JPH1121560A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013061996A1 (en) * | 2011-10-25 | 2013-05-02 | 有限会社美炭産業 | Process and device for producing palm kernel shell charcoal |
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