JP4028899B2 - Carbonization equipment - Google Patents
Carbonization equipment Download PDFInfo
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- JP4028899B2 JP4028899B2 JP32226195A JP32226195A JP4028899B2 JP 4028899 B2 JP4028899 B2 JP 4028899B2 JP 32226195 A JP32226195 A JP 32226195A JP 32226195 A JP32226195 A JP 32226195A JP 4028899 B2 JP4028899 B2 JP 4028899B2
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- raw material
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- carbonization
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- 238000003763 carbonization Methods 0.000 title claims description 30
- 239000002994 raw material Substances 0.000 claims description 33
- 239000007789 gas Substances 0.000 claims description 20
- 238000001035 drying Methods 0.000 claims description 16
- 239000002023 wood Substances 0.000 claims description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 9
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 9
- 239000000567 combustion gas Substances 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 239000010903 husk Substances 0.000 claims description 6
- 239000002699 waste material Substances 0.000 claims description 5
- 235000009419 Fagopyrum esculentum Nutrition 0.000 claims description 4
- 235000007164 Oryza sativa Nutrition 0.000 claims description 4
- 239000002154 agricultural waste Substances 0.000 claims description 4
- 235000009566 rice Nutrition 0.000 claims description 4
- 230000007723 transport mechanism Effects 0.000 claims description 4
- 238000010000 carbonizing Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- -1 etc. Substances 0.000 claims description 2
- 240000008620 Fagopyrum esculentum Species 0.000 claims 1
- 240000007594 Oryza sativa Species 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 239000003610 charcoal Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 241000219051 Fagopyrum Species 0.000 description 3
- 241000209094 Oryza Species 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 241000287828 Gallus gallus Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000004380 ashing Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 210000003746 feather Anatomy 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000003870 refractory metal Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
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)
Description
【0001】
【産業上の利用分野】
本発明は建築廃木材,間伐材等を粉砕して得られた原料チップや蕎麦殻,籾殻等の農産廃棄物等を炭化させて炭を製造する炭化装置に関するものである。
【0002】
【従来の技術とその課題】
従来より土質改善等に用いられる炭は、外国から輸入した炭を国内で粉砕して用いられていたが、近年では農林産資源を保護するために建築廃木材,間伐材を粉砕等によりチップ化したものや、蕎麦殻,籾殻等の農産廃棄物等を炭化させて木炭として利用することが行われている。
【0003】
図2は従来の撹拌流動式の炭化装置の概念図である。
炉(11)内は分散板(11c)により上方に位置する撹拌部(11a)と、下方に位置する空気供給部(11b)とに分けられている。
原料は炉内温度を検出する温度制御計(12)に制御されるモーター(13)によって撹拌部(11a)内に投入され、撹拌機(14)により撹拌部(11a)内で撹拌される。空気供給部(11b)から撹拌部(11a)に空気が送られ、撹拌部(11a)内の原料が炭化する。炭化物は撹拌部(11a)側面に設けられた炭化物排出口(15)より炉外に排出される。排気ガスはサイクロン(16)を介して除塵して装置外に排出される。
【0004】
しかしこの方式では原料と空気との接触が多くなり、原料が必要以上に燃焼してしまい、得られる炭化物の量が少なくなってしまい、生産効率が良くない。
【0005】
図3はスクリュー炉式の炭化装置の概念図である。この方式では原料を加熱室(23)内に設けられた炭化筒(21)内に投入し、炭化筒(21)内に設けられたスクリュー(22)により炭化筒(21)内を移動しながら加熱して炭化させる。この加熱は炭化筒(21)から排出される乾留ガスと補助燃料投入口(24)から供給される補助燃料の燃焼により行っている。
【0006】
この方式では原料を間接的に加熱しているため、加熱の効率が悪く、生産に多くのエネルギーを消費する点で好ましくない。
【0007】
そこで、原料を連続的に効率よく炭化させることのできる炭化装置が求められている。
【0008】
【課題を解決するための手段】
本発明の炭化装置は、建築廃木材、間伐材等を粉砕して得られた木材チップや、蕎麦殻、籾殻等の農産廃棄物を原料とする炭化装置であって、原料に着火すると共に原料を不完全燃焼させて一酸化炭素ガスを発生させる着火室(2)と、空気が供給される二次空気供給口(3c)を上部に備え、着火室(2)から導かれた一酸化炭素ガスと二次空気供給口(3c)から供給された空気とをガス燃焼させ、該ガス燃焼の輻射熱により原料を炭化させ炭化物を排出する炭化室(3)と、原料を着火室(2)から炭化室(3)に導くための搬送機構(4),(5)とを備えていることを特徴とする。
【0009】
更には上記に加えて、着火に先立って原料を乾燥させるための乾燥室(1)と、原料を乾燥室(1)から着火室(2)に導くための搬送機構(4),(5)とを備えており、原料の乾燥には炭化室(3)から導いた燃焼ガスを利用していることを特徴とする。
【0010】
【実施の形態】
以下、本発明を好適な実施例を用いて説明する。図1は本発明の炭化装置の概念図である。
本実施例では原料として間伐材をチップ状にしたものを用いた。間伐材は十分に乾燥していないので、着火部(2)に直接投入せずに、乾燥室(1)に設けた原料投入口(1a)から供給し、乾燥工程を経て着火室(2)に導くようにしている。
なお、原料として建築廃木材等の乾燥している物を用いる場合には、乾燥室(1)を省略して直接着火室(2)に投入するようにしてもよい。
乾燥は後工程で生じた燃焼ガスを燃焼ガス吸入口(1b)より乾燥室(1)に導いて有効利用することによりエネルギーの消費を少なくしている。排ガスは排ガス排出口(1c)から排出され、除塵される。
【0011】
原料は原料投入口(1a)から各室(1),(2),(3)を貫くように設けられたシャフト(4)に取り付けられた羽根(5)により次工程に送られる。このシャフト(4)は耐熱のためにパイプ状として内部に水流が流れる水冷式とした。また、羽根(5)はスクリュー状のものでもよく、羽根(5)の形状や数は搬送量に合わせて適宜決めればよい。
【0012】
着火室(2)にはバーナー口(2b)が設けられており、バーナーからの火炎が室内に導かれる。又、分散板(2a)を介して室内に一次空気が供給される。分散板(2a)としては耐火性金属のパンチングメタルや、ロストル,孔を有したレンガ等を用いることができる。
供給された一次空気の供給量を必要最小限に調整することにより材料を不完全燃焼させる。この不完全燃焼により生じた一酸化炭素ガスは着火室と炭化室との間の隔壁(7)の上部に設けられている一酸化炭素ガス通路(8)より次の炭化室(3)内の上方のガス燃焼域(3a)に導かれる。
【0013】
炭化室(3)の上方に設けられた二次空気供給口(3c)からは、着火室より送られてきた一酸化炭素ガスが燃焼するのに必要な二次空気が供給され、ガス燃焼域(3a)において一酸化炭素ガスが燃焼する。その燃焼による熱が材料に放射されるが、材料の近傍の炭化域(3b)は無酸素状態であるので材料は燃焼せずに炭化される。炭化室(3)内では材料をより効率的に炭化させるためにシャフト(4)に取り付けられた羽根のようにねじれているパドル(6)により原料を上下に撹拌しつつ炭化物出口(3d)に移送する。
このようにして得られた炭化物は炭化物出口(3d)より装置外に排出される。燃焼ガスは先述のように燃焼ガス排出口(3e)から乾燥室(1)に送られ(図中、燃焼ガス経路の記載省略)、材料の乾燥に利用される。
【0014】
なお、図4に示すように、乾燥室(1)又は着火室(2)に原料を投入するための原料供給装置(9)を設けてもよい。
【0015】
【発明の効果】
以上述べたように、本発明により、無酸素状態で輻射熱により直接加熱,炭化させることができるので、原料が燃え過ぎて灰化する割合が少なく、大きな歩留りが得られる。更に必要な燃料も少なくてよいので、効率的に連続して炭化物を得ることができる。
【図面の簡単な説明】
【図1】本発明の炭化装置の概念図。
【図2】従来の炭化装置の概念図(その1)。
【図3】従来の炭化装置の概念図(その2)。
【図4】原料供給装置を備えた炭化装置の概念図。
【符号の説明】
(1) 乾燥室
(1a) 原料投入口
(1b) 燃焼ガス吸入口
(1c) 排ガス排出口
(2) 着火室
(2a) 空気分散板(一次空気供給口)
(2b) バーナー口
(3) 炭化室
(3a) ガス燃焼域
(3b) 炭化域
(3c) 二次空気供給口
(3d) 炭化物排出口
(3e) 燃焼ガス排出口
(4) シャフト
(5) 羽根
(6) パドル
(7) 隔壁(着火室と炭化室の間)
(8) 一酸化炭素ガス通路
(9) 原料供給装置[0001]
[Industrial application fields]
The present invention relates to carbonization apparatus for manufacturing building waste wood, thinned wood, etc. The pulverizng-obtained raw material chips and buckwheat, charcoal by carbonizing the agricultural waste such as rice hulls.
[0002]
[Prior art and its problems]
Charcoal used for soil quality improvement has been used by crushing imported charcoal imported from abroad in recent years, but in recent years it has been converted into chips by crushing waste construction wood and thinned wood to protect agricultural and forestry resources. It has been practiced that charcoal and agricultural waste such as buckwheat husk and rice husk are carbonized and used as charcoal.
[0003]
FIG. 2 is a conceptual diagram of a conventional stirring flow type carbonization apparatus.
The interior of the furnace (11) is divided into an agitation section (11a) located above by a dispersion plate (11c) and an air supply section (11b) located below.
The raw material is charged into the stirring section (11a) by a motor (13) controlled by a temperature controller (12) that detects the temperature in the furnace, and is stirred in the stirring section (11a) by a stirrer (14). Air is sent from the air supply unit (11b) to the stirring unit (11a), and the raw material in the stirring unit (11a) is carbonized. The carbide is discharged out of the furnace through a carbide discharge port (15) provided on the side surface of the stirring section (11a). The exhaust gas is discharged through the cyclone (16) and discharged out of the apparatus.
[0004]
However, in this system, the contact between the raw material and air increases, the raw material burns more than necessary, and the amount of carbide obtained is reduced, resulting in poor production efficiency.
[0005]
FIG. 3 is a conceptual diagram of a screw furnace type carbonization apparatus. In this method, the raw material is charged into a carbonization cylinder (21) provided in the heating chamber (23), and moved inside the carbonization cylinder (21) by a screw (22) provided in the carbonization cylinder (21). Heat to carbonize. This heating is performed by burning dry distillation gas discharged from the carbonization cylinder (21) and auxiliary fuel supplied from the auxiliary fuel inlet (24).
[0006]
In this method, since the raw material is indirectly heated, the heating efficiency is poor, which is not preferable in that much energy is consumed for production.
[0007]
Therefore, there is a need for a carbonization apparatus that can continuously and efficiently carbonize the raw material.
[0008]
[Means for Solving the Problems]
The carbonization device of the present invention is a carbonization device that uses wood chips obtained by pulverizing building waste wood, thinned wood, etc., and agricultural waste such as buckwheat husks, rice husks, etc. as raw materials. An ignition chamber (2) for incomplete combustion to generate carbon monoxide gas and a secondary air supply port (3c) to which air is supplied are provided at the top, and carbon monoxide led from the ignition chamber (2) Gas combustion of the gas and air supplied from the secondary air supply port (3c), carbonizing the raw material by radiant heat of the gas combustion and discharging the carbide, and the raw material from the ignition chamber (2) A transport mechanism (4) and (5) for guiding to the carbonization chamber (3) is provided.
[0009]
Furthermore, in addition to the above, a drying chamber (1) for drying the raw material prior to ignition, and a transport mechanism (4), (5) for guiding the raw material from the drying chamber (1) to the ignition chamber (2) And the combustion gas introduced from the carbonization chamber (3) is used for drying the raw material.
[0010]
[Embodiment]
The present invention will be described below with reference to preferred embodiments. FIG. 1 is a conceptual diagram of the carbonization apparatus of the present invention.
In this example, a thinned wood chip was used as a raw material. Since the thinned wood is not sufficiently dry, it is not directly fed into the ignition section (2), but is supplied from the raw material inlet (1a) provided in the drying chamber (1), and after passing through the drying process, the ignition chamber (2) To guide you to.
In addition, when using dry things, such as building waste wood, as a raw material, you may make it abbreviate | omit a drying chamber (1) and throw in into an ignition chamber (2) directly.
Drying reduces the consumption of energy by guiding the combustion gas generated in the subsequent process from the combustion gas inlet (1b) to the drying chamber (1) for effective use. The exhaust gas is discharged from the exhaust gas outlet (1c) and removed.
[0011]
The raw material is sent to the next process from the raw material input port (1a) by a blade (5) attached to a shaft (4) provided so as to penetrate each chamber (1), (2), (3). This shaft (4) was made into a pipe shape for heat resistance, and a water-cooled type in which a water flow flows inside. The blades (5) may be screw-shaped, and the shape and number of the blades (5) may be appropriately determined according to the transport amount.
[0012]
The ignition chamber (2) is provided with a burner port (2b), and a flame from the burner is guided into the room. Further, primary air is supplied into the room through the dispersion plate (2a). As the dispersion plate (2a), a refractory metal punching metal, a rooster, a brick having a hole, or the like can be used.
The material is incompletely burned by adjusting the supply amount of the supplied primary air to the minimum necessary. The carbon monoxide gas generated by this incomplete combustion passes through the carbon monoxide gas passage (8) provided in the upper part of the partition wall (7) between the ignition chamber and the carbonization chamber, and enters the next carbonization chamber (3). It is led to the upper gas combustion zone (3a).
[0013]
The secondary air supply port (3c) provided above the carbonization chamber (3) is supplied with secondary air necessary for burning the carbon monoxide gas sent from the ignition chamber, and the gas combustion zone In (3a), the carbon monoxide gas burns. Heat from the combustion is radiated to the material, but the material is carbonized without burning because the carbonized region (3b) near the material is in an oxygen-free state. In the carbonization chamber (3), in order to carbonize the material more efficiently, the paddle (6) twisted like a blade attached to the shaft (4) is stirred up and down to the carbide outlet (3d). Transport.
The carbide thus obtained is discharged out of the apparatus through the carbide outlet (3d). As described above, the combustion gas is sent from the combustion gas discharge port (3e) to the drying chamber (1) (the description of the combustion gas path is omitted in the figure), and is used for drying the material.
[0014]
In addition, as shown in FIG. 4, you may provide the raw material supply apparatus (9) for charging a raw material into a drying chamber (1) or an ignition chamber (2).
[0015]
【The invention's effect】
As described above, according to the present invention, since it can be directly heated and carbonized by radiant heat in an oxygen-free state, the raw material is burned too much and the ratio of ashing is small, and a large yield can be obtained. Furthermore, since less fuel is required, carbides can be obtained efficiently and continuously.
[Brief description of the drawings]
FIG. 1 is a conceptual diagram of a carbonization apparatus of the present invention.
FIG. 2 is a conceptual diagram of a conventional carbonization apparatus (part 1).
FIG. 3 is a conceptual diagram of a conventional carbonization apparatus (part 2).
FIG. 4 is a conceptual diagram of a carbonization device provided with a raw material supply device.
[Explanation of symbols]
(1) Drying room
(1a) Raw material input
(1b) Combustion gas inlet
(1c) Exhaust gas outlet
(2) Ignition room
(2a) Air distribution plate (primary air supply port)
(2b) Burner port
(3) Carbonization chamber
(3a) Gas combustion zone
(3b) Carbonized zone
(3c) Secondary air supply port
(3d) Carbide outlet
(3e) Combustion gas outlet
(4) Shaft
(5) Feather
(6) Paddle
(7) Bulkhead (between ignition chamber and carbonization chamber)
(8) Carbon monoxide gas passage
(9) Raw material supply equipment
Claims (2)
前記原料に着火すると共に前記原料を不完全燃焼させて一酸化炭素ガスを発生させる着火室と、
空気が供給される二次空気供給口を上部に備え、前記着火室から導かれた一酸化炭素ガスと前記二次空気供給口から供給された空気とをガス燃焼させ、該ガス燃焼の輻射熱により前記原料を炭化させ炭化物を排出する炭化室と、
前記原料を着火室から炭化室に導くための搬送機構とを備えていることを特徴とする炭化装置。It is a carbonization equipment that uses wood chips obtained by crushing building waste wood, thinned wood, etc., and agricultural waste such as buckwheat husks, rice husks as raw materials,
An ignition chamber for igniting the raw material and incompletely burning the raw material to generate carbon monoxide gas;
A secondary air supply port to which air is supplied is provided in the upper portion, and carbon monoxide gas guided from the ignition chamber and air supplied from the secondary air supply port are gas-combusted, and by the radiant heat of the gas combustion A carbonization chamber for carbonizing the raw material and discharging carbide,
A carbonization apparatus comprising: a transport mechanism for guiding the raw material from the ignition chamber to the carbonization chamber.
前記原料の乾燥には炭化室から導いた燃焼ガスを利用していることを特徴とする請求項1記載の炭化装置。A drying chamber for drying the raw material prior to ignition, and a transport mechanism for guiding the raw material from the drying chamber to the ignition chamber,
2. The carbonization apparatus according to claim 1, wherein the raw material is dried by using combustion gas introduced from a carbonization chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32226195A JP4028899B2 (en) | 1995-11-15 | 1995-11-15 | Carbonization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32226195A JP4028899B2 (en) | 1995-11-15 | 1995-11-15 | Carbonization equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09137167A JPH09137167A (en) | 1997-05-27 |
| JP4028899B2 true JP4028899B2 (en) | 2007-12-26 |
Family
ID=18141683
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32226195A Expired - Fee Related JP4028899B2 (en) | 1995-11-15 | 1995-11-15 | Carbonization equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4028899B2 (en) |
-
1995
- 1995-11-15 JP JP32226195A patent/JP4028899B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09137167A (en) | 1997-05-27 |
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