JP2000063848A - Carbonization furnace by heated steam - Google Patents
Carbonization furnace by heated steamInfo
- Publication number
- JP2000063848A JP2000063848A JP10239715A JP23971598A JP2000063848A JP 2000063848 A JP2000063848 A JP 2000063848A JP 10239715 A JP10239715 A JP 10239715A JP 23971598 A JP23971598 A JP 23971598A JP 2000063848 A JP2000063848 A JP 2000063848A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- carbonization
- heating
- heated
- kiln
- 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
- 238000003763 carbonization Methods 0.000 title claims abstract description 48
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- 229920006395 saturated elastomer Polymers 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims description 26
- 238000001816 cooling Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- 238000009423 ventilation Methods 0.000 claims description 6
- 239000000919 ceramic Substances 0.000 claims description 5
- 230000005674 electromagnetic induction Effects 0.000 claims description 5
- 229910001120 nichrome Inorganic materials 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 4
- 238000011068 loading method Methods 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 10
- 229910052799 carbon Inorganic materials 0.000 abstract description 8
- 239000007788 liquid Substances 0.000 abstract description 5
- 239000002023 wood Substances 0.000 description 8
- 238000005338 heat storage Methods 0.000 description 6
- 239000003610 charcoal Substances 0.000 description 5
- 239000011269 tar Substances 0.000 description 4
- 238000005979 thermal decomposition reaction Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000011232 storage material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- KXZJHVJKXJLBKO-UHFFFAOYSA-N chembl1408157 Chemical compound N=1C2=CC=CC=C2C(C(=O)O)=CC=1C1=CC=C(O)C=C1 KXZJHVJKXJLBKO-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 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
- 239000003973 paint Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 235000010288 sodium nitrite Nutrition 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 239000000725 suspension Substances 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Coke Industry (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、木材等の木質物、そ
の他有機物からなる被炭化物を加熱水蒸気を用いて炭化
させるために使用する加熱水蒸気による炭化炉に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating steam-using carbonization furnace used for carbonizing woody materials such as wood and other materials to be carbonized by heating steam.
【0002】[0002]
【従来の技術】炭化炉として最も代表的な炭窯は、排水
性の良好な窯底の上に窯壁および天井を築き、その内部
を炭化室としたもので、窯口近くに加熱室を設け、反対
側に煙道と煙突が設けられる。そして、製炭の際には、
加熱室で木材等の燃材を燃やし、炭化室に立て込まれて
いる被炭化物としての木材を乾燥させ、乾燥が進んでそ
れに着火してからは、窯口を封じ通風口だけを残して、
木材を上木や樹皮の一部の燃焼による加熱を続ける。2. Description of the Related Art The most typical charcoal kiln as a carbonization furnace is one in which a kiln wall and a ceiling are built on a kiln bottom with good drainage, and the interior is used as a carbonization chamber. A heating chamber is provided near the kiln mouth. , A flue and a chimney are provided on the opposite side. And when making charcoal,
Combustion materials such as wood are burned in the heating chamber to dry wood as the material to be carbonized that has been placed in the carbonization chamber, and after the drying progresses and it ignites, the kiln mouth is sealed and only the ventilation opening is left,
Continue heating the wood by burning some of the wood and bark.
【0003】炭化は、このようにして被炭化物を加熱分
解した後に残る固体残渣であって、ほゞ同じ要領におい
て工業的に炉を構築し、化石燃料や電熱等の他の加熱手
段によって製炭が行なわれる。[0003] Carbonization is a solid residue that remains after the substance to be carbonized is heated and decomposed in this way, and a furnace is industrially constructed in almost the same manner, and carbonization is performed by other heating means such as fossil fuel or electric heat. Is performed.
【0004】[0004]
【発明が解決しようとする課題】炭化物の利用について
は、家庭や業務、工業、農業等の各種産業において調理
や暖房、乾燥等の燃料として用いられるだけでなく、化
粧品、研磨材、塗料等に加工され、また、二硫化炭素、
シアン化ソーダ、硫化ソーダの製造等に用いられ、さら
に、活性炭としても広く工業用等に用いられる。The use of carbide is not only used as fuel for cooking, heating, drying, etc. in various industries such as home, business, industry and agriculture, but also for cosmetics, abrasives, paints, etc. Processed and also carbon disulfide,
It is used for the production of sodium cyanide, sodium sulfide, etc., and is also widely used as an activated carbon for industrial purposes.
【0005】これらの用途として一般的に重要なこと
は、前記の他、炭素含有量が多いことであるが、これ
は、主に乾燥条件や熱分解条件(加熱温度およびその上
昇速度)により異なり、電気窯等による炭化温度が低く
炭化時間の短い乾留炭では80%、自己燃焼が多く窯内
の温度が700℃程度で炭化させる黒炭では80〜90
%、炭化温度が1,000℃程度で白熱した木炭を外に
出して消し灰で消化する白炭では90〜95%である。In addition to the above, the carbon content generally important for these uses is that the carbon content is high, but this mainly depends on the drying conditions and thermal decomposition conditions (heating temperature and its rising rate). , 80% for dry-distilled coal with a low carbonization temperature and short carbonization time in an electric kiln, etc.
%, 90% to 95% for white charcoal in which charcoal that glows at a carbonization temperature of about 1,000 ° C. is put out and digested with erased ash.
【0006】上記のような従来の炭化炉のうち、炭焼窯
では2〜3日、電熱窯の場合であると24〜36時間の
時間を要し、生産性が悪く、また、炭化物の利用を妨げ
るタール分の生成量が過度に多く、有用な燻液が少ない
という問題があった。Among the conventional carbonization furnaces as described above, it takes 2-3 days for a charcoal kiln and 24 to 36 hours for an electric heating kiln, resulting in poor productivity and use of carbide. There was a problem that the amount of tars that interfered was excessively large, and the useful liquid smoke was small.
【0007】この発明は、上記のような実情に鑑みて、
炭化時間が短いにもかゝわらず、炭素含有量が多く、ま
た、タール分が少なく、燻液が多く生成される加熱水蒸
気による炭化炉を提供することを目的とした。The present invention has been made in view of the above circumstances.
An object of the present invention is to provide a carbonization furnace using heated steam that has a high carbon content, a low tar content, and a large amount of smoked liquid even though the carbonization time is short.
【0008】[0008]
【課題を解決するための手段】上記の目的を達成するた
めに、この発明は、飽和の水蒸気発生装置と、その水蒸
気を未飽和に加熱する過熱水蒸気発生装置と、被炭化物
を加熱水蒸気で加熱する炭化反応室を有する加熱蒸気窯
とからなり、炭化反応室において、加熱水蒸気を通す通
気管を均等に配管し、通気管に加熱水蒸気の噴射ノズル
を配列して取り付け、さらに、加熱蒸気窯においては、
被炭化物を載せて搬入、搬出する搬送装置を設けたこと
を特徴とする加熱水蒸気による炭化炉を構成した。In order to achieve the above object, the present invention relates to a saturated steam generator, a superheated steam generator for heating the steam to an unsaturated state, and an object to be heated with heated steam. And a heating steam kiln having a carbonization reaction chamber, and in the carbonization reaction chamber, a ventilation pipe for passing the heating steam is evenly installed, and a nozzle for heating the steam is arranged and attached to the ventilation pipe. Is
A carbonization furnace using heated steam is provided, which is provided with a transfer device for loading and unloading the object to be carbonized.
【0009】[0009]
【作用】加熱水蒸気には、温度設定が比較的自由であ
り、被炭化物の材質に応じて設定された高温の加熱水蒸
気が得られ、それを炭化反応室において、被炭化物に噴
射ノズルにより均等に当てられると、酸素が遮断された
雰囲気中において高温に加熱され炭化する。木質系の炭
化反応においては、構成成分のヘミセルローズでは10
0〜300℃、セルローズでは240〜400℃、リグ
ニンでは230〜550℃で反応が進行し炭化が完了す
る。そして、炭化反応は、熱分解反応と加水分解反応が
平行して進むので、従来の熱分解方式よりも反応が速く
進行する。[Function] The temperature of the heated steam is relatively free to set, and high-temperature heated steam set according to the material to be carbonized can be obtained. When applied, it is heated to a high temperature and carbonized in an atmosphere in which oxygen is blocked. In the wood-based carbonization reaction, the composition of hemicellulose is 10
The reaction proceeds at 0-300 ° C., 240-400 ° C. for cellulose and 230-550 ° C. for lignin to complete carbonization. Further, in the carbonization reaction, since the thermal decomposition reaction and the hydrolysis reaction proceed in parallel, the reaction proceeds faster than the conventional thermal decomposition method.
【0010】上記の構成に加えて、加熱蒸気窯におい
て、炭化反応室の前に被炭化物を加熱する予熱室を設
け、周壁に赤外線の輻射熱が望めるセラミックスを内張
りすると、さらに炭化速度が早まり、しかも、炭素率が
高くなる。また、後に冷却室を設けると、冷却された炭
化物は、外に排出されると余熱により自然に乾燥され
る。In addition to the above structure, in the heating steam kiln, if a preheating chamber for heating the material to be carbonized is provided in front of the carbonization reaction chamber and the peripheral wall is lined with ceramics capable of radiant heat of infrared rays, the carbonization rate is further increased. , The carbon rate becomes high. If a cooling chamber is provided later, the cooled carbide is naturally dried by residual heat when discharged outside.
【0011】さらに加えて、過熱水蒸気発生装置におい
て、水蒸気発生装置からの送気管に接続される伝熱管
に、電磁誘導によるヒーターと、ニクロム線によるヒー
ターとを被着してあると、加熱水蒸気の加熱温度の調整
がしやすくなる。In addition, in the superheated steam generator, if a heater by electromagnetic induction and a heater by a nichrome wire are attached to the heat transfer pipe connected to the air supply pipe from the steam generator, The heating temperature can be adjusted easily.
【0012】[0012]
【発明の実施の形態】この発明においては、搬送装置5
について、台車8や吊り車を用いたレール方式の他、ベ
ルトや転りロールを用いたコンベヤ方式等を採ることが
できる。BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, a conveying device 5
Regarding the above, as well as a rail system using the carriage 8 or a suspension car, a conveyor system using a belt or rolling rolls can be adopted.
【0013】また、水蒸気発生装置1については、重油
等の燃料や電熱で、直接水を沸騰させるボイラー方式の
他、予め蓄えておいた熱で蒸気をつくる蓄熱方式、さら
にはその併用方式等を採ることができる。そして、蓄熱
方式によれば、必要な量の加熱水蒸気を必要な時に得ら
れやすいし、安価な深夜電力を利用することもできる。
蓄熱材には、例えば、マグネシアやシリカ等を主成分と
する固体、硝酸ナトリウム、亜硝酸ナトリウム、硝酸カ
リウム等の高温時に融解して液体になる物質、あるいは
これらの混合物等を用いることができる。As for the steam generator 1, in addition to a boiler system in which water is directly boiled by fuel such as heavy oil or electric heat, a heat storage system in which steam is generated by heat stored in advance, and a combination system thereof is used. Can be taken. Further, according to the heat storage method, it is possible to easily obtain a necessary amount of heated steam when necessary, and it is possible to use inexpensive late-night power.
As the heat storage material, for example, a solid containing magnesia, silica, or the like as a main component, a substance such as sodium nitrate, sodium nitrite, or potassium nitrate that melts at a high temperature to become a liquid, or a mixture thereof can be used.
【0014】加熱蒸気窯3において、予熱室15、炭化
反応室16、冷却室17を構成するシャッター11,1
2,13,14については、扉形式の他、エアーカーテ
ンとすることもできる。In the heating steam kiln 3, shutters 11 and 1 constituting a preheating chamber 15, a carbonization reaction chamber 16 and a cooling chamber 17 are provided.
The doors 2, 13 and 14 may be air curtains instead of the door type.
【0015】[0015]
【発明の効果】以上説明したように、この発明の加熱水
蒸気による炭化炉によれば、熱分解反応と加水分解反応
とにより、速やかに炭化させることができ、しかも、そ
れが酸素が遮断された雰囲気中になされるために、炭素
率が高く、タール分の少ない良質の炭化物を生産するこ
とができ、しかも、連続運転が可能であるから、生産性
を高めることができ、有用な燻液も多量に得られる等の
優れた効果がある。As described above, according to the carbonization furnace using the heated steam of the present invention, the carbonization can be quickly carried out by the thermal decomposition reaction and the hydrolysis reaction, and the oxygen is blocked. Since it is carried out in the atmosphere, it is possible to produce a high-quality carbide having a high carbon rate and a low tar content, and moreover, since continuous operation is possible, productivity can be increased and useful smoke It has excellent effects such as large amounts.
【0016】また、予熱室を設け、セラミックスの内張
りがあると、さらに炭化速度が早まり、しかも、炭素率
が高くなる。また、後に冷却室を設けると、さらに生産
性が良くなる(請求項2)。If a preheating chamber is provided and a ceramic lining is provided, the carbonization rate is further increased and the carbon content is increased. Further, if a cooling chamber is provided later, the productivity is further improved (claim 2).
【0017】また、伝熱管に、電磁誘導によるヒーター
と、ニクロム線によるヒーターとを被着してあると、加
熱水蒸気の加熱温度の調整がしやすくなり、炭化物の材
質に合わせて運転しやすい(請求項3)。Further, when the heater by electromagnetic induction and the heater by nichrome wire are attached to the heat transfer tube, the heating temperature of the heated steam can be easily adjusted and the operation can be easily performed according to the material of the carbide ( Claim 3).
【0018】[0018]
【実施例】次に、この発明の実施例を図面に基づいて具
体的に説明する。Embodiments of the present invention will now be specifically described with reference to the drawings.
【0019】図1および図2は、一実施例を示したもの
で、その加熱水蒸気による炭化炉は、ボイラーによる水
蒸気発生装置1と、電気による過熱水蒸気発生装置2
と、搬送装置5付きの加熱蒸気窯3等からなっている。FIG. 1 and FIG. 2 show one embodiment. The carbonization furnace using the heated steam includes a steam generator 1 using a boiler and a superheated steam generator 2 using electricity.
And a heating steam kiln 3 with a transfer device 5 and the like.
【0020】過熱水蒸気発生装置2は、水蒸気発生装置
1から配管4によって供給される水蒸気を電磁誘導によ
るヒーター6aと、ニクロム線によるヒーター6bとに
より1,000℃程度までに自由に温度設定して加熱さ
れる。The superheated steam generator 2 sets the temperature of the steam supplied from the steam generator 1 through the pipe 4 freely to about 1,000 ° C. by the heater 6a by electromagnetic induction and the heater 6b by the nichrome wire. Be heated.
【0021】加熱蒸気窯3は、横に長い円筒形の金属製
の筒形であって、その中に被炭化物7の台車8を搬送す
るレール9を通しに設けたもので、順次シャッター1
1,12,13,14を設けることによって、予熱室1
5,炭化反応室16、冷却室17が設けられ、炭化反応
室16においては、セラミックス19がタイルで内張り
され、上下左右に過熱水蒸気の通気管21,21,・・
を配設し、各通気管21には、噴射ノズル23,23,
・・が配列されている。The heating steam kiln 3 is a metal cylinder having a horizontally long cylindrical shape, in which a rail 9 for carrying a cart 8 for the article to be carbonized 7 is provided through, and the shutter 1 is sequentially opened.
By providing 1, 12, 13, and 14, the preheating chamber 1
5. A carbonization reaction chamber 16 and a cooling chamber 17 are provided. In the carbonization reaction chamber 16, ceramics 19 are lined with tiles, and the superheated steam vent pipes 21, 21, ...
And each of the ventilation pipes 21 is provided with an injection nozzle 23, 23,
.. are arranged.
【0022】また、冷却室17には、通水管24,2
4,・・が配管され、それに噴水ノズル26,26,・
・が取り付けられている。Further, in the cooling chamber 17, water passage pipes 24, 2
4, ... are piped and fountain nozzles 26, 26 ,.
・ Is attached.
【0023】上記の炭化炉の使用例を次に説明する。An example of using the above carbonization furnace will be described below.
【0024】被炭化物7として約100kgの木材を台
車8に立て込みに積み、レール9によって、予熱室15
に60分、炭化反応室16に120分、冷却室17に6
0〜90分と、それぞれ滞留させ、滞留中においてはシ
ャッター11,12,13,14を閉じ、炭化反応室1
6では、噴射ノズル23,23,・・から約800℃の
加熱水蒸気を均等に当てた。冷却室17から出された炭
化物7はそのまま放置して自然乾燥させた。About 100 kg of wood as the material to be carbonized 7 is piled up vertically on the trolley 8 and the rail 9 is used to preheat the chamber 15.
60 minutes, carbonization reaction chamber 16 120 minutes, cooling chamber 17 6 minutes
0 to 90 minutes, respectively, and the shutters 11, 12, 13, and 14 are closed during the retention, and the carbonization reaction chamber 1
In No. 6, heated steam of about 800 ° C. was uniformly applied from the injection nozzles 23, 23, ... The carbide 7 discharged from the cooling chamber 17 was left as it was and naturally dried.
【0025】このようにして得られた炭化物7aは、炭
素率は、C/H比で95%であり、良質の炭化物7aが
得られた。副生物のタール分は少なく、燻液は多量に排
出された。また、木材の他に、他の有機物質としてのプ
ラスチックや台所で出る厨介物からでも同じように炭化
物が得られることが分かった。The carbide 7a thus obtained had a carbon ratio of 95% in terms of C / H ratio, and a good quality carbide 7a was obtained. The by-product tar content was small, and a large amount of smoke was discharged. It was also found that carbides can be obtained from other organic substances such as plastics and kitchen wastes in the kitchen, in addition to wood.
【0026】図3は、水蒸気発生装置1が蓄熱材を利用
した場合を示したもので、タンク26内に、固体と液体
の蓄熱材28が混合して充填され、その中に、電気ヒー
ター30と蒸気を内部で発生させる伝熱管32が配設さ
れる。FIG. 3 shows a case where the steam generator 1 uses a heat storage material. The tank 26 is filled with the solid and liquid heat storage material 28 mixed therein, and the electric heater 30 is filled therein. A heat transfer tube 32 that internally generates steam is disposed.
【図1】この発明の加熱水蒸気による炭化炉のほゞ全体
を示す説明図である。FIG. 1 is an explanatory view showing an entire carbonization furnace using heated steam according to the present invention.
【図2】同炭化炉の要部としての炭化反応室の断面図で
ある。FIG. 2 is a sectional view of a carbonization reaction chamber as a main part of the carbonization furnace.
【図3】加熱水蒸気による炭化炉における水蒸気発生装
置が蓄熱方式である場合の説明図である。FIG. 3 is an explanatory diagram when a steam generator in a carbonization furnace using heated steam is a heat storage system.
P 加熱水蒸気による炭化炉 1 水蒸気発生装置 2 過熱水蒸気発生装置 3 加熱蒸気窯 4 送気管 5 搬送装置 6a 電磁誘導によるヒーター 6b ニクロム線によるヒーター 7 被炭化物 7a 炭化物 10 伝熱管 15 予熱室 16 炭化反応室 17 冷却室 19 セラミックス 21 通気管 23 噴射ノズル 整理番号 P-2061 P Carbonization furnace with heated steam 1 Steam generator 2 Superheated steam generator 3 heating steam kiln 4 Air pipe 5 Conveyor 6a Electromagnetic induction heater 6b Nichrome wire heater 7 Carbide 7a Carbide 10 heat transfer tubes 15 Preheating room 16 Carbonization reaction chamber 17 Cooling chamber 19 Ceramics 21 Vent pipe 23 Injection nozzle Reference number P-2061
Claims (3)
未飽和に加熱する過熱水蒸気発生装置と、被炭化物を加
熱水蒸気で加熱する炭化反応室を有する加熱蒸気窯とか
らなり、炭化反応室において、加熱水蒸気を通す通気管
を均等に配管し、通気管に加熱水蒸気の噴射ノズルを配
列して取り付け、さらに、加熱蒸気窯においては、被炭
化物を載せて搬入、搬出する搬送装置を設けたことを特
徴とする加熱水蒸気による炭化炉。1. A saturated steam generator, a superheated steam generator for heating the steam to an unsaturated state, and a heating steam kiln having a carbonization reaction chamber for heating an object to be carbonized with heated steam, in a carbonization reaction chamber. , The ventilation pipes for passing the heated steam are evenly arranged, and the injection nozzles for the heated steam are arranged and attached to the ventilation pipes. Further, in the heating steam kiln, a carrying device for loading and unloading the material to be carbonized is provided. A carbonization furnace using heated steam.
被炭化物を加熱する予熱室を設け、後に冷却室を設け、
さらに、炭化反応室には、周壁にセラミックスを内張り
したことを特徴とする請求項1記載の加熱水蒸気による
炭化炉。2. In a heating steam kiln, a preheating chamber for heating an object to be carbonized is provided before the carbonization reaction chamber, and a cooling chamber is provided after that.
The carbonization furnace with heated steam according to claim 1, characterized in that the carbonization reaction chamber is lined with ceramics on the peripheral wall.
生装置からの送気管に接続される伝熱管に、電磁誘導に
よるヒーターと、ニクロム線によるヒーターとを被着し
たことを特徴とする請求項1または2記載の加熱水蒸気
による炭化炉。3. A superheated steam generator, wherein a heater by electromagnetic induction and a heater by nichrome wire are attached to a heat transfer pipe connected to an air supply pipe from the steam generator. A carbonization furnace using the heated steam described in 2.
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JP23971598A JP3609944B2 (en) | 1998-08-26 | 1998-08-26 | Carbonization furnace with heated steam |
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JP23971598A JP3609944B2 (en) | 1998-08-26 | 1998-08-26 | Carbonization furnace with heated steam |
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JP2000063848A true JP2000063848A (en) | 2000-02-29 |
JP3609944B2 JP3609944B2 (en) | 2005-01-12 |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001192670A (en) * | 1999-10-29 | 2001-07-17 | Ryoichi Okamoto | Method of manufacturing carbonized material and pyrolizer for organic waste |
JP2002194362A (en) * | 2000-12-27 | 2002-07-10 | Kogi Corp | Method for carbonizing with overheated steam |
US7113695B2 (en) | 2004-05-12 | 2006-09-26 | Aoki Kogyo Kabushikikaisha | Heat treatment system using superheated steam |
JP2007022840A (en) * | 2005-07-14 | 2007-02-01 | Tanaka Kenzai Kk | Method for manufacturing magnetized carbonized matter and waste water treatment method |
JP2008075161A (en) * | 2006-09-25 | 2008-04-03 | Takamatsu Mekki:Kk | Reflow treatment method of connection terminal |
WO2013011555A1 (en) * | 2011-07-19 | 2013-01-24 | 株式会社ワンワールド | Apparatus and method for carbonizing organic material |
JP2014148630A (en) * | 2013-02-04 | 2014-08-21 | Kyushu Institute Of Technology | Production method of bamboo vinegar |
CN104403678A (en) * | 2014-10-13 | 2015-03-11 | 浙江安吉双虎竹木业有限公司 | Carbonization furnace structure |
JP2017044384A (en) * | 2015-08-25 | 2017-03-02 | 中部電力株式会社 | High-temperature fluid generation device |
-
1998
- 1998-08-26 JP JP23971598A patent/JP3609944B2/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001192670A (en) * | 1999-10-29 | 2001-07-17 | Ryoichi Okamoto | Method of manufacturing carbonized material and pyrolizer for organic waste |
JP2002194362A (en) * | 2000-12-27 | 2002-07-10 | Kogi Corp | Method for carbonizing with overheated steam |
US7113695B2 (en) | 2004-05-12 | 2006-09-26 | Aoki Kogyo Kabushikikaisha | Heat treatment system using superheated steam |
CN100362080C (en) * | 2004-05-12 | 2008-01-16 | 小野达实 | Heat treatment system using superheated steam |
JP2007022840A (en) * | 2005-07-14 | 2007-02-01 | Tanaka Kenzai Kk | Method for manufacturing magnetized carbonized matter and waste water treatment method |
JP2008075161A (en) * | 2006-09-25 | 2008-04-03 | Takamatsu Mekki:Kk | Reflow treatment method of connection terminal |
WO2013011555A1 (en) * | 2011-07-19 | 2013-01-24 | 株式会社ワンワールド | Apparatus and method for carbonizing organic material |
JPWO2013011555A1 (en) * | 2011-07-19 | 2015-02-23 | 株式会社ワンワールド | Carbonizing apparatus and method for carbonizing organic matter |
JP2014148630A (en) * | 2013-02-04 | 2014-08-21 | Kyushu Institute Of Technology | Production method of bamboo vinegar |
CN104403678A (en) * | 2014-10-13 | 2015-03-11 | 浙江安吉双虎竹木业有限公司 | Carbonization furnace structure |
JP2017044384A (en) * | 2015-08-25 | 2017-03-02 | 中部電力株式会社 | High-temperature fluid generation device |
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