JP4220083B2 - Suction dry distillation gasification combustion equipment for mature solid substances - Google Patents
Suction dry distillation gasification combustion equipment for mature solid substances Download PDFInfo
- Publication number
- JP4220083B2 JP4220083B2 JP30980799A JP30980799A JP4220083B2 JP 4220083 B2 JP4220083 B2 JP 4220083B2 JP 30980799 A JP30980799 A JP 30980799A JP 30980799 A JP30980799 A JP 30980799A JP 4220083 B2 JP4220083 B2 JP 4220083B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- combustion
- heat exchange
- heat
- base
- 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 - Fee Related
Links
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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Processing Of Solid Wastes (AREA)
- Coke Industry (AREA)
Description
【発明の属する技術分野】
【0001】
本発明は産業廃棄物に類する固体物質を焼却や、改質炭化剤等に再生する技術に関するものである。
【従来技術】
【0002】
生産活動における副生物や、経済生活活動から出る副生物の中には、焼却燃焼して有効な熱に転換出来るのに、処理上の制約や技術的困難から活用されずに放置されている物が多い、社会環境上ゆるがせに出来ないことから多くの手段が考案されているが、大型装置でなければ制約条件をクリア出来ないとして、その活用が伸び悩んでおり、有効な活用処理技術の開発が必要とされている。
【発明が解決しようとする課題】
【0003】
本発明者は、今の社会環境の中で、前項の技術的困難を克服するには何をなすべきか、鋭意検討して課題内容を整理し、
▲イ▼処理すべき産業廃棄物的資源である固体物質は、発火点温度が高く、自燃力が弱く、且つ粗密で量が多い、と云う特徴をふまえた上で、高温完全燃焼に到達し、その燃焼熱を有効な蒸気熱に転換する熱交換手段。
▲ロ▼前項の物質の特徴を考慮しながら、その物質に応じて完全灰化か、高温の燃焼炭化か等の燃焼結果を調整出来る手段。
▲ハ▼社会の求めるそれ等物質の燃焼経過は厳しい条件を課せられているのでそれを克服する手段。
と云う具体的技術目標を設定した。
【課題を解決するための手段】
【0004】
本発明者等は燃焼手段の改良について既に出願(特許願平7−77060号)し、それに準拠した平成11年1月7日提出の特許願−成熟植物素材の炭化装置(特許願平11−40473)に基いて対象物質、手段を改良拡大して國内優先権出願するものである。
成熟固体物質とは例えば、成熟した植物体の様に木化現象つまり成熟してリグニン層の形成が完成した副生物、又は経済生活活動による完成された物質の廃棄副生物がある。前者は高温で炭化処理することによって更に付加価値を生み出せるが、後者にあっては厳しい条件のもとで高温燃焼で完全灰化する外ない。
いづれの固体物質も前項▲イ▼の特性から、乾溜→ガス化→燃焼反応と云う燃焼工程が長いので、その対応手段として本願の炉を開発したものである。
【0005】
新開発の炉は、堅型炉と基部において燃焼室が一体化された斜傾炉を備えたもので処理する物質に合わせて▲1▼素材の供給と、▲2▼煙突における吸引力と、▲3▼対向流送風量、の3要因を相関調整する機構を有し課題の解決に資するものである。
【0006】
又、現今の社会環境は燃焼排ガスの質を最大重要視する厳しさに合わせて、遠赤外線の力を活用出来る炉体構造と燃焼空気供給方法の特徴機構を活かして、助燃物質添加等により空気量を最小限に抑制しながらNOxの発生を少なくすると共に、ダイオキシン等の悪性ガスの生成ゾーンや熱交換水管腐食ゾーンを越える高温完全燃焼に到達する。
【0007】
更には海洋性腐植物質の添加は、当該物質が原素に近い状態で存在し、且つ構造式上不飽和で塩基置換性能が高いと云う特徴を有することから、高温雰囲気の中で昇華ガス化し燃焼ガスの浄化に貢献して積極的環境浄化を目指すものである。
【実施例】
【0008】
以下図面に基いて−実施例の装置構造と燃焼作用とその調整について述べる。
図1−は吸引乾溜ガス化燃焼装置の縦断側面図である。
1−堅型基部炉体であるが、上部に熱交換水管を接続する為横断図は円形である。
2−は上部熱交換炉体である。3−は斜傾炉体で燃焼室が基部炉体と一体化されており、乾溜段階を受け持つ炉で、素材の流れが平面的であることが望ましいので底面が平で側上部は偏長方半円形である。4−は1と2との炉体内面炉材で、耐高熱性(耐1,500℃)のキャスターや北海道産の鉱石シリカブラックと、火山溶岩礫の遠赤外線放射力の強い物質を混合して成型している。5−は複数の素材分散装置である。6−は素材供給口で,7−の素材供給装置が装架されている。8−はバーナー口で空気供給制御機構を備えており、9−のバーナーが着火当初装着されている。10−は直列高圧空気噴射管で13−の炉外高圧送風機に接続し、11−はラッパ形単列の高圧空気噴射装置で12−の炉外高圧送風機に接続されている。10−2及び11−2はそれぞれの空気膜で燃焼反応層となり電磁波バリヤ化する。14−は熱交換貫流水管で2の炉体内に納まり、下部は15−のカスケードポンプが連結され、上端は16−の圧力弁を介して外部に蒸気を供給する。17−は煙突基部で、18−は煙突である。19−はベンチュリスクラバ噴射口で、20−の炉外高圧送風機に連結されている。21−は炉底で、21−2は燃焼部位となる。22−は燃焼残留物溜りである。溜りには23−の水冷の掻き出しスクリューが装着されている。
【0009】
以上の構成に基いて
まず20の高圧送風機が稼動すると19のベンチュリスクラバが機能して炉内に強い負圧が生ずる。17から有意の水分と素材が供給され、9のバーナーが着火されると、煙は基部へ下降した後18の煙突に流れる。着火が安定したところで、まず13暫くして12及び13の高圧送風機が稼動すると10と11から高圧空気が噴射され、10−2と11−2の燃焼反応層が形成され、炉内は急速に高温となり繊維質素材であればバーナーは外されて空気調節装置が操作され、素材が粗大(RDFの如き)であればバーナー着火は継続される。
素材は5の複数の素材分散装置でバウンドしながら、3の斜傾炉の底辺を流れながら乾溜ガス化段階を経過し、水で灰は液化されるか、炭化物は消火冷却される設定である。
4のそれぞれの炉壁は遠赤外線を反射し合い、10−2と11−2では激しい燃焼反応が起こり電磁波バリヤとなっていよいよ高温となり、相乗効果で高温となった熱線を照射された素材は3で乾溜ガス化が進み、21に達した燃焼物は最も高温となり21−2の燃焼部位から発する幅射熱線は14の熱交換貫流水管に直接照射し、高率の熱交換が進んで効率よく蒸気が発生し、16の圧力弁を押し上げて外部に供給される。熱交換を終えた燃焼排ガスはベンチュリスクラバの空気で温度が下がり煙突から排出される。
【0010】
改めて本発明装置機能をまとめてみると、
本願燃焼熱交換炉は、堅型基部炉と斜傾炉が燃焼室を一体化されており、強い負圧のもとで乾溜→ガス化→燃焼反応と云う長い工程をそれぞれの位置で十分に反応させる時間経過を与える為に開発したもので、高温の燃焼雰囲気を長い行程でつくり出し維持して、有機質(セルロース)の気化ガス化を完了させ蒸し焼状態にする。その点で燃料に直接空気を吹きつけ供給する従来法と技術思想が異なる。
【0011】
炉体内壁は燃焼促進効率の高い複数の遠赤外線放射機能素材が充分使用されており、複数の助燃物質を添加された燃焼物の供給と、煙突の吸引力と、燃焼空気の供給と云う3つの要因を相関調整しながら運転すると、それぞれ設定された機能が作動するが、それに加えて内壁炉材から効率の高い遠赤外線が放射反射し合い、対向流の高圧燃焼空気噴射によってつくり出される電磁波バリヤも高度の機能を発現し、包み込まれた燃焼部は益々高温となり燃料物素材はそれ等熱線の相乗作用を受け有機質がガス化して燃え尽きる。その結果燃焼部位から、熱交換水管に直照射される放射幅射熱線は遠赤外線の力を借りて熱交換機能を高める。
【0012】
改めて斜傾炉ではそれ等が強い負圧のもとで進むので、燃焼反応は空気の吹出側で激しく、炉底面を流れる素材に熱線を照射する。炉の底辺にそって流れる素材の層と、気化ガスが燃えて電磁波を出しながら流れる層とは気体と固体の質量の差と、放射輻射熱線−電磁波線には放射圧がある機能によって分離機能が作用して乾溜炭素化が完了し、到達した堅型の炉底部位置で竪型炉の電磁波バリヤに包み込んで完全に燃焼を終わらせる機構である。本願燃焼法が燃焼空気の供給をコントロールされている機構のもとで、特に斜傾炉では噴射された高圧空気は乾溜気化された燃焼ガスと即反応するから、その酸素は噴射装置の近くで消費されてしまう。したがって素材層には酸素がとどかず、熱線照射によって乾溜ガス化が進むだけで気体と固体の上述の関係で結果的に素材流層は酸欠状態で推移流動し、乾溜炭素化域に到達する。
素材の質に合わせて供給量を少なくして炉内の滞留時間を長くすれば完全に灰化し、供給量を増やして流速を速くすれば有機質(セルロース等)がガス化してリグリン層が残っている状態で取り出せば活性炭構造の炭化材となる。従来の燃焼技術思想と異なる、熱交換の立場から見つけた新しい燃焼法の本願技術特徴がその作用効果を出し得るのである。
【発明の効果】
【0013】
以上詳述した様に本発明装置は、処理する物質のもっている本質的特性をふまえて、完全な熱交換と、高率の熱交換を達成するものである。
現今の社会環境の中にあって産業廃棄物的資源処理と、エネルギー源に活用転換することとは一日もゆるがせに出来ない課題である。加えて成熟植物資源素材にあっては高品質の炭素材とすることで総体的に炭化つまり燃焼ガス化して排出する部分を減らして大きな付加価値を生み出し有用活用部分を残す物質循環のメリットは莫大で、更にそれを必要とする社会需要は、人類の生存の為に環境浄化と云う面から拡大の一途にある。本願装置が燃焼過程における燃焼排ガスの浄化手段を目指した機構と共に社会に貢献できる分野は大きい。
【0014】
尚、本願が燃焼と熱交換の段階で止めているのは、本発明者等による先願の特許願平10年12月16日提出の環境浄化型高能率熱交換燃焼装置や、特許願平11年9月16日提出の環境浄化型廃油燃焼発電装置との関連において、処理する固体物質の特性に合わせて、複数の先願との合体利用の一分野、特に斜傾炉による固体物質の吸引乾溜ガス化工程のより完全化を目指したものである。
具体的な利用項目としては優良な成熟植物繊維素材の炭化、木材チップや建築廃材の炭化による有用資源化や、生活産廃物にもRDF化して発電するに当たっての熱転換並びに熱交換の効率向上等、更にはマグネシウムの特性を助燃剤に利用出来ることは、マグネシウム時代と云われる21世紀にあっては、日本が資源として誇れる環境にあることの利用効果の向上による社会貢献は非常に大きい。
【図面の簡単な説明】
【図1】−は成熟固体物質の吸引乾溜ガス化検証装置の縦断側面図である。
【符号の説明】
1−は堅型基部炉体。2−は上部熱交換炉体。3−斜傾炉体。4−内装炉壁。5−素材分散装置。6−素材供給口。7−素材供給装置。8−バーナー口で空気供給制御部。9−バーナー。10−直列高圧空気噴射装置。11−ラッパ状単列高圧空気噴射装置。10−2及び11−2は噴射空気膜。12−高圧送風機。13−高圧送風機。14−熱交換水管。15−カスケートポンプ。16−圧力弁。17−煙突基部。18−煙突。19−ベンチュリスクラバ噴射口。20−高圧送風機。21−炉底部。21−2−燃焼部位。22−燃焼残物溜り。23−水冷スクリュー。BACKGROUND OF THE INVENTION
[0001]
The present invention relates to a technique for incinerating a solid substance similar to industrial waste or regenerating it into a modified carbonizer.
[Prior art]
[0002]
Some by-products in production activities and by-products from economic life activities can be converted to effective heat by incineration, but are left unused due to processing restrictions and technical difficulties Many methods have been devised because they cannot be relaxed in the social environment, but the use of them is stagnant as it cannot clear the constraints unless it is a large device, and the development of effective utilization processing technology Is needed.
[Problems to be solved by the invention]
[0003]
The present inventor has intensively studied what should be done in order to overcome the technical difficulties in the previous paragraph in the current social environment,
▲ I ▼ Solid materials, which are industrial waste resources to be treated, reach high temperature complete combustion based on the characteristics of high ignition point temperature, weak self-combustion power, coarseness and large quantity. , A heat exchange means for converting the combustion heat into effective steam heat.
(B) Means that can adjust the combustion results such as complete ashing or high-temperature combustion carbonization according to the material while taking into account the characteristics of the material of the previous item.
▲ C: A means of overcoming the burning process of these substances demanded by society is imposed by severe conditions.
A specific technical goal was set.
[Means for Solving the Problems]
[0004]
The present inventors have already filed an application for improvement of combustion means (Patent Application No. 7-77060) and filed on January 7, 1999 in accordance with it-Carbonization device for mature plant material (Patent Application No. 11- No. 40473) to improve and expand the target substance and means, and apply for domestic priority.
The mature solid material includes, for example, a by-product such as a mature plant body, that is, a by-product in which the formation of a lignin layer is completed by maturation, or a waste by-product of a material that has been completed through economic life activities. The former can be further added value by carbonizing at high temperature, but the latter can be completely ashed by high temperature combustion under severe conditions.
All of the solid substances have a long combustion process of dry distillation → gasification → combustion reaction due to the characteristics of {circle around (1)} above, so the furnace of the present application has been developed as a countermeasure.
[0005]
The newly developed furnace is equipped with a tilt furnace with a combustion chamber integrated in the solid furnace and the base. (1) Supply of materials according to the material to be treated, (2) Suction power in the chimney, (3) A mechanism that correlates and adjusts the three factors of the counterflow air flow rate contributes to solving the problem.
[0006]
In addition, the current social environment is in line with the strictest importance of the quality of combustion exhaust gas, making use of the characteristics of the furnace structure and combustion air supply method that can utilize the power of far-infrared rays, and by adding auxiliary combustion substances, etc. While suppressing the amount to the minimum, the generation of NOx is reduced, and high temperature complete combustion exceeding the production zone of malignant gas such as dioxin and the heat exchange water pipe corrosion zone is reached.
[0007]
Furthermore, the addition of marine humic substances is characterized by the fact that the substance is present in a state close to the raw material, and is structurally unsaturated and has high base substitution performance. It aims to actively purify the environment by contributing to the purification of combustion gases.
【Example】
[0008]
In the following, based on the drawings, the device structure, combustion action and adjustment of the embodiment will be described.
FIG. 1 is a longitudinal side view of a suction dry distillation gasification combustion apparatus.
1-Solid base furnace body, but the cross section is circular in order to connect the heat exchange water pipe to the top.
2- is an upper heat exchange furnace body. 3- is a tilting furnace body, and the combustion chamber is integrated with the base furnace body. It is a furnace that takes charge of the dry distillation stage. It is desirable that the material flow is flat, so that the bottom surface is flat and the upper side is flat. Semicircular. 4- is a furnace inner surface furnace material of 1 and 2, which is composed of casters with high heat resistance (1,500 ° C resistance) and ore silica black from Hokkaido, and materials with strong far-infrared radiation of volcanic lava gravel. And molding. 5- is a plurality of material dispersing devices.
[0009]
Based on the above configuration, when 20 high-pressure blowers are operated, 19 venturi scrubbers function and a strong negative pressure is generated in the furnace. When significant moisture and material are supplied from 17 and the 9 burner is ignited, the smoke descends to the base and then flows into 18 chimneys. When the ignition is stabilized, first, when the
The material bounces at a plurality of material dispersing devices of 5, while passing through the bottom of the tilting furnace of 3 and passes through the dry distillation gasification stage, so that ash is liquefied with water or carbide is extinguished and cooled. .
Each furnace wall of 4 reflects far-infrared rays, and in 10-2 and 11-2, a severe combustion reaction occurs and becomes an electromagnetic wave barrier. In Fig. 3, dry distillation gasification progressed, and the combustion product that reached 21 became the highest temperature, and the radiant heat rays emitted from the combustion site of 21-2 were directly irradiated to the 14 heat exchange once-through water pipes, and the high rate of heat exchange progressed and the efficiency Steam is often generated, and the 16 pressure valves are pushed up and supplied to the outside. After the heat exchange, the flue gas is ventilated by venturi scrubber air and discharged from the chimney.
[0010]
When the device function of the present invention is summarized again,
The combustion heat exchange furnace of the present application has a solid base furnace and a tilting furnace integrated into the combustion chamber, and a long process of dry distillation → gasification → combustion reaction is sufficiently performed at each position under a strong negative pressure. Developed to give the reaction time lapse, create and maintain a high-temperature combustion atmosphere in a long stroke, complete vaporization and gasification of organic matter (cellulose) and put it into a steamed state. In this respect, the technical idea is different from the conventional method in which air is directly blown into the fuel.
[0011]
The inner wall of the furnace is sufficiently made of a plurality of far infrared radiation functional materials having high combustion promotion efficiency, and is called supply of combustion products to which a plurality of auxiliary substances are added, suction power of a chimney, and supply of combustion air 3 When operating while correlating the two factors, each set function operates, but in addition to that, highly efficient far-infrared rays are radiated and reflected from the inner wall furnace material, and electromagnetic waves generated by high-pressure combustion air injection in the counterflow The barrier also exhibits advanced functions, and the encased combustion section becomes increasingly hot, and the fuel material is subjected to the synergistic action of these heat rays and the organic matter is gasified and burned out. As a result, the radiation width radiation line directly irradiated from the combustion site to the heat exchange water pipe enhances the heat exchange function with the aid of far infrared rays.
[0012]
In the tilting furnace again, they proceed under strong negative pressure, so the combustion reaction is intense on the air blowing side, and the material flowing through the bottom of the furnace is irradiated with heat rays. The material layer that flows along the bottom of the furnace and the layer that flows while the vaporized gas burns and emits electromagnetic waves are separated by the difference in mass between the gas and solid, and the radiation heat ray-electromagnetic wave radiation has a radiation pressure function. This is the mechanism that completes the combustion by enclosing the carbonization in the vertical furnace at the position of the bottom of the solid furnace that has reached the dry-type carbonization by the action of the Under the mechanism in which the combustion method of the present application controls the supply of combustion air, especially in a tilting furnace, the injected high-pressure air reacts immediately with the combustion gas vaporized in dry distillation, so the oxygen is close to the injection device. It will be consumed. Therefore, oxygen does not reach the material layer, and only gasification progresses by irradiation with heat rays. As a result, the material flow layer transitions and flows in an oxygen-deficient state due to the above-mentioned relationship between gas and solid, and reaches the carbonization region. .
If the amount of supply is reduced according to the quality of the material and the residence time in the furnace is lengthened, it will completely ash, and if the amount of supply is increased and the flow rate is increased, the organic matter (cellulose etc.) will be gasified and the ligrin layer will remain. If it is taken out in the state where it is, it becomes a carbonized material of activated carbon structure. This technical feature of the new combustion method found from the viewpoint of heat exchange, which is different from the conventional combustion technology idea, can exert its effect.
【The invention's effect】
[0013]
As described in detail above, the apparatus of the present invention achieves complete heat exchange and high-rate heat exchange based on the essential characteristics of the substance to be treated.
In today's social environment, the disposal of industrial waste resources and the conversion to energy sources are issues that cannot be relaxed for a day. In addition, for mature plant resource materials, the benefits of material recycling are enormous, creating high added value by reducing the part that is carbonized, that is, converted into combustion gas, and producing large added value by using high-quality carbon material. In addition, social demands that require it are expanding from the perspective of environmental purification for the survival of humankind. There are many fields where the device of the present application can contribute to society together with a mechanism aimed at purifying flue gas in the combustion process.
[0014]
It should be noted that the present application stops at the stage of combustion and heat exchange, such as the environmental purification type high efficiency heat exchange combustion apparatus filed on December 16, 2010, the patent application filed earlier by the present inventors, and the like. In connection with the environmentally-purified waste oil combustion power generation device submitted on September 16, 2011, in accordance with the characteristics of the solid material to be processed, the field of combined use with multiple prior applications, especially for the solid material by the tilting furnace It aims to make the suction dry distillation gasification process more complete.
Specific use items include carbonization of excellent mature plant fiber materials, conversion of useful resources by carbonization of wood chips and building waste materials, and heat conversion and improvement of heat exchange efficiency when generating power by converting RDF into domestic waste. In addition, the fact that magnesium can be used as a combustion aid in the 21st century, which is said to be the magnesium era, greatly contributes to society by improving the utilization effect of Japan's pride as an environment.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a longitudinal side view of an apparatus for verifying gasification of a mature solid substance by suction dry distillation.
[Explanation of symbols]
1- is a solid base furnace body. 2- is an upper heat exchange furnace body. 3-Tilt furnace body. 4-Interior furnace wall. 5- Material disperser. 6-Material supply port. 7-Material supply device. 8-Air supply control unit with burner port. 9-Burner. 10-series high pressure air injection device. 11-trumpet single row high pressure air injection device. Reference numerals 10-2 and 11-2 denote jet air films. 12—High pressure blower. 13—High pressure blower. 14-Heat exchange water tube. 15-Cask skate pump. 16-pressure valve. 17-Chimney base. 18-Chimney. 19-Venturi scrubber spout. 20—High pressure blower. 21-Furnace bottom. 21-2- Combustion site. 22-Combustion residue reservoir. 23-water-cooled screw.
Claims (1)
斜傾炉は頂部が長半円形で底部を平面の断面より成り、上部に素材供給口とバーナー口が設けられ、粗密な素材が自然に押し出し流下する傾斜度で有意の高さと長さをもって堅型炉に組み合わされ、底辺途中に素材がバウンドする素材分散装置が設けられ、それに対向する上部炉頂部には、底辺に対して斜め上向きに直列カーテン状高圧空気噴射管が複数設けられ、炉外の高圧送風装置に接続されている。
堅型基部炉上端に炉内径と同じ内径と有意の高さを有する堅形貫流パイプ並列型、或いは渦巻きパイプ型の熱交換貫流水管が重ねて設けられ、下端をカスケートポンプに接続され、上端は圧力弁を介して外部に接続されており、水管は周囲を基部炉壁と同じ資材で囲まれ上部熱交換炉を成す。
炉最上部は絞り込まれて煙突基部となり、強力な吸引機能を有する煙突を備えて炉内には強い負圧が働いている。
堅型基部炉上端位置付近中央から燃焼ガスの流れに斜めに対向し燃焼部位を包み込む火元方向に向けたラッパ形単列カーテン状の高圧空気噴射装置が設けられ、炉外の高圧送風機に接続されている。
堅型基部炉の底部は、斜傾炉底部の底辺を延長したロストル構造で、端近くで燃焼灰或いは炭化剤の落下口が開口され、落下した燃焼残物は常時水冷スクリューで外部にかき出され水で液化は又は冷却される。
前述装置の傾斜炉上部から助燃剤等を添加がされた素材物質が供給され、バーナーが着火されると熱が発生し炉壁も熱する。熱せられた炉壁から赤外線が反射放射されて相乗作用で乾溜気化ガスが生じ負圧に引かれて下降しながら、複数の対向する高圧空気膜と燃焼反応しつつ、ガスは累進高温化し、素材物質は酸欠炭化が進み、基部炉に到達するまでには炭化段階が終わり完全な燃料炭素状となる。
堅型炉では、対向流送風膜での放射反応が効率よく機能し、燃料炭素炎は高温放射ガス体に進相して幅射熱線を熱交換水管に直照射して、高率の熱交換が進行し高能率熱交換の為の燃焼を達成する。
以上の機能のもとで、▲1▼素材物質の供給スピードと、▲2▼煙突の吸引力と、▲3▼対向流送風量の、3要因を相関調整することによって素材物質の質に応じて炭素材として取出すか、完全な炭化まで燃焼させるか、求める状態に燃焼段階を調節出来る機構の構造を有することを特徴とする成熟固体物質の吸引乾溜ガス化燃焼装置。At the base position of the circular rigid combustion heat exchanger, the inside of the rigid base connecting part and the inclined part of the combustion heat exchanger having the inclined furnace part branched while the combustion chambers are integrally connected is heat resistant. It is constructed of a material with excellent radiation function such as far infrared rays, which has excellent combustion heat exchange acceleration efficiency, and is surrounded by a heat insulating material and an iron plate.
The tilting furnace has a long semicircular top and a flat cross section at the bottom, and a material supply port and a burner port are provided at the top. Combined with the mold furnace, a material dispersion device that bounces the material in the middle of the bottom is provided, and the top furnace top facing it is provided with a plurality of series curtain-shaped high-pressure air injection tubes obliquely upward with respect to the bottom. Connected to the high-pressure blower.
At the upper end of the rigid base furnace, a heat exchange once-through water pipe of a solid once-through pipe parallel type or swirl pipe type having the same inner diameter and significant height as the furnace inner diameter is overlapped, and the lower end is connected to a skate pump and the upper end Is connected to the outside through a pressure valve, and the water pipe is surrounded by the same material as the base furnace wall to form an upper heat exchange furnace.
The top of the furnace is squeezed into a chimney base, which has a chimney with a strong suction function and a strong negative pressure is working in the furnace.
A trumpet-shaped single-row curtain-shaped high-pressure air injection device facing the combustion gas flow from the center near the upper end of the rigid base furnace and facing the combustion area is provided and connected to a high-pressure blower outside the furnace. Has been.
The bottom of the rigid base furnace is a rooster structure with the bottom of the tilted furnace bottom extended, with a drop of combustion ash or charcoal opening near the end, and the fallen combustion residue is constantly pumped out with a water-cooled screw. And then liquefied or cooled with water.
When the material material to which the auxiliary combustor or the like is added is supplied from the upper part of the tilt furnace of the above-mentioned apparatus and the burner is ignited, heat is generated and the furnace wall is also heated. Infrared radiation is reflected and radiated from the heated furnace wall, and a dry-distilled gas is generated by a synergistic action and is pulled down by negative pressure. The material undergoes oxygen deficient carbonization, and by the time it reaches the base furnace, the carbonization stage is completed and it becomes a complete fuel carbon.
In a solid furnace, the radiation reaction at the counter-flow blown membrane functions efficiently, and the fuel carbon flame advances to the high-temperature radiant gas body and directly irradiates the radiant heat ray to the heat exchange water pipe to achieve a high rate of heat exchange. Progresses to achieve combustion for high efficiency heat exchange.
Based on the above functions, (1) the supply speed of the material, (2) the suction power of the chimney, and (3) the counterflow air flow are adjusted to correlate with the quality of the material. It has a structure of a mechanism capable of adjusting the combustion stage to a desired state, whether it is taken out as a carbon material, combusted until complete carbonization, or a mature solid substance gasification combustion gasification combustion apparatus.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30980799A JP4220083B2 (en) | 1999-01-07 | 1999-09-25 | Suction dry distillation gasification combustion equipment for mature solid substances |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11-40473 | 1999-01-07 | ||
JP4047399 | 1999-01-07 | ||
JP30980799A JP4220083B2 (en) | 1999-01-07 | 1999-09-25 | Suction dry distillation gasification combustion equipment for mature solid substances |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2000297916A JP2000297916A (en) | 2000-10-24 |
JP2000297916A5 JP2000297916A5 (en) | 2007-10-11 |
JP4220083B2 true JP4220083B2 (en) | 2009-02-04 |
Family
ID=26379928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30980799A Expired - Fee Related JP4220083B2 (en) | 1999-01-07 | 1999-09-25 | Suction dry distillation gasification combustion equipment for mature solid substances |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4220083B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4824827B1 (en) * | 2010-09-13 | 2011-11-30 | 弥一 小原 | Steam boiler using solid biomass or coal as fuel |
CN105567265A (en) * | 2016-01-08 | 2016-05-11 | 李卓 | Straw carbonization apparatus |
CN118579786B (en) * | 2024-07-18 | 2024-10-18 | 山西龙清环保新材料有限公司 | Carbonization-activation integrated active carbon sintering equipment |
-
1999
- 1999-09-25 JP JP30980799A patent/JP4220083B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2000297916A (en) | 2000-10-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104748125B (en) | Pyrolysis volatile matter combustion system | |
CN107760387B (en) | High-nitrogen biomass waste gasification combustion heat supply system and process | |
CN207877656U (en) | A kind of novel household garbage pyrolysis gasification furnace | |
CN106338068A (en) | Household garbage pyrolysis and gasification processing system | |
CN2879022Y (en) | Biomass vaporization boiler | |
CN1834535A (en) | Smokeless coal burning boiler and gas synthetizing equipment thereof | |
CN110894948A (en) | System and method for treating household garbage | |
CN102746902A (en) | Gasification method of organic wastes and special gasification furnace | |
CN103423775A (en) | Biomass semi-gasification furnace | |
WO2016206431A1 (en) | Burner used for biomass-gas industrial water heater | |
CN207913462U (en) | Adsorbent desorption and regeneration retracting device | |
JP4220083B2 (en) | Suction dry distillation gasification combustion equipment for mature solid substances | |
CN102635940B (en) | Gasification combined-combustion hot-blast stove | |
CN209778617U (en) | system for handle mud | |
CN214949206U (en) | Low-order clean bituminous coal burning civil stove | |
CN108423680A (en) | A kind of two sections of chemical activation stoves of self-heat-supply | |
CN205048450U (en) | Automatic arrange sediment multi - functional garbage and burn burning furnace | |
CN105861061A (en) | Novel furnace core structure of medium and large biomass gasification device | |
WO2015023169A1 (en) | Domestic boiler operating on solid fuel of variable moisture content | |
JP2000297916A5 (en) | ||
CN106642136A (en) | Heat accumulating type spiral pyrolysis device and application thereof | |
CN208136186U (en) | The downdraft combustion furnace of bamboo timber stoving and bamboo and wood charcoal production zero-emission cigarette is realized simultaneously | |
CN106051777A (en) | Porous medium combustion device for garbage pyrolysis | |
CN201697112U (en) | Boiler combusting biomass fuel gas | |
CN205939156U (en) | A porous medium burner for garbage pyrolytic |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20060922 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20060922 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20070316 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20080226 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20080422 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20080620 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20080916 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20081004 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111018 |
|
R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111018 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111018 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111018 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111018 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111121 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20121121 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20131121 Year of fee payment: 5 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |