JP2005140346A - Continuous combustion type small furnace device for biological waste such as poultry manure - Google Patents

Continuous combustion type small furnace device for biological waste such as poultry manure Download PDF

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JP2005140346A
JP2005140346A JP2003374114A JP2003374114A JP2005140346A JP 2005140346 A JP2005140346 A JP 2005140346A JP 2003374114 A JP2003374114 A JP 2003374114A JP 2003374114 A JP2003374114 A JP 2003374114A JP 2005140346 A JP2005140346 A JP 2005140346A
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Hiroshi Shimizu
浩 清水
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<P>PROBLEM TO BE SOLVED: To provide a continuous combustion type small furnace device for biological waste such as poultry manure capable of corresponding to the biological waste such as poultry manure in units of production site, sufficiently preventing air pollution by a continuous combustion type small scale furnace having no obligations of a structural criterion such as a dust collector, and providing effective utilization of a biomass resource by increasing an actual throughput. <P>SOLUTION: In a structure of a primary furnace, a deposit layer is constantly maintained porous even with respect to a raw material to be treated such as the poultry manure that consolidates easily, a necessary minimum of air is sent to carbon content combustion which is a gasification heat source, a quantity of combustion heat is effectively transferred into the deposit layer to be used as a heat source for pyrolysis and drying, a generation gas permeation speed from the deposit layer to an upper space is maintained small to prevent dust floating, and mixed foreign matter of the raw material to be treated is coped with without difficulty. And a structure is provided for carrying out gas combustion of produced gas by an even high temperature, adjusting high temperature exhaust gas to a proper temperature by heat exchange or outside air introduction, and precedently drying the raw material to be treated to prevent dust scattering even when increasing the actual throughput. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、ブロイラー糞や採卵用鶏糞やコンバイン廃稲藁や園芸廃材やチップ残樹皮や間伐材などの生物系廃棄物を、集塵装置など構造装置の設置義務が無い毎時200kg未満の小型炉により燃焼処理し、必要時には比較的高水分の原料を燃焼排気で燃焼の事前に乾燥処理することで実質処理量を増加し、かつ、比較的安価に製造可能な連続燃焼式によって大気汚染を良く防止し、燃焼熱量を近接地域で有効利用できる小型炉に関する。   The present invention is a small furnace of less than 200 kg per hour without broiler manure, poultry manure for egg collection, combine waste rice straw, horticultural waste material, chip residual bark, thinning material, etc. By using a continuous combustion system that can be manufactured at a relatively low cost, it is possible to reduce air pollution by increasing the actual throughput by drying the material with relatively high water content before combustion with combustion exhaust gas when necessary. The present invention relates to a small furnace that can prevent and effectively use the heat of combustion in an adjacent area.

小型燃焼炉として従来は簡易なバッチ式が一般であったが、ブロイラー糞では床暖房用熱源とする為に連続燃焼式が使われ、共に排気中のダイオキシン量の規制へ対応する必要が生じ、煤塵や硫黄酸化物の排出に対しても規制が強化される状況にあり、バッチ式では燃焼開始時と終了時にダイオキシンが規制値を逸脱する事を批判されるし、床暖房用では気温差に応じて燃焼を断続するのが一般なので実状は連続燃焼ではなく、いずれも抜本的な改良が必要であるのに対し、法規制の事前から特公平5−57483や特開平10−8064や特開平2000−356335などの成果を蓄積したが、比較的高水分であって圧縮すると固決し易い鶏糞など生物系廃棄物には適合し難いし、1次炉内に鋼板製の遮断壁を設けるのでは耐熱耐久性が困難だったし、その他の実体にも沿うよう切迫した事態に合わせた一層の改良を必要とした。   Conventionally, as a small combustion furnace, a simple batch type was generally used, but in the broiler feces, a continuous combustion type was used to provide a heat source for floor heating, and it was necessary to comply with the regulations on the amount of dioxins in the exhaust. Regulations are also being strengthened for dust and sulfur oxide emissions, and in batch systems, it is criticized that dioxins deviate from the regulation values at the start and end of combustion, and for floor heating, there is a temperature difference. Since the combustion is generally interrupted accordingly, the actual condition is not continuous combustion, and all of these require radical improvement. On the other hand, Japanese Patent Publication No. 5-57483, Japanese Patent Laid-Open No. 10-8064 and Japanese Patent Laid-Open No. 2000-356335 etc. have been accumulated, but it is difficult to adapt to biological waste such as chicken manure which is relatively high in moisture and easily fixed when compressed, and it is not possible to provide a steel plate barrier in the primary furnace. Heat resistance It was a flame, was the need for further improvements to meet the impending situation so that along to other entities.

鶏糞など生物系廃棄物を対象とする連続投入式の小型燃焼炉において、排気ガス中のダイオキシン濃度を規制値以下へ充分に収め、しかも、高価な集塵装置などを設置しなくても煤塵飛散を極めて僅少に収め、発生熱量の大幅な制御で昼夜も連続燃焼を保ち、1次炉の耐熱耐久性を長期間保持して在来の鶏糞燃焼炉よりも安価な装置とし、比較的高水分な鶏糞などの生物系廃棄物も安定して処理し、小型炉ならば近接地へ配管容易なので資源を有効利用して需要へ応える。   In a continuous charging type small combustion furnace for biological waste such as chicken manure, the concentration of dioxin in exhaust gas is kept below the regulation value and dust is scattered without installing expensive dust collectors. Is extremely low, keeps continuous combustion day and night by controlling the amount of generated heat, keeps the heat resistance and durability of the primary furnace for a long period of time, and makes it a cheaper device than a conventional chicken manure combustion furnace, with relatively high moisture It can handle biological waste such as chicken manure stably, and if it is a small furnace, it can be easily piped to a nearby area, so resources are used effectively to meet demand.

ブロイラーは農家への委託飼育だが規模拡大の傾向に在り、毎時燃焼量が増加すると小型炉として有利な大気汚染防止の規制には沿い難く、採卵養鶏は更に大規模だし暖房を必要としないのが一般であって、鶏糞を有機肥料として生産販売するのは不利なので焼却処分する状態だから一層重大であり、従って、抜け羽などが浮上し易い難点を持つ鶏糞をも支障なく燃焼炉の高温排気で事前乾燥して重量軽減し、鶏糞発生量に対する燃焼処理量を許容値内で増加すると有利であり、その他の生物系廃棄物も過剰な実状にあり、例えばコンバインで切断放棄する稲藁は水田圃場へ対して過剰な場合には火を付け煙が車路へ流れる現状であり、従ってバイオマス資源を生産者の利益とする本発明は地球環境をも保全する。   Broilers are farmed to farmers, but they are on a growing trend, and if the amount of combustion per hour increases, it is difficult to comply with the air pollution prevention regulations that are advantageous as a small furnace, and egg-raising chickens are even larger and do not require heating. In general, it is disadvantageous to produce and sell chicken manure as organic fertilizer, so it is more serious because it is incinerated. It is advantageous to reduce the weight by pre-drying and increase the amount of combustion treatment with respect to the amount of chicken manure generated within the allowable value, and other biological waste is also in an excessive state, for example, rice straw that is abandoned by cutting with combine is used in paddy field However, the present invention, which uses a biomass resource as a producer's benefit, protects the global environment.

上記目的を達成するために、本発明の連続燃焼式小型炉においては、1次炉内に設けた広幅で緩傾斜(15度位)の床面上へ原料供給装置を薄厚状に同幅で開口連結し、該床面を滑落限界角(40度位)の底面へ連結して該底面の末端は残滓排出装置へ接続し、該底面と接合する1次炉の他の外壁はアーチ形を形成して耐熱耐久性を保持し、アーチの天面を該底面と近接角度に保持して1次炉内の堆積層をポーラスに保持し、該天面は供給装置の高さで緩傾斜へ変異して1次炉内へ狭間隙に上部空間を形成し、該底面および相対の天面へは極細径の通気管を多数個設置して空気ポンプへ集合連結することで該堆積層を効率的に熱分解ガス化し、該上部空間は該床面位置で上向きの収束空間へ連結してから排気管へ連結し、該排気管を円錐筒内へ連結してブロワにより薄膜状に分割通気して均一高温にガス燃焼し、その高温排気を吸引ブロワで適正温度へ調整する。   In order to achieve the above-mentioned object, in the continuous combustion type small reactor of the present invention, the raw material supply device is formed in the same width in a thin shape on the floor surface of the wide and gentle inclination (about 15 degrees) provided in the primary furnace. Opening connection, connecting the floor surface to the bottom surface of the sliding limit angle (about 40 degrees), the bottom end of the bottom surface is connected to the residue discharge device, and the other outer wall of the primary furnace joined to the bottom surface is arched It is formed to maintain heat resistance and durability, and the top surface of the arch is held close to the bottom surface to hold the deposited layer in the primary furnace porous, and the top surface is gently inclined at the height of the supply device. Efficiently forms an upper space in a narrow gap in the primary furnace, and installs a large number of ultrafine vent pipes on the bottom surface and the relative top surface, and collectively connects them to an air pump to make the deposited layer efficient And the upper space is connected to the upward converging space at the floor surface position and then connected to the exhaust pipe, and the exhaust pipe is connected to the conical cylinder. Divided vented into a thin film by the gas combustion in uniform high temperature by a blower and connected to adjust the hot exhaust suction blower to the proper temperature.

上記の連続燃焼式小型炉に接続して、密閉容器内に滑落限界角(40度位)で通気可能な底面を設置して下方空間を構成し、該吸引ブロワの吐出管を内装して外気導入した排気管を該空間へ連結し、該容器上部へ原料供給蓋を設置して該底面の傾斜末端に当たる該容器側面へは排出蓋を設置し、密閉容器内で原料中の過剰水分を蒸発する時に、該容器上部へは零細網で被覆した多孔天面を該底面と平行に設置して原料中の浮上し易い粒子の放散を阻止し、該天面の上方空間を煙突へ連結する。   Connected to the above-mentioned continuous combustion type small furnace, a bottom surface that can be ventilated at a sliding-down limit angle (about 40 degrees) is installed in a sealed container to form a lower space, and a discharge pipe of the suction blower is installed to Connect the introduced exhaust pipe to the space, install a raw material supply lid on the upper part of the container, install a discharge lid on the side of the container that hits the inclined end of the bottom surface, and evaporate excess moisture in the raw material in the sealed container At the time, a porous top surface covered with a fine mesh is placed in parallel with the bottom surface of the upper part of the container to prevent the particles floating easily in the raw material from being diffused, and the space above the top surface is connected to the chimney.

上記の連続燃焼式小型炉において、該残滓排出装置は所定厚の底盤を水平に間欠移動するよう構成して該底盤の始端側上面へ該底面の末端を接続し、該底盤の末端側上方へ接続する1次炉外壁の必要寸法を垂直な可動蓋に構成し、該可動蓋は該底盤上で旋回できるよう構成し、該可動蓋には加重機を設置して、混合異物も支障なく排出する。   In the above-described continuous combustion type small furnace, the residue discharging device is configured to intermittently move a bottom plate of a predetermined thickness horizontally, connecting the end of the bottom surface to the upper surface on the start end side of the bottom plate, and moving upward on the end side of the bottom plate. The required dimensions of the outer wall of the primary furnace to be connected are configured as a vertical movable lid, and the movable lid is configured to be able to turn on the bottom plate. A weighting machine is installed on the movable lid, and mixed foreign substances are discharged without any problem. To do.

上記のように構成された生物系廃棄物の燃焼装置について、最も現実的で緊急を要するブロイラー鶏糞を原料対象に説明すると、通常は40%位の含水率なので即座に燃焼可能ではあるが、粘着性が有るので多数本並列のスクリュウ式供給装置で1次炉内へ広幅に薄高状で圧送し、抵抗力が大だとスクリュウはホッパー内へ逆送するので1次炉内に所定高の堆積層を保ち、投入圧力により滑送可能な緩傾斜(15度位)で同幅の床面を保った後、自重での滑落限界角(40度位)の底面で幅寸法は若干縮小しつつ水平移動式排出装置へ接続し、該底面と直角にアーチ形で接続する1次炉の他の外壁は耐火煉瓦などの崩壊を防ぎ、アーチ形の天面の傾斜角は該底面と平行程度にして1次炉内堆積層の過大な自重圧縮を防いで固決し易い原料をもポーラスに保持し、投入装置の高さ位置で天面は傾斜角を緩めると堆積層上面は天面と小間隙を保って広幅で広面積の上部空間を形成し、該底面および相対の天面には極細の通気管を多数個配列し空気ポンプへ集合連結して所定量を所定位置から分散通気すると、運転当初には石油添加の紙類を堆積層上へ投入するなどで着火燃焼し、該通気管を配列する堆積層部分を燃焼層に形成する。   The most realistic and urgent broiler chicken manure for the biological waste combustor constructed as described above will be described as a raw material subject. Usually, the moisture content is about 40%, but it can be burned immediately. Because of this, a large number of screw-type supply devices in parallel are fed into the primary furnace in a wide, thin and high state, and if the resistance is large, the screw is fed back into the hopper, so that a predetermined height is set in the primary furnace. After maintaining the deposited layer and maintaining the same width floor surface with a gentle slope (about 15 degrees) that can be slid by the input pressure, the width dimension is slightly reduced at the bottom of the sliding limit angle (about 40 degrees) under its own weight. However, the other outer wall of the primary furnace connected to the horizontal moving discharge device and connected in an arch shape at right angles to the bottom surface prevents the collapse of refractory bricks, etc. The inclination angle of the top surface of the arch shape is parallel to the bottom surface The raw material which is easy to fix by preventing excessive self-compression of the deposited layer in the primary furnace When the top surface is held at the height of the charging device and the inclination of the top surface is relaxed, the top surface of the deposited layer maintains a small gap with the top surface to form a wide and wide upper space, and the bottom surface and the relative top surface In this case, a large number of ultrafine ventilation pipes are arranged and connected to an air pump, and a predetermined amount is dispersed and ventilated from a predetermined position. A deposited layer portion in which the ventilation pipes are arranged is formed in the combustion layer.

1次炉内上部空間の該床面位置で上向きの収束空間を接続して排気口へ連結し、該滑落限界の床面および相対する天面へ配列した多数個の極細通気管から空気ポンプで均等稀薄に通気し、堆積層が着火昇温して外壁材も高温になって定常状態へ達っすると該位置は高温(800〜1000℃)の燃焼層を形成して供給酸素量を消尽し、燃焼層の発生ガス通過位置に熱分解層を250〜500℃で形成し、小間隙な上部空間への高温ガス通過と外壁からの熱伝達で供給原料の乾燥層が100℃以下で該底面上に形成され、該通気管を配列しない1次炉内下部に一酸化炭素を発生しつつ均一化するおき燃焼層を形成し、所定比率の炭分を残す残滓を水平移動の排出装置の間断作動で1次炉外へ排出して常態を保ち、一方、発生ガスは該排気口へ繋がる円錐筒の内周からブロワによる薄膜状の限定通気で失火させずにガス燃焼し、ガス温度を高めてから更に薄膜状に追加通気して燃焼筒内で1,100℃位の均一高温度へガス燃焼し、廃棄物燃焼炉は理論空気量に対する空気比4.5位が普通だが本発明では均一燃焼により1.5位で良く、1次炉への通気量は合計空気比の1/4位なので全体では通常炉の実に1/12の少量が1次炉内へ通気するのみでガス化作用し、不燃の窒素ガスが小な影響も強く、投入装置から炉内対面まで広幅な該堆積層の上面は広面積でも在るので、該上部空間への発生ガスの通過速度は微小なので微粒子の粉塵も浮上し難い。   At the floor position of the upper space in the primary furnace, an upward converging space is connected and connected to the exhaust port, and air is pumped from a number of ultrafine vent pipes arranged on the floor surface at the sliding limit and on the opposite top surface. When the deposit layer ignites evenly and the deposition layer ignites and the outer wall material reaches a high temperature and reaches a steady state, the location forms a high temperature (800 to 1000 ° C) combustion layer and exhausts the amount of oxygen supplied. The pyrolysis layer is formed at 250 to 500 ° C. at the generated gas passage position of the combustion layer, and the dry layer of the feedstock is 100 ° C. or less due to the passage of the high temperature gas to the small space and the heat transfer from the outer wall. A combustion layer is formed in the lower part of the primary furnace, which is formed on the primary furnace where carbon monoxide is generated and is uniformed, and a residue that leaves a predetermined proportion of carbon is cut off. When discharged from the primary furnace during operation, the normal state is maintained, while the generated gas is connected to the exhaust port. The gas is burned from the inner circumference of the conical cylinder without causing a misfire with a thin-film limited ventilation with a blower, the gas temperature is increased, and then the additional gas is further vented into a thin film to obtain a uniform high temperature of about 1,100 ° C in the combustion cylinder. In the present invention, a waste combustion furnace generally has an air ratio of about 4.5 to the theoretical air volume, but in the present invention, it may be about 1.5 by uniform combustion, and the ventilation rate to the primary furnace is 1 / of the total air ratio. Since it is 4th place, a small amount of 1/12 of the normal furnace is gasified only by aeration into the primary furnace, and non-combustible nitrogen gas has a strong influence, and the wide range from the charging device to the inside of the furnace Since the upper surface of the deposited layer is large, the passing speed of the generated gas to the upper space is very small, so that the dust of fine particles hardly rises.

ガス燃焼後の排気は高温保持筒を通過する過程でダイオキシン類を充分に抑制し、該保持筒は熱交換式でも良いが安価に外周から放熱しても端末は800℃位と成り、吸引ブロワのエゼクタ効果による外気導入で容易に400℃位のとなるので密閉容器の底部へ圧送すると、該容器内へ投入した鶏糞など高水分原料を急速に予備乾燥し、乾燥原料は滑落底面末端の排出蓋と容器上部の投入蓋から随時に交換し、その時には飛散し易い抜け毛が多い鶏糞でも、滑落天面を多孔板として更に細かい篩目を敷くと、原料は天面に沿って流下しつつ容易に飛散防止できるし、100℃以上で排気すれば結露は無く、採卵鶏ならば燃焼量よりも多量に乾燥処理した残量を他所へ供給できる。ブロイラーの場合では該保持筒に熱交換筒を接続して、床暖房用に熱湯利用した後の排気は200℃前後なので、吸引ブロワのエゼクタ効果で外気導入して安全に排出もできるが、その排気を同様に予備乾燥用へ使用できる作用は上記と同じできる。   Exhaust after gas combustion sufficiently suppresses dioxins in the process of passing through the high-temperature holding cylinder, and the holding cylinder may be heat exchange type, but the terminal is at about 800 ° C. even if heat is released from the outer periphery at low cost, and the suction blower Because it is easily 400 ° C due to the introduction of the outside air due to the ejector effect, high-moisture raw materials such as chicken manure introduced into the container are rapidly pre-dried and the dried raw material is discharged from the bottom of the sliding bottom. Even if the chicken manure with a lot of hair loss that easily scatters is replaced from time to time, the raw material can easily flow down along the top surface. If it is exhausted at 100 ° C. or higher, there is no condensation, and if it is an egg-laying hen, the remaining amount dried after the combustion amount can be supplied to other places. In the case of broilers, the exhaust after connecting a heat exchange cylinder to the holding cylinder and using hot water for floor heating is around 200 ° C., so the outside air can be introduced and discharged safely by the ejector effect of the suction blower. The effect that the exhaust can be used for pre-drying can be the same as described above.

オールイン・オールアウトで飼育するブロイラー糞には石やボルト等の異物が混入し易く、投入装置のスクリュウ軸などを通過する異物も相応に巨大なので排出装置は作動不能と成るが、その時、所定の加重を加えた回転式の可動蓋を設置することで、所定限の異物が混合排出する時のみに回転開口して安全に排出し、常時は加重を受けた可動蓋で密閉状態として外気の異常進入を阻止する。   The broiler feces bred in all-in and all-out are likely to be contaminated with foreign matter such as stones and bolts, and the foreign matter that passes through the screw shaft of the feeding device is correspondingly large, making the discharge device inoperable. By installing a rotating movable lid with a weight of, the rotating opening is opened and discharged safely only when a predetermined amount of foreign matter is mixed and discharged. Prevent abnormal entry.

本発明は、以上説明したように構成されているので、以下に記載されるような効果を奏する。   Since the present invention is configured as described above, the following effects can be obtained.

鶏糞は燃焼炉内で圧縮されると固決して塊状に成るので、流動性を失うと共に通気が不均一になると云う難解な課題があったのを解消し、炉内堆積層を常時ポーラスに維持して斉一に燃焼処理すると共に、燃焼熱量を熱分解と水分蒸発用へ効果的に熱伝導するよう1次炉内を整備して通気量を極小に止め、かつ、広幅に維持して堆積層に広い表面積を確保することで発生ガスの通過速度を僅少にすると云う本発明の特性から、鶏糞など原料中へ混入する抜け毛と乾燥や熱分解で軽量化した糞微粒子の粉塵浮上量も微小であり、燃焼筒内で均一高温にガス燃焼した後の煤塵量は更に僅少となるので、高価な集塵装置など無しでも煙突からの煤塵飛散量は充分に許容値内へ収まって公害を防ぎ、国際競争の激化に悩む養鶏業へ貢献する。   Since chicken manure is compressed and solidified in a combustion furnace, it eliminates the difficult problem of loss of fluidity and non-uniform ventilation, and keeps the furnace deposition layer porous at all times. In order to conduct the combustion process at the same time, the inside of the primary furnace is maintained to effectively transfer the heat of combustion to thermal decomposition and water evaporation, and the ventilation volume is kept to a minimum, and it is kept wide to form a deposition layer. Due to the characteristics of the present invention that the passage speed of the generated gas is reduced by securing a large surface area, the hair loss mixed into the raw materials such as chicken manure and the dust floating amount of the feces particulates reduced in weight by drying and pyrolysis are also minute. The amount of soot after gas combustion at a uniform high temperature in the combustion cylinder becomes even smaller, so even without an expensive dust collector, the amount of soot scattered from the chimney is well within the permissible value to prevent pollution. Contribute to the poultry industry that is struggling with intensifying competition.

ブロイラー糞には石やボルトのような異物が混入する事が多く、投入装置を通過できない異物は事前に排除できるが、かなり大きくても通過した異物は燃焼せずに残滓へ混入して排出装置の障害物となっていたのを、本発明によって臨機応変に対応して昼夜に渡り支障なく連続作動する。   Foreign materials such as stones and bolts are often mixed in broiler droppings, and foreign materials that cannot pass through the charging device can be eliminated in advance. According to the present invention, the present invention can be continuously operated day and night without trouble.

毎時200kg以上では集塵装置や中和装置などを設置義務とする構造基準が適用されて設備費が高額になるが、燃焼炉への投入以前に乾燥処理すれば原料重量は軽減できて燃焼炉の実質処理量を増加できるし、排ガス中の水蒸気が減少して燃焼自体にも有利であり、特に、暖房を必要としない採卵鶏業はブロイラー業より大規模で糞量が多くて焼却処理に困窮しているので、事前乾燥による許容燃焼量増加の効果は大きく、乾燥処理した鶏糞を植物用温室などの冷暖房用熱源に供給して資源活用できるが、その時、本発明では乾燥中にも鶏糞中の抜け毛などが飛散し無いように出来るので、目的へ容易に応え得る。   At 200 kg / h or more, structural standards that require installation of dust collectors and neutralizers are applied, resulting in high equipment costs. However, if the material is dried before being introduced into the combustion furnace, the weight of the raw material can be reduced and the combustion furnace The amount of steam in the exhaust gas is reduced, which is advantageous for combustion itself. Especially, the egg-laying henry industry that does not require heating is larger than the broiler industry and has a large amount of feces and is therefore incinerated. Because of the difficulty, the effect of increasing the allowable combustion amount by pre-drying is great, and the dried chicken dung can be supplied to a heat source for air conditioning such as a greenhouse for plants. The hair loss inside can be prevented from scattering, so that the purpose can be easily met.

最も切迫した対象原料は鶏糞だが、本発明は稲藁や樹皮や間伐材や住宅廃材などの生物系廃棄物の全般に適応できるので、活用されずに放置される莫大な資源を有効活用して石油へ代替し、地球環境を保全し得る。   The most urgent target raw material is chicken manure, but the present invention can be applied to all biological waste such as rice straw, bark, thinned wood, and house waste, so it can effectively utilize huge resources that are left unused. It can substitute for oil and preserve the global environment.

実施例について図面を参照して説明すると、装置の要部を示す図1において、ホッパー1内へ鶏糞など原料を投入して多列スクリュウの例で示す投入装置2を駆動すると、原料は1次炉3内へ広幅で薄高状に緩傾斜の床面4を滑動した後に角度増加の底面5を自重滑落し、底面5と近似角度を成す外壁の天面6との間にポーラスな堆積層7を形成し、底面5の端末は水平な床盤8へ接続してモーターなどで間欠逆転に移動する排出装置9を構成し、装置9の排出側は加重付きの可動蓋10として異物を臨機に排出し、床面5および相対の天面6には極細径の通気管11を多数個配列して空気ポンプ12へ集合連結し通気すると、点線矢印の如くC:燃焼層で酸素分を燃尽し、発生熱量の通過でB:熱分解層を形成し、高温の発生ガスと1次炉3の外壁からの熱伝導でA:乾燥層を形成し、層7の下端側には燃焼を均一化するD:おき燃焼層を通気無しで形成し、一方、装置2への逆流で過重投入を避けることで層7上へは広幅で充分面積の上部空間13を形成し、透過ガス流速は極めて微少なので粉塵は浮上し難く、装置2より上方の天面6は緩傾斜で底面4位置に上向きの収束空間14を設けて排気管15へ連結し、管15の外径を円錐筒16内へ繋ぎ筒外壁17で密封に覆って追加ブロワ18へ繋ぎ、筒16末端を燃焼筒19内へ連結することで、筒16内と筒19内で順次に均一な高温度(約1,100℃)へ達するようガス燃焼する。   The embodiment will be described with reference to the drawings. In FIG. 1 showing the main part of the apparatus, when the raw material such as chicken manure is introduced into the hopper 1 and the charging device 2 shown in the example of the multi-row screw is driven, the raw material is primary. After sliding a gently sloping floor surface 4 wide and thin into the furnace 3, the bottom surface 5 with increased angle is slid down by itself, and a porous deposition layer is formed between the bottom surface 5 and the top surface 6 of the outer wall forming an approximate angle. 7, the terminal of the bottom surface 5 is connected to a horizontal floor 8 and constitutes a discharge device 9 that moves intermittently reversely by a motor or the like. When a large number of ultrafine-diameter ventilation pipes 11 are arranged on the floor surface 5 and the relative top surface 6 and connected to the air pump 12 and ventilated, C: burns oxygen in the combustion layer as indicated by the dotted arrow. B: P: Pyrolysis layer is formed by passage of generated heat, and high temperature generated gas and primary furnace A: A dry layer is formed by heat conduction from the outer wall of the A, and the combustion is made uniform at the lower end side of the layer 7 D: A vertical combustion layer is formed without ventilation, while an overload is applied to the apparatus 2 by backflow. By avoiding this, a wide and sufficiently large upper space 13 is formed on the layer 7, and the permeate gas flow rate is extremely small so that the dust does not rise easily. The top surface 6 above the device 2 is inclined gently upward toward the bottom surface 4 position. The converging space 14 is provided and connected to the exhaust pipe 15, the outer diameter of the pipe 15 is connected to the conical cylinder 16, covered with a cylinder outer wall 17 and sealed to an additional blower 18, and the end of the cylinder 16 is connected to the combustion cylinder 19. As a result, gas combustion is performed in the cylinder 16 and the cylinder 19 so as to reach a uniform high temperature (about 1,100 ° C.) sequentially.

次いで装置の全体を平面図で示す図2によって見ると、投入装置2は多列スクリュウ式であって接続する1次炉3内の底面4も同じ広幅であり、床面5では緩角度に幅寸法を詰めて排出装置9へ連結し、1次炉3の天面5はアーチ形の中央部を成すことを示し、側面展開図の図3を併せて説明するに、14・17・19は先に説明したと同一であるし、排出装置9は排滓誘導枠20へ向けて作動し、燃焼筒19から直立状の高温保持筒21を上向きに回転流して800℃位へ放熱し、熱交換筒22へ連結して下向流し、排気管23から吸引ブロワ24の吐出管25を内装する煙突25へ連結することを示し、図3では更に詳細に、筒22内への円形多管式の熱交換パイプ27の設置により250℃位に冷却し、煙突26内へ吐出管25を内装するエゼクタ構成の外気導入で充分に200℃以下にして排気する例を示す。   Next, when the entire apparatus is viewed in FIG. 2 which is a plan view, the charging apparatus 2 is a multi-row screw type, and the bottom surface 4 in the primary furnace 3 to be connected is also wide, and the floor surface 5 has a gentle angle. It is connected to the discharge device 9 with a reduced size, and the top surface 5 of the primary furnace 3 is shown to form an arch-shaped central part, and FIG. It is the same as described above, and the discharge device 9 operates toward the exhaust guide frame 20, and radiates heat from the combustion cylinder 19 upwardly through the upright high temperature holding cylinder 21 to about 800 ° C. FIG. 3 shows that the exhaust pipe 23 is connected to the chimney 25 that houses the discharge pipe 25 of the suction blower 24, and FIG. 3 shows the circular multi-tube type into the cylinder 22 in more detail. The heat exchange pipe 27 is cooled to about 250 ° C. and the discharge pipe 25 is installed in the chimney 26. Ejector sufficiently to 200 ° C. or less in the outside air introduction structure showing an example of exhaust that.

他の実施例を平面図の図4と側面展開図の図5で示すが、前記した例と多くが共通であって高温保持筒21までは同一だが、熱交換筒22を備えずに筒21から吸引ブロワ24の吐出管25によるエゼクタ効果で外気導入して排気管23内は適正温度(約400℃)へ調整し、密閉容器28内の滑落限界(40度位)の傾斜底面29が構成する下方空間30へ排気管23は吐出し、該底面29は通気可能に構成してあって傾斜下端の該底面上には排出蓋31を設置し、反対側上部に供給蓋32を設けて該容器28内の原料充填層を排気通過で急速乾燥し、該供給蓋32を起点として傾斜する多孔天面33は零細網で被覆してあるので原料中の抜け羽も通過できずに飛散を防ぎ、天面33の上側空間34から100℃以上で結露せずに煙突25を経て排出する。   Another embodiment is shown in FIG. 4 in a plan view and FIG. 5 in a side development view. Many of the examples are common and up to the high temperature holding cylinder 21 is the same, but without the heat exchange cylinder 22, the cylinder 21 is provided. The outside air is introduced by the ejector effect of the discharge pipe 25 of the suction blower 24, the inside of the exhaust pipe 23 is adjusted to an appropriate temperature (about 400 ° C.), and the inclined bottom surface 29 of the sliding limit (about 40 degrees) in the sealed container 28 is configured. The exhaust pipe 23 discharges into the lower space 30, and the bottom surface 29 is configured to allow ventilation. A discharge lid 31 is provided on the bottom surface at the lower end of the slope, and a supply lid 32 is provided on the upper side on the opposite side. The raw material packed layer in the container 28 is rapidly dried by exhaust passage, and the porous top surface 33 inclined with the supply lid 32 as a starting point is covered with a fine mesh, so that the wings in the raw material cannot pass and prevent scattering. The chimney 25 from the upper space 34 of the top surface 33 without condensation at 100 ° C. or higher Through to be discharged.

燃焼炉の要部に対する縦断面図である。It is a longitudinal cross-sectional view with respect to the principal part of a combustion furnace. 燃焼炉全体の平面図である。It is a top view of the whole combustion furnace. 燃焼炉全体の側面展開図である。It is a side development view of the whole combustion furnace. 他の実施例における平面図である。It is a top view in another Example. 他の実施例における一部断面の側面展開図である。It is a side expanded view of the partial cross section in another Example.

符号の説明Explanation of symbols

1 ホッパー
2 投入装置
3 1次炉
4 底面
5 床面
6 天面
7 堆積層
8 モーター軸
9 排出装置
10 可動蓋
11 通気管
12 空気ポンプ
13 上部空間
14 収束空間
15 排気管
16 円錐筒
17 筒外壁
18 追加ブロワ
19 燃焼筒
20 廃滓誘導枠
21 高温保持筒
22 熱交換筒
23 排気管
24 吸引ブロワ
25 吐出管
26 煙突
27 熱交換バイプ
28 密閉容器
29 傾斜底面
30 下方空間
31 排出蓋
32 供給蓋
33 多孔天面
34 上方空間
DESCRIPTION OF SYMBOLS 1 Hopper 2 Loading device 3 Primary furnace 4 Bottom surface 5 Floor surface 6 Top surface 7 Deposition layer 8 Motor shaft 9 Discharge device 10 Movable lid 11 Vent pipe 12 Air pump 13 Upper space 14 Converging space 15 Exhaust pipe 16 Conical cylinder 17 Cylinder outer wall 18 Additional blower 19 Combustion cylinder
20 Waste guide frame 21 High temperature holding cylinder 22 Heat exchange cylinder 23 Exhaust pipe 24 Suction blower 25 Discharge pipe 26 Chimney 27 Heat exchange vial 28 Sealed container 29 Inclined bottom surface 30 Lower space 31 Discharge lid 32 Supply lid 33 Porous top surface 34 Upper space

Claims (3)

1次炉(3)内に設けた広幅で緩傾斜(15度位)の床面(4)上へ原料供給装置(2)を薄厚状で同一幅に開口連結し、該床面(4)を滑落限界角(40度位)の底面(5)へ連結して該底面(5)の末端は残滓排出装置(9)へ接続し、該底面(5)と接合する1次炉(3)の他の外壁が形成するアーチ形の天面(6)は該底面(5)と近接角度を保持し、かつ、該天面(6)は供給装置(2)高で緩傾斜へ変異して1次炉(3)内へ堆積層(7)と上部空間(13)を形成し、該底面(5)および相対の天面(6)へは極細径の通気管(11)を多数個設置して空気ポンプ(12)へ集合連結することで該堆積層(7)を熱分解ガス化し、該床面(4)位置で該上部空間(13)を上向き収束空間(14)を経て排気管(15)へ連結し、該排気管(15)を円錐筒(16)へ連結してブロワ(18)により薄膜状に分割通気してガス燃焼し、高温排気を吸引ブロワ(24)によって適正温度へ調整する鶏糞など生物系廃棄物の連続燃焼式小型炉装置。 The raw material supply device (2) is connected to the floor (4) having a thin thickness and the same width on the floor surface (4) having a wide and gentle inclination (about 15 degrees) provided in the primary furnace (3). Is connected to the bottom surface (5) of the sliding limit angle (about 40 degrees), the end of the bottom surface (5) is connected to the residue discharging device (9), and the primary furnace (3) joined to the bottom surface (5) The arched top surface (6) formed by the other outer wall maintains a close angle with the bottom surface (5), and the top surface (6) is deformed to a gentle slope at the height of the feeding device (2). A deposition layer (7) and an upper space (13) are formed in the primary furnace (3), and a large number of ultrafine vent pipes (11) are installed on the bottom surface (5) and the relative top surface (6). Then, the accumulated layer (7) is pyrolyzed and gasified by collectively connecting to the air pump (12), and the upper space (13) is directed upward through the converging space (14) at the position of the floor surface (4), and the exhaust pipe Link to (15) The exhaust pipe (15) is connected to the conical cylinder (16), divided into a thin film by the blower (18) and gas-fired, and the high temperature exhaust is adjusted to an appropriate temperature by the suction blower (24). A continuous combustion type small furnace for waste. 密閉容器(28)内に通気可能な傾斜底面(29)を滑落限界角(40度位)に設置して下方空間(30)を構成し、該吸引ブロワ(24)の吐出管(25)を内装した排気管(23)は該空間(30)へ連結し、該容器(28)上部へは供給蓋(32)を設置し、該底面(29)の下端末が当たる該容器(30)側面へは排出蓋(31)を設置し、該容器(30)上部へは零細網で被覆した多孔天面(33)を該底面(29)と平行に設置し、該天面(29)の上方空間(34)を煙突(26)へ連結した請求項1記載の鶏糞など生物系廃棄物の連続燃焼式小型炉装置。 An inclined bottom surface (29) that can be ventilated in the sealed container (28) is installed at a sliding limit angle (about 40 degrees) to form a lower space (30), and a discharge pipe (25) of the suction blower (24) is connected to the discharge container (25). The internal exhaust pipe (23) is connected to the space (30), the supply lid (32) is installed on the top of the container (28), and the side surface of the container (30) to which the lower end of the bottom surface (29) hits. A discharge lid (31) is installed at the top, and a porous top surface (33) covered with a fine mesh is installed at the top of the container (30) in parallel with the bottom surface (29), above the top surface (29). The continuous combustion type small furnace apparatus for biological waste such as chicken manure according to claim 1, wherein the space (34) is connected to the chimney (26). 該残滓排出装置(9)は所定厚の底盤(8)を水平に間欠移動に構成して該底(8)の始端側上面へ該底面(5)の末端を接続し、該底盤(8)の末端側上面へ接続する1次炉(3)外壁の必要寸法を垂直な可動蓋(10)に構成し、該可動蓋(10)に加重機を設置した請求項1記載の鶏糞など生物系廃棄物の連続燃焼式小型炉装置。
The residue discharging device (9) is configured such that a bottom plate (8) having a predetermined thickness is horizontally and intermittently moved, and an end of the bottom surface (5) is connected to an upper surface on the start end side of the bottom (8), and the bottom plate (8) 2. The biological system such as chicken manure according to claim 1, wherein the required dimension of the outer wall of the primary furnace (3) connected to the upper surface on the terminal side is configured in a vertical movable lid (10), and a loader is installed on the movable lid (10). Waste continuous combustion small furnace equipment.
JP2003374114A 2003-11-04 2003-11-04 Continuous combustion type small furnace device for biological waste such as poultry manure Pending JP2005140346A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8307770B2 (en) 2006-03-10 2012-11-13 Pyropure Limited Waste treatment apparatus and method
CN109504410A (en) * 2018-11-22 2019-03-22 上海九泽环保科技有限公司 Pyrolysis gasification system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8307770B2 (en) 2006-03-10 2012-11-13 Pyropure Limited Waste treatment apparatus and method
US9851100B2 (en) 2006-03-10 2017-12-26 Pyropure Limited Waste treatment apparatus and method
CN109504410A (en) * 2018-11-22 2019-03-22 上海九泽环保科技有限公司 Pyrolysis gasification system

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