JPS60152812A - Biomass incinerator - Google Patents

Biomass incinerator

Info

Publication number
JPS60152812A
JPS60152812A JP833984A JP833984A JPS60152812A JP S60152812 A JPS60152812 A JP S60152812A JP 833984 A JP833984 A JP 833984A JP 833984 A JP833984 A JP 833984A JP S60152812 A JPS60152812 A JP S60152812A
Authority
JP
Japan
Prior art keywords
air
cylinder
combustion
fuel
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP833984A
Other languages
Japanese (ja)
Other versions
JPH0557483B2 (en
Inventor
Hiroshi Shimizu
浩 清水
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP833984A priority Critical patent/JPS60152812A/en
Publication of JPS60152812A publication Critical patent/JPS60152812A/en
Publication of JPH0557483B2 publication Critical patent/JPH0557483B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/10Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of field or garden waste or biomasses

Abstract

PURPOSE:To perform a complete combustion with a minimum air ratio by a method wherein gas is ignited with sufficiently more volume of secondary air than a volume of primary air within the secondary combustion cylinder and the combustible gas is enclosed by required amount of air the outer circumference thereof, resulting in the formation of the flame in the shape of that of a candle flame. CONSTITUTION:When a lid 21 and a valve 22 are closed, fuel is dropped at one side within a cylinder 1 partitioned by a plate 11 as indicated by an arrow if a shutter 20 is opened, drives an ash discharging unit 15 to cause the fuel to be accumulated on the part 15 at the opening 10 substantially in a horizontal direction. When a blower 5 is operated after an ignition, the primary air passes through a space between the cylinders 1 and 3, exists from the hole 9 to burn the accumulated fuel, the gas ascends at one side as shown by an arrow and reaches from the part 10 to the part 2. The secondary air passes through the space between the cylinders 1 and 2, and passes through a narrow passage at the outer circumference of the opening 10 from the air passage 13, injects into the cylinder 2. The fuel guides the gas in the cylinder 1 from the opening 10 under the effect of ejection and the secondary combustion is performed like a flame of candle in such a way it encloses the gas from its periphery in the cylinder 2.

Description

【発明の詳細な説明】 本発明は、住宅廃材や工場残材や間伐材等を原材とする
木材チップ、粗大物を選別除去してほぼ斉一粒子群とし
た樹皮、あるいはもみ殻等、流動性やや雑であり、かさ
密度率であり、揮発ガス分が多く9発熱量低であり、か
つ含水率やや大なる場合の多いバイオマスを直接に燃料
として、自動1′的に、高熱効率に、完全燃焼させるた
めのバイオマス燃焼炉に拘るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention utilizes wood chips made from residential waste, factory leftovers, thinned wood, etc., bark, rice husks, etc. that are made into almost uniform particle groups by sorting and removing coarse materials, Directly using biomass, which has low properties, low bulk density, high volatile gas content, low calorific value, and slightly high moisture content, as an automatic 1', high thermal efficiency, It concerns a biomass combustion furnace for complete combustion.

まず第1図に示す本発明の1実施例について説明する。First, one embodiment of the present invention shown in FIG. 1 will be described.

(1)は1次燃焼筒、(2)は2次燃焼筒、(3)は外
筒、(4)は(21(31間の空間を上下に気密に分割
する仕切板、(5)はブロワ、(6,6’)は給気管、
(7)は(5)の入気口面積の調節蓋、(8,8’)は
おのおの(6,6’)に設けたオリイフィス、(9)は
(4)より下位の(1)に設けた多数の通気穴、αOは
(1)の上部に設けた開口、 (II)は(1)を横断
する仕切板、 Ql’)は同じく補助仕切板、(12は
(2)を包む外筒、(13は(10を包み(2)に連る
2次空気路、04は(2)内の加熱体、 QEIはロス
ドル等の灰出器、00はu9の駆動器、 a′71は気
密の灰出蓋、(1日は燃料のホッパであり、(1)の上
部を(11、11’)で仕切った1室に(10が、他室
に圓が連結しである。(19は(18上方の貯留ビン、
eOは(19のシャッタ、 (211は(1日の蓋、e
2は電磁弁、 23は温度センサ。
(1) is the primary combustion tube, (2) is the secondary combustion tube, (3) is the outer tube, (4) is the partition plate that airtightly divides the space between the (21 (31) vertically, and (5) is the Blower, (6, 6') is air supply pipe,
(7) is an adjustment lid for the inlet area of (5), (8, 8') is an orifice installed at each (6, 6'), and (9) is an orifice installed at (1) below (4). αO is an opening provided at the top of (1), (II) is a partition plate that crosses (1), Ql') is also an auxiliary partition plate, and (12 is an outer cylinder that encloses (2)). , (13 is the secondary air passage that wraps (10) and continues to (2), 04 is the heating element in (2), QEI is the ash extractor such as Rosdol, 00 is the driver of u9, a'71 is the airtight The ash discharge lid (1st) is a fuel hopper, and the upper part of (1) is divided by (11, 11') into one chamber (10), and the other chamber is connected by a circle. (19 is (18 upper storage bin,
eO is (19 shutters, (211 is (1 day lid, e
2 is a solenoid valve, 23 is a temperature sensor.

(271は0日のカバーである。(271 is the cover for day 0.

1 次に作用について説明する。燃料はビンa9へ貯留
され、蓋e11は弁(22により開状態にあり、シャッ
タeQを開くと2重線矢印のように自然落下して筒+t
i内の板(II)により仕切られた1室側へ充満し、灰
出器αυを駆動器0θで回動すると板01)の下端から
ほぼ水平にDB上へ堆積するので、その堆積面上へ石油
を散布する等して点火する。ついで、ブロワ(5)を作
動すると、管(6)へオリフィス(8)を経て分流した
1次空気は2点線矢印のように筒(11(3)間の空間
を経て(りから(1)内へ入って堆積燃料を燃焼し、燃
焼ガスは実線矢印のように板ttnによル(1)の片側
室を上昇して(10から(2)へ至る。一方、(5)か
ら(8つを経て(6ツへ分流した2次空気は9点線矢印
のように筒+11(3+間を経て大部分は(10外周の
狭路(13から(2)へ噴流し、aOからの1次燃焼ガ
スと混合して(2)内で2次燃焼し、2次空気の残部は
f2+(12間を通って先端部小穴から(2)内へ入る
。(14は2次空気による着火を助け、かつ、混合を促
進して2次燃焼を良好にする。燃焼が欠乏した時、及び
、停電等でQ3からのエゼクタ効果が無い時−等では、
センサ33部の昇温を感知して弁e2が切れ、スプリン
グ力等で圓が、ホッパ(18を閉塞し、煙焔の上昇を防
止する。
1 Next, the effect will be explained. The fuel is stored in the bin a9, the lid e11 is in the open state by the valve (22), and when the shutter eQ is opened, it naturally falls as shown by the double line arrow to the cylinder +t.
The first chamber partitioned by plate (II) in i is filled with water, and when the ash extractor αυ is rotated by the driver 0θ, the ash is deposited almost horizontally on DB from the lower end of plate 01), so that the ash is deposited on the DB surface. ignite it by spraying oil on it. Next, when the blower (5) is operated, the primary air that is divided into the pipe (6) via the orifice (8) passes through the space between the pipes (11 (3)) as shown by the two-dot arrow. The combustion gas enters the interior and burns the deposited fuel, and the combustion gas ascends through the chamber on one side of the door (1) through the plate ttn as shown by the solid line arrow (from (10) to (2). On the other hand, from (5) to (8) The secondary air that has been divided into (6) passes through the cylinder +11 (3+) as shown by the 9 dotted line arrow, and most of it flows from (10 to the narrow passage (13) on the outer circumference (2), and the primary air from aO It mixes with the combustion gas and undergoes secondary combustion in (2), and the remainder of the secondary air passes through f2+ (12) and enters (2) through the small hole at the tip. (14 helps the secondary air ignite. , and promotes mixing to improve secondary combustion.When combustion is insufficient or when there is no ejector effect from Q3 due to power outage, etc.
The valve e2 is opened upon sensing the temperature rise of the sensor 33, and the valve closes the hopper (18) due to spring force, thereby preventing the smoke from rising.

次に効果について説明する。対象とするバイオマス燃料
はかさ密度率であり1発熱量低である。
Next, the effects will be explained. The target biomass fuel has a bulk density ratio and low calorific value.

含水率やや大なる場合には、容積当り発熱量はさらに低
くなる。よって、1次燃焼に必要な温度を均一に維持さ
せるには集約した必要堆積容積を常に保ち、その容積に
1次空気を可及的均一に作用させる事が有効である。本
発明では、筒(1)の上部を板Iで2室に区分すること
により、灰出器卸の単一な間けつ駆動にて燃焼面をなす
堆積表面を燃料が被覆消火することなく燃焼量に応じて
ホウ80日から自然落下して補充して、上記要件を具備
できる。また、対象燃料は揮発成分が多いので、1次燃
焼にはガス化に必要限の空気を均一に送り。
When the water content is slightly higher, the calorific value per volume becomes even lower. Therefore, in order to uniformly maintain the temperature required for primary combustion, it is effective to always maintain a concentrated required deposition volume and to allow primary air to act on that volume as uniformly as possible. In the present invention, the upper part of the cylinder (1) is divided into two chambers by the plate I, so that fuel burns without covering the fuel accumulation surface that forms the combustion surface and extinguishing it by a single intermittent drive of the ash extractor. The above requirements can be met by naturally falling and replenishing from 80 days depending on the amount. In addition, since the target fuel has many volatile components, the amount of air necessary for gasification is uniformly sent during the primary combustion.

生成ガス分を誘引しての2次燃焼を理想的なガス燃焼と
することで完全燃焼化が可能である。本発明における第
1図の1実施例ではf13からの2次空気によるエゼク
タ効果で、(2)と(6,6’)間に圧力差を生ぜしめ
て1次燃、焼ガスを確実に(1oへと誘引して、ホッパ
a日側へと煙を出さないのみが、仕切板(11,11’
)を経ての熱伝導による燃料の予備乾燥での蒸気を(1
1’)間や(111上端の開口を経てαo疋と誘引し、
60%dl)位までの燃料を支障なく燃焼できる。(9
)からの1次空気は全給気量の173位とすると、筒(
1)内は650℃位に押えられて耐熱容易であり、かつ
、燃焼主体が(2)内でのガス燃焼となって空気比1.
2位で完全燃焼し、熱交換後の排熱損失を減じて高熱効
率にできる。その際、筒(2)より小角で小穴を持つ筒
状の04は、ガスと空気の混合を助ける。また、 Q3
を(1Gの外周に構成したことにより、ローソクの焔の
ように2次空気が燃焼ガスの外周を流れつつ順次に反応
して良く燃焼し、がっ、筒(2)を過熱し難い。さらに
、筒(1)(31間のttJi141下空間は(6)か
らの1次空気が、板(4)上空間は(6ツがらの2次空
気が、おのおの回流して(1)を空冷し。
Complete combustion is possible by inducing the generated gas and making the secondary combustion an ideal gas combustion. In one embodiment of the present invention shown in FIG. 1, the ejector effect of the secondary air from f13 creates a pressure difference between (2) and (6, 6') to ensure the primary combustion and combustion gas (1o The only way to prevent smoke from emitting to the hopper side is to use the partition plate (11, 11'
) The steam from the pre-drying of the fuel by heat conduction through (1
1') Through the opening at the top of the gap (111), it is attracted to αohi,
It can burn up to 60% dl) of fuel without any problem. (9
), the primary air from the cylinder (
The temperature inside 1) is kept at around 650°C, making it easily heat resistant, and the main combustion is gas combustion inside (2), resulting in an air ratio of 1.
Complete combustion occurs in the second position, reducing waste heat loss after heat exchange and achieving high thermal efficiency. At this time, the cylindrical 04, which is smaller in angle than the cylinder (2) and has small holes, helps mix the gas and air. Also, Q3
By configuring (1G) on the outer periphery, the secondary air flows around the outer periphery of the combustion gas like a candle flame, reacts sequentially and burns well, and it is difficult to overheat the cylinder (2). , the space below the ttJi141 between the tubes (1) and (31) is filled with the primary air from (6), and the space above the plate (4) is filled with secondary air from the (six), which is circulated and cooled (1). .

かつ、おのおの予熱された後に給気して燃焼を良好にで
きる。筒+21Qa間も空冷できる。か(て2本発明に
より燃焼困難とされていたバイオマス燃料を支障なく自
動的に高熱効率に完全燃焼させつる。
In addition, air can be supplied after each unit has been preheated to improve combustion. Air cooling is also possible between the cylinder and 21Qa. (2) The present invention allows biomass fuel, which has been considered difficult to burn, to be completely combusted automatically and with high thermal efficiency without any problems.

煙突からタールが流れる如き在来の燃焼炉とは雲泥の差
がある。
There is a huge difference from traditional combustion furnaces, where tar flows from the chimney.

次に本発明の第2実施例を第2図によって説明スル。(
11〜(61,(91〜+lE!、 (171,(18
は第1図で説明したると同一である。eF3は通勤杆、
(26は桿杆、(27は電磁弁、(28,28’)はお
のおの(6,6’)内に設けた風量調節弁、(29,2
9’)は弁(28,28’)を回動する腕杆、θOはそ
の調節ダイヤルである。
Next, a second embodiment of the present invention will be explained with reference to FIG. (
11~(61, (91~+lE!, (171, (18
is the same as explained in FIG. eF3 is a commuter stick,
(26 is a rod, (27 is a solenoid valve, (28, 28') is an air volume control valve installed in each (6, 6'), (29, 2
9') is an arm rod that rotates the valve (28, 28'), and θO is its adjustment dial.

次に第2実施例の作用を説明する。弁e′Aの駆動力で
杆eυは」1下に通勤し、かつ、(20を経て08を矢
印のように摺動させて灰出しする。また、ダイヤルθO
の単一操作で弁(28,28’)が連動して作動する。
Next, the operation of the second embodiment will be explained. With the driving force of the valve e'A, the rod eυ moves down by 1, and slides 08 through 20 as shown by the arrow to remove the ash.
The valves (28, 28') are operated in conjunction with a single operation.

次に第2実施例の効果を説明する。第1図の実施例では
灰出器0Bの回動で燃料を移動したが9本実施例では突
起を持つ杆2Bの上下退動で重力移動を助成し、一層流
動難なる燃料へも支障な(対応可能とできる。また、第
1図の実施例ではブロワ(5)の人気口の蓋(7)の作
動と、オリイフィス(8゜8′)とにより(6,6’)
の空気量を比例的に調節したが2本実施例では寸法差あ
る杆(28,28’)により弁(28,28’)を異な
る開度に調節し、(6)の1次空気量を極度に減じた時
も(I3からのエゼクタ効果を充分に維持可能とした。
Next, the effects of the second embodiment will be explained. In the embodiment shown in Fig. 1, the fuel is moved by the rotation of the ash extractor 0B, but in this embodiment, the vertical movement of the rod 2B with a protrusion assists gravity movement, so that it does not interfere with the fuel, which is even more difficult to flow. In addition, in the embodiment shown in FIG.
In this embodiment, the valves (28, 28') are adjusted to different opening degrees using rods (28, 28') with different dimensions, and the primary air volume in (6) is adjusted proportionally. Even when it is extremely reduced (the ejector effect from I3 can be maintained sufficiently).

その時は、2次空気過剰で熱効率を減するが、燃焼量調
節範囲を拡大できる効果がある。弁(28,28’)の
連動に限らず。
In that case, the thermal efficiency is reduced due to excess secondary air, but it has the effect of expanding the combustion amount control range. Not limited to interlocking of valves (28, 28').

蓋(7)と弁(28,28’)の計3個中の1個または
連動するいずれか2個の作動で、第1図の1実施例か本
実施例の如く空気量を調節して燃焼量を容易に調節可能
である。また、加熱器(14に螺旋の整流板を附設して
いて、2次燃焼焔を旋回流にし、混合を促進して一層完
全に燃焼できる。
The amount of air can be adjusted by operating one or any two of the three lids (7) and valves (28, 28') in conjunction with each other, as in the first embodiment shown in Fig. 1 or this embodiment. The amount of combustion can be easily adjusted. In addition, a spiral rectifying plate is attached to the heater (14), which turns the secondary combustion flame into a swirling flow to promote mixing and achieve more complete combustion.

次に本発明の第3実施例を第3図によって説明スル。(
11〜(61,+81〜f13. QB、 QB、 (
18〜QO,Quハ第1図で説明したると同一である。
Next, a third embodiment of the present invention will be explained with reference to FIG. (
11~(61,+81~f13. QB, QB, (
18 to QO and Qu are the same as explained in FIG.

011は筒(11内で(9)1間に設けた温度センサ、
θaは熱交換器、(33は冷水管、θ4は熱水管、0日
はea内に装置したサイクロン、θ0は排気口である。
011 is a temperature sensor installed between (9) and 1 in the cylinder (11),
θa is a heat exchanger, (33 is a cold water pipe, θ4 is a hot water pipe, day 0 is a cyclone installed in ea, and θ0 is an exhaust port.

次に第3実施例の作用について説明する。この事例はも
み殻のような灰分の多い燃料の場合で。
Next, the operation of the third embodiment will be explained. This example is for a fuel with a high ash content, such as rice husk.

かつ、熱水用熱交換器を直装した場合を示す。α9は屋
根裏等を利用した燃料貯留庫からのシュートとして示し
、停止時・停電時および異常時でセンサ(23部の過熱
時には弁e2が切れてシャッタeOがα9を閉塞し、0
9内への類焼を防ぐ。灰出器α日はスクリュで例示して
あり、センサ011部の灰が焼借し設定温度以下となっ
た時、(IOが駆動して灰出し、燃焼不充分の高温度の
灰が移動して来ると00は停止し、燃料の重力移動を自
動制御する。点火時はタイマーにて設定時間後から上記
の作動を開始する。
This also shows the case where a hot water heat exchanger is directly installed. α9 is shown as a chute from the fuel storage in the attic, etc., and when the sensor (23 part) overheats, valve e2 opens and shutter eO closes α9,
9. Prevent fire from spreading inside. The ash ejector α day is illustrated with a screw, and when the ash in the sensor 011 section falls below the burnt set temperature, the IO is activated to take out the ash, and the ash at a high temperature due to insufficient combustion is moved. 00 stops and automatically controls the gravity movement of the fuel.When igniting, the above operation starts after a set time with a timer.

−次通気穴(9)部は過熱し易いので、交換可能の耐熱
筒を設けである。また、2次燃焼筒(2)は極短であっ
て、サイクロン0!3を0003へほぼ直接に合せて結
び、冷却後の排気をブロワ(5)で吸引して(2+ (
’6゜6′)間に圧力差を設けた実施例である。
- Since the secondary ventilation hole (9) is prone to overheating, a replaceable heat-resistant cylinder is provided. In addition, the secondary combustion cylinder (2) is extremely short, and the cyclone 0!3 is connected almost directly to 0003, and the cooled exhaust gas is sucked by the blower (5) (2
This is an embodiment in which a pressure difference is provided between 6° and 6'.

次に′第3実施例の効果を説明する。通常の木材、は灰
分0.3%位であるから手動にて残留灰を採出するにて
足りるが、もみ殻は灰分17〜2296なので。
Next, the effects of the third embodiment will be explained. Normal wood has an ash content of about 0.3%, so it is sufficient to manually extract the residual ash, but rice husks have an ash content of 17 to 2,296.

・第3実施例の如くして本発明を実施し得る。また。- The present invention can be implemented as in the third embodiment. Also.

バイオマスとくに木屑等を燃料とする時は火の子の飛散
の危険を伴うが1本実施例のように熱交換器中にサイク
ロンを装置するとこれを防ぎ、かつ。
When biomass, especially wood chips, etc., is used as fuel, there is a risk of flying sparks, but this can be prevented by installing a cyclone in the heat exchanger as in this embodiment.

旋回流で伝熱性が向上して熱交換率を高め、効果□が著
しい。また、排気側にブロワ(5)を装置する時。
The swirling flow improves heat transfer and increases the heat exchange rate, making the effect □ remarkable. Also, when installing a blower (5) on the exhaust side.

充分に冷却しても風量が増加して不利であるが。Even if it is sufficiently cooled, the amount of air increases, which is disadvantageous.

筒け)等の気密構造に厳密性か軽減される点が利点であ
り、(13によるエゼクタ効果のみに依らずとも(2+
 (6、6’)間に圧力差を生ぜしめうる例として示す
The advantage is that it reduces the strictness of airtight structures such as (tube), and it does not depend only on the ejector effect due to (13).
(6, 6') is shown as an example in which a pressure difference can be generated between them.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の1実施例をなす装置の側断面図、第2
図は第2実施例の側断面図、第3図は第3実施例の側断
面図である。 (1)1次燃焼筒 (2)2次燃焼筒 (3)外筒(4
)仕切板 (5)ブロワ (6,6’)給気管(7)一
部器 (8,8’)オリイフイス (9)通気穴惺口開
口 (11,11’)仕切板 u2外筒f13空気路 
(14加熱体 (1日灰出器 00駆動器α1灰出ti
 C18ホッパ α9ビン eOシャンタ211蓋 (
22電磁弁 (23温度センサ (24カツく−C8遥
動杆 QCJ桿杆 闘電磁弁 (28,2E3’)調節弁 (29,29’)腕杆θO
ダイヤル θ刀温度センサ (32熱交換器θ3冷水管
 θ4熱水管 8!3サイクロンθ0排気l」 特許出願人 手続補正書(自発) 昭和60年4月12日 昭和60年4月−9日差出 特許庁長官 志賀 字 殿 1、事件の表示 昭和59年 特許願 第008339号2、発明の名称 3、補正をする看 事件との関係 特上出願人 ウェブ0ツブ( 住所(02020) 1lii岡市上田堤1丁目24−
19明 細 書 1、発明の名称 バイオマス;熱焼★戸2、特許請求の
範囲
Fig. 1 is a side sectional view of a device constituting one embodiment of the present invention;
The figure is a side sectional view of the second embodiment, and FIG. 3 is a side sectional view of the third embodiment. (1) Primary combustion tube (2) Secondary combustion tube (3) Outer tube (4
) Partition plate (5) Blower (6, 6') Air supply pipe (7) Partial component (8, 8') Orifice (9) Ventilation hole outlet opening (11, 11') Partition plate u2 outer cylinder f13 air passage
(14 heating element (1 day ash extractor 00 driver α1 ash extractor ti
C18 hopper α9 bottle eO shunter 211 lid (
22 Solenoid valve (23 Temperature sensor (24 Cut-C8 swinging rod QCJ rod Fighting solenoid valve (28, 2E3') Control valve (29, 29') Arm rod θO
Dial θ sword temperature sensor (32 heat exchanger θ3 cold water pipe θ4 hot water pipe 8!3 cyclone θ0 exhaust l) Patent applicant procedural amendment (voluntary) April 12, 1985 Patent submitted from April to 9, 1985 Office Commissioner Shiga Aza 1, Indication of the case 1983 Patent Application No. 008339 2, Title of the invention 3, Relationship with the amended case Special applicant Web 0 Tubu (Address (02020) 1lii Ueda Tsutsumi, Oka City 1 Chome 24-
19 Specification 1, Title of the invention Biomass; Heat-burning door 2, Claims

【1】1火燃焼i!Ii (1)の下部に通気穴(9)
と仄出H(15)とを設け、通気穴(9) +、t 1
 :X’結気管(6)へ結び、筒(1)の上部の一側に
1.を開0(10)を、相対の他側1こは燃料ホッパ(
18)を居室し、開口(10)の外周には2次絽気管(
6°)と結7丁空気路(13)&iりけ、2次絽気管(
6゛)から空気路(13)へ至る空気W抗を1次給気管
(6)から通気穴(9)へ至る2気抵抗より小さくし、
かつ、開口(1θ)と空気路(13)とを同心に2次燃
焼筒(2)へ連結し、筒(1)内まりも筒〔2〕内を低
圧力に保つように装置1.てなるバイオマス燃焼炉。
[1] 1 fire combustion i! Ventilation hole (9) at the bottom of Ii (1)
and a vent H (15), and a ventilation hole (9) +, t 1
:X' Tie to the tracheal tube (6) and attach 1. to one side of the upper part of the tube (1). Open 0 (10), and the other side of the relative is the fuel hopper (
18), and a secondary trachea (
6°) and the 7th airway (13) and the secondary trachea (
6゛) to the air passage (13) is made smaller than the 2-air resistance from the primary air supply pipe (6) to the ventilation hole (9),
Moreover, the opening (1θ) and the air passage (13) are concentrically connected to the secondary combustion cylinder (2), and the apparatus 1. A biomass combustion furnace.

【2、特許請求の範囲(1)に記載のもので、給気管(
6,6°)をブロワ(5)へ結び、2次燃焼筒(2)と
空気路(13)とを以てエゼクタ−を機成してなるバイ
オマス燃焼炉。 【3】特許請求の範囲(1)に記載のもので、2次燃焼
筒(2)を熱交換器(32)へ介してブロワ(5)へ結
んでなるバイオマス燃焼炉。
[2. The air supply pipe (
A biomass combustion furnace comprising an ejector that is connected to a blower (5) and a secondary combustion tube (2) and an air passage (13). [3] A biomass combustion furnace according to claim (1), comprising a secondary combustion cylinder (2) connected to a blower (5) via a heat exchanger (32).

【4】特許請求の範囲(1)に記載のもので、外筒(3
)を以て燃焼筒(1)を囲んで二!筒とした下端へ給気
管(6°)を、その上端へ空気路(13)を連結してな
るバイオマス燃焼炉。
[4] What is described in claim (1), the outer cylinder (3
) surrounding the combustion tube (1) and 2! A biomass combustion furnace consisting of a cylindrical lower end connected to an air supply pipe (6°) and an air passage (13) connected to its upper end.

【5】特許請求の範囲(1)に記載のもので、燃焼筒(
1)内を開口(10)とホッパ(18)の間で区分する
仕切板(11,11°)を設けてなるバイオマス燃焼炉
[5] The combustion tube (
1) A biomass combustion furnace provided with a partition plate (11, 11°) that divides the interior between an opening (10) and a hopper (18).

【6】特許請求の範囲(1)に記載のもので、調ll′
l蔚(7)と:II節井(28,28°)との計3個中
のいずれか1個または運動する2個を設けてなるバイオ
マス燃焼炉。
[6] What is described in claim (1),
A biomass combustion furnace equipped with either one or two moving out of a total of three: I (7) and II Noshi (28, 28°).

【7】特許請求の範囲(1)に記載のもので、ホッパ(
18)部位置に設けた温度センサ(23)に拠ってIN
(21)を作動してなるバイオマス燃焼炉。 3、発明の詳細な説明 (産業上の利用分野) 本発明1才、木質廃材チップ・
樹皮・籾殻・lKi真等、流動性陶で、嵩記原小で、揮
発ガス分が多で、低発熱量で、がっ、含水率が大なる場
合の多いバ1′オ7スをヌ1称とする燃焼炉に係るもの
である。 〔従来技術〕 上記のバイオ771才未利用)f源であ
って、充分に活用されていなかった。多くは焼却炉で処
分され、熱利用する場合も、その焼却炉を若干改良した
程度の炉であるに過ぎなかった。 燃焼に2次空気を用いるの(ま公知であるが、補助的で
あって完全燃焼できず、従って、熱交lΦ器に1よター
ルがN1し、かつ、燃焼空気比(よ3〜10位に高く、
熱効率は低劣であった。高水分の湯@(才とくに響かっ
た。 (問題をN決するための手段) 本発明は、1次燃焼筒
と、その下部に設けた1次通気穴、および、1次燃焼筒
の上部に設けた開口とその%同逢成す2次空気、路との
双方に同心で連結する2次燃焼筒とから機成され、2次
空気路からの噴流空気によるエゼクタ−効果、あるいl
ct 2次燃焼筒へ熱交換器を介して連結した吸引ブロ
ワの効果型こ拠って、1次燃焼面内より2次燃焼筒内を
低圧力に保つように装置されていて、1次空気量よりも
2次空%量の方が格段と多い様に空気抵坑差が設けてあ
り、1次燃焼筒内1こて少量の空気で蒸焼きにして主じ
た111発ガスを、2次燃焼筒内で1次空気量よりも充
分1こ多い2次空気にてガス燃焼し、かつ、可燃ガスを
必要量の空気で分周から包んでローソクの焔の杼にして
最小の空気比で完全燃焼させる事が可能な炉の芸1に係
るものである。 第1図に拠って本発明の第1実施例を説明する。(1)
は1次燃焼丙、(2)は2次燃焼両、(3)(は丙(1
)を囲う外面、(4)は仕切板で(2)(3)間を上下
に気召に分割し、(5)はブロワ、(6,6゛)は蛤気
管、(7)は(5)の人気口の:IN節蓋部器8’、8
’)は各ぐ(6,6’)に設けたオリフィス、(9)(
才(1)の下部に設けた5斂の通気穴、(10)は(1
)の上部に設けた開口、(11,1ビ)は(1)を分割
する仕切板、(12)Iよ(2)を包も外筒、(13)
は(10)を包み(2〕へ逼る空気路、(14)は(2
)内の加熱体であり、(5)口(6)E (8’) 0
(9)ノISf! +7)空気抵1冗ハ、(5)9(6
°)C:)(8”)φ(13)口(2〕の間の空気抵1
五より大するように、オリフィス(6,6°〕を辷1て
調節してあ己。(15)は仄出器、〔16)は(15)
の駆動器 (17)]よ気t:M、、c18)は燃料の
ホッパであり、(1)内を(11,11°)で区りした
片fi11に!IL11が、 It!l倶1]こ(18
)が連&占しである。、1日し、ホッパ(18) (ま
ロータリー71ダ−等を川して筒(1)・\)a結して
あっても良い。(+91 fjl l;学fA i甫鼻
6ヒレ・、(21))lよシャッタ、(21) 1.t
 l 181の脈、1.22)は電@升、(23)1.
を温度セ〉′す、+24)fは115)のカバーである
。 次に第20に示す第2実施例を説明する。(1)−一(
6)、(9)−一(15)、(17)、(18)+2第
11]で説明したのと同一である。(25JIjj吊薊
憚、(26)tは@憚、L27111よ別の電磁井、(
訳:。 28°〕は各ぐ(6i6’)の風量:A部会、C,;4
9゜29°)はその腕桿、(30)Iよその調節ダイヤ
ルである。 次に第312fこ示す第3実施例を説明する。(1)〜
(6)、(8)〜(13)、(15)、〔16)、(1
8)〜(2U)、(22)は第1図で説明したのと同一
である。(31)は筒(1)内で(9)と(15)との
開位置(ご=11けた温度センサ、(32)は熱交換器
、[31(よ冷水管、(34)ia熱水管、(35)は
(32)内に89けたサイクロン、(3b)は排気口で
ある。 次に本発明の作用1こついて、まず、第1[2)こ示す
第1実施例1こ拠って説明する。燃料はビン(19)へ
貯蔵され、蓋〔21)は井(22)で開状態にある時、
シャッタ(2(1)を開くと2重線矢印のように燃料は
、11.(11)で仕切られた筒(1)内の片側/\落
下し、仄出1t((15)を[2仙すると板(11゜)
の下端から開口(10)側の(15〕上にほぼ水平にI
祥積するので、その堆積面λ石油を歓布する等して点火
する。ホッパ〔18〕がフィダーを介して簡(1)・\
連結する場合で(よ、フィダーの駆動で同様の堆積面を
形成した1kに遵火する。次でブロワ(5)を作動する
と、1次空Xiよ筒(1’)(3)間の空間を経た後に
穴(9)から出て堆積v8籾を燃焼し、ガスは実線矢印
の径に#Jj、(11)で仕切られた(1)内の片側を
上昇して(10)から(2)へ至る。一方、2次空気は
筒(1+ T21間の空間を通り(13)から(10)
外周のIJ lを経て(2)へ噴流し エゼククー効果
を以て(10)から(1)内のガスを誘引して、(2)
内でガスを外周から包むようIこしてローソクの焔の様
に2次燃焼する。(14)は青火を助け、燃焼を促進す
る。 燃料の欠乏時や停電時等には、センサ(23)が昇温を
感知して(21)でホッパ(18)を閉!する。 次に第2図の実施例の作用を説明する。弁(27)の駆
動力で桿(25)Iま上下に1岳約し、かつ、(26)
を経て(15)を矢印の様に慴動させて 2Ii線矢印
の動きを促進する。−また、ダイヤノ【川30)の箪−
操作で弁(28,28°)が通観する。その他は第1実
施例と同一である。 次に第30の実施例について説明する。この事例は籾殻
の様な灰分の多い燃料の場合で、かつ、ブロワ(5)を
吸引式とした時の事例である。(19)は屋根1等から
のシュートとして示し、センサ(23)の加熱時にはシ
ャッタ(20)が閉まる。 仄出器(15)はスクリュ一式で例示し、センサ(31
)部が焼尽して低温になると(16)は駆動する様に、
タイマーで点火後の所定時間から自動制御する。1次空
気穴(9)(よ遇やきし鴇いので交換式にしている。2
次燃焼筒(2)1よ短小であって、サイクロン(35)
がその役割を補助し、熱交換器(32)で冷却後の排気
をブロワ(5)で吸引す否ことで、而(2)と管(6,
6°)との間に圧大差を設けた実施例である。その他(
よ第1実施例亡同−である。 次に本発明の効果について説明する。燃焼に2次空気を
用いるのは公知であるが、本発明では子の使用比率の次
元がiなる。γ【(9)がらのIIり空気(才金給気量
の1/3位とする故、筒に)内の燃料は不完全燃焼で揮
発ガスを范んに発生し、かつ、M (1)内は 650
度C位にあさえられて耐熱容易であり、燃焼の主体1よ
(2)内でのガス燃焼となり、かつ、空気がガスを外周
から包むようにして順次に反応して極小の空気比・約1
.2で完全燃焼する。その結果、熱交換器等へのタール
N1がなく、がっ、空気比重なる事は排熱損失を滅じる
故、高熱効率に出来る。また 筒(1〕内rの仕切板(
11,11°)の作用で新燃料の供給と畑面の確保・排
ガスとが区分されて燃焼が安定し、かつ、その不完全燃
焼の過程で高水力のVT燃籾の乾燥が伴い、乾燥C>1
2溜0囚体tS焼の順序に整然と流れ、燃焼困難とされ
た高水分の6θ%wb位までのバイオマスをも支障なく
完全燃焼させる番が出来る。これ(よ、本発明の用件を
満たして始めて達成し得る峯である。一方、空気路(1
3)が開口(10)を包む外周式エゼクタ−に構成され
た峯により、(10)を冷却g易にしたのみでなく、2
.欠空気が面(1)外周を冷却して(1)のヌ1り!V
i1ス惺−1!向上し、かつ、加温空気と成って燃焼を
改善する事が容易な構造へと構成出来た。箇(2)と筒
(12)との間にも七千の空気を通して冷却1.、かく
て、I01!安価なIl板1こて副久容%と成しく尋た
。なお、調1i麗(7)と調部会(28,28’ )と
の計3個中の1個または速動する2個での作動で、上記
の1次と2次との空気量比を保持して絶対量を変化し燃
焼量を調節する事も出来る。また、温度センサ(23)
に拠って薫(21)を作動させて容1こ不時の1に故を
防止する事も出来る。 4、図面の簡単な説明 第1!21よ本発明の1実施例を成す装置の側断面図で
あり、第23は第2実施例の側断面図であり、第33]
才第3実施例の債IWT面図である。 (1)1次燃焼筒 (2)2次燃焼筒 (3)外筒 (4)仕切i (5)ブロワ(6,6°)
kδ気管 (7)調箱原 〔8,8°〕オリフイス (9)通気穴(lO)開口 
(11,11’ )仕切板(12) り) 筒 (13
) 空 気 路 (14) 刀ロ 熱 イ本(15)仄
出器 (16)駆動器 (17)気密蓋(18)ホッパ
 (19)ビン (2θ)シャッタ(21) W (2
2) を磁弁 (23)温度センサ(24)カバー (
25)揺動憚 (26)腕憚(27)電磁丼 (28,
28°)調節井(29,29’ )腕憚 (30)ダイ
ヤル(31)温度センサ (32)軌交換器(33)冷
水管 (34)ダハ本管 (35)サイクロン (36)排気口
[7] A device according to claim (1), which includes a hopper (
18) Based on the temperature sensor (23) installed at the
A biomass combustion furnace operated by (21). 3. Detailed description of the invention (industrial application field) This invention is one year old, wood waste chips
Fluid ceramics such as bark, rice husks, lKi, etc., have a high volatile gas content, a low calorific value, and a high moisture content. This refers to the combustion furnace referred to as the first name. [Prior Art] The above-mentioned bio-771-year-old (unused) f source has not been fully utilized. Most of the waste was disposed of in incinerators, and even when it was used for heat, it was only a slightly improved incinerator. Using secondary air for combustion (this is well known, but it is auxiliary and does not allow complete combustion; therefore, there is N1 of tar in the heat exchanger, and the combustion air ratio (3 to 10 degrees) is used for combustion. high,
Thermal efficiency was poor. High-moisture hot water @ (This was a particularly clever idea. (Means for resolving the problem) It consists of a secondary combustion tube concentrically connected to both the opening and the secondary air passageway, and the ejector effect due to the jet air from the secondary air passageway.
ct The effect type of the suction blower connected to the secondary combustion cylinder via a heat exchanger is designed to maintain a lower pressure inside the secondary combustion cylinder than in the primary combustion surface, and the amount of primary air is There is a difference in air resistance so that the amount of air in the secondary air is much higher than that in the primary combustion cylinder. Gas is combusted in the combustion cylinder with secondary air that is sufficiently larger than the primary air amount by 1, and the combustible gas is wrapped in the required amount of air from the frequency division to form a candle flame shuttle with the minimum air ratio. This relates to the first feature of a furnace that can achieve complete combustion. A first embodiment of the present invention will be described with reference to FIG. (1)
is the primary combustion C, (2) is the secondary combustion both, (3) (is the C (1)
), (4) is a partition plate that divides (2) and (3) into upper and lower airways, (5) is a blower, (6,6゛) is a clam trachea, (7) is (5) )'s popular mouth: IN segment lid part 8', 8
') is the orifice provided in each leg (6, 6'), (9) (
(10) has five vent holes at the bottom of (1).
), (11, 1 Bi) is the partition plate that divides (1), (12) I and (2) are the outer cylinders, (13)
is the air path that wraps around (10) and goes to (2), and (14) is the air path that goes to (2).
), (5) mouth (6) E (8') 0
(9)ノISf! +7) Air resistance 1 +, (5) 9 (6)
°) C:) (8”) φ (13) Air resistance between the opening (2) 1
Adjust the orifice (6, 6°) by one side so that it is larger than 5. (15) is the ejector, [16] is (15)
The driver (17)] is the fuel hopper, and the inside of (1) is divided by (11, 11°) into the piece fi11! IL11 is It! 1] this (18
) is ren & fortune-telling. , 1 day, and hopper (18) (or rotary 71 da - etc. can be connected to pipe (1) / \) a. (+91 fjl l; GakufA iho nose 6 fin・, (21)) lyo shutter, (21) 1. t
l 181 pulse, 1.22) is Den @ Masu, (23) 1.
+24) f is the cover of 115). Next, a second embodiment shown in No. 20 will be described. (1)-1(
6), (9)-1 (15), (17), (18)+2 This is the same as explained in 11th]. (25JIjj hanging 薊憚, (26) t is @ 憚, L27111 another electromagnetic well, (
reason:. 28°] Air volume of each arm (6i6'): A section, C, ;4
9°29°) is the arm stick, and (30) is the adjustment dial on the I side. Next, a third embodiment shown in section 312f will be explained. (1)~
(6), (8) to (13), (15), [16), (1
8) to (2U) and (22) are the same as explained in FIG. (31) is the open position of (9) and (15) in the cylinder (1) (11-digit temperature sensor, (32) is the heat exchanger, [31 (very cold water pipe, (34) IA hot water pipe) , (35) is an 89-digit cyclone in (32), and (3b) is an exhaust port. To explain, when the fuel is stored in the bottle (19) and the lid [21] is in the open position in the well (22),
When the shutter (2 (1)) is opened, fuel falls on one side of the cylinder (1) partitioned by 11. (11) as shown by the double line arrow, and leaks 1 t ((15) to [2 Send it to the board (11°)
from the lower end of the opening (10) side to the top of (15)
As it accumulates, λ oil is poured onto the surface of the accumulation and ignited. Hopper [18] passes through feeder (1).\
When connecting (Yo), the feeder is driven to control the fire on 1k, which has formed a similar deposition surface.Next, when the blower (5) is operated, the space between the primary space Xi and the cylinders (1') and (3) is After passing through the hole (9), the accumulated v8 paddy is burned, and the gas rises from #Jj to the diameter of the solid line arrow, one side of (1) partitioned by (11), and flows from (10) to (2). ).On the other hand, the secondary air passes through the space between the cylinder (1+T21) and passes from (13) to (10).
It flows into (2) through IJl on the outer periphery, attracts the gas in (1) from (10) with the Ezekku effect, and then (2)
Inside, the gas is evaporated from the outside and combusted like a candle flame. (14) helps blue fire and promotes combustion. When there is a fuel shortage or a power outage, the sensor (23) detects a rise in temperature and closes the hopper (18) at (21)! do. Next, the operation of the embodiment shown in FIG. 2 will be explained. The driving force of the valve (27) moves the rod (25) up and down by one angle, and (26)
After that, move (15) like an arrow to promote the movement of the 2Ii line arrow. -Also, the diamond [river 30] chest-
The valve (28, 28°) can be seen through operation. The rest is the same as the first embodiment. Next, a 30th embodiment will be described. This example is a case where the fuel has a high ash content, such as rice husk, and the blower (5) is a suction type. (19) is shown as a chute from the roof 1, etc., and the shutter (20) closes when the sensor (23) is heated. The bubbling device (15) is exemplified by a set of screws, and the sensor (31
) part burns out and becomes low temperature, so that (16) is driven,
It is automatically controlled from a predetermined time after ignition using a timer. Primary air hole (9) (Because it is very convenient, I made it replaceable. 2
The next combustion cylinder (2) is shorter and smaller than 1, and the cyclone (35)
assists in its role, and by sucking the exhaust air cooled by the heat exchanger (32) with the blower (5),
6°). others(
This is the same as the first embodiment. Next, the effects of the present invention will be explained. It is known that secondary air is used for combustion, but in the present invention, the dimension of the child usage ratio is i. γ [(9) The fuel in the air (which is about 1/3 of the amount of air supplied to the cylinder) is incompletely combusted, generating plenty of volatile gas, and M (1 ) is 650
It is easily heat resistant as it is heated to around 100°C, and gas combustion occurs within the combustion main body 1 and (2), and the air wraps the gas from the outside and reacts sequentially, resulting in an extremely small air ratio of about 1
.. Complete combustion occurs at 2. As a result, there is no tar N1 to the heat exchanger, etc., and the air specific gravity eliminates waste heat loss, resulting in high thermal efficiency. Also, the partition plate (inner r) of the tube (1)
11, 11°) separates the supply of new fuel from the field and exhaust gas to stabilize combustion, and in the process of incomplete combustion, the high hydraulic power VT combustion paddy dries, resulting in drying. C>1
It flows in an orderly sequence of 2 reservoirs, 0 prisoners, and tS firing, making it possible to completely burn biomass with a high moisture content of up to about 6θ%wb, which was considered difficult to burn, without any problems. This goal can only be achieved by satisfying the requirements of the present invention.
3) not only makes it easier to cool down (10), but also allows the 2
.. The lack of air cools the outer periphery of surface (1), and (1) disappears! V
i1su-1! We were able to create a structure that makes it easy to improve combustion by converting it into heated air. 7,000 air is also passed between the tube (2) and the tube (12) for cooling.1. ,Thus, I01! I asked about the cheap Il plate 1 trowel subduration%. In addition, by operating one or two of the three fast-moving units, Cho 1i Rei (7) and Chobekai (28, 28'), the air volume ratio between the primary and secondary air can be adjusted. It is also possible to hold it and change the absolute amount to adjust the combustion amount. In addition, the temperature sensor (23)
It is also possible to activate Kaoru (21) depending on the situation to prevent an accidental accident. 4. Brief description of the drawings No. 1! 21 is a side sectional view of the device constituting one embodiment of the present invention, No. 23 is a side sectional view of the second embodiment, and No. 33]
FIG. 4 is a bond IWT surface view of a third embodiment. (1) Primary combustion tube (2) Secondary combustion tube (3) Outer tube (4) Partition i (5) Blower (6,6°)
kδ trachea (7) Hokohara [8,8°] orifice (9) Ventilation hole (lO) opening
(11,11') Partition plate (12) Tube (13
) Air path (14) Heat pipe (15) Buffer (16) Driver (17) Airtight lid (18) Hopper (19) Bottle (2θ) Shutter (21) W (2
2) Solenoid valve (23) Temperature sensor (24) Cover (
25) Swinging (26) Arms (27) Electromagnetic bowl (28,
28°) Control well (29, 29') Armpit (30) Dial (31) Temperature sensor (32) Track exchanger (33) Cold water pipe (34) Roof main pipe (35) Cyclone (36) Exhaust port

Claims (1)

【特許請求の範囲】 (1)1次燃焼筒(1)の下部に1次給気管(6)に連
なる通気穴(9)と灰出器卸とを設け、(1)の上部を
仕切板(11,11’)によって2室に分割して、その
1室の」二面をホッパ(1日へ結び、他室の上部には開
口(10を設け、2次給気管(6′)に連なる空気路α
3と口(10とを合せて2次燃焼筒(2)へ結び、管(
6,6’)と筒(2)との間に設定した圧力差を設けて
なるバイオマス燃焼炉。 (2、特許請求の範囲(1)に記載のもので、空気路0
3を開口αOの外周に構成し、かつ、1次燃焼筒(1)
と外筒(3)と仕切板(4)とがなす空間の、1端に空
気路α3を他端に給気管(6′)を設けてなるバイオマ
ス燃焼炉。 (3)特許請求の範囲(1)に記載のもので、調節蓋(
7)および調節弁(28,28’)の計3個中の1個ま
たは連動する2個によって、給気管(6)と(6ツとの
空気量を調節可能にしてなるパイ、オマス燃焼炉。 (4)特許請求の範囲(1)に記載のもので、仕切板0
にて分割さてホッパ1日へ連なる燃焼筒(1)の1室内
に、遥動杆eOを設けてなるバイオマス燃焼炉。 (5)特許請求の範囲(1)に記載のもので、給気穴(
9)より充分下方に設けた販出器(1Bを、穴(1!3
との中間部に設けた温度センサθりによってオンオフし
てなるバイオマス燃焼炉。 (6)特許請求の範囲(1)に記載のもので、ホッパa
8部位の1次燃焼筒(1)壁面に設けた温度センサe3
によって蓋211を作動してホップ(1日を閉塞可能と
し。 または、シャッタeOを作動してビン四を閉塞可能とし
てなるバイオマス燃焼炉。 (7)特許請求の範囲(1)に記載のもので、熱交換器
82内に設けたサイクロン09を開口α0と2次空気路
(13とに合せて結び、サイクロンθ9を2次燃焼筒(
2)として作用させてなるバイオマス燃焼炉。
[Claims] (1) A ventilation hole (9) connected to the primary air supply pipe (6) and an ash extractor are provided in the lower part of the primary combustion tube (1), and the upper part of (1) is provided with a partition plate. Divided into two chambers by (11, 11'), two sides of one chamber are connected to a hopper (1 day), an opening (10 is provided at the top of the other chamber, and a secondary air supply pipe (6') is connected to the hopper (1 day). Continuous air passage α
3 and the port (10), connect it to the secondary combustion cylinder (2), and connect the pipe (
A biomass combustion furnace in which a set pressure difference is provided between the cylinder (2) and the cylinder (2). (2. According to claim (1), the air passage is 0.
3 is configured on the outer periphery of the opening αO, and the primary combustion cylinder (1)
A biomass combustion furnace comprising an air passage α3 at one end and an air supply pipe (6') at the other end of a space formed by an outer cylinder (3) and a partition plate (4). (3) The adjustment lid (
7) and control valves (28, 28'), one or two of which are interlocked, allows the amount of air between the air supply pipe (6) and (6) to be adjusted. (4) According to claim (1), the partition plate 0
A biomass combustion furnace in which a swinging rod eO is installed in one chamber of a combustion tube (1) connected to a hopper. (5) What is described in claim (1), with an air supply hole (
9) Place the vending device (1B) well below the hole (1!3
A biomass combustion furnace that is turned on and off by a temperature sensor θ installed in the middle between the two. (6) According to claim (1), the hopper a
Temperature sensor e3 installed on the wall of 8 primary combustion cylinders (1)
A biomass combustion furnace in which the lid 211 is actuated to make it possible to close the hop (1 day) or the shutter eO is actuated to make it possible to close the bin 4. (7) The biomass combustion furnace according to claim (1) , the cyclone 09 provided in the heat exchanger 82 is connected to the opening α0 and the secondary air passage (13), and the cyclone θ9 is connected to the secondary combustion tube (13).
2) A biomass combustion furnace that functions as
JP833984A 1984-01-19 1984-01-19 Biomass incinerator Granted JPS60152812A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP833984A JPS60152812A (en) 1984-01-19 1984-01-19 Biomass incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP833984A JPS60152812A (en) 1984-01-19 1984-01-19 Biomass incinerator

Publications (2)

Publication Number Publication Date
JPS60152812A true JPS60152812A (en) 1985-08-12
JPH0557483B2 JPH0557483B2 (en) 1993-08-24

Family

ID=11690439

Family Applications (1)

Application Number Title Priority Date Filing Date
JP833984A Granted JPS60152812A (en) 1984-01-19 1984-01-19 Biomass incinerator

Country Status (1)

Country Link
JP (1) JPS60152812A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100378402C (en) * 2006-01-17 2008-04-02 金云峰 Forced blowing type refuse combustion device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008190808A (en) * 2007-02-06 2008-08-21 Soai:Kk Combustion device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5755840U (en) * 1980-09-12 1982-04-01
JPS58139U (en) * 1981-06-24 1983-01-05 東北三共有機株式会社 Complete combustion device
JPS5893607U (en) * 1981-12-18 1983-06-24 株式会社山本製作所 Paddy grain combustion equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58139B2 (en) * 1977-07-01 1983-01-05 日立電子株式会社 Method for manufacturing face plate for image pickup tube
JPS5590695A (en) * 1978-12-25 1980-07-09 Okazaki Kikai Kogyo Kk Forced moisture regulating method and apparatus for paper sheet

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5755840U (en) * 1980-09-12 1982-04-01
JPS58139U (en) * 1981-06-24 1983-01-05 東北三共有機株式会社 Complete combustion device
JPS5893607U (en) * 1981-12-18 1983-06-24 株式会社山本製作所 Paddy grain combustion equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100378402C (en) * 2006-01-17 2008-04-02 金云峰 Forced blowing type refuse combustion device

Also Published As

Publication number Publication date
JPH0557483B2 (en) 1993-08-24

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